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CapMachine/CapMachine.Wpf/PPCalculation/REFPROP/FLUIDS/HMX.BNC

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HMX !Mnemonic for mixture model, must match hfmix on call to SETUP.
4 !Version number
! Changelog:
! ---------
! 06-03-13 MLH, Update all interaction parameters for thermal conductivity due to model revisions.
! 07-05-13 MLH, Update h2 and he mixture viscosity int par due to model revisions.
! 07-10-13 EWL, Add Gernert model for mixtures of nitrogen, oxygen, argon, carbon dioxide, carbon monoxide, and water.
! 08-15-13 EWL, Add parameters for CO2/R1216, R32/R1234yf, R125/R1234yf, R134A/R1234yf, R32/R1234ze(E).
! 05-07-14 MLH, Revise C1/CO, N2/He, CO2/H2, CO2/He, H2/CO, H2/Ar, CO/He, CO/Ar, He/Ar, R32/R125 thermal conductivity parameters.
! 02-12-15 EWL, Add nitrogen/methanol.
! 07-16-15 EWL, Update propane/ethanol.
! 10-20-15 EWL, Add parameters for R1234ze with R125, R134a, and R1234yf.
! 11-09-15 EWL, Re-add old LJ6 mixture model for compatibility with version 9.0.
! 05-03-16 EWL, Add helium/neon.
! 01-12-17 EWL, Add R134A/R245fa.
! 02-02-17 IHB, Remove entries with wrong CAS# for R1234ze(E).
! 02-16-17 EWL, Add neon/hydrogen, neon/xenon, and helium/krypton, and place all noble gas entries together.
! 07-26-17 EWL, Change entire file to new format required by version 10 of Refprop.
! 01-01-18 EWL, Change entries with either oxygen or argon that use all 1's so that the (nitrogen/other fluid) parameters are used.
! 02-28-18 IHB, Add mixture parameters of Neumann (2017) for SO2 containing systems.
! 03-19-18 IHB, Add CO2/CO parameters of Souza and Herrig (2018).
! 04-12-18 EWL, Change all mixtures with no departure function to XR0.
! 04-13-18 IHB, Refit ethylene glycol/water.
! 05-11-18 IHB, Refit all TC and VC parameters.
! 05-11-18 IHB, Add Blackham helium-hydrogen mixture model.
! 05-14-18 IHB, Add Neumann argon-ammonia mixture model.
! 05-17-18 IHB, Add mixture parameters of Thol et al. (2018) for methane mixed with isobutane, butane, isopentane, and pentane.
! 05-18-18 EWL, Add ammonia/water mixture model of Bell et al. (2018).
#BNC !Binary mixing coefficients
BNC
? Binary mixing coefficients for the various mixing rules used with the HMX model:
?
? KWi: (i = 1,2,3,...,A,B,...) ---> Kunz-Wagner mixing rules
? model BetaT GammaT BetaV GammaV Fij not used
?
? GGi: (i = same as KWi) ---> Official GERG-2008 mixing rules
? model BetaT GammaT BetaV GammaV Fij not used
?
? LJi: (i = 1,2,3) ---> Lemmon-Jacobsen mixing rules
? model zeta xi Fpq beta gamma not used
?
? TR1: ---> Tillner-Roth mixing rules
? model Kv alpha not used not used not used not used
?
? LIN: ---> Linear mixing rules
? model Kt Kv not used not used not used not used
?
? TRN: ---> Transport mixing rules
? model a1 a2 a3 a4 a5 a6
?
? ST1: ---> Surface tension rules
? model a1 a2 a3 a4 a5 a6
?
? PR1 (Peng-Robinson): ---> Peng-Robinson mixing rules
? model kij not used not used not used not used not used
?
? If a binary mixture contains both GG and KW (or LJ) mixing rules, the GG line must
? be placed first, and then the KW line. If the GERG08 routine has been called,
? then only the GG model only is read, thus implementing the full GERG-2008 model.
?
? Coefficients for binary critical lines (where the # sign is a number from 1 to 7):
?
? TC#: (type I mixtures)
? model a1 a2 a3 a4 a5 a6
? Where Tc of the mixture is calculated with the following equation:
? Tc = x1*Tc1 + x2*Tc2 + x2*(a1*x1 + a2*x1**2 + a3*x1**3 + a4*x1**4 + a5*x1**5 + a6*x1**6)
?
? VC#: (type I mixtures)
? model a1 a2 a3 a4 a5 a6
? Where Vc of the mixture is calculated with the following equation:
? Vc = x1*Vc1 + x2*Vc2 + x2*(a1*x1 + a2*x1**2 + a3*x1**3 + a4*x1**4 + a5*x1**5 + a6*x1**6)
?
? Format for a binary pair:
? Line 1: Comments beginning with '?' (these are read by Fortran and displayed by GUI)
? 2: Additional comments beginning with '?' (multiple lines with a ? can be used)
? 3: HASH_1 / HASH_2
? 4: model binary parameters
? 5: model Tc line parameters
? 6: model Vc line parameters
? 7: model Pr line parameters
? 8: separator line ('!')
? Only lines 3 and 8 are required
?
?
?
? Selection of mixture model when more than one is present:
?
? If the GERG-08 model is off, The last line in the HMX.BNC for a given
? binary pair will always be the one used.
?
? If the GERG-08 option is on, the line containing GG is used if available.
? New mixture models always follow the lines with GG in the HMX.BNC.
?
? Order of sorting of binary pairs:
?
? 1. Each binary pair shall be internally sorted by normal boiling point temperatures of the fluids.
? For instance for the pair hydrogen + water, hydrogen has a lower NBP, therefore the order is
? hydrogen, water.
?
? Exception: Methane is always the first fluid listed in the binary pair.
?
? 2. The binary pairs (once internally sorted) shall be first sorted by the NBP of the first component, then,
? by the NBP of the second component.
?
? Note: If you need to swap the order of a binary pair, the kij (for PR), Fij, gammaT, and gammaV values do
? not need to be adjusted, but beta_{ij} = 1/beta_{ji}, thus the betaT and betaV values need to be
? modified, which will introduce a small discrepancy from tabulated values. Also, the coefficients
? for the critical line (TCx, VCx) need to be refitted. Other models are mostly symmetric so no swapping
? of parameters is needed.
?
? Here is a sample entry (the block must start in column 1, not column 3 as shown below):
?
? !
? ?Rxxx/Rxxx
? ?Example setup for a new mixture
? HASH_1/HASH_2
? KW0 1. 1. 1. 1. 0. 0.
? TC1 0. 0. 0. 0. 0. 0.
? VC1 0. 0. 0. 0. 0. 0.
? !
?
!
?Methane/Helium [C1/HE]
?Kunz and Wagner (2007)
8ae7a700/3b8eed30
KW0 1. 3.159776855 1. 0.881405683 0. 0. 0. 0. 0. 0. 0. 0.
TC5 261.35575 -23.712303 47.134844 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -1.2463518 2.4401771 -1.1787725 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Hydrogen [C1/H2]
?Kunz and Wagner (2007)
8ae7a700/8d757b40
KW7 1. 1.352643115 1. 1.018702573 1. 0. 0. 0. 0. 0. 0. 0.
TC5 66.626615 445.38361 -381.30154 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.369107 0.59576944 -0.23854726 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.28 0.207 0.99 0.98 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0156 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Nitrogen [C1/N2]
?Kunz and Wagner (2007)
8ae7a700/edbdc8e0
KW3 0.99809883 0.979273013 0.998721377 1.013950311 1. 0. 0. 0. 0. 0. 0. 0.
TC1 8.2656641 8.4386197 -72.010236 295.68631 -432.5271 214.03443 0. 0. 0. 0. 0. 0.
VC1 0.030785658 -0.40640575 1.165118 -1.4324897 0.71471081 -0.060260427 0. 0. 0. 0. 0. 0.
TRN -0.3594 0.9076 -6.1172e-2 3.9842e-2 0.03 0. 0. 0. 0. 0. 0. 0.
PR1 0.0311 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
ST1 0.085 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Carbon monoxide [C1/CO]
?Kunz and Wagner (2007)
8ae7a700/091cb7e0
KW0 0.987411732 0.987473033 0.997340772 1.006102927 0. 0. 0. 0. 0. 0. 0. 0.
TC1 7.3105409 49.231542 -157.34847 407.13639 -521.73627 248.09754 0. 0. 0. 0. 0. 0.
VC1 -0.072684592 0.25182629 -0.87609567 1.8275163 -1.8405443 0.70666027 0. 0. 0. 0. 0. 0.
TRN -0.0165 -0.2493 0. 0. -0.05 0. 0. 0. 0. 0. 0. 0.
PR1 0.03 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Argon [C1/AR]
?Kunz and Wagner (2007)
8ae7a700/ed016370
KW0 0.990954281 0.989843388 1.034630259 1.014678542 0. 0. 0. 0. 0. 0. 0. 0.
TC1 10.983036 -11.230122 21.65572 70.253825 -166.24191 99.289073 0. 0. 0. 0. 0. 0.
VC1 0.013323354 -0.11710195 0.32400353 -0.52697552 0.46498161 -0.15989564 0. 0. 0. 0. 0. 0.
PR1 0.023 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Oxygen [C1/O2]
?Kunz and Wagner (2007)
8ae7a700/edc36840
KW0 1. 0.95 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -13.316793 42.464364 -141.35364 386.4149 -472.30294 216.38368 0. 0. 0. 0. 0. 0.
VC1 -0.0053338713 -0.019100265 0.040372695 -0.098736403 0.12952941 -0.048045147 0. 0. 0. 0. 0. 0.
!
?Methane/Krypton [C1/KR]
?E.W. Lemmon, NIST (2002)
8ae7a700/d7c8c510
XR0 1. 0.9930853 1. 1.0003826 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.3978996 0.087824916 -1.4217036 2.6992092 -2.6666172 1.2591837 0. 0. 0. 0. 0. 0.
VC1 -0.0034692786 -0.014567719 0.093180764 -0.23768497 0.28043171 -0.12710519 0. 0. 0. 0. 0. 0.
!
?Methane/Ethylene [C1/ETY]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
8ae7a700/9c1062b0
KW0 1.004 1.021 1. 0.99 0.106 0. 0. 0. 0. 0. 0. 0.
TC1 60.403688 -89.261163 246.01218 -226.88406 -47.397509 124.29729 0. 0. 0. 0. 0. 0.
VC1 0.025731572 -0.3865135 1.2741434 -2.357786 2.1060516 -0.74990731 0. 0. 0. 0. 0. 0.
PR1 0.0215 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Ethane [C1/C2]
?Kunz and Wagner (2007)
8ae7a700/434e2a40
KW1 0.996336508 1.049707697 0.997547866 1.006617867 1. 0. 0. 0. 0. 0. 0. 0.
TC1 53.728792 -48.517713 68.413989 359.36428 -731.27631 404.35817 0. 0. 0. 0. 0. 0.
VC1 0.0015054136 -0.52864618 2.1935987 -4.1799033 3.7578541 -1.3862557 0. 0. 0. 0. 0. 0.
TRN 0.0331 -0.2549 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 -0.0026 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Nitrous oxide [C1/N2O]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.36% from 49 bubble-point pressures
8ae7a700/e0647c00
XR0 0.98876 1.02354 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 55.750676 53.560147 -403.50019 1065.6766 -1253.5869 583.0493 0. 0. 0. 0. 0. 0.
VC1 -0.0003927645 -0.37036629 1.467206 -3.2714398 3.5776896 -1.5668698 0. 0. 0. 0. 0. 0.
!
?Methane/Carbon dioxide [C1/CO2]
?Kunz and Wagner (2007)
8ae7a700/77c8bee0
KW4 1.02262449 0.975665369 0.999518072 1.002806594 1. 0. 0. 0. 0. 0. 0. 0.
TC1 57.574775 -257.09178 1259.2 -3155.1727 3415.6784 -1341.0002 0. 0. 0. 0. 0. 0.
VC1 -0.022761512 -0.17876692 0.60327625 -1.3813423 1.0825174 -0.071173262 0. 0. 0. 0. 0. 0.
TRN -0.00677 -0.3342 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0919 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Hydrogen sulfide [C1/H2S]
?Kunz and Wagner (2012)
8ae7a700/c6c03020
KW0 1.011090031 0.961155729 1.012599087 1.040161207 0. 0. 0. 0. 0. 0. 0. 0.
TC1 168.27846 -1277.8949 7994.9235 -21047.751 22408.985 -8155.322 0. 0. 0. 0. 0. 0.
VC1 0.0080736295 -0.85848911 4.542042 -11.912958 12.570234 -4.5019219 0. 0. 0. 0. 0. 0.
!
?Methane/Carbonyl sulfide [C1/COS]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8ae7a700/e7f902e0
XR0 1. 1.0391 1. 1.1443 0. 0. 0. 0. 0. 0. 0. 0.
TC1 118.78062 141.03191 -1018.3296 3302.5873 -4668.4773 2342.9893 0. 0. 0. 0. 0. 0.
VC1 0.074129512 -0.85345573 3.3411955 -7.3546407 7.6952327 -3.2099588 0. 0. 0. 0. 0. 0.
PR1 0.0289 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Propylene [C1/PRY]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
8ae7a700/56d778b0
XR0 0.998 1.117 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 153.63351 134.85783 -1017.3035 3686.3762 -5050.4971 2370.3993 0. 0. 0. 0. 0. 0.
VC1 0.14456934 -1.6472315 6.9362126 -15.482244 16.587911 -7.0245934 0. 0. 0. 0. 0. 0.
PR1 0.033 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Propane [C1/C3]
?Kunz and Wagner (2007)
8ae7a700/70c6aac0
KW2 0.989680305 1.098655531 1.00482707 1.038470657 1. 0. 0. 0. 0. 0. 0. 0.
TC1 113.31704 49.977969 -1095.2649 4486.0455 -5938.0614 2625.9911 0. 0. 0. 0. 0. 0.
VC1 -0.17200582 0.070545756 1.2331694 -3.8691319 4.6124256 -2.3061849 0. 0. 0. 0. 0. 0.
TRN -0.0182 -0.0263 0. 0. -0.03 0. 0. 0. 0. 0. 0. 0.
PR1 0.014 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/R22 [C1/R22]
?E.W. Lemmon, NIST (2002)
?Huber (2017) Dilute gas viscosity fit to Hongo et al., J. Chem. Eng. Jpn., 1988, 21, 632-38 AAD 0.7%
8ae7a700/57716470
XR0 1. 1.1114773 1. 1.0219928 0. 0. 0. 0. 0. 0. 0. 0.
TC1 145.63098 376.1223 -2428.4325 7358.5099 -9498.5114 4326.6375 0. 0. 0. 0. 0. 0.
VC1 0.14137435 -1.583063 6.3626751 -13.716366 14.234131 -5.9227283 0. 0. 0. 0. 0. 0.
TRN -0.214 0.250 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Ammonia [C1/NH3]
?Neumann et al. (2018)
?Previous model (w/ Fij=0.154) is the superceded model of T.M. Blackham and E.W. Lemmon, NIST (2010)
?TRN fit9/17 to Trans. Faraday Soc., 1965, 61, 2422; AAD 0.9%
8ae7a700/e9847540
KW0 0.985 0.977 1. 1. 0.154 0. 0. 0. 0. 0. 0. 0.
KW0 1.022371 0.940156 1.006058 1.069834 0.0 0. 0. 0. 0. 0. 0. 0.
TC5 221.98348 -345.32796 214.5401 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.0096032548 -0.42812815 0.13910992 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.22 0.80 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Dimethyl ether [C1/DME]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8ae7a700/8f27e300
XR0 1. 1.1118 1. 1.1094 0. 0. 0. 0. 0. 0. 0. 0.
TC1 150.41662 637.33689 -3948.3052 11470.896 -14460.072 6456.6752 0. 0. 0. 0. 0. 0.
VC1 0.12250411 -1.3739853 5.9199375 -13.998006 15.735929 -6.9877971 0. 0. 0. 0. 0. 0.
!
?Methane/Isobutane [C1/C4I]
?Thol et al. (2018)
?The deprecated KW0 model is from Kunz and Wagner (2007)
8ae7a700/47ade7e0
GG0 0.980315756 1.161117729 1.011240388 1.054319053 0.771035405688 0. 0. 0. 0. 0. 0. 0.
KWE 0.9405 0.9917 1.0434 1.143 1. 0. 0. 0. 0. 0. 0. 0.
TC1 219.12033 -79.353521 -1046.2718 4982.7394 -6843.2123 3116.0525 0. 0. 0. 0. 0. 0.
VC1 0.1554148 -2.904025 12.755462 -28.407478 30.647718 -12.967248 0. 0. 0. 0. 0. 0.
PR1 0.0256 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Sulfur dioxide [C1/SO2]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.52% from 5 bubble-point pressures
?TRN fit 9/17 to Trans. Faraday Soc., 1965, 61, 2422 AAD 1.2%
8ae7a700/7fad4b80
XR0 1.03694 1.07082 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 189.13309 386.36376 -908.23551 507.32329 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.017475113 -0.38275778 0.35136353 -0.58062359 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.50 0.91 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Perfluorobutane [C1/C4F10]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.75% from 34 bubble-point pressures
8ae7a700/a8f85e00
XR0 1.013695 1.12365 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 150.05746 1210.5 -6384.6397 17805.418 -21997.435 9603.5815 0. 0. 0. 0. 0. 0.
VC1 0.61646808 -4.6280244 15.253081 -28.903122 27.305938 -10.3025 0. 0. 0. 0. 0. 0.
!
?Methane/Butane [C1/C4]
?Thol et al. (2018)
?The deprecated KW0 model is from Kunz and Wagner (2007)
8ae7a700/7b3b4080
GG0 0.99417491 1.171607691 0.979105972 1.045375122 1. 0. 0. 0. 0. 0. 0. 0.
KWK 0.9421 1.0307 1.035 1.118 1. 0. 0. 0. 0. 0. 0. 0.
TC1 266.47579 99.963589 -2471.8114 8031.9246 -8869.4887 3179.3075 0. 0. 0. 0. 0. 0.
VC1 0.57656331 -7.5073689 31.411801 -64.517137 64.744872 -25.70277 0. 0. 0. 0. 0. 0.
TRN 0.003 -0.1292 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0133 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Neopentane [C1/C5A]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8ae7a700/5a410790
XR0 1. 1.1976 1. 1.0772 0. 0. 0. 0. 0. 0. 0. 0.
TC1 232.62762 365.59151 -1286.5122 3110.1764 -2020.6123 -152.1481 0. 0. 0. 0. 0. 0.
VC1 0.61590907 -5.8943034 24.498329 -52.047417 53.674531 -21.813501 0. 0. 0. 0. 0. 0.
!
?Methane/Isopentane [C1/C5I]
?Thol et al. (2018)
?The deprecated KW0 model is from Kunz and Wagner (2007)
8ae7a700/86ee46a0
GG0 1. 1.188899743 1. 1.343685343 0. 0. 0. 0. 0. 0. 0. 0.
KWI 0.886 0.993 1.023 1.076 1. 0. 0. 0. 0. 0. 0. 0.
TC1 209.55092 -699.65509 9149.5807 -29391.915 38510.866 -17739.298 0. 0. 0. 0. 0. 0.
VC1 1.0892505 -6.9862487 27.991411 -71.932549 88.864592 -40.453763 0. 0. 0. 0. 0. 0.
PR1 -0.0056 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Pentane [C1/C5]
?Thol et al. (2018)
?The deprecated KW0 model is from Kunz and Wagner (2007)
8ae7a700/76bc0290
GG0 0.992127525 1.249173968 0.94833012 1.124508039 0. 0. 0. 0. 0. 0. 0. 0.
KWQ 0.9082 1.03884 1.0287400 1.13209 1. 0. 0. 0. 0. 0. 0. 0.
TC1 339.184 -1619.322 9881.692 -25340.658 31628.483 -14956.281 0. 0. 0. 0. 0. 0.
VC1 -0.0021106769 -2.1811004 15.745925 -44.683709 54.883366 -25.086474 0. 0. 0. 0. 0. 0.
PR1 0.023 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Methanol [C1/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
8ae7a700/c41aa690
KW0 0.972 1.308 0.713 1.137 1.276 0. 0. 0. 0. 0. 0. 0.
TC5 415.48219 -48.512715 -627.17926 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 0.042785911 -1.0376636 1.0785778 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Hexane [C1/C6]
?Kunz and Wagner (2007)
8ae7a700/cb03ba40
KW0 0.981844797 1.330570181 0.958015294 1.052643846 0. 0. 0. 0. 0. 0. 0. 0.
TC2 197.18927 2407.8721 -9927.4899 18355.73 -11006.114 0. 0. 0. 0. 0. 0. 0.
VC2 0.26133007 -0.33336517 -3.6431848 9.4187123 -6.8977135 0. 0. 0. 0. 0. 0. 0.
PR1 0.0422 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Ethanol [C1/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
8ae7a700/3d5f67e0
KW0 0.954 1.366 1. 1. 1.486 0. 0. 0. 0. 0. 0. 0.
TC4 366.91974 -730.79275 2967.4275 -2928.9371 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.089812666 -1.7613441 3.8639066 -3.1551953 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Benzene [C1/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
8ae7a700/f2cfb460
KW2 0.982 1.266 1. 1. 0.955 0. 0. 0. 0. 0. 0. 0.
TC4 404.59007 -640.12629 3210.7167 -2760.654 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.086290075 0.21756408 -0.20721291 -0.65501277 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0363 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Cyclohexane [C1/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8ae7a700/6e225350
KW0 1. 1.3145 1. 1.0835 -0.3986 0. 0. 0. 0. 0. 0. 0.
TC2 266.43871 2053.857 -8130.4106 15286.696 -9698.5647 0. 0. 0. 0. 0. 0. 0.
VC2 0.34264843 -0.76702177 -3.59698 10.692424 -8.0922034 0. 0. 0. 0. 0. 0. 0.
PR1 0.0389 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Heptane [C1/C7]
?Kunz and Wagner (2007)
8ae7a700/b398a3b0
KW0 0.977431529 1.379850328 0.962050831 1.156655935 0. 0. 0. 0. 0. 0. 0. 0.
TC2 278.88763 2272.4971 -9517.5188 17654.464 -10197.023 0. 0. 0. 0. 0. 0. 0.
VC2 0.50307626 -2.1033679 1.12263 4.4145301 -5.1959744 0. 0. 0. 0. 0. 0. 0.
PR1 0.0352 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Water [C1/H2O]
?Kunz and Wagner (2007)
8ae7a700/b43a7600
KW0 1.063333913 0.775810513 1.012783169 1.585018334 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Methylcyclohexane [C1/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
8ae7a700/0429edd0
XR0 0.98 1.363 0.961 1.041 0. 0. 0. 0. 0. 0. 0. 0.
TC2 277.60384 1535.076 -4977.1019 9638.038 -5908.7759 0. 0. 0. 0. 0. 0. 0.
VC2 0.19275907 0.51320709 -5.351121 9.8511409 -6.2659827 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Toluene [C1/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
8ae7a700/a49b8b50
KW0 0.967 1.34 0.961 1.085 1.313 0. 0. 0. 0. 0. 0. 0.
TC4 497.4649 -1055.1197 3396.1022 -2040.8506 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.06085318 -1.520147 4.2655579 -3.8090137 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.097 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Octane [C1/C8]
?Kunz and Wagner (2007)
8ae7a700/f174a9b0
KW0 0.957473785 1.449245409 0.994740603 1.116549372 0. 0. 0. 0. 0. 0. 0. 0.
TC2 474.19589 -474.45097 5993.1865 -18913.282 28394.961 -14559.475 0. 0. 0. 0. 0. 0.
VC2 1.2194434 -10.346055 38.531447 -75.099212 73.481776 -29.105933 0. 0. 0. 0. 0. 0.
PR1 0.0496 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Nonane [C1/C9]
?Kunz and Wagner (2012)
8ae7a700/7f94dc20
KW0 0.947716769 1.528532478 1.002852287 1.141895355 0. 0. 0. 0. 0. 0. 0. 0.
TC1 556.54901 -1867.7155 15371.86 -43098.616 56589.442 -26318.448 0. 0. 0. 0. 0. 0.
VC1 1.0042526 -7.4661054 30.096603 -65.745028 70.88971 -30.359681 0. 0. 0. 0. 0. 0.
PR1 0.0474 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Decane [C1/C10]
?Kunz and Wagner (2012)
8ae7a700/111888d0
KW0 0.937777823 1.568231489 1.033086292 1.146089637 0. 0. 0. 0. 0. 0. 0. 0.
TC2 505.95064 593.76617 -571.2221 1810.9467 86.374464 0. 0. 0. 0. 0. 0. 0.
VC2 1.1025601 -6.071885 14.939157 -17.224358 6.6475926 0. 0. 0. 0. 0. 0. 0.
PR1 0.0422 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methane/Dodecane [C1/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
8ae7a700/8bc8dec0
XR0 0.904 1.716 1. 0.978 0. 0. 0. 0. 0. 0. 0. 0.
TC2 522.8763 746.8273 -1184.4366 2433.9579 749.47067 0. 0. 0. 0. 0. 0. 0.
VC2 1.3961158 -9.7811738 27.574811 -32.654611 12.629944 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Hydrogen [HE/H2]
?Richardson, I.A., Blackham, T.M., Leachman, J.W., and Lemmon, E.W., in preparation, 2018.
3b8eed30/8d757b40
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
KWL 0.93145 0.735 0.78125 1.232 1.0 0. 0. 0. 0. 0. 0. 0.
TC5 9.6260634 63.22221 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.043521732 -0.16178703 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.04 -2.04 0. 0. -0.24 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Neon [HE/NE]
?E.W. Lemmon, NIST (2016)
?Huber (2017) Dilute gas viscosity fit to Kestin et al., J. Chem. Phys., 1972, 56, 5837 AAD 1%
3b8eed30/b912fce0
KW6 1.168 1.371 1.0097 0.899 -3.25 0. 0. 0. 0. 0. 0. 0.
TC6 66.263074 -86.414339 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 -0.028796916 -0.13863006 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.490 0.912 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Nitrogen [HE/N2]
?Kunz and Wagner (2007)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
3b8eed30/edbdc8e0
KW0 1.443274759254 1.47183158 1.031458392792 0.932629867 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN 0.01 -3.62 0. 0. -0.22 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Carbon monoxide [HE/CO]
?Kunz and Wagner (2007)
3b8eed30/091cb7e0
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN 0. 0. 0. 0. -0.15 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Argon [HE/AR]
?Kunz and Wagner (2007)
3b8eed30/ed016370
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.10 -2.85 0.73 -3.84 -0.21 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Oxygen [HE/O2]
?Kunz and Wagner (2007)
3b8eed30/edc36840
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.21 -0.30 -0.11 0.22 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Krypton [HE/KR]
?E.W. Lemmon, NIST (2017)
3b8eed30/d7c8c510
KW7 0.790 2.013 1.052 2.016 1.41 0. 0. 0. 0. 0. 0. 0.
TC6 93.711814 621.21927 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 -0.057796222 0.25772324 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Ethane [HE/C2]
?Kunz and Wagner (2007)
3b8eed30/434e2a40
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Carbon dioxide [HE/CO2]
?Kunz and Wagner (2007)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
3b8eed30/77c8bee0
KW0 1.301443406154 3.207456948 1.181129015264 0.864141549 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.03 -1.9 0. 0. -0.15 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Hydrogen sulfide [HE/H2S]
?Kunz and Wagner (2012)
3b8eed30/c6c03020
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Propane [HE/C3]
?Kunz and Wagner (2007)
3b8eed30/70c6aac0
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Isobutane [HE/C4I]
?Kunz and Wagner (2007)
3b8eed30/47ade7e0
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Butane [HE/C4]
?Kunz and Wagner (2007)
3b8eed30/7b3b4080
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Isopentane [HE/C5I]
?Kunz and Wagner (2007)
3b8eed30/86ee46a0
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Pentane [HE/C5]
?Kunz and Wagner (2007)
3b8eed30/76bc0290
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Hexane [HE/C6]
?Kunz and Wagner (2007)
3b8eed30/cb03ba40
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Heptane [HE/C7]
?Kunz and Wagner (2007)
3b8eed30/b398a3b0
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Water [HE/H2O]
?Kunz and Wagner (2007)
3b8eed30/b43a7600
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Octane [HE/C8]
?Kunz and Wagner (2007)
3b8eed30/f174a9b0
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Nonane [HE/C9]
?Kunz and Wagner (2012)
3b8eed30/7f94dc20
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Helium/Decane [HE/C10]
?Kunz and Wagner (2012)
3b8eed30/111888d0
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Parahydrogen/Orthohydrogen [PH2/OH2]
?ideal mixture
8d757b4a/8d757b4b
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -0.00066932776 0.00030452149 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 1.2268439e-06 7.4675821e-05 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Deuterium [H2/D2]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.87% from 150 bubble-point pressures
8d757b40/639b18a0
XR0 1.0087153 0.99511 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0.43594975 -0.81988847 -0.10252257 -0.84503691 0.57703816 -0.17357626 0. 0. 0. 0. 0. 0.
VC1 -0.0029824454 -0.0012893186 -0.010439783 0.031459786 -0.035038004 0.016263248 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Neon [H2/NE]
?T.M. Blackham and E.W. Lemmon, NIST (2016)
8d757b40/b912fce0
KW0 1.00705 0.7819 0.8285 1.2007 0.1617 0. 0. 0. 0. 0. 0. 0.
TC1 -3.5586395 -39.197727 -7.9951888 125.86282 -160.37683 67.357139 0. 0. 0. 0. 0. 0.
VC1 -0.059705897 0.23136946 -1.4027676 3.802705 -3.7645868 1.2182147 0. 0. 0. 0. 0. 0.
TRN -0.597 -0.521 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Nitrogen [H2/N2]
?Kunz and Wagner (2007)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
8d757b40/edbdc8e0
KW0 1.056932362449 1.175696583 1.028243731995 0.970115357 0. 0. 0. 0. 0. 0. 0. 0.
TC5 82.32723 142.90419 -257.22316 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.045388691 0.1993407 -0.85043649 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.648 0.310 0. 0. -0.18 0. 0. 0. 0. 0. 0. 0.
PR1 0.103 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Carbon monoxide [H2/CO]
?Kunz and Wagner (2007)
8d757b40/091cb7e0
KW0 1. 1.377504607 1. 1.121416201 0. 0. 0. 0. 0. 0. 0. 0.
TC5 75.919088 78.56909 -63.490127 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.028296776 0.049075053 -0.29083792 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -1.19 0.99 0. 0. -0.3 0. 0. 0. 0. 0. 0. 0.
PR1 0.0919 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Argon [H2/AR]
?Kunz and Wagner (2007)
8d757b40/ed016370
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 151.68281 58.790188 -342.72091 128.07591 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.015079669 -0.55518345 0.54421326 -1.0693979 0. 0. 0. 0. 0. 0. 0. 0.
TRN -1.04 0.819 0. 0. -0.23 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Oxygen [H2/O2]
?Kunz and Wagner (2007)
8d757b40/edc36840
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 172.27905 -90.788314 265.68194 -309.97889 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.0015078729 -0.61531173 1.0234489 -1.6997459 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.846 0.668 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Ethane [H2/C2]
?Kunz and Wagner (2007)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
8d757b40/434e2a40
KW0 1.071846019853 1.902008495 1.080652125274 1.10607204 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.517 0.704 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 -0.0667 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Carbon dioxide [H2/CO2]
?Kunz and Wagner (2007)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
8d757b40/77c8bee0
KW0 1.061210409483 1.782924792 1.106020762383 1.15279255 0. 0. 0. 0. 0. 0. 0. 0.
TC5 276.33352 98.105182 553.84635 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.079218106 0.64171394 -1.5972227 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.923 0.853 0. 0. -0.15 0. 0. 0. 0. 0. 0. 0.
PR1 -0.1622 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Hydrogen sulfide [H2/H2S]
?Kunz and Wagner (2012)
8d757b40/c6c03020
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Propane [H2/C3]
?Kunz and Wagner (2007)
8d757b40/70c6aac0
KW0 1. 2.308215191 1. 1.07400611 0. 0. 0. 0. 0. 0. 0. 0.
TC4 392.95504 159.83801 422.78891 184.6038 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.22407138 -1.3575447 2.3229117 -1.7771107 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.587 0.769 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 -0.0833 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Isobutane [H2/C4I]
?Kunz and Wagner (2007)
8d757b40/47ade7e0
KW0 1. 1.895305393 1. 1.147595688 0. 0. 0. 0. 0. 0. 0. 0.
TC6 654.2241 153.9533 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.20356098 -1.1420628 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Butane [H2/C4]
?Kunz and Wagner (2007)
8d757b40/7b3b4080
KW0 1. 2.509259945 1. 1.232939523 0. 0. 0. 0. 0. 0. 0. 0.
TC4 406.46881 568.15873 -538.60728 1645.8066 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.29252944 -1.3158554 2.1852007 -1.793986 0. 0. 0. 0. 0. 0. 0. 0.
PR1 -0.397 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Isopentane [H2/C5I]
?Kunz and Wagner (2007)
8d757b40/86ee46a0
KW0 1. 1.996386669 1. 1.184340443 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Pentane [H2/C5]
?Kunz and Wagner (2007)
8d757b40/76bc0290
KW0 1. 2.013859174 1. 1.188334783 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Hexane [H2/C6]
?Kunz and Wagner (2007)
8d757b40/cb03ba40
KW0 1. 3.021197546 1. 1.243461678 0. 0. 0. 0. 0. 0. 0. 0.
TC4 414.56784 1659.9246 -3593.5752 5132.6865 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.50376773 -1.6617495 2.1029854 -1.3990736 0. 0. 0. 0. 0. 0. 0. 0.
PR1 -0.03 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Heptane [H2/C7]
?Kunz and Wagner (2007)
8d757b40/b398a3b0
KW0 1. 3.169143057 1. 1.159131722 0. 0. 0. 0. 0. 0. 0. 0.
TC4 527.52253 1554.5424 -3433.351 5278.7597 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.77547721 -3.7472255 6.631606 -4.5149458 0. 0. 0. 0. 0. 0. 0. 0.
PR1 -0.1167 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Water [H2/H2O]
?Kunz and Wagner (2007)
8d757b40/b43a7600
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Octane [H2/C8]
?Kunz and Wagner (2007)
8d757b40/f174a9b0
KW0 1. 2.191555216 1. 1.305249405 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Nonane [H2/C9]
?Kunz and Wagner (2012)
8d757b40/7f94dc20
KW0 1. 2.23435404 1. 1.342647661 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Decane [H2/C10]
?Kunz and Wagner (2012)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
8d757b40/111888d0
KW0 0.939127547072 3.786003724 0.589845787544 1.120233729 0. 0. 0. 0. 0. 0. 0. 0.
TC2 975.6797 -2812.5934 21226.451 -44175.4 31892.779 0. 0. 0. 0. 0. 0. 0.
VC2 1.9573238 -11.442356 25.994648 -32.377492 17.409408 0. 0. 0. 0. 0. 0. 0.
!
?Deuterium/Neon [D2/NE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.22% from 78 bubble-point pressures
639b18a0/b912fce0
XR0 0.98882 0.83393 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -7.4496076 -15.746878 -2.8836103 15.933243 16.071726 -17.399345 0. 0. 0. 0. 0. 0.
VC1 -0.030872895 0.099042496 -0.61064314 2.053454 -2.6346688 1.126848 0. 0. 0. 0. 0. 0.
!
?Deuterium/Nitrogen [D2/N2]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.43% from 7 bubble-point pressures
639b18a0/edbdc8e0
XR0 1.015610027687 1.22898 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC6 87.358513 9.9631415 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.0052835267 -0.18465217 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Neon/Nitrogen [NE/N2]
?E.W. Lemmon, NIST (2016)
b912fce0/edbdc8e0
KW6 1.025641025641 1.148 0.915750915751 0.988 1.7 0. 0. 0. 0. 0. 0. 0.
TC4 68.872082 -226.46158 1236.6301 -1406.6155 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.050052697 0.38823513 -1.049847 0.47919706 0. 0. 0. 0. 0. 0. 0. 0.
!
?Neon/Argon [NE/AR]
?I. Cullimore and E.W. Lemmon, NIST (2010)
b912fce0/ed016370
XR0 1.004 1.0994 1. 1.051 0. 0. 0. 0. 0. 0. 0. 0.
TC5 106.87301 123.06812 -237.65551 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 0.0023132717 -0.11063645 -0.13234369 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Neon/Oxygen [NE/O2]
?E.W. Lemmon, NIST (2002)
b912fce0/edc36840
XR0 1. 1.1554168 1. 1.0260610 0. 0. 0. 0. 0. 0. 0. 0.
TC4 145.19391 -324.69591 1425.4339 -1819.6391 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.0053608063 -0.29716916 0.65120388 -0.8388041 0. 0. 0. 0. 0. 0. 0. 0.
!
?Neon/Krypton [NE/KR]
?I. Cullimore and E.W. Lemmon, NIST (2010)
b912fce0/d7c8c510
XR0 1.02385 1.1957 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 228.76603 -213.30985 1381.4554 -1752.0482 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.060222157 -0.73986324 1.8448565 -2.0874123 0. 0. 0. 0. 0. 0. 0. 0.
!
?Neon/Xenon [NE/XE]
?E.W. Lemmon, NIST (2017)
b912fce0/71fd7fa0
KW0 1. 1.283 0.894 1.213 1. 0. 0. 0. 0. 0. 0. 0.
TC6 284.17179 290.17676 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 -0.043924482 -0.11642056 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.07218 -0.44937 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Carbon monoxide [N2/CO]
?J. Gernert and R. Span, J. Chem. Thermodyn., 93:274-293, 2016. DOI:10.1016/j.jct.2015.05.015
edbdc8e0/091cb7e0
GG0 1. 0.993425388 1. 1.008690943 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1.002409 0.9941 1. 1.001317 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -0.35923679 -0.92421566 -0.60879081 0.082295098 -0.17026141 0.1046605 0. 0. 0. 0. 0. 0.
VC1 -0.0010980197 0.0022188761 -0.0029926803 0.0070973839 -0.0078890781 0.0041536766 0. 0. 0. 0. 0. 0.
PR1 0.0307 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Argon [N2/AR]
?J. Gernert and R. Span, J. Chem. Thermodyn., 93:274-293, 2016. DOI:10.1016/j.jct.2015.05.015
edbdc8e0/ed016370
GG0 0.999069843 0.990034831 1.004166412 1.002212182 0. 0. 0. 0. 0. 0. 0. 0.
XR0 0.999442 0.989311 1.006697 1.001549 0. 0. 0. 0. 0. 0. 0. 0.
TC1 1.313096 -5.8612607 12.758033 -18.233466 13.511914 -3.7454367 0. 0. 0. 0. 0. 0.
VC1 -0.0042457596 -0.015126646 0.065240314 -0.17809237 0.22184594 -0.10402674 0. 0. 0. 0. 0. 0.
PR1 -0.0026 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
ST1 0.015 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Oxygen [N2/O2]
?Kunz and Wagner (2007)
edbdc8e0/edc36840
KW0 0.997190589 0.995157044 0.99952177 0.997082328 0. 0. 0. 0. 0. 0. 0. 0.
TC1 2.4442564 -1.3286105 -2.1788958 15.020532 -20.000629 10.535041 0. 0. 0. 0. 0. 0.
VC1 -0.021747863 0.054592723 -0.12438063 0.12481413 -0.033799775 -0.017312933 0. 0. 0. 0. 0. 0.
PR1 -0.0119 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
ST1 0.04 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/R14 [N2/R14]
?E.W. Lemmon, NIST (2014)
edbdc8e0/dba9f950
XR0 1. 1.0674 1. 1.1693 0. 0. 0. 0. 0. 0. 0. 0.
TC1 55.871913 141.95982 -718.33749 2055.6423 -2570.5049 1187.9357 0. 0. 0. 0. 0. 0.
VC1 0.036731782 -0.36479889 1.661734 -4.3269079 5.1825309 -2.4295266 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Ethylene [N2/ETY]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
edbdc8e0/9c1062b0
KW0 1. 1.036 1. 1.058 0.269 0. 0. 0. 0. 0. 0. 0.
TC1 123.13655 332.51475 -3690.8203 13853.204 -21425.658 11095.382 0. 0. 0. 0. 0. 0.
VC1 0.046894795 -1.0449218 3.7615419 -6.9521902 5.3661902 -1.6030395 0. 0. 0. 0. 0. 0.
PR1 0.0856 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Ethane [N2/C2]
?Kunz and Wagner (2007)
edbdc8e0/434e2a40
KW6 1.007671428 1.098650964 0.978880168 1.042352891 1. 0. 0. 0. 0. 0. 0. 0.
TC1 46.753902 1538.7508 -10441.445 31701.316 -41920.358 19316.82 0. 0. 0. 0. 0. 0.
VC1 0.020555887 -0.65178605 2.4510046 -5.3840033 5.3009674 -2.4226674 0. 0. 0. 0. 0. 0.
PR1 0.0515 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/R13 [N2/R13]
?E.W. Lemmon, NIST (2014)
edbdc8e0/126c90a0
XR0 1. 1.181 1. 1.1727 0. 0. 0. 0. 0. 0. 0. 0.
TC2 109.50638 580.7692 -2483.8622 5201.357 -3582.2213 0. 0. 0. 0. 0. 0. 0.
VC2 0.059019468 0.19591652 -2.5783577 5.620114 -4.0932849 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Carbon dioxide [N2/CO2]
?Kunz and Wagner (2007)
edbdc8e0/77c8bee0
KW5 1.005894529 1.107654104 0.977794634 1.047578256 1. 0. 0. 0. 0. 0. 0. 0.
TC4 78.848836 215.44623 -559.77793 399.92995 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.056437426 -0.10467104 0.29646798 -0.84831941 0. 0. 0. 0. 0. 0. 0. 0.
PR1 -0.017 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Hydrogen sulfide [N2/H2S]
?Kunz and Wagner (2012)
edbdc8e0/c6c03020
KW0 1.004692366 0.9601742 0.910394249 1.256844157 0. 0. 0. 0. 0. 0. 0. 0.
TC5 230.82965 -24.587558 -388.65482 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.015675072 -0.35184311 -0.076494902 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.1767 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Propylene [N2/PRY]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
edbdc8e0/56d778b0
XR0 0.99 1.197 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 292.28749 -259.65318 944.16194 -262.48473 -1140.3651 0. 0. 0. 0. 0. 0. 0.
VC2 0.14199185 -1.2616818 2.2647414 -1.4883113 -0.51801042 0. 0. 0. 0. 0. 0. 0.
PR1 0.09 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Propane [N2/C3]
?Kunz and Wagner (2007)
edbdc8e0/70c6aac0
KW0 1.002677329 1.201264026 0.974424681 1.081025408 0. 0. 0. 0. 0. 0. 0. 0.
TC4 297.73689 -344.9873 1541.6292 -1587.1917 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.17296819 -1.4716172 3.0696306 -2.6745622 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0852 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/R22 [N2/R22]
?E.W. Lemmon, NIST (2002)
edbdc8e0/57716470
XR0 1. 1.2360548 1. 1.0311034 0. 0. 0. 0. 0. 0. 0. 0.
TC4 284.3887 -237.05542 1259.3952 -1346.4634 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.14152943 -1.3029039 2.9276246 -2.7904489 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Ammonia [N2/NH3]
?I. Cullimore and E.W. Lemmon, NIST (2010)
edbdc8e0/e9847540
KW0 1. 0.9745 1. 1.1249 1.6257 0. 0. 0. 0. 0. 0. 0.
TC5 224.9718 393.02863 -612.15336 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.14293165 0.31391839 -1.0856128 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.2193 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/R12 [N2/R12]
?E.W. Lemmon, NIST (2002)
edbdc8e0/98829b70
XR0 1. 1.2981559 1. 1.0625855 0. 0. 0. 0. 0. 0. 0. 0.
TC4 319.32278 -547.82261 2267.1716 -1926.5956 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.12009744 -0.91082668 1.9956286 -2.010985 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0107 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Dimethyl ether [N2/DME]
?I. Cullimore and E.W. Lemmon, NIST (2010)
edbdc8e0/8f27e300
KW0 1. 1.1633 1. 0.9861 1.1162 0. 0. 0. 0. 0. 0. 0.
TC5 257.01923 356.35329 -530.13115 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.069173113 -0.16792919 -0.2933627 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/R13I1 [N2/CF3I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.28% from 24 bubble-point pressures
edbdc8e0/d26ca240
XR0 0.9987715 1.30226 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 371.82336 -591.9198 2642.7983 -2435.7889 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.34532032 -2.2032049 4.3345708 -3.4455642 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/R227ea [N2/R227EA]
?E.W. Lemmon, NIST (2002)
edbdc8e0/40091ee0
XR0 1. 1.3734074 1. 1.1099760 0. 0. 0. 0. 0. 0. 0. 0.
TC4 292.00657 -212.01269 1428.6605 -1034.3071 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.11941869 -0.46241989 0.53614685 -0.84575045 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Isobutane [N2/C4I]
?Kunz and Wagner (2007)
edbdc8e0/47ade7e0
KW0 0.99286813 1.284462634 0.98641583 1.100576129 0. 0. 0. 0. 0. 0. 0. 0.
TC4 356.6576 -322.4834 1575.6601 -1303.5876 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.23539973 -1.7548261 3.4901651 -2.8420393 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.1033 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Sulfur dioxide [N2/SO2]
?T. Neumann, Development of New Helmholtz Models for Binary Mixtures Relevant for CCS; Master's thesis, Lehrstuhl Fuer Thermodynamik, Ruhr Universitaet, Bochum, Germany, 2017.
edbdc8e0/7fad4b80
XR0 0.956138119888 1.1946588 1.106654368048 1.2155808 0. 0. 0. 0. 0. 0. 0. 0.
TC5 256.95476 429.22663 -735.197 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.073582742 0.58298005 -2.0328828 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Butane [N2/C4]
?Kunz and Wagner (2007)
edbdc8e0/7b3b4080
KW0 0.994515234 1.304886838 0.99608261 1.146949309 0. 0. 0. 0. 0. 0. 0. 0.
TC4 347.33839 -211.38579 1509.597 -1224.681 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.25655412 -1.7871882 3.7135042 -3.1819971 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.08 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Isopentane [N2/C5I]
?Kunz and Wagner (2007)
edbdc8e0/86ee46a0
KW0 1. 1.38177077 1. 1.154135439 0. 0. 0. 0. 0. 0. 0. 0.
TC5 383.8575 158.9649 458.49554 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 0.23694131 -0.7548795 0.18636293 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0922 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Pentane [N2/C5]
?Kunz and Wagner (2007)
edbdc8e0/76bc0290
KW0 1. 1.419029041 1. 1.078877166 0. 0. 0. 0. 0. 0. 0. 0.
TC4 429.24691 -73.621625 1308.778 -754.2016 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.42928765 -2.5806949 5.170065 -4.2025733 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Novec649 [N2/N649]
?E.W. Lemmon, NIST (2011)
edbdc8e0/a9e22c00
KW8 0.980392156863 1.608 0.707714083510 1.9 0.65 0. 0. 0. 0. 0. 0. 0.
TC5 1145.4933 -4318.0106 5807.1895 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 1.056782 -4.3279726 3.727205 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Cyclopentane [N2/CC5]
?I. Cullimore and E.W. Lemmon, NIST (2010)
edbdc8e0/43ab1810
KW0 0.9474 1.3697 0.8725 1.2294 2.2557 0. 0. 0. 0. 0. 0. 0.
TC5 472.06608 -912.1598 1810.8518 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.44973041 0.9508422 -0.88239563 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Methanol [N2/MEO]
?E.W. Lemmon, NIST (2015)
edbdc8e0/c41aa690
XR0 0.998 1.5293 0.534 1.529 0. 0. 0. 0. 0. 0. 0. 0.
TC6 674.06777 -367.06551 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.41531344 -1.9874228 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Hexane [N2/C6]
?Kunz and Wagner (2007)
edbdc8e0/cb03ba40
KW0 1. 1.472607971 1. 1.195952177 0. 0. 0. 0. 0. 0. 0. 0.
TC4 447.3985 120.12079 750.18606 173.22173 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.47224205 -2.3488581 4.1591926 -3.3060733 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.1496 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Ethanol [N2/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
edbdc8e0/3d5f67e0
KW0 0.927 1.666 1. 1. 0.778 0. 0. 0. 0. 0. 0. 0.
TC4 482.47939 -45.864424 955.04627 -1396.9459 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.28509172 -2.2248859 3.6913596 -2.5385 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Benzene [N2/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
edbdc8e0/f2cfb460
KW0 1. 1.435 1. 1. 0.257 0. 0. 0. 0. 0. 0. 0.
TC4 539.32269 182.82052 1018.9556 -800.22757 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.37154867 -2.4359013 4.6523333 -3.8181658 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.1641 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Cyclohexane [N2/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
edbdc8e0/6e225350
KW0 1. 1.442 1. 1.0177 0.735 0. 0. 0. 0. 0. 0. 0.
TC4 496.81812 -133.49556 1471.6785 -866.34816 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.31242852 -2.9527715 6.058237 -4.6374991 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Heptane [N2/C7]
?Kunz and Wagner (2007)
edbdc8e0/b398a3b0
KW0 1. 1.520975334 1. 1.40455409 0. 0. 0. 0. 0. 0. 0. 0.
TC4 494.49609 380.53454 -720.71638 2310.8826 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.71351455 -4.1181406 8.8217789 -6.9387669 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.1441 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Isooctane [N2/C8I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.32% from 39 bubble-point pressures
edbdc8e0/c2dd9ef0
XR0 0.9911294 1.55448 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 547.46128 -13.404836 1870.9427 -991.20624 0. 0. 0. 0. 0. 0. 0. 0.
VC4 1.0685019 -5.6320286 9.7137741 -6.4358794 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Water [N2/H2O]
?J. Gernert and R. Span, J. Chem. Thermodyn., 93:274-293, 2016. DOI:10.1016/j.jct.2015.05.015
edbdc8e0/b43a7600
GG0 1. 0.968808467 1. 1.094749685 0. 0. 0. 0. 0. 0. 0. 0.
KWD 1.048054 0.805147 0.926245 0.733443 1. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Methylcyclohexane [N2/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
edbdc8e0/0429edd0
XR0 0.991 1.542 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC3 426.47745 808.54158 156.88667 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC3 0.4822434 -1.2933271 0.25315228 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Toluene [N2/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
edbdc8e0/a49b8b50
XR0 1. 1.524 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 646.77584 4.6699993 1719.8515 -1246.5943 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.47746995 -2.9167857 5.5244454 -4.4129736 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Octane [N2/C8]
?Kunz and Wagner (2007)
edbdc8e0/f174a9b0
KW0 1. 1.733280051 1. 1.186067025 0. 0. 0. 0. 0. 0. 0. 0.
TC4 620.35179 -572.95531 2389.4842 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.547952 -1.2485215 0.32116 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 -0.41 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/p-Xylene [N2/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.99% from 265 bubble-point pressures
edbdc8e0/01b0e650
XR0 0.99471 1.63462 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 680.38497 -100.46563 1692.9973 -595.20939 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.79886547 -4.6084709 8.6705369 -6.3363916 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Nonane [N2/C9]
?Kunz and Wagner (2012)
edbdc8e0/7f94dc20
KW0 0.95637945 1.749119996 1. 1.100405929 0. 0. 0. 0. 0. 0. 0. 0.
TC2 528.55505 1202.2818 -2522.2161 5064.3659 -1859.2599 0. 0. 0. 0. 0. 0. 0.
VC2 1.0859716 -5.2049539 9.4831174 -7.9452837 1.5842443 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Propylcyclohexane [N2/C3CC6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.34% from 31 bubble-point pressures
edbdc8e0/206f01b0
XR0 0.9880837 1.69332 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 504.37184 1287.585 -1703.4249 3871.2387 -1941.8768 0. 0. 0. 0. 0. 0. 0.
VC2 0.49393184 1.3359147 -13.752399 24.999804 -14.908958 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Decane [N2/C10]
?Kunz and Wagner (2012)
edbdc8e0/111888d0
KW0 0.957934447 1.822157123 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 635.1066 948.2692 -1088.6368 2911.4457 -822.15024 0. 0. 0. 0. 0. 0. 0.
VC2 1.3752234 -7.2033101 14.666022 -14.913058 5.2526756 0. 0. 0. 0. 0. 0. 0.
PR1 0.1122 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrogen/Dodecane [N2/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
edbdc8e0/8bc8dec0
KW0 0.927 1.949 1. 1. 0.898 0. 0. 0. 0. 0. 0. 0.
TC2 585.66576 674.80273 -1265.8096 4130.4541 -338.15763 0. 0. 0. 0. 0. 0. 0.
VC2 1.1756505 -12.142183 46.47288 -67.589583 31.656424 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Argon [CO/AR]
?Kunz and Wagner (2007)
091cb7e0/ed016370
KW0 1. 0.954215746 1. 1.159720623 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -11.401124 0.12893995 -2.691392 -0.15584403 1.2189825 -0.1648905 0. 0. 0. 0. 0. 0.
VC1 0.0066726018 0.078100234 -0.24960426 0.42775855 -0.3429319 0.1072869 0. 0. 0. 0. 0. 0.
TRN 0. 0. 0. 0. -0.05 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Oxygen [CO/O2]
?Mixing rules of nitrogen/carbon monoxide used as an estimate.
091cb7e0/edc36840
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 0.993425388 1. 1.008690943 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -0.21116315 -0.82575781 0.9841548 -1.4386256 1.0768365 -0.32914467 0. 0. 0. 0. 0. 0.
VC1 -0.013065151 0.018012506 -0.036718091 0.032549206 -0.016347285 0.00033465408 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Ethylene [CO/ETY]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.88% from 83 bubble-point pressures
091cb7e0/9c1062b0
XR0 0.964889969737 1.09111 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 135.95886 6.1604161 -578.54718 1985.1802 -2618.1142 1267.6958 0. 0. 0. 0. 0. 0.
VC1 0.10531159 -1.8131531 8.3974908 -20.034399 23.000447 -10.253933 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Ethane [CO/C2]
?Kunz and Wagner (2007)
091cb7e0/434e2a40
KW0 1. 1.069224728 1. 1.201417898 0. 0. 0. 0. 0. 0. 0. 0.
TC1 84.392932 1192.9057 -8314.753 24546.493 -31468.664 14243.483 0. 0. 0. 0. 0. 0.
VC1 0.098959644 -1.2356392 4.9328768 -10.440397 10.400055 -4.3141832 0. 0. 0. 0. 0. 0.
PR1 -0.0226 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Carbon dioxide [CO/CO2]
?L. Souza and S. Herrig (2018)
?#This new mixture model (BCC) replaces the one (KW0) of J. Gernert and R. Span, J. Chem. Thermodyn., 93:274-293, 2016. DOI:10.1016/j.jct.2015.05.015.
?#Refprop will by default read and use the last line for the interaction parameters, which is KWZ.
091cb7e0/77c8bee0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
KW0 0.993245 1.068392 1.030855 1.245499 0. 0. 0. 0. 0. 0. 0. 0.
BCC 1.010323485374 1.1621298 0.967303497373 1.0001623 1. 0. 0. 0. 0. 0. 0. 0.
TC1 133.089 480.4 -2152.1 1634.0 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0.0333 -0.8354 1.7938 -3.0014 1.5712 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Hydrogen sulfide [CO/H2S]
?Kunz and Wagner (2012)
091cb7e0/c6c03020
KW0 1.025536736 1.022749748 0.795660392 1.101731308 0. 0. 0. 0. 0. 0. 0. 0.
TC5 478.76002 -1646.2673 1821.6838 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.0155601 -0.51551155 0.30918297 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0544 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Propylene [CO/PRY]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from nitrogen and argon)
091cb7e0/56d778b0
XR0 1. 1.184 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 290.94714 -508.44569 2289.4857 -2899.5592 613.31183 0. 0. 0. 0. 0. 0. 0.
VC2 0.13007962 -1.1022488 1.8104033 -0.92961723 -0.82372952 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Propane [CO/C3]
?Kunz and Wagner (2007)
091cb7e0/70c6aac0
KW0 1. 1.197564208 1. 1.108143673 0. 0. 0. 0. 0. 0. 0. 0.
TC5 169.73679 550.71798 -605.32902 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 0.00069732785 0.077267724 -0.61023464 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0259 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Isobutane [CO/C4I]
?Kunz and Wagner (2007)
091cb7e0/47ade7e0
KW0 1. 1.161390082 1. 1.087272232 0. 0. 0. 0. 0. 0. 0. 0.
TC6 360.61857 70.275278 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.11898981 -0.68542074 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Sulfur dioxide [CO/SO2]
?T. Neumann, Development of New Helmholtz Models for Binary Mixtures Relevant for CCS; Master's thesis, Lehrstuhl Fuer Thermodynamik, Ruhr Universitaet, Bochum, Germany, 2017.
091cb7e0/7fad4b80
XR0 1. 1.177903242 1. 1.00724143 0. 0. 0. 0. 0. 0. 0. 0.
TC6 380.00814 -108.72892 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.032653889 -0.51698921 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Butene [CO/1BE]
?I. Cullimore and E.W. Lemmon, NIST (2010)
091cb7e0/cd7a06d0
XR0 1. 1.3077 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 415.52219 -1035.4373 4109.4203 -3793.0282 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.27007889 -1.9253262 3.891367 -3.239322 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Butane [CO/C4]
?Kunz and Wagner (2007)
091cb7e0/7b3b4080
KW0 1. 1.173916162 1. 1.084740904 0. 0. 0. 0. 0. 0. 0. 0.
TC6 409.53691 20.63681 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.17420286 -0.84537416 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Isopentane [CO/C5I]
?Kunz and Wagner (2007)
091cb7e0/86ee46a0
KW0 1. 1.199326059 1. 1.116694577 0. 0. 0. 0. 0. 0. 0. 0.
TC6 474.46304 147.62057 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.26337149 -1.08041 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Pentane [CO/C5]
?Kunz and Wagner (2007)
091cb7e0/76bc0290
KW0 1. 1.206043295 1. 1.119954454 0. 0. 0. 0. 0. 0. 0. 0.
TC6 526.93714 63.464868 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.29222981 -1.2041815 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Hexane [CO/C6]
?Kunz and Wagner (2007)
091cb7e0/cb03ba40
KW0 1. 1.233272781 1. 1.155145836 0. 0. 0. 0. 0. 0. 0. 0.
TC6 573.64265 242.15416 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.43281574 -1.7109755 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Ethanol [CO/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
091cb7e0/3d5f67e0
XR0 1. 1.56 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC6 501.42397 249.37562 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.29906836 -1.1071069 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Benzene [CO/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
091cb7e0/f2cfb460
XR0 1. 1.435 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 541.77893 63.195681 1487.1892 -1466.2962 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.40459236 -2.4973872 4.5264075 -3.5368144 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Cyclohexane [CO/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
091cb7e0/6e225350
XR0 0.9917 1.4608 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 506.72574 155.37847 647.58571 -467.72925 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.55328886 -3.7649489 6.8280166 -4.7045335 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Heptane [CO/C7]
?Kunz and Wagner (2007)
091cb7e0/b398a3b0
KW0 1. 1.256123503 1. 1.190354273 0. 0. 0. 0. 0. 0. 0. 0.
TC5 703.12631 96.419031 344.09763 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 0.78393703 -4.3021072 3.8471464 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Water [CO/H2O]
?J. Gernert and R. Span, J. Chem. Thermodyn., 93:274-293, 2016. DOI:10.1016/j.jct.2015.05.015
091cb7e0/b43a7600
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
KWD 0.95609 0.823984 0.940426 0.766756 0.9897 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Toluene [CO/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from nitrogen and oxygen)
091cb7e0/a49b8b50
XR0 1. 1.499 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 670.32029 -452.4779 3217.0193 -2821.6074 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.46711616 -2.8588848 5.3418814 -4.240314 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Octane [CO/C8]
?Kunz and Wagner (2007)
091cb7e0/f174a9b0
KW0 1. 1.276565536 1. 1.219206702 0. 0. 0. 0. 0. 0. 0. 0.
TC5 674.57911 876.30937 -665.5371 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 0.71616575 -3.5656941 2.0677547 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/p-Xylene [CO/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.19% from 30 bubble-point pressures
091cb7e0/01b0e650
XR0 0.981810006018 1.62153 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 664.14305 -28.089455 1283.3088 -293.56223 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.79350638 -4.672599 8.8096433 -6.3641839 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/m-Xylene [CO/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.78% from 49 bubble-point pressures
091cb7e0/0f99ff70
XR0 0.984390035020 1.5975 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 689.72142 -405.03593 2548.9699 -1485.3722 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.63267435 -3.5959375 6.8364306 -5.304559 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Nonane [CO/C9]
?Kunz and Wagner (2012)
091cb7e0/7f94dc20
KW0 1. 1.294070556 1. 1.252151449 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Decane [CO/C10]
?Kunz and Wagner (2012)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
091cb7e0/111888d0
KW0 0.952748775110 1.803567587 1. 0.87018496 0. 0. 0. 0. 0. 0. 0. 0.
TC2 589.96688 1780.5965 -5000.6972 10254.567 -5805.4943 0. 0. 0. 0. 0. 0. 0.
VC2 1.4293761 -7.7150469 14.97211 -13.822042 4.0749286 0. 0. 0. 0. 0. 0. 0.
!
?Carbon monoxide/Dodecane [CO/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
091cb7e0/8bc8dec0
XR0 0.933 1.941 1. 0.87 0. 0. 0. 0. 0. 0. 0. 0.
TC2 639.03913 695.4566 -321.19564 2176.8745 58.559559 0. 0. 0. 0. 0. 0. 0.
VC2 1.5635821 -9.8153896 27.601019 -36.798592 16.939969 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Oxygen [AR/O2]
?J. Gernert and R. Span, J. Chem. Thermodyn., 93:274-293, 2016. DOI:10.1016/j.jct.2015.05.015
ed016370/edc36840
GG0 0.999976897534 0.990430423 1.000253217103 0.993907223 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1.000961924409 0.988822 0.993540002901 1.001341 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -2.6853083 -1.5077593 0.72170393 -0.70533935 0.70746719 -0.26216748 0. 0. 0. 0. 0. 0.
VC1 -0.0011216077 0.003445881 0.00011008219 0.0032042113 -0.0041476441 0.0013354076 0. 0. 0. 0. 0. 0.
PR1 0.0104 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Krypton [AR/KR]
?E.W. Lemmon, NIST (2002)
ed016370/d7c8c510
XR0 1. 1.0025306 1. 1.0037297 0. 0. 0. 0. 0. 0. 0. 0.
TC1 22.887153 13.340547 -97.947494 270.15416 -333.64333 157.94135 0. 0. 0. 0. 0. 0.
VC1 -0.010287396 -0.0068909099 -0.054312832 0.16954011 -0.22658033 0.10494375 0. 0. 0. 0. 0. 0.
!
?Argon/Ethane [AR/C2]
?Mixing rules of nitrogen/ethane used as an estimate.
ed016370/434e2a40
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
KW6 1.007671428 1.098650964 0.978880168 1.042352891 1. 0. 0. 0. 0. 0. 0. 0.
TC1 71.506608 242.01906 -1256.9336 4408.7148 -6219.1352 2960.0578 0. 0. 0. 0. 0. 0.
VC1 0.075392482 -0.57498334 2.8173713 -7.5008829 8.5085377 -3.6129785 0. 0. 0. 0. 0. 0.
!
?Argon/Carbon dioxide [AR/CO2]
?T. Neumann, Lehrstuhl Fuer Thermodynamik, Ruhr Universitaet, Bochum, Germany, 2017.
?#This new mixture model (KWN) replaces the one (KWC) of J. Gernert and R. Span, J. Chem. Thermodyn., 93:274-293, 2016. DOI:10.1016/j.jct.2015.05.015.
ed016370/77c8bee0
GG0 1.003499339677 1.050971635 0.991677418665 1.029205465 0. 0. 0. 0. 0. 0. 0. 0.
KWC 1.027147 0.968781 1.001378 1.02971 1. 0. 0. 0. 0. 0. 0. 0.
KWN 1.001296679200 1.0396748 0.996248228795 1.0138330 1. 0. 0. 0. 0. 0. 0. 0.
TC2 88.297068 -89.798322 1037.5025 -3216.2793 2393.0292 0. 0. 0. 0. 0. 0. 0.
VC2 0.032556386 -0.57062399 1.9074597 -4.0303175 2.5528503 0. 0. 0. 0. 0. 0. 0.
TRN 0.25755 -2.23753 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Hydrogen sulfide [AR/H2S]
?Mixing rules of nitrogen/Hydrogen sulfide used as an estimate.
ed016370/c6c03020
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1.004692366 0.9601742 0.910394249 1.256844157 0. 0. 0. 0. 0. 0. 0. 0.
TC4 186.55901 154.84185 -1050.248 844.67509 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.018859401 -0.57539223 0.9155803 -0.61664562 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Propylene [AR/PRY]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
ed016370/56d778b0
XR0 1. 1.158 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 182.56246 1056.0377 -6512.5168 18223.817 -21583.881 8659.4771 0. 0. 0. 0. 0. 0.
VC1 0.20292535 -2.189211 8.9814186 -20.495515 23.047984 -10.387503 0. 0. 0. 0. 0. 0.
!
?Argon/Propane [AR/C3]
?Mixing rules of nitrogen/propane used as an estimate.
ed016370/70c6aac0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1.002677329 1.201264026 0.974424681 1.081025408 0. 0. 0. 0. 0. 0. 0. 0.
TC1 185.93764 814.51898 -4338.8397 10921.895 -10841.941 3267.6634 0. 0. 0. 0. 0. 0.
VC1 0.25668304 -2.7952662 12.390479 -28.667577 32.024714 -14.044235 0. 0. 0. 0. 0. 0.
!
?Argon/R22 [AR/R22]
?E.W. Lemmon, NIST (2002)
ed016370/57716470
XR0 1. 1.1883347 1. 1.0519798 0. 0. 0. 0. 0. 0. 0. 0.
TC1 175.69418 1205.9405 -7650.0831 22059.786 -26928.054 11228.023 0. 0. 0. 0. 0. 0.
VC1 0.20080798 -2.1913878 9.1747378 -20.798516 23.267264 -10.620401 0. 0. 0. 0. 0. 0.
!
?Argon/Ammonia [AR/NH3]
?T. Neumann (2018), unpublished (BAA)
?Older XR0 model: I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.14% from 65 bubble-point pressures
?TRN fit 9/17 to J. Chem. Phys., 1964, 40, 2988-95, Trans. Faraday Soc., 1965, 61, 2422 AAD 1.4%
ed016370/e9847540
XR0 0.9662022 1.06504 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
BAA 1.146326 0.998353 0.756526 1.041113 1. 0. 0. 0. 0. 0. 0. 0.
TC5 257.71367 -25.457127 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.0086170038 -0.23414391 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
TRN -0.52 0.92 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Isobutane [AR/C4I]
?Mixing rules of nitrogen/isobutane used as an estimate.
ed016370/47ade7e0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 0.99286813 1.284462634 0.98641583 1.100576129 0. 0. 0. 0. 0. 0. 0. 0.
TC2 232.74193 807.43185 -3429.4245 7360.9374 -4810.2884 0. 0. 0. 0. 0. 0. 0.
VC2 0.23304459 -1.4853187 3.1502917 -2.8237156 0.37557143 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Butane [AR/C4]
?Kunz and Wagner (2007)
ed016370/7b3b4080
KW0 1. 1.245039498 1. 1.214638734 0. 0. 0. 0. 0. 0. 0. 0.
TC4 306.9044 -228.72292 1454.9321 -1096.9136 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.23694893 -1.3652016 2.705699 -2.2328633 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Neopentane [AR/C5A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.33% from 30 bubble-point pressures
ed016370/5a410790
XR0 1.000190036107 1.28707 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 301.15112 728.1911 -2911.3133 6918.1677 -4973.0106 0. 0. 0. 0. 0. 0. 0.
VC2 0.56141973 -3.8633168 9.7909886 -11.34681 4.3116427 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Isopentane [AR/C5I]
?Mixing rules of nitrogen/isopentane used as an estimate.
ed016370/86ee46a0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.38177077 1. 1.154135439 0. 0. 0. 0. 0. 0. 0. 0.
TC4 367.83429 -171.44058 1350.6631 -583.78117 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.38901326 -2.039574 4.0320775 -3.1133551 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Pentane [AR/C5]
?Mixing rules of nitrogen/pentane used as an estimate.
ed016370/76bc0290
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.419029041 1. 1.078877166 0. 0. 0. 0. 0. 0. 0. 0.
TC4 375.33749 -77.207938 1297.8555 -550.49263 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.37119079 -1.8559021 3.4954978 -2.7449677 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Cyclopentane [AR/CC5]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3% from 25 bubble-point pressures
ed016370/43ab1810
XR0 0.979799954243 1.36013 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 495.46266 -634.10531 3130.423 -2624.7491 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.22282846 -1.5350229 2.8246955 -2.180464 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Methanol [AR/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
ed016370/c41aa690
XR0 1. 1.436 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC6 487.6183 330.31807 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.33831397 -1.1080881 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Hexane [AR/C6]
?Mixing rules of nitrogen/hexane used as an estimate.
ed016370/cb03ba40
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.472607971 1. 1.195952177 0. 0. 0. 0. 0. 0. 0. 0.
TC2 364.4596 422.3785 -313.09173 1735.4377 -704.03962 0. 0. 0. 0. 0. 0. 0.
VC2 0.35238442 -1.0995632 1.3491342 -0.82725042 -0.42108404 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Ethanol [AR/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
ed016370/3d5f67e0
XR0 1. 1.492 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC6 475.62442 298.55193 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.30291703 -1.0043125 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Benzene [AR/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
ed016370/f2cfb460
XR0 1.01 1.397 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 514.64607 -36.404414 1933.8601 -1689.3714 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.36916779 -1.9395215 3.1566758 -2.3592405 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Heptane [AR/C7]
?Mixing rules of nitrogen/heptane used as an estimate.
ed016370/b398a3b0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.520975334 1. 1.40455409 0. 0. 0. 0. 0. 0. 0. 0.
TC4 416.70705 486.07025 -645.59642 1907.1459 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.59273531 -2.6884561 5.3084674 -4.0552043 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Water [AR/H2O]
?J. Gernert and R. Span, J. Chem. Thermodyn., 93:274-293, 2016. DOI:10.1016/j.jct.2015.05.015
ed016370/b43a7600
GG0 1. 1.070941866 1. 1.038993495 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1.472528508152 0.921 1.063379547808 1.050952 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Toluene [AR/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from oxygen)
ed016370/a49b8b50
XR0 1. 1.45 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 601.26027 29.707349 1585.4131 -1067.3236 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.4439868 -2.4992096 4.4522823 -3.3689233 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Octane [AR/C8]
?Mixing rules of nitrogen/octane used as an estimate.
ed016370/f174a9b0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.733280051 1. 1.186067025 0. 0. 0. 0. 0. 0. 0. 0.
TC2 394.68971 859.77162 -888.92511 2189.8849 252.11776 0. 0. 0. 0. 0. 0. 0.
VC2 0.72231322 -2.3626308 3.6322806 -2.6921697 -0.12821722 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Nonane [AR/C9]
?Mixing rules of nitrogen/nonane used as an estimate.
ed016370/7f94dc20
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 0.95637945 1.749119996 1. 1.100405929 0. 0. 0. 0. 0. 0. 0. 0.
TC2 483.66831 491.49487 956.36755 -979.68544 2028.5617 0. 0. 0. 0. 0. 0. 0.
VC2 0.7596741 -2.4375229 3.5192391 -3.0189635 0.47485182 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Decane [AR/C10]
?Mixing rules of nitrogen/decane used as an estimate.
ed016370/111888d0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 0.957934447 1.822157123 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 575.4673 182.62341 2625.6705 -3283.8448 3117.4115 0. 0. 0. 0. 0. 0. 0.
VC2 0.90177657 -3.1931422 5.4963786 -6.7477568 3.0117941 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Krypton [O2/KR]
?E.W. Lemmon, NIST (2002)
edc36840/d7c8c510
XR0 1. 0.9729000 1. 1.0043319 0. 0. 0. 0. 0. 0. 0. 0.
TC1 18.618747 -10.19424 -15.566191 26.99212 -23.40938 10.79737 0. 0. 0. 0. 0. 0.
VC1 -0.010439485 -0.06406133 0.2762606 -0.70498538 0.86654964 -0.40211752 0. 0. 0. 0. 0. 0.
PR1 0.02 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Ethane [O2/C2]
?Mixing rules of nitrogen/ethane used as an estimate.
edc36840/434e2a40
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
KW6 1.007671428 1.098650964 0.978880168 1.042352891 1. 0. 0. 0. 0. 0. 0. 0.
TC1 61.534791 308.67771 -1574.0146 5071.9442 -6767.8997 3108.3052 0. 0. 0. 0. 0. 0.
VC1 0.098042542 -0.66005182 3.0150345 -7.6916133 8.6268043 -3.6920587 0. 0. 0. 0. 0. 0.
!
?Oxygen/Nitrous oxide [O2/N2O]
?I. Cullimore and E.W. Lemmon, NIST (2010)
edc36840/e0647c00
XR0 0.9525 1.1068 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 108.79406 258.74838 -1679.8578 4225.6673 -4627.366 1967.988 0. 0. 0. 0. 0. 0.
VC1 0.098519015 -1.5902972 7.2906051 -16.968448 19.169437 -8.4539369 0. 0. 0. 0. 0. 0.
PR1 0.0478 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Carbon dioxide [O2/CO2]
?J. Gernert and R. Span, J. Chem. Thermodyn., 93:274-293, 2016. DOI:10.1016/j.jct.2015.05.015
edc36840/77c8bee0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.031986 1. 1.08446 0. 0. 0. 0. 0. 0. 0. 0.
TC2 143.50606 -415.55821 2047.2334 -4206.532 2648.0917 0. 0. 0. 0. 0. 0. 0.
VC2 0.034999957 -0.51142673 1.2403567 -1.8026811 0.83407525 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Hydrogen sulfide [O2/H2S]
?Mixing rules of nitrogen/Hydrogen sulfide used as an estimate.
edc36840/c6c03020
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1.004692366 0.9601742 0.910394249 1.256844157 0. 0. 0. 0. 0. 0. 0. 0.
TC4 177.4735 185.30612 -1159.453 944.72452 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.01134943 -0.45627412 0.54307455 -0.41858905 0. 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Propylene [O2/PRY]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from nitrogen and argon)
edc36840/56d778b0
XR0 1. 1.155 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 260.4861 -375.4569 1507.2648 -1357.1199 -22.746861 0. 0. 0. 0. 0. 0. 0.
VC2 0.085727788 -0.28568851 -1.2328142 3.7220665 -2.9957678 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Propane [O2/C3]
?Mixing rules of nitrogen/propane used as an estimate.
edc36840/70c6aac0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1.002677329 1.201264026 0.974424681 1.081025408 0. 0. 0. 0. 0. 0. 0. 0.
TC1 200.79727 424.84778 -2035.3143 5162.2672 -4485.6647 814.81203 0. 0. 0. 0. 0. 0.
VC1 0.26709724 -3.0034337 13.780296 -32.287187 36.157662 -15.758841 0. 0. 0. 0. 0. 0.
!
?Oxygen/Isobutane [O2/C4I]
?Mixing rules of nitrogen/isobutane used as an estimate.
edc36840/47ade7e0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 0.99286813 1.284462634 0.98641583 1.100576129 0. 0. 0. 0. 0. 0. 0. 0.
TC4 339.8529 -632.73051 2283.2417 -1542.2945 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.24461987 -1.5593368 3.2519315 -2.5642677 0. 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Sulfur dioxide [O2/SO2]
?T. Neumann, Development of New Helmholtz Models for Binary Mixtures Relevant for CCS; Master's thesis, Lehrstuhl Fuer Thermodynamik, Ruhr Universitaet, Bochum, Germany, 2017.
edc36840/7fad4b80
XR0 1.077631495289 1.0358782 0.820178826870 1.6606317 0. 0. 0. 0. 0. 0. 0. 0.
TC5 320.18341 -643.57555 1410.5615 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 0.041496302 -0.43696999 0.35817635 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Butane [O2/C4]
?Mixing rules of nitrogen/butane used as an estimate.
edc36840/7b3b4080
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 0.994515234 1.304886838 0.99608261 1.146949309 0. 0. 0. 0. 0. 0. 0. 0.
TC5 112.55546 990.04363 -634.6221 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 0.034604136 0.26876469 -0.76612988 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Isopentane [O2/C5I]
?Mixing rules of nitrogen/isopentane used as an estimate.
edc36840/86ee46a0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.38177077 1. 1.154135439 0. 0. 0. 0. 0. 0. 0. 0.
TC2 297.06835 689.66584 -2346.8879 5664.1109 -3557.6277 0. 0. 0. 0. 0. 0. 0.
VC2 0.46931955 -3.167115 8.9824936 -11.448626 4.7651198 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Pentane [O2/C5]
?Mixing rules of nitrogen/pentane used as an estimate.
edc36840/76bc0290
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.419029041 1. 1.078877166 0. 0. 0. 0. 0. 0. 0. 0.
TC2 320.50982 549.2605 -1345.9607 3839.9849 -2433.5462 0. 0. 0. 0. 0. 0. 0.
VC2 0.44851574 -3.0035645 8.7152779 -11.807114 5.3346231 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Methanol [O2/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
edc36840/c41aa690
XR0 1. 1.436 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC6 464.03333 373.5572 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 0.32165679 -1.0208164 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Hexane [O2/C6]
?Mixing rules of nitrogen/hexane used as an estimate.
edc36840/cb03ba40
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.472607971 1. 1.195952177 0. 0. 0. 0. 0. 0. 0. 0.
TC2 364.35075 283.12345 395.32939 350.64249 276.36034 0. 0. 0. 0. 0. 0. 0.
VC2 0.34756527 -1.1881125 2.1988833 -2.6387545 0.75133427 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Ethanol [O2/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from argon)
edc36840/3d5f67e0
XR0 1. 1.492 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 434.3221 182.74793 1606.8974 -2499.5921 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.36324559 -1.8879651 3.5416343 -3.9145358 0. 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Benzene [O2/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from argon/benzene)
edc36840/f2cfb460
XR0 1.01 1.397 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 446.49456 805.16983 -2070.8551 5851.416 -4736.7264 0. 0. 0. 0. 0. 0. 0.
VC2 0.34863718 -1.8007281 3.0288212 -2.6229799 0.36683187 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Cyclohexane [O2/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
edc36840/6e225350
XR0 1. 1.3883 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 400.63488 1276.3412 -4520.5152 9384.484 -6348.7166 0. 0. 0. 0. 0. 0. 0.
VC2 0.58165262 -3.9960136 9.2791517 -10.57655 4.2339179 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Heptane [O2/C7]
?Mixing rules of nitrogen/heptane used as an estimate.
edc36840/b398a3b0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.520975334 1. 1.40455409 0. 0. 0. 0. 0. 0. 0. 0.
TC2 336.0584 1563.1299 -5688.4042 11147.2 -5700.6141 0. 0. 0. 0. 0. 0. 0.
VC2 0.58048467 -2.546298 4.7557988 -2.8506983 -0.93070131 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Water [O2/H2O]
?J. Gernert and R. Span, J. Chem. Thermodyn., 93:274-293, 2016. DOI:10.1016/j.jct.2015.05.015
edc36840/b43a7600
GG0 1. 0.964767932 1. 1.143174289 0. 0. 0. 0. 0. 0. 0. 0.
KWD 1.25306 0.807842 1.028197 0.87346 0.6017 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Toluene [O2/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
edc36840/a49b8b50
XR0 1. 1.45 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 610.81633 -243.04241 2444.046 -1768.7952 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.4115782 -2.2135193 3.7670494 -2.8248923 0. 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Octane [O2/C8]
?Mixing rules of nitrogen/octane used as an estimate.
edc36840/f174a9b0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.733280051 1. 1.186067025 0. 0. 0. 0. 0. 0. 0. 0.
TC2 397.96809 710.32657 -177.1244 832.03674 1202.356 0. 0. 0. 0. 0. 0. 0.
VC2 0.69985274 -2.3217889 4.0129756 -3.6192137 0.42529026 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Nonane [O2/C9]
?Mixing rules of nitrogen/nonane used as an estimate.
edc36840/7f94dc20
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 0.95637945 1.749119996 1. 1.100405929 0. 0. 0. 0. 0. 0. 0. 0.
TC2 479.18539 384.99682 1442.6868 -1831.4015 2627.5898 0. 0. 0. 0. 0. 0. 0.
VC2 0.72208467 -2.3379917 3.9739731 -4.3198331 1.2953999 0. 0. 0. 0. 0. 0. 0.
!
?Oxygen/Decane [O2/C10]
?Mixing rules of nitrogen/decane used as an estimate.
edc36840/111888d0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 0.957934447 1.822157123 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 566.18173 121.22474 2889.3599 -3695.4098 3441.7335 0. 0. 0. 0. 0. 0. 0.
VC2 0.82804111 -2.8135077 5.2396661 -7.3241236 3.579644 0. 0. 0. 0. 0. 0. 0.
!
?Krypton/Xenon [KR/XE]
?E.W. Lemmon, NIST (2002)
d7c8c510/71fd7fa0
XR0 1. 1.0196370 1. 1.0054519 0. 0. 0. 0. 0. 0. 0. 0.
TC1 36.830077 8.068718 -21.585289 81.341152 -108.20145 56.898636 0. 0. 0. 0. 0. 0.
VC1 -0.0011726807 -0.11053989 0.45594385 -1.1441553 1.348071 -0.62590472 0. 0. 0. 0. 0. 0.
!
?Krypton/Ethane [KR/C2]
?I. Cullimore and E.W. Lemmon, NIST (2010)
d7c8c510/434e2a40
XR0 0.992161920825 1.0437 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 77.463334 -112.95403 423.91948 -637.41161 459.51856 -96.584034 0. 0. 0. 0. 0. 0.
VC1 0.070429601 -0.72804854 2.8506858 -5.9774852 6.143216 -2.4983796 0. 0. 0. 0. 0. 0.
!
?Krypton/Carbon dioxide [KR/CO2]
?I. Cullimore and E.W. Lemmon, NIST (2010)
d7c8c510/77c8bee0
KW0 0.948047023132 1.0466 1. 1. 0.6362 0. 0. 0. 0. 0. 0. 0.
TC4 22.938377 -86.078962 56.299691 102.99507 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.046133009 -0.24958109 0.53524332 -0.28905627 0. 0. 0. 0. 0. 0. 0. 0.
!
?Krypton/Propylene [KR/PRY]
?E.W. Lemmon, NIST (2002)
d7c8c510/56d778b0
XR0 1. 1.0773977 1. 1.0390195 0. 0. 0. 0. 0. 0. 0. 0.
TC1 143.02583 -69.793539 183.66812 385.88866 -1072.9732 669.10454 0. 0. 0. 0. 0. 0.
VC1 0.14990825 -1.6111589 6.7086883 -14.533051 15.11626 -6.1431356 0. 0. 0. 0. 0. 0.
!
?Krypton/Ammonia [KR/NH3]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.66% from 8 bubble-point pressures
d7c8c510/e9847540
XR0 1.011818 0.92419 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC5 195.93561 -121.63192 -237.21332 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 0.012094799 -0.50387452 0.34704159 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R14/Ethane [R14/C2]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.39% from 29 bubble-point pressures
dba9f950/434e2a40
XR0 0.985386715016 0.89216 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 40.751699 -242.62648 404.31107 -646.81355 621.61728 -232.11702 0. 0. 0. 0. 0. 0.
VC1 0.015926882 -0.69049323 1.9548014 -2.7926436 2.3806908 -0.88378313 0. 0. 0. 0. 0. 0.
!
?R14/R23 [R14/R23]
?E.W. Lemmon, NIST (2002)
dba9f950/20e26c20
XR0 1. 0.9467580 1. 1.0002627 0. 0. 0. 0. 0. 0. 0. 0.
TC1 19.10499 -15.886457 -130.30032 207.7437 -141.73029 36.884938 0. 0. 0. 0. 0. 0.
VC1 0.0099817743 -0.41317553 1.1093816 -1.6813855 1.4301996 -0.48569227 0. 0. 0. 0. 0. 0.
PR1 0.1056 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R14/R13 [R14/R13]
?E.W. Lemmon, NIST (2002)
dba9f950/126c90a0
XR0 1. 0.9927242 1. 1.0048844 0. 0. 0. 0. 0. 0. 0. 0.
TC1 26.760325 4.8302191 -28.299427 31.662495 -23.742041 11.053083 0. 0. 0. 0. 0. 0.
VC1 0.001845221 -0.16309464 0.42057344 -0.82844369 0.88037759 -0.38980519 0. 0. 0. 0. 0. 0.
!
?R14/Toluene [R14/TOL]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.69% from 8 bubble-point pressures
dba9f950/a49b8b50
XR0 0.920319984215 1.18828 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 379.121 2097.5258 -10158.026 16751.377 -8966.5434 0. 0. 0. 0. 0. 0. 0.
VC2 0.32111985 -2.1705806 0.56948947 6.3186027 -6.336111 0. 0. 0. 0. 0. 0. 0.
!
?Xenon/Ethylene [XE/ETY]
?I. Cullimore and E.W. Lemmon, NIST (2010)
71fd7fa0/9c1062b0
XR0 1. 0.9798 1. 1.0048 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -10.807249 -3.9625488 6.1751301 -3.284418 0.96949742 -0.20443103 0. 0. 0. 0. 0. 0.
VC1 0.0079320578 -0.043740013 0.13561029 -0.24080144 0.21221718 -0.073521095 0. 0. 0. 0. 0. 0.
!
?Xenon/Ethane [XE/C2]
?E.W. Lemmon, NIST (2002)
71fd7fa0/434e2a40
XR0 1. 1.0112641 1. 1.0034307 0. 0. 0. 0. 0. 0. 0. 0.
TC1 9.5105977 1.1314707 2.4463395 -2.3011284 2.5612217 -1.2415915 0. 0. 0. 0. 0. 0.
VC1 0.022737406 -0.13079629 0.44911292 -0.80987949 0.7204002 -0.25072682 0. 0. 0. 0. 0. 0.
!
?Xenon/Hydrogen chloride [XE/HCL]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.92% from 23 bubble-point pressures
71fd7fa0/74b17450
XR0 1.0176667 0.90579 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -26.86521 -74.023103 137.23361 -403.67509 492.91298 -185.36322 0. 0. 0. 0. 0. 0.
VC1 -0.0080928306 -0.03011077 -0.059244749 0.25682178 -0.06625653 -0.10095822 0. 0. 0. 0. 0. 0.
!
?Xenon/R41 [XE/R41]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.08% from 31 bubble-point pressures
71fd7fa0/8ee31230
XR0 1.0229865 0.91395 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -17.716966 -45.537098 37.820905 -247.94347 324.24329 -110.94611 0. 0. 0. 0. 0. 0.
VC1 0.0085402966 -0.05391574 -0.20702565 0.83639799 -0.78425124 0.18349719 0. 0. 0. 0. 0. 0.
!
?Xenon/Sulfur hexafluoride [XE/SF6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.61% from 81 bubble-point pressures
71fd7fa0/7a75e610
XR0 1.0366024 0.92846 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 14.917677 -105.69919 272.02089 -593.67279 432.52045 -84.185518 0. 0. 0. 0. 0. 0.
VC1 0.09140308 -0.74005621 2.7301657 -5.6308842 6.0108613 -2.4827799 0. 0. 0. 0. 0. 0.
!
?Xenon/Propylene [XE/PRY]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.04% from 51 bubble-point pressures
71fd7fa0/56d778b0
XR0 1.009784814856 1.01223 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 50.834875 -39.095889 145.2394 -240.17555 182.36937 -57.821064 0. 0. 0. 0. 0. 0.
VC1 0.09408819 -0.80389808 2.9054501 -5.4939221 5.0439612 -1.7877691 0. 0. 0. 0. 0. 0.
!
?Xenon/Propane [XE/C3]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.41% from 22 bubble-point pressures
71fd7fa0/70c6aac0
XR0 0.995113990308 1.04133 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 58.881565 -18.01086 103.76133 -67.727694 -9.527182 41.277674 0. 0. 0. 0. 0. 0.
VC1 0.10932857 -0.93080378 3.6140789 -7.2575402 7.0838862 -2.7088242 0. 0. 0. 0. 0. 0.
!
?Xenon/Cyclopropane [XE/CC3]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.05% from 15 bubble-point pressures
71fd7fa0/bc9f5400
XR0 0.934273835661 0.94711 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 56.417427 59.841957 -1500.2598 3933.5628 -3993.8225 1517.9095 0. 0. 0. 0. 0. 0.
VC1 0.10288664 -1.6580781 5.754365 -8.746048 6.4791817 -1.9999054 0. 0. 0. 0. 0. 0.
!
?Xenon/R40 [XE/R40]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.83% from 15 bubble-point pressures
71fd7fa0/2b938200
XR0 1.0366562 1.03491 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 69.601574 15.11646 108.39865 -139.20864 -110.36295 112.37635 0. 0. 0. 0. 0. 0.
VC1 -0.01246851 -0.11472194 0.40240151 -1.2033541 1.2650277 -0.45073544 0. 0. 0. 0. 0. 0.
!
?Xenon/Cyclopentane [XE/CC5]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.08% from 10 bubble-point pressures
71fd7fa0/43ab1810
XR0 0.953688868544 1.17726 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 170.20452 209.83692 -517.26585 1526.8123 -1504.2696 723.73449 0. 0. 0. 0. 0. 0.
VC1 0.062860476 -1.1019074 6.0474436 -16.164601 20.051569 -9.5263116 0. 0. 0. 0. 0. 0.
!
?Xenon/Methanol [XE/MEO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.63% from 13 bubble-point pressures
71fd7fa0/c41aa690
XR0 1.068855683106 0.77335 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Xenon/Hexane [XE/C6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.81% from 21 bubble-point pressures
71fd7fa0/cb03ba40
XR0 0.980786394531 1.16656 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 213.14622 124.52252 -42.562777 796.76358 -918.85842 426.63579 0. 0. 0. 0. 0. 0.
VC1 0.3276724 -2.7884815 11.927367 -27.235873 29.829687 -12.732174 0. 0. 0. 0. 0. 0.
!
?Ethylene/Ethane [ETY/C2]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/434e2a40
KW0 1. 0.991 1. 1.008 0.025 0. 0. 0. 0. 0. 0. 0.
TC1 -0.60995231 -6.2635402 7.835161 -10.602054 8.5840532 -3.0992636 0. 0. 0. 0. 0. 0.
VC1 0.021314372 -0.11629539 0.32896935 -0.38429265 0.12565163 0.056616093 0. 0. 0. 0. 0. 0.
PR1 0.0089 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethylene/Carbon dioxide [ETY/CO2]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/77c8bee0
KW0 1. 0.957 0.986193293886 0.991 0.014 0. 0. 0. 0. 0. 0. 0.
TC4 -18.778299 -27.187283 21.464745 0.37862566 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.012017351 -0.32453252 1.1604872 -0.84583599 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0552 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethylene/Propylene [ETY/PRY]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/56d778b0
XR0 1.004 1.016 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 49.751183 -9.9145481 -55.872145 331.00017 -514.11557 266.9726 0. 0. 0. 0. 0. 0.
VC1 0.07951997 -0.71129901 2.499407 -4.4985405 3.8670433 -1.2616072 0. 0. 0. 0. 0. 0.
!
?Ethylene/Propane [ETY/C3]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/70c6aac0
XR0 1.006036217304 1.014 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 57.229306 -17.072227 -23.345825 281.9545 -496.44961 271.04241 0. 0. 0. 0. 0. 0.
VC1 0.083251293 -0.68131918 2.258924 -3.9671943 3.3351465 -1.0549348 0. 0. 0. 0. 0. 0.
!
?Ethylene/R1216 [ETY/R1216]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.34% from 46 bubble-point pressures
9c1062b0/edc3a7b0
XR0 1.01864 0.99653 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 54.533012 15.32768 -40.888892 176.81305 -384.95902 227.04832 0. 0. 0. 0. 0. 0.
VC1 0.16331586 -1.3188641 4.6171104 -8.6875007 7.9065383 -2.6749889 0. 0. 0. 0. 0. 0.
!
?Ethylene/Isobutane [ETY/C4I]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/47ade7e0
XR0 0.995024875622 1.057 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 102.72365 44.954528 -358.5386 1399.3566 -1898.7661 929.84909 0. 0. 0. 0. 0. 0.
VC1 0.21918783 -2.0266541 7.5802048 -14.482087 13.43846 -4.904353 0. 0. 0. 0. 0. 0.
!
?Ethylene/Butene [ETY/1BE]
?I. Cullimore and E.W. Lemmon, NIST (2010)
9c1062b0/cd7a06d0
XR0 1. 1.0486 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 91.794504 149.52661 -652.24828 1816.9071 -2254.027 1048.893 0. 0. 0. 0. 0. 0.
VC1 0.13122101 -1.0438457 3.3869372 -6.222695 5.6770996 -2.0964537 0. 0. 0. 0. 0. 0.
!
?Ethylene/Perfluorobutane [ETY/C4F10]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.63% from 50 bubble-point pressures
9c1062b0/a8f85e00
XR0 1.0415148 0.97341 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 83.02599 26.25761 412.02944 -1121.9222 750.84558 -95.938768 0. 0. 0. 0. 0. 0.
VC1 0.2885942 -1.524769 3.8236077 -7.4751011 7.683333 -2.761501 0. 0. 0. 0. 0. 0.
!
?Ethylene/Butane [ETY/C4]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/7b3b4080
XR0 0.978473581213 1.058 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 103.12629 134.64808 -800.77338 2356.6309 -2851.3327 1326.4637 0. 0. 0. 0. 0. 0.
VC1 0.21717188 -2.1310655 7.9581564 -15.295729 14.556088 -5.5429337 0. 0. 0. 0. 0. 0.
PR1 0.0922 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethylene/Isopentane [ETY/C5I]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
9c1062b0/86ee46a0
KW0 0.990099009901 1.09 1. 1. 0.4 0. 0. 0. 0. 0. 0. 0.
TC1 124.8437 258.79365 -1298.2168 3736.9804 -4423.9747 1945.3777 0. 0. 0. 0. 0. 0.
VC1 0.2806391 -2.6932309 10.30924 -20.348117 19.675299 -7.6080892 0. 0. 0. 0. 0. 0.
!
?Ethylene/Diethyl ether [ETY/DEE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.96% from 32 bubble-point pressures
9c1062b0/46a701e0
XR0 0.9890121 1.10874 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 142.93687 349.57795 -1566.1629 4325.2445 -5117.9541 2262.7713 0. 0. 0. 0. 0. 0.
VC1 0.061584329 -0.77973233 3.3517057 -8.4686557 10.194312 -4.8378363 0. 0. 0. 0. 0. 0.
!
?Ethylene/Pentane [ETY/C5]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
9c1062b0/76bc0290
KW0 0.990099009901 1.1 1. 1. 0.48 0. 0. 0. 0. 0. 0. 0.
TC1 114.4108 328.34316 -1510.9723 4343.408 -5182.5389 2275.0682 0. 0. 0. 0. 0. 0.
VC1 0.081325404 -0.73075136 2.958894 -6.9776313 7.8112355 -3.5582354 0. 0. 0. 0. 0. 0.
!
?Ethylene/Acetone [ETY/ACT]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.69% from 35 bubble-point pressures
9c1062b0/342481e0
XR0 1.0078308 1.10077 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 189.5239 814.50623 -4609.1573 13087.827 -16471.486 7367.9756 0. 0. 0. 0. 0. 0.
VC1 0.43046993 -3.7827937 14.072764 -27.756348 26.553967 -10.11863 0. 0. 0. 0. 0. 0.
!
?Ethylene/Methanol [ETY/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/c41aa690
XR0 0.955 1.143 1.481 0.857 0. 0. 0. 0. 0. 0. 0. 0.
TC4 132.04375 463.07128 326.8233 -1267.8968 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.22491599 -0.31650891 -1.5223687 1.2601643 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethylene/Hexane [ETY/C6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/cb03ba40
KW0 0.995024875622 1.106 1. 1.096 0.649 0. 0. 0. 0. 0. 0. 0.
TC1 160.30129 275.64107 -1683.0329 5620.9274 -7046.0548 3134.0655 0. 0. 0. 0. 0. 0.
VC1 0.055875813 -1.4910626 7.7792751 -18.053497 19.090953 -7.8937682 0. 0. 0. 0. 0. 0.
!
?Ethylene/Ethanol [ETY/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/3d5f67e0
XR0 1. 1.149 0.788 1.159 0. 0. 0. 0. 0. 0. 0. 0.
TC1 239.48677 105.73874 -387.23294 1355.3553 -3620.9984 2908.3633 0. 0. 0. 0. 0. 0.
VC1 0.18700403 -2.0160497 8.0803484 -19.065189 21.374693 -8.9895089 0. 0. 0. 0. 0. 0.
!
?Ethylene/Benzene [ETY/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/f2cfb460
XR0 0.978473581213 1.124 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 245.02192 477.65158 -2582.6613 7206.4101 -8545.5668 3639.9409 0. 0. 0. 0. 0. 0.
VC1 0.23494378 -2.4794957 10.619065 -25.109655 28.907229 -13.052252 0. 0. 0. 0. 0. 0.
PR1 0.0311 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethylene/Cyclohexane [ETY/CC6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.62% from 83 bubble-point pressures
9c1062b0/6e225350
XR0 0.9987416 1.12037 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 195.13707 940.05193 -4547.0704 11728.873 -13570.747 5692.359 0. 0. 0. 0. 0. 0.
VC1 0.2981048 -2.6180785 9.5136768 -20.945926 23.354008 -10.428567 0. 0. 0. 0. 0. 0.
!
?Ethylene/Heptane [ETY/C7]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/b398a3b0
KW0 0.985221674877 1.15 1. 1.085 0.799 0. 0. 0. 0. 0. 0. 0.
TC1 223.74739 200.9792 -850.02977 2671.0871 -2322.7212 605.10126 0. 0. 0. 0. 0. 0.
VC1 0.39807007 -4.1786728 17.189032 -35.643875 36.151835 -14.730887 0. 0. 0. 0. 0. 0.
PR1 0.0144 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethylene/Toluene [ETY/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/a49b8b50
XR0 0.992063492063 1.173 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 277.49517 999.29411 -4904.3226 12462.513 -12869.204 4344.7835 0. 0. 0. 0. 0. 0.
VC1 0.38805023 -4.0224324 17.726837 -41.176529 46.172608 -20.322969 0. 0. 0. 0. 0. 0.
!
?Ethylene/Octane [ETY/C8]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/f174a9b0
KW0 0.973709834469 1.2 1. 1.072 0.942 0. 0. 0. 0. 0. 0. 0.
TC1 260.1343 -251.16931 2683.258 -7577.0684 11277.208 -5843.2894 0. 0. 0. 0. 0. 0.
VC1 0.4290118 -4.5399174 19.850294 -43.59133 46.794345 -20.098536 0. 0. 0. 0. 0. 0.
!
?Ethylene/Nonane [ETY/C9]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/7f94dc20
KW0 0.968054211036 1.23 1. 1.064 1.09 0. 0. 0. 0. 0. 0. 0.
TC1 306.38776 -817.51031 6751.9449 -18975.562 26431.851 -13251.12 0. 0. 0. 0. 0. 0.
VC1 0.25190889 -3.5267614 19.863258 -48.886476 55.198714 -24.366644 0. 0. 0. 0. 0. 0.
!
?Ethylene/Decane [ETY/C10]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
9c1062b0/111888d0
KW0 0.957854406130 1.26 1. 1.058 1.24 0. 0. 0. 0. 0. 0. 0.
TC1 429.76693 -2010.9442 14290.482 -39992.496 53183.515 -25616.888 0. 0. 0. 0. 0. 0.
VC1 0.69558729 -7.6603584 36.226741 -82.186771 89.248507 -38.204021 0. 0. 0. 0. 0. 0.
PR1 0.0253 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Hydrogen chloride [C2/HCL]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.64% from 115 bubble-point pressures
434e2a40/74b17450
XR0 0.99182 0.90586 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -54.023788 -12.275469 -122.79826 423.49581 -406.52684 137.41162 0. 0. 0. 0. 0. 0.
VC1 -0.025291495 0.13378435 -1.0787575 3.8648678 -5.3006003 2.4759183 0. 0. 0. 0. 0. 0.
!
?Ethane/R23 [C2/R23]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.47% from 44 bubble-point pressures
434e2a40/20e26c20
XR0 1.00597 0.87082 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -56.0584 -5.5788066 -385.28818 949.62541 -774.51782 233.21585 0. 0. 0. 0. 0. 0.
VC1 0.0033715128 -0.31241083 1.5899157 -2.8051452 1.7631877 -0.21930139 0. 0. 0. 0. 0. 0.
!
?Ethane/Carbon dioxide [C2/CO2]
?Kunz and Wagner (2007)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
434e2a40/77c8bee0
KW0 0.986318629304 0.90094953 0.997480645180 1.032876701 0. 0. 0. 0. 0. 0. 0. 0.
TC2 -53.749652 -107.73154 338.34034 -311.91717 111.8934 0. 0. 0. 0. 0. 0. 0.
VC2 -0.10210039 0.66045034 -1.1374867 0.60143076 0.031412034 0. 0. 0. 0. 0. 0. 0.
PR1 0.1322 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/R116 [C2/R116]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.26% from 60 bubble-point pressures
434e2a40/04997260
XR0 1.03539 0.89844 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 -34.200254 5.7723937 -196.5499 171.44765 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.031154728 -0.11553456 0.34397171 -0.37980586 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Hydrogen sulfide [C2/H2S]
?Kunz and Wagner (2012)
434e2a40/c6c03020
KW0 0.990197354 0.90273666 1.010817909 1.030988277 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -41.737977 -42.5386 -1.666272 24.404624 -10.750846 10.957219 0. 0. 0. 0. 0. 0.
VC1 -0.042825459 0.10873299 -0.54949394 1.6139071 -1.9432002 0.83759053 0. 0. 0. 0. 0. 0.
PR1 0.0833 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Propylene [C2/PRY]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
434e2a40/56d778b0
XR0 1. 1.002 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 25.658821 -13.608887 -5.7686988 98.114485 -161.86041 88.456265 0. 0. 0. 0. 0. 0.
VC1 0.062630189 -0.52449679 1.7951532 -3.0848133 2.5484087 -0.79190456 0. 0. 0. 0. 0. 0.
PR1 0.0089 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Propane [C2/C3]
?Kunz and Wagner (2007)
434e2a40/70c6aac0
KW0 0.996199694 1.01473019 0.997607277 1.00303472 0.13042476515 0. 0. 0. 0. 0. 0. 0.
TC1 21.755864 10.600449 -66.834298 235.72629 -300.48249 147.1984 0. 0. 0. 0. 0. 0.
VC1 0.05534725 -0.39078431 1.134395 -1.5236717 0.83686273 -0.087278688 0. 0. 0. 0. 0. 0.
TRN 0.0557 -0.2792 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0011 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/R218 [C2/R218]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.88% from 41 bubble-point pressures
434e2a40/00bd3610
XR0 1.03147 0.93581 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 13.137481 -0.56225063 -22.715122 -141.34718 99.587002 -2.4803879 0. 0. 0. 0. 0. 0.
VC1 0.082152929 -0.24947999 -0.15392916 1.1963119 -1.3297699 0.51947438 0. 0. 0. 0. 0. 0.
!
?Ethane/R1216 [C2/R1216]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.02% from 50 bubble-point pressures
434e2a40/edc3a7b0
XR0 1.01157 0.93961 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 28.236331 -55.975345 40.212379 -170.83284 182.07563 -59.683333 0. 0. 0. 0. 0. 0.
VC1 0.11435858 -1.0395719 3.2009566 -4.9882838 4.0529848 -1.2940259 0. 0. 0. 0. 0. 0.
!
?Ethane/Dimethyl ether [C2/DME]
?I. Cullimore and E.W. Lemmon, NIST (2010) (estimated from methane/dimethyl ether and propane/dimethyl ether)
434e2a40/8f27e300
XR0 1. 1.0388 1. 1.0476 0. 0. 0. 0. 0. 0. 0. 0.
TC1 43.627397 65.636547 -277.07529 799.91934 -987.20686 465.75609 0. 0. 0. 0. 0. 0.
VC1 0.027853676 -0.092901963 0.15548331 -0.14634492 -0.013260952 0.033098535 0. 0. 0. 0. 0. 0.
!
?Ethane/Isobutane [C2/C4I]
?Kunz and Wagner (2007)
434e2a40/47ade7e0
KW0 1. 1.033283811 1. 1.006616886 0.260632376098 0. 0. 0. 0. 0. 0. 0.
TC1 52.456211 53.184638 -278.73271 863.62239 -1071.6821 498.72603 0. 0. 0. 0. 0. 0.
VC1 0.17405607 -1.4936387 5.1273395 -8.8003655 7.244113 -2.2776891 0. 0. 0. 0. 0. 0.
PR1 -0.0067 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Perfluorobutane [C2/C4F10]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.31% from 84 bubble-point pressures
434e2a40/a8f85e00
XR0 1.0288172 0.97003 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 52.856697 59.612379 -56.788848 -8.2825387 -181.37451 162.65904 0. 0. 0. 0. 0. 0.
VC1 0.21030551 -0.91271959 1.5913516 -2.2524074 2.1160524 -0.68848334 0. 0. 0. 0. 0. 0.
!
?Ethane/Butane [C2/C4]
?Kunz and Wagner (2007)
434e2a40/7b3b4080
KW0 0.999130554 1.034832749 0.999157205 1.006179146 0.281570073085 0. 0. 0. 0. 0. 0. 0.
TC1 56.651488 85.094265 -394.89635 1140.4347 -1396.3973 646.77212 0. 0. 0. 0. 0. 0.
VC1 0.093228931 -0.82961674 2.4782782 -3.7669535 2.6636847 -0.6891244 0. 0. 0. 0. 0. 0.
TRN 0.035 -0.1858 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0096 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Isopentane [C2/C5I]
?Kunz and Wagner (2007)
434e2a40/86ee46a0
KW0 1. 1.021150247 1. 1.045439935 0. 0. 0. 0. 0. 0. 0. 0.
TC1 128.69118 89.995277 -591.27728 1773.6685 -2280.3419 1089.4838 0. 0. 0. 0. 0. 0.
VC1 0.32241588 -2.7145416 9.4813927 -17.325853 15.533938 -5.4475848 0. 0. 0. 0. 0. 0.
!
?Ethane/Pentane [C2/C5]
?Kunz and Wagner (2007)
434e2a40/76bc0290
KW0 0.998688946 1.066665676 0.993851009 1.026085655 0. 0. 0. 0. 0. 0. 0. 0.
TC1 118.23236 253.55324 -1057.2558 2933.3488 -3597.0207 1654.7328 0. 0. 0. 0. 0. 0.
VC1 0.21926907 -1.418655 4.5941618 -8.9485436 8.8218377 -3.5362157 0. 0. 0. 0. 0. 0.
PR1 0.0078 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Acetone [C2/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
434e2a40/342481e0
KW0 1.004722194313 0.9769 1. 1. 2.1862 0. 0. 0. 0. 0. 0. 0.
TC5 0.085926156 334.89415 -701.19771 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.5440779 1.2506687 -1.4606677 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.1307 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Methanol [C2/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
434e2a40/c41aa690
KW0 0.977 1.011 1. 1. 2.751 0. 0. 0. 0. 0. 0. 0.
TC5 41.885415 202.8554 -674.2108 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.34749774 0.74190402 -1.1736595 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.027 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Hexane [C2/C6]
?Kunz and Wagner (2007)
434e2a40/cb03ba40
KW0 1. 1.092177796 1. 1.169701102 0. 0. 0. 0. 0. 0. 0. 0.
TC1 163.03118 178.86324 -833.00664 3055.8798 -4055.9785 1958.6825 0. 0. 0. 0. 0. 0.
VC1 0.23547984 -1.7337546 7.6119964 -17.361093 18.662868 -7.7832066 0. 0. 0. 0. 0. 0.
PR1 -0.01 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Ethanol [C2/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
434e2a40/3d5f67e0
XR0 0.994 1.086 1. 1.179 0. 0. 0. 0. 0. 0. 0. 0.
TC1 155.91033 224.97318 -1323.448 4794.1472 -7439.3616 3991.8553 0. 0. 0. 0. 0. 0.
VC1 0.12699398 -0.93191095 3.6851959 -8.9503267 9.5038939 -3.8389919 0. 0. 0. 0. 0. 0.
!
?Ethane/Benzene [C2/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
434e2a40/f2cfb460
XR0 1. 1.081 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 208.30675 403.60211 -2378.0403 7447.2735 -10018.49 4722.3362 0. 0. 0. 0. 0. 0.
VC1 0.16613808 -1.5686797 5.9368711 -13.379754 14.600957 -6.3808861 0. 0. 0. 0. 0. 0.
PR1 0.0322 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Cyclohexane [C2/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
434e2a40/6e225350
XR0 0.9958 1.1004 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 180.27986 524.34236 -2313.0455 6050.9022 -7150.9672 3132.338 0. 0. 0. 0. 0. 0.
VC1 0.2259901 -1.9288429 6.7119222 -14.614609 16.269704 -7.3218135 0. 0. 0. 0. 0. 0.
PR1 0.0178 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Heptane [C2/C7]
?Kunz and Wagner (2007)
434e2a40/b398a3b0
KW0 1. 1.134532014 1. 1.057666085 0. 0. 0. 0. 0. 0. 0. 0.
TC1 238.03961 312.33361 -1271.4542 4006.5275 -4725.8397 1980.9739 0. 0. 0. 0. 0. 0.
VC1 0.57948437 -4.8829662 19.258381 -40.145656 40.721502 -16.275978 0. 0. 0. 0. 0. 0.
PR1 0.0067 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Isooctane [C2/C8I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.73% from 5 bubble-point pressures
434e2a40/c2dd9ef0
XR0 0.90358 1.22877 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 236.50805 -14.993792 470.58302 -683.26905 1056.7003 0. 0. 0. 0. 0. 0. 0.
VC2 0.49582377 -2.9656817 6.0229849 -3.8283459 -0.3483379 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Water [C2/H2O]
?Kunz and Wagner (2007)
434e2a40/b43a7600
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC5 262.01995 -653.18075 454.98444 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.049518196 -0.15899219 -0.373517 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Methylcyclohexane [C2/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
434e2a40/0429edd0
XR0 0.988 1.122 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 180.30224 549.40745 -1823.772 4735.9619 -5369.4596 2210.4864 0. 0. 0. 0. 0. 0.
VC1 0.093578476 -0.34487244 1.6897266 -7.6038255 12.00178 -6.6300916 0. 0. 0. 0. 0. 0.
!
?Ethane/Toluene [C2/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
434e2a40/a49b8b50
XR0 1. 1.129 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 241.06057 994.27981 -5396.7522 14840.573 -17544.121 7311.899 0. 0. 0. 0. 0. 0.
VC1 0.32561736 -3.17938 13.087394 -29.223339 31.682758 -13.65709 0. 0. 0. 0. 0. 0.
!
?Ethane/Octane [C2/C8]
?Kunz and Wagner (2007)
434e2a40/f174a9b0
KW0 0.984068272 1.168636194 1.007469726 1.071917985 0. 0. 0. 0. 0. 0. 0. 0.
TC1 270.45341 200.49979 52.493062 -196.05499 1134.1685 -804.79532 0. 0. 0. 0. 0. 0.
VC1 0.91351903 -7.6505309 29.790106 -61.277226 62.232448 -25.015018 0. 0. 0. 0. 0. 0.
PR1 0.0185 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/m-Xylene [C2/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.32% from 34 bubble-point pressures
434e2a40/0f99ff70
XR0 0.98799 1.17616 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 337.16286 264.03068 -1672.4449 5669.7549 -6094.0741 1917.8098 0. 0. 0. 0. 0. 0.
VC1 0.61099877 -6.3157553 27.989133 -62.848502 67.564318 -28.349644 0. 0. 0. 0. 0. 0.
!
?Ethane/Nonane [C2/C9]
?Kunz and Wagner (2012)
434e2a40/7f94dc20
KW0 1. 1.05603303 1. 1.14353473 0. 0. 0. 0. 0. 0. 0. 0.
TC1 355.49399 455.05887 -1431.6148 4078.773 -6726.4705 3909.6299 0. 0. 0. 0. 0. 0.
VC1 1.1171448 -8.4924915 27.902815 -52.227919 49.584818 -18.469946 0. 0. 0. 0. 0. 0.
!
?Ethane/Propylcyclohexane [C2/C3CC6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.76% from 26 bubble-point pressures
434e2a40/206f01b0
XR0 0.9812387 1.195 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 283.19893 335.47734 831.86693 -3605.5691 6765.2316 -4114.694 0. 0. 0. 0. 0. 0.
VC1 0.27193194 -1.5999318 8.5587239 -27.394202 37.654379 -18.910685 0. 0. 0. 0. 0. 0.
!
?Ethane/Decane [C2/C10]
?Kunz and Wagner (2012)
434e2a40/111888d0
KW0 0.970918061 1.237191558 0.995676258 1.098361281 0. 0. 0. 0. 0. 0. 0. 0.
TC1 403.90754 -573.9619 5564.2272 -15291.547 20330.114 -9611.9875 0. 0. 0. 0. 0. 0.
VC1 1.0955735 -8.6619728 34.546961 -73.646863 77.428498 -32.130885 0. 0. 0. 0. 0. 0.
PR1 0.0144 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethane/Undecane [C2/C11]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.01% from 19 bubble-point pressures
434e2a40/62f46c40
XR0 0.9430937 1.27938 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 444.47036 -1212.5731 9727.7149 -27451.25 36052.453 -16699.836 0. 0. 0. 0. 0. 0.
VC1 1.2956507 -11.242948 43.643501 -89.544558 92.158054 -37.997352 0. 0. 0. 0. 0. 0.
!
?Ethane/Dodecane [C2/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
434e2a40/8bc8dec0
XR0 0.97 1.3 1. 1.24 0. 0. 0. 0. 0. 0. 0. 0.
TC1 427.1959 -1076.0104 8819.6211 -23836.19 31067.545 -14205.392 0. 0. 0. 0. 0. 0.
VC1 1.3595402 -11.90462 50.471372 -106.02591 107.96924 -43.407186 0. 0. 0. 0. 0. 0.
!
?Nitrous oxide/R125 [N2O/R125]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.72% from 16 bubble-point pressures
e0647c00/25c5a3a0
XR0 0.97626 0.77302 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 100.13833 -450.30104 -113.19421 367.81334 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.20752868 -2.7166327 6.6115272 -4.4358531 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nitrous oxide/Dodecane [N2O/C12]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.99% from 58 bubble-point pressures
e0647c00/8bc8dec0
XR0 0.965763677628 1.2736 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 325.99668 1494.3662 -5130.6721 9558.4959 -4875.927 0. 0. 0. 0. 0. 0. 0.
VC2 1.161682 -6.5750314 14.782139 -14.32966 4.0939649 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen chloride/R41 [HCL/R41]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.51% from 27 bubble-point pressures
74b17450/8ee31230
XR0 0.98722 1.10901 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 71.620312 -22.171569 1.258592 141.09211 -194.25202 117.97306 0. 0. 0. 0. 0. 0.
VC1 -0.030662347 0.21904485 -0.85708419 1.8154571 -1.7692669 0.63638787 0. 0. 0. 0. 0. 0.
!
?Hydrogen chloride/R32 [HCL/R32]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.19% from 40 bubble-point pressures
74b17450/7b05bb60
XR0 1.00252 0.9976 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 10.966898 1.2818729 -8.8118746 14.908891 -17.783497 7.9865652 0. 0. 0. 0. 0. 0.
VC1 0.055930808 -0.36117153 1.2261768 -2.1232974 1.7937542 -0.5763791 0. 0. 0. 0. 0. 0.
!
?Hydrogen chloride/Propane [HCL/C3]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.52% from 150 bubble-point pressures
74b17450/70c6aac0
XR0 1.021430010186 0.9176 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 30.527376 -149.19423 384.13235 -774.02909 598.64754 -155.70495 0. 0. 0. 0. 0. 0.
VC1 0.12672785 -1.0934682 4.0684414 -7.6554791 7.1395785 -2.5783365 0. 0. 0. 0. 0. 0.
!
?Hydrogen chloride/Chlorine [HCL/CL]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.14% from 32 bubble-point pressures
74b17450/828f1c80
XR0 1.004006 0.96115 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 53.188003 -64.312181 35.816794 -63.158453 14.530818 14.935689 0. 0. 0. 0. 0. 0.
VC1 0.047179895 -0.49469527 1.8428862 -3.448896 3.1256987 -1.0667061 0. 0. 0. 0. 0. 0.
!
?Hydrogen chloride/R40 [HCL/R40]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.94% from 12 bubble-point pressures
74b17450/2b938200
XR0 0.98451 1.08265 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 58.435416 81.313626 -215.19333 705.48161 -850.64724 435.00031 0. 0. 0. 0. 0. 0.
VC1 -0.0029217544 -0.025790944 0.1747239 -0.49215389 0.65094857 -0.34296176 0. 0. 0. 0. 0. 0.
!
?Hydrogen chloride/Sulfur dioxide [HCL/SO2]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.17% from 31 bubble-point pressures
74b17450/7fad4b80
XR0 0.9942 1.05144 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 57.993568 59.83074 -159.92755 502.2819 -601.73238 288.91715 0. 0. 0. 0. 0. 0.
VC1 0.00097310742 -0.0089955563 -0.017821683 0.057843989 -0.072544277 0.012178035 0. 0. 0. 0. 0. 0.
!
?Hydrogen chloride/R142b [HCL/R142B]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.56% from 34 bubble-point pressures
74b17450/f2a8b2e0
XR0 1.00828 1.00217 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 58.487569 50.50634 -97.868184 260.3092 -318.41346 142.12641 0. 0. 0. 0. 0. 0.
VC1 0.1705152 -1.0975625 3.5037561 -5.9521196 5.0020065 -1.6044951 0. 0. 0. 0. 0. 0.
!
?Hydrogen chloride/Butane [HCL/C4]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3% from 33 bubble-point pressures
74b17450/7b3b4080
XR0 1.030736564349 0.94381 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 83.370144 -78.478268 435.73777 -901.788 588.01298 -127.99414 0. 0. 0. 0. 0. 0.
VC1 0.27252351 -2.4234847 9.2542073 -18.121603 17.171072 -6.1334122 0. 0. 0. 0. 0. 0.
!
?Hydrogen chloride/Methanol [HCL/MEO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.08% from 138 bubble-point pressures
74b17450/c41aa690
XR0 0.900690009609 1.65053 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 443.50125 -108.516 408.21487 -367.89881 1483.3939 0. 0. 0. 0. 0. 0. 0.
VC2 -0.14099006 1.3649858 -5.2700636 9.5501623 -6.0876821 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen chloride/Hexane [HCL/C6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.93% from 6 bubble-point pressures
74b17450/cb03ba40
XR0 1.014810036187 1.01449 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 203.95749 -91.652751 970.04868 -1644.7127 1015.406 -89.943255 0. 0. 0. 0. 0. 0.
VC1 0.32603007 -2.0969732 6.9464848 -13.93683 13.899297 -5.2238925 0. 0. 0. 0. 0. 0.
!
?R23/R13 [R23/R13]
?E.W. Lemmon, NIST (2002)
20e26c20/126c90a0
KWT 1. 0.9350994 1. 0.9580030 -0.929 0. 0. 0. 0. 0. 0. 0.
TC1 -25.991077 -23.002542 -6.6503153 11.529489 32.891208 -22.741772 0. 0. 0. 0. 0. 0.
VC1 -0.00090156964 -0.06516735 0.22782787 -0.19311103 -0.22962158 0.23949632 0. 0. 0. 0. 0. 0.
PR1 0.1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R23/Carbon dioxide [R23/CO2]
?E.W. Lemmon, NIST (2002)
20e26c20/77c8bee0
XR0 1. 0.9797140 1. 1.0099333 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -11.844694 1.2740564 1.0931873 0.26061071 0.16557246 -0.50941053 0. 0. 0. 0. 0. 0.
VC1 0.041526502 -0.24505898 0.87260579 -1.558068 1.3861738 -0.48445064 0. 0. 0. 0. 0. 0.
!
?R23/R116 [R23/R116]
?E.W. Lemmon, NIST (2004)
20e26c20/04997260
XR0 1. 0.9090532 1. 1.0229397 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -34.655642 -41.615524 -30.706194 101.72167 -32.228406 -12.147235 0. 0. 0. 0. 0. 0.
VC1 0.042838059 -0.41679135 2.0210332 -3.8162344 2.7591931 -0.61917166 0. 0. 0. 0. 0. 0.
!
?R23/Sulfur hexafluoride [R23/SF6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.51% from 9 bubble-point pressures
20e26c20/7a75e610
XR0 0.994449974691 0.91843 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -6.625139 -161.27937 386.23603 -707.15258 701.49869 -260.66345 0. 0. 0. 0. 0. 0.
VC1 0.059558178 -0.61656501 2.1344973 -3.174777 2.1612576 -0.58279753 0. 0. 0. 0. 0. 0.
!
?R23/R32 [R23/R32]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.36% from 16 bubble-point pressures
20e26c20/7b05bb60
XR0 1.00116 1.00385 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 12.998433 -2.8586252 4.8522865 -5.7112393 2.5594525 -0.27340213 0. 0. 0. 0. 0. 0.
VC1 -0.019599602 0.083882011 -0.32571221 0.57775453 -0.51234875 0.17341329 0. 0. 0. 0. 0. 0.
!
?R23/R125 [R23/R125]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.42% from 19 bubble-point pressures
20e26c20/25c5a3a0
XR0 1.00316 1.00309 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 18.382669 0.65165196 2.1102952 -7.183096 6.8253324 -4.4267891 0. 0. 0. 0. 0. 0.
VC1 0.07892805 -0.49438358 1.6164036 -2.7968457 2.4066735 -0.79569242 0. 0. 0. 0. 0. 0.
!
?R23/Propylene [R23/PRY]
?E.W. Lemmon, NIST (2002)
20e26c20/56d778b0
XR0 1. 0.9107001 1. 1.0085527 0. 0. 0. 0. 0. 0. 0. 0.
TC1 26.261734 -200.8026 410.62979 -732.82557 631.10293 -195.87756 0. 0. 0. 0. 0. 0.
VC1 0.05527492 -0.82039281 3.1127159 -5.9842573 5.9266349 -2.2919042 0. 0. 0. 0. 0. 0.
!
?R23/R143a [R23/R143A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.72% from 16 bubble-point pressures
20e26c20/0deae990
XR0 1.008095 1.00381 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 22.733392 3.64523 -5.3534643 2.2220473 -13.125397 4.031293 0. 0. 0. 0. 0. 0.
VC1 0.072804784 -0.39580704 1.1112065 -1.692927 1.266485 -0.34800863 0. 0. 0. 0. 0. 0.
!
?R23/Propane [R23/C3]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.77% from 32 bubble-point pressures
20e26c20/70c6aac0
XR0 1.012002347845 0.87585 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 40.262105 -236.49615 457.58416 -961.48532 829.32843 -223.16022 0. 0. 0. 0. 0. 0.
VC1 0.082015261 -1.2142557 4.7022019 -10.063614 11.236106 -4.7825924 0. 0. 0. 0. 0. 0.
!
?R23/R22 [R23/R22]
?E.W. Lemmon, NIST (2002)
20e26c20/57716470
XR0 1. 0.9894644 1. 1.0038900 0. 0. 0. 0. 0. 0. 0. 0.
TC1 25.675694 -28.649235 44.94702 -62.84484 46.243669 -14.150169 0. 0. 0. 0. 0. 0.
VC1 0.029904188 -0.30968782 1.0304759 -1.8169304 1.5796755 -0.53421864 0. 0. 0. 0. 0. 0.
!
?R23/R12 [R23/R12]
?E.W. Lemmon, NIST (2002)
20e26c20/98829b70
XR0 1. 0.9266031 1. 1.0187876 0. 0. 0. 0. 0. 0. 0. 0.
TC1 47.05747 -133.02435 177.14624 -332.03279 303.36262 -104.00587 0. 0. 0. 0. 0. 0.
VC1 0.032174788 -0.57888778 1.9135545 -3.3588035 3.1220434 -1.0991827 0. 0. 0. 0. 0. 0.
!
?R23/R134a [R23/R134A]
?E.W. Lemmon, NIST (2002)
20e26c20/ff1c0560
XR0 1. 1.0105431 1. 1.0141263 0. 0. 0. 0. 0. 0. 0. 0.
TC1 38.993256 -1.7635694 26.459695 -34.022767 25.894136 -5.4900878 0. 0. 0. 0. 0. 0.
VC1 0.10647842 -0.74082625 2.4371812 -4.3101409 3.7838634 -1.3021004 0. 0. 0. 0. 0. 0.
!
?R23/R152a [R23/R152A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.14% from 16 bubble-point pressures
20e26c20/63f364b0
XR0 0.9996501 1.02378 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 41.271422 27.007192 -34.136645 96.656315 -119.7453 59.789906 0. 0. 0. 0. 0. 0.
VC1 0.034747946 -0.19644346 0.53994347 -1.1133972 1.1781746 -0.51739207 0. 0. 0. 0. 0. 0.
!
?R23/R227ea [R23/R227EA]
?E.W. Lemmon, NIST (2002)
20e26c20/40091ee0
XR0 1. 1.0091096 1. 1.0483990 0. 0. 0. 0. 0. 0. 0. 0.
TC1 56.055102 -55.349646 194.60353 -276.7705 218.21221 -56.259239 0. 0. 0. 0. 0. 0.
VC1 0.011485759 -0.020314663 -0.067652143 0.44024372 -0.70363321 0.37663007 0. 0. 0. 0. 0. 0.
!
?R23/Isobutane [R23/C4I]
?E.W. Lemmon, NIST (2002)
20e26c20/47ade7e0
XR0 1. 0.9040920 1. 1.0362036 0. 0. 0. 0. 0. 0. 0. 0.
TC1 100.1942 -299.63822 747.46384 -1708.8618 1826.651 -721.0466 0. 0. 0. 0. 0. 0.
VC1 0.16410123 -2.0482686 7.2192198 -13.169833 12.243056 -4.3581954 0. 0. 0. 0. 0. 0.
!
?R23/Butane [R23/C4]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2% from 37 bubble-point pressures
20e26c20/7b3b4080
XR0 1.024338277473 0.89836 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 113.35039 -383.58941 2082.8216 -5859.7785 6535.6174 -2583.9245 0. 0. 0. 0. 0. 0.
VC1 0.19660583 -2.5351364 9.8722184 -21.016649 21.505816 -7.9862849 0. 0. 0. 0. 0. 0.
!
?R23/R114 [R23/R114]
?E.W. Lemmon, NIST (2002)
20e26c20/b1698aa0
XR0 1. 0.9415606 1. 1.0521610 0. 0. 0. 0. 0. 0. 0. 0.
TC1 76.679568 11.199376 -204.92653 120.94499 106.15589 -92.241392 0. 0. 0. 0. 0. 0.
VC1 0.093626144 -0.8854813 1.8443882 -1.7950004 0.8789137 -0.091555152 0. 0. 0. 0. 0. 0.
!
?R23/R11 [R23/R11]
?E.W. Lemmon, NIST (2002)
20e26c20/6f9b71e0
XR0 1. 0.9362767 1. 1.0321197 0. 0. 0. 0. 0. 0. 0. 0.
TC1 122.72499 -109.23875 524.89378 -1901.9767 2300.4118 -911.12779 0. 0. 0. 0. 0. 0.
VC1 0.11700508 -2.0472517 7.5136307 -14.06708 12.729299 -4.3364281 0. 0. 0. 0. 0. 0.
!
?R23/Isopentane [R23/C5I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.02% from 26 bubble-point pressures
20e26c20/86ee46a0
XR0 1.029261916280 0.93001 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 196.83364 -593.27955 3297.6814 -8050.0537 7876.7709 -2733.6085 0. 0. 0. 0. 0. 0.
VC1 0.42395168 -4.3504346 16.648376 -33.287688 31.256083 -10.730538 0. 0. 0. 0. 0. 0.
!
?R23/Pentane [R23/C5]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.01% from 26 bubble-point pressures
20e26c20/76bc0290
XR0 1.034960981971 0.94007 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 218.30652 -789.98902 4511.9399 -10454.243 9643.7018 -3100.8855 0. 0. 0. 0. 0. 0.
VC1 0.34584145 -3.3418054 12.317045 -24.662812 22.69683 -7.3907888 0. 0. 0. 0. 0. 0.
!
?R23/R113 [R23/R113]
?E.W. Lemmon, NIST (2002)
20e26c20/d2a09ee0
XR0 1. 0.9469168 1. 1.0698503 0. 0. 0. 0. 0. 0. 0. 0.
TC1 209.79408 -337.32129 1443.6946 -4033.9408 4613.8484 -1797.2005 0. 0. 0. 0. 0. 0.
VC1 0.13367293 -2.3580608 8.4437239 -16.340998 15.894458 -5.9010611 0. 0. 0. 0. 0. 0.
!
?R23/Ethanol [R23/ETO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.5% from 9 bubble-point pressures
20e26c20/3d5f67e0
XR0 1.104764850802 1.05138 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 156.05437 435.59056 -98.532692 -457.54724 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.0030605666 0.9413457 -3.9760331 2.6793076 0. 0. 0. 0. 0. 0. 0. 0.
!
?R23/Toluene [R23/TOL]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.65% from 9 bubble-point pressures
20e26c20/a49b8b50
XR0 0.969090002199 1.07054 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 341.66934 148.72125 -1057.6449 2459.327 -2348.5738 865.84524 0. 0. 0. 0. 0. 0.
VC1 0.42031863 -4.6810841 18.884894 -40.555062 43.276467 -18.272091 0. 0. 0. 0. 0. 0.
!
?R13/Propylene [R13/PRY]
?E.W. Lemmon, NIST (2002)
126c90a0/56d778b0
XR0 1. 0.9573813 1. 1.0000414 0. 0. 0. 0. 0. 0. 0. 0.
TC1 11.830152 -95.432241 195.49243 -326.51919 277.95753 -90.712852 0. 0. 0. 0. 0. 0.
VC1 0.031666571 -0.56458629 2.1440728 -4.0506413 3.7315028 -1.3105688 0. 0. 0. 0. 0. 0.
!
?R13/Ammonia [R13/NH3]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.06% from 20 bubble-point pressures
126c90a0/e9847540
XR0 0.962843855612 0.76464 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 43.756288 -835.70353 1004.1763 -336.29886 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.009790522 -1.4819346 3.4508872 -1.9457398 0. 0. 0. 0. 0. 0. 0. 0.
!
?R13/R12 [R13/R12]
?E.W. Lemmon, NIST (2002)
126c90a0/98829b70
XR0 1. 0.9876934 1. 1.0026221 0. 0. 0. 0. 0. 0. 0. 0.
TC1 32.281299 -37.609309 52.194061 -73.671689 52.826962 -14.490434 0. 0. 0. 0. 0. 0.
VC1 -0.0059368789 -0.17038893 0.51264231 -0.96177497 0.91155218 -0.3550581 0. 0. 0. 0. 0. 0.
PR1 0.0337 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R13/Isobutane [R13/C4I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.48% from 35 bubble-point pressures
126c90a0/47ade7e0
XR0 1.004490070616 0.98045 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 71.500867 -140.70604 389.04633 -707.54083 607.42732 -203.95617 0. 0. 0. 0. 0. 0.
VC1 0.15374787 -1.735709 6.3858985 -12.07625 11.123126 -3.9583369 0. 0. 0. 0. 0. 0.
!
?R13/Butane [R13/C4]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.54% from 49 bubble-point pressures
126c90a0/7b3b4080
XR0 1.002707309736 0.98279 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 72.42503 -64.502608 166.67385 -395.72633 387.2827 -135.43678 0. 0. 0. 0. 0. 0.
VC1 0.13244349 -1.6473388 5.8652433 -11.074738 10.341179 -3.7745709 0. 0. 0. 0. 0. 0.
!
?R13/R11 [R13/R11]
?E.W. Lemmon, NIST (2002)
126c90a0/6f9b71e0
XR0 1. 1.0143855 1. 1.0087681 0. 0. 0. 0. 0. 0. 0. 0.
TC1 90.487632 37.514345 -167.70782 449.05756 -615.331 319.98226 0. 0. 0. 0. 0. 0.
VC1 0.019535761 -1.0661427 4.5639871 -10.186415 10.920389 -4.6321294 0. 0. 0. 0. 0. 0.
!
?R13/R113 [R13/R113]
?E.W. Lemmon, NIST (2002)
126c90a0/d2a09ee0
XR0 1. 1.0452965 1. 1.0322528 0. 0. 0. 0. 0. 0. 0. 0.
TC1 146.41081 34.697136 -232.92654 972.79933 -1407.1021 701.09009 0. 0. 0. 0. 0. 0.
VC1 0.1223839 -1.9679019 8.4076843 -18.513135 19.577619 -8.1428708 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R41 [CO2/R41]
?E.W. Lemmon, NIST (2002)
77c8bee0/8ee31230
KWT 1. 0.9941317 1. 0.9771864 -0.5483 0. 0. 0. 0. 0. 0. 0.
TC4 1.6307812 2.1221377 -6.9179744 4.7564803 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.0070070234 0.030351291 -0.10688398 0.095604093 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R116 [CO2/R116]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.28% from 77 bubble-point pressures
77c8bee0/04997260
XR0 1.03808 0.89857 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 -22.582177 -33.068959 -1.0819653 -174.35614 161.84014 0. 0. 0. 0. 0. 0. 0.
VC2 0.086316671 -0.22372117 -0.083927179 1.1051298 -1.060739 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Hydrogen sulfide [CO2/H2S]
?Kunz and Wagner (2012)
77c8bee0/c6c03020
KW0 1.016034583 0.92601888 0.906630564 1.024085837 0. 0. 0. 0. 0. 0. 0. 0.
TC1 2.6996099 -35.327602 -175.55981 317.21748 -246.10571 77.410804 0. 0. 0. 0. 0. 0.
VC1 -0.021259778 -0.078140616 0.22362099 -0.23030624 0.3172238 -0.20352428 0. 0. 0. 0. 0. 0.
PR1 0.0974 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R32 [CO2/R32]
?E.W. Lemmon, NIST (2002)
77c8bee0/7b05bb60
XR0 1. 0.9978225 1. 1.0058521 0. 0. 0. 0. 0. 0. 0. 0.
TC1 19.991596 11.563958 -86.779718 234.36023 -284.36318 131.80385 0. 0. 0. 0. 0. 0.
VC1 0.049510217 -0.21277213 0.30248328 0.31601486 -1.1088756 0.71957569 0. 0. 0. 0. 0. 0.
PR1 0.017 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Carbonyl sulfide [CO2/COS]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.61% from 56 bubble-point pressures
77c8bee0/e7f902e0
XR0 1.00023 0.9445 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 21.248652 -20.968213 -95.393007 122.82578 -55.489822 0. 0. 0. 0. 0. 0. 0.
VC2 0.050056058 -0.37698911 0.85096842 -0.9029262 0.40696635 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R125 [CO2/R125]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.34% from 37 bubble-point pressures
77c8bee0/25c5a3a0
XR0 1.0115 0.96741 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 20.47391 2.3928647 -84.27176 177.47969 -229.30598 111.64651 0. 0. 0. 0. 0. 0.
VC1 0.17434201 -1.1781787 3.7027808 -5.8353778 4.4058671 -1.1898407 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Propylene [CO2/PRY]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
77c8bee0/56d778b0
KW0 0.997 0.945 1.096 1.014 -0.362 0. 0. 0. 0. 0. 0. 0.
TC1 56.960898 -160.89533 485.49492 -741.73712 470.35678 -94.770901 0. 0. 0. 0. 0. 0.
VC1 0.15225809 -1.0466355 3.5457055 -6.2040042 5.0465593 -1.470663 0. 0. 0. 0. 0. 0.
PR1 0.0933 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R143a [CO2/R143A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.63% from 61 bubble-point pressures
77c8bee0/0deae990
XR0 1.02027 0.98474 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 28.440649 26.692475 -97.476537 195.97958 -278.90142 134.65479 0. 0. 0. 0. 0. 0.
VC1 0.14991504 -0.87202915 2.6788815 -4.4589358 3.6426407 -1.0715182 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Propane [CO2/C3]
?Kunz and Wagner (2007)
77c8bee0/70c6aac0
KW0 1.033620538 0.908772477 0.996898004 1.047596298 0. 0. 0. 0. 0. 0. 0. 0.
TC1 48.57998 -169.52443 533.6575 -1211.6094 1045.2649 -320.06654 0. 0. 0. 0. 0. 0.
VC1 0.13463218 -1.0657605 3.7372775 -7.3707777 7.4625108 -2.8161649 0. 0. 0. 0. 0. 0.
PR1 0.1241 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R22 [CO2/R22]
?E.W. Lemmon, NIST (2002)
77c8bee0/57716470
XR0 1. 1.0037903 1. 1.0261472 0. 0. 0. 0. 0. 0. 0. 0.
TC1 37.587891 20.982165 -144.16695 443.32831 -562.09093 269.42895 0. 0. 0. 0. 0. 0.
VC1 0.097583712 -0.60210716 1.7021897 -2.1695976 0.96939343 0.075853831 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R1216 [CO2/R1216]
?E.W. Lemmon, NIST (2013)
77c8bee0/edc3a7b0
XR0 1.005 0.99 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 41.306207 21.54718 -123.12846 391.8086 -545.72293 282.78308 0. 0. 0. 0. 0. 0.
VC1 0.22826954 -1.5858351 5.1337992 -8.4363496 6.6201932 -1.8855376 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R12 [CO2/R12]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.93% from 25 bubble-point pressures
77c8bee0/98829b70
XR0 1.01811 0.9576 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 61.563545 -50.518211 117.80494 -221.29219 59.613811 41.413349 0. 0. 0. 0. 0. 0.
VC1 0.11583021 -0.94180416 3.0956746 -5.3264321 4.3135379 -1.1738744 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R1234yf [CO2/R1234YF]
?E.W. Lemmon, NIST (2013); based on simulation data from Gabriele Raabe
77c8bee0/40377b40
KW0 1.017 1. 1. 1.015 -0.657 0. 0. 0. 0. 0. 0. 0.
TC1 100.09245 -60.854081 147.43601 134.44467 -586.74873 390.41195 0. 0. 0. 0. 0. 0.
VC1 0.24279221 -1.5729101 5.2164944 -9.1773252 7.7025515 -2.3930602 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R134a [CO2/R134A]
?E.W. Lemmon, NIST (2013)
77c8bee0/ff1c0560
XR0 1. 1.008 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 49.093631 53.934432 -250.9285 683.1532 -834.73689 391.16822 0. 0. 0. 0. 0. 0.
VC1 0.20946816 -1.3603262 4.0156276 -5.8967106 3.9314947 -0.83680246 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Dimethyl ether [CO2/DME]
?I. Cullimore and E.W. Lemmon, NIST (2010)
77c8bee0/8f27e300
XR0 1. 1.028 1. 1.0194 0. 0. 0. 0. 0. 0. 0. 0.
TC1 62.859956 46.212643 -223.57012 751.82786 -990.71716 480.84126 0. 0. 0. 0. 0. 0.
VC1 0.06904102 -0.4674217 1.6186686 -3.0642863 2.8289019 -1.0383734 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R152a [CO2/R152A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.86% from 164 bubble-point pressures
77c8bee0/63f364b0
XR0 1.00224 1.00646 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 48.274479 93.808115 -346.39491 813.06818 -960.04452 440.48921 0. 0. 0. 0. 0. 0.
VC1 0.13476199 -0.57746423 0.74644932 0.49553232 -2.0335959 1.2975092 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R1234ze(E) [CO2/R1234ZEE]
?E.W. Lemmon, NIST (2013); based on simulation data from Gabriele Raabe
77c8bee0/9905ef70
KW0 1. 1.023 1. 1. -0.084 0. 0. 0. 0. 0. 0. 0.
TC1 77.751312 -15.252326 -39.746467 517.36041 -868.37266 475.56774 0. 0. 0. 0. 0. 0.
VC1 0.2774201 -2.3186144 8.5288064 -15.493571 13.353162 -4.3399534 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R227ea [CO2/R227EA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.4% from 224 bubble-point pressures
77c8bee0/40091ee0
XR0 1.00608 1.00235 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 67.427648 -4.3127871 -83.322612 539.75595 -869.56082 469.17438 0. 0. 0. 0. 0. 0.
VC1 0.072469112 -0.3188513 0.37013484 0.61175201 -1.8350497 1.1749626 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R124 [CO2/R124]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.56% from 19 bubble-point pressures
77c8bee0/36953260
XR0 0.99517 1.01028 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 78.847896 34.326727 -300.03662 1002.476 -1290.1115 622.51507 0. 0. 0. 0. 0. 0.
VC1 0.22368689 -1.7316022 5.6689507 -9.2766055 7.2224967 -2.09014 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Isobutane [CO2/C4I]
?Kunz and Wagner (2007)
77c8bee0/47ade7e0
KW0 1.023339824 0.929982936 1.076551882 1.081909003 0. 0. 0. 0. 0. 0. 0. 0.
TC1 96.778936 -258.36519 1051.7857 -1945.8096 1443.4482 -386.90202 0. 0. 0. 0. 0. 0.
VC1 0.27833133 -2.430942 9.2524376 -17.702726 15.901943 -5.2221451 0. 0. 0. 0. 0. 0.
PR1 0.12 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Sulfur dioxide [CO2/SO2]
?T. Neumann, Development of New Helmholtz Models for Binary Mixtures Relevant for CCS; Master's thesis, Lehrstuhl Fuer Thermodynamik, Ruhr Universitaet, Bochum, Germany, 2017.
77c8bee0/7fad4b80
XR0 1.020063 1.0079753 0.8898650 1.0057783 0. 0. 0. 0. 0. 0. 0. 0.
TC1 80.373621 70.401317 -361.91147 527.0854 -444.65537 204.83788 0. 0. 0. 0. 0. 0.
VC1 0.0081604458 -0.30413534 0.77418579 -1.2573493 1.2318384 -0.48447047 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R142b [CO2/R142B]
?E.W. Lemmon, NIST (2002)
77c8bee0/f2a8b2e0
XR0 1. 0.9888000 1. 1.0626246 0. 0. 0. 0. 0. 0. 0. 0.
TC1 70.847667 99.665432 -528.26086 1333.8322 -1584.5092 733.44497 0. 0. 0. 0. 0. 0.
VC1 0.19824707 -1.3408742 3.8384223 -5.3879515 3.4064145 -0.65129412 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Butene [CO2/1BE]
?I. Cullimore and E.W. Lemmon, NIST (2010)
77c8bee0/cd7a06d0
XR0 1.0199 0.968 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 89.720287 53.31431 -186.32671 494.08375 -885.25114 498.74983 0. 0. 0. 0. 0. 0.
VC1 0.1996978 -1.4411311 4.0278714 -5.8168877 3.6501862 -0.55061835 0. 0. 0. 0. 0. 0.
PR1 0.0593 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Perfluorobutane [CO2/C4F10]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.49% from 83 bubble-point pressures
77c8bee0/a8f85e00
XR0 1.0416341 0.95201 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 65.454283 71.870638 87.569612 -284.87772 -178.88494 285.45627 0. 0. 0. 0. 0. 0.
VC1 0.34118467 -1.5517587 3.0523228 -4.2985975 3.660475 -1.0979154 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Butane [CO2/C4]
?Kunz and Wagner (2007)
77c8bee0/7b3b4080
KW0 1.018171004 0.911498231 1.174760923 1.222437324 0. 0. 0. 0. 0. 0. 0. 0.
TC1 69.746117 -182.62618 1168.0229 -2414.7119 1902.7409 -543.17459 0. 0. 0. 0. 0. 0.
VC1 0.23571428 -1.5299442 5.7602793 -11.54968 10.599205 -3.4165077 0. 0. 0. 0. 0. 0.
PR1 0.1333 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Neopentane [CO2/C5A]
?I. Cullimore and E.W. Lemmon, NIST (2010)
77c8bee0/5a410790
XR0 1.0573 0.9567 1. 1.0801 0. 0. 0. 0. 0. 0. 0. 0.
TC1 119.80989 -29.229938 402.70058 -327.24378 -846.55177 749.46817 0. 0. 0. 0. 0. 0.
VC1 0.4909663 -3.8691671 14.171149 -27.158146 24.579131 -8.1122179 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/R123 [CO2/R123]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.26% from 18 bubble-point pressures
77c8bee0/efdfede0
XR0 0.98639 1.05886 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 127.2964 243.49022 -942.9386 2421.0995 -2722.4428 1217.0667 0. 0. 0. 0. 0. 0.
VC1 0.42834085 -3.4653431 12.612315 -24.329669 23.34767 -8.8525688 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Isopentane [CO2/C5I]
?Miyamoto et al. (2017)
77c8bee0/86ee46a0
GG0 1.019180957 0.961218039 1.060793104 1.116793198 0. 0. 0. 0. 0. 0. 0. 0.
KW5 1.0048 0.9852 1.1167 1.005 0.8202 0. 0. 0. 0. 0. 0. 0.
TC1 90.061147 50.171938 325.25612 -174.87437 -525.91332 346.91386 0. 0. 0. 0. 0. 0.
VC1 0.61597968 -4.277879 14.921178 -26.89283 22.554166 -6.8858441 0. 0. 0. 0. 0. 0.
PR1 0.1219 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Diethyl ether [CO2/DEE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.61% from 61 bubble-point pressures
77c8bee0/46a701e0
XR0 1.01217 1.03241 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 145.71719 198.80342 -669.53422 2038.2396 -2808.7355 1358.566 0. 0. 0. 0. 0. 0.
VC1 0.09568237 -0.79404483 2.5791406 -5.5494138 5.8339667 -2.359402 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Pentane [CO2/C5]
?Kunz and Wagner (2007)
77c8bee0/76bc0290
KW0 1.027000795 0.979217302 1.024311498 1.068406078 0. 0. 0. 0. 0. 0. 0. 0.
TC1 155.69816 17.353023 517.53418 -888.3354 -73.013561 451.52678 0. 0. 0. 0. 0. 0.
VC1 0.39134116 -2.575229 8.4889764 -16.625833 15.946646 -5.702706 0. 0. 0. 0. 0. 0.
PR1 0.1222 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Novec649 [CO2/N649]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.66% from 26 bubble-point pressures
77c8bee0/a9e22c00
XR0 1.04359 1.03509 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 147.85872 230.3203 -850.80376 3519.559 -5438.1583 2750.1507 0. 0. 0. 0. 0. 0.
VC1 1.1941758 -10.159977 39.652878 -78.696253 74.212078 -26.389293 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Cyclopentane [CO2/CC5]
?I. Cullimore and E.W. Lemmon, NIST (2010)
77c8bee0/43ab1810
XR0 1.0223 0.9782 1. 1.045 0. 0. 0. 0. 0. 0. 0. 0.
TC1 190.91582 -7.220297 847.13738 -1569.7966 -155.9802 905.94715 0. 0. 0. 0. 0. 0.
VC1 0.080240372 -0.68102056 1.7966719 -3.9515675 3.9909776 -1.3661816 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Acetone [CO2/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
77c8bee0/342481e0
KW0 0.978377849525 1.0433 1. 1.1177 1.6093 0. 0. 0. 0. 0. 0. 0.
TC5 119.86178 -425.52689 581.189 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.31977264 0.3441259 -0.043486214 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Methanol [CO2/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
77c8bee0/c41aa690
KW0 0.996 1.015 1.026 1.236 1.77 0. 0. 0. 0. 0. 0. 0.
TC4 -76.895048 1393.7976 -3400.644 2170.3686 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.23738619 1.1498989 -2.8917741 1.8767096 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.023 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Hexane [CO2/C6]
?Kunz and Wagner (2007)
77c8bee0/cb03ba40
KW0 1. 1.038675574 1. 0.851343711 0. 0. 0. 0. 0. 0. 0. 0.
TC1 238.83871 343.98533 -1457.062 4444.2708 -6078.7681 2855.2065 0. 0. 0. 0. 0. 0.
VC1 0.45512662 -3.1568508 8.7198006 -14.979581 13.680909 -5.1569253 0. 0. 0. 0. 0. 0.
PR1 0.11 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Benzene [CO2/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
77c8bee0/f2cfb460
KW2 0.99 0.966 1.044 1.152 2.894 0. 0. 0. 0. 0. 0. 0.
TC4 49.755802 36.039892 204.69556 -462.24029 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.73200407 2.6122009 -4.4063222 2.3304192 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0774 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Cyclohexane [CO2/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
77c8bee0/6e225350
KW0 1. 1. 1.19 1.0106 0.0184 0. 0. 0. 0. 0. 0. 0.
TC1 188.03347 887.07952 -4309.8782 12159.812 -15595.978 6949.4113 0. 0. 0. 0. 0. 0.
VC1 0.34773244 -2.2906896 6.3608677 -11.494948 10.617889 -4.0323489 0. 0. 0. 0. 0. 0.
PR1 0.1052 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Dimethyl carbonate [CO2/DMC]
?I. Cullimore and E.W. Lemmon, NIST (2010)
77c8bee0/859e6f80
KW0 0.967 1.0856 1. 0.9916 1.5222 0. 0. 0. 0. 0. 0. 0.
TC1 219.14254 -552.20115 1035.406 -507.93459 -419.54506 634.93247 0. 0. 0. 0. 0. 0.
VC1 -0.10702768 -2.3504474 11.409476 -24.446884 25.184427 -10.188692 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Heptane [CO2/C7]
?Kunz and Wagner (2007)
77c8bee0/b398a3b0
KW0 1.011806317 1.046169823 1.205469976 1.164585914 0. 0. 0. 0. 0. 0. 0. 0.
TC1 252.13856 256.62019 -1060.6139 4835.5857 -6819.225 2980.6068 0. 0. 0. 0. 0. 0.
VC1 0.69473153 -5.1651425 20.529231 -43.639835 43.933087 -16.92816 0. 0. 0. 0. 0. 0.
PR1 0.1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Water [CO2/H2O]
?J. Gernert and R. Span, J. Chem. Thermodyn., 93:274-293, 2016. DOI:10.1016/j.jct.2015.05.015
77c8bee0/b43a7600
GG0 0.997372205 0.775453996 0.949055959 1.542328793 0. 0. 0. 0. 0. 0. 0. 0.
KWG 1.030538 0.828472 1.021392 0.895156 1. 0. 0. 0. 0. 0. 0. 0.
TC5 330.60568 22.81513 -565.24879 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.044830796 -0.23329959 0.055111106 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.12 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Methylcyclohexane [CO2/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
77c8bee0/0429edd0
XR0 1.024 1.016 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 208.22087 931.38105 -3841.2509 12869.143 -19993.416 10330.157 0. 0. 0. 0. 0. 0.
VC1 0.19905253 0.63496418 -6.3422118 11.777777 -9.8130823 3.2311773 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Toluene [CO2/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
77c8bee0/a49b8b50
KW0 1. 1.024 1.047 1.134 1.257 0. 0. 0. 0. 0. 0. 0.
TC1 253.32692 35.527214 -1880.3559 10592.541 -18302.152 9813.6702 0. 0. 0. 0. 0. 0.
VC1 0.063063069 -1.88036 9.056062 -19.99178 18.871065 -6.4208404 0. 0. 0. 0. 0. 0.
PR1 0.1056 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Octane [CO2/C8]
?Kunz and Wagner (2007)
77c8bee0/f174a9b0
KW0 1.02969078 1.074455386 1.026169373 1.104043935 0. 0. 0. 0. 0. 0. 0. 0.
TC1 268.57286 1135.1143 -5841.8854 17590.095 -22773.713 10287.006 0. 0. 0. 0. 0. 0.
VC1 1.0515967 -8.3564042 30.248257 -58.629117 55.076651 -19.886552 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Ethylbenzene [CO2/EBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.99% from 95 bubble-point pressures
77c8bee0/a4c64370
XR0 1.00091 1.09145 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 306.91026 1614.4184 -8823.0011 23923.584 -28400.284 11858.147 0. 0. 0. 0. 0. 0.
VC1 0.80270805 -6.6546436 22.793889 -42.640317 40.168266 -15.240129 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/p-Xylene [CO2/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.98% from 119 bubble-point pressures
77c8bee0/01b0e650
XR0 1.0034 1.1043 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 341.28341 1435.3697 -8646.6789 24747.837 -29898.096 12503.161 0. 0. 0. 0. 0. 0.
VC1 0.73449812 -5.5987485 18.753984 -35.241572 33.455377 -12.892755 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/o-Xylene [CO2/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.93% from 102 bubble-point pressures
77c8bee0/32008e80
XR0 1.00114 1.10292 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 352.31339 1468.7481 -9552.1465 27926.753 -34343.214 14649.709 0. 0. 0. 0. 0. 0.
VC1 0.46710273 -3.8683216 13.119395 -25.168479 24.127419 -9.4595587 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Nonane [CO2/C9]
?Kunz and Wagner (2012)
77c8bee0/7f94dc20
KW0 1.00768862 1.140671202 1. 0.973386152 0. 0. 0. 0. 0. 0. 0. 0.
TC1 327.70023 712.60753 -1495.7923 3844.0872 -3554.0105 775.45487 0. 0. 0. 0. 0. 0.
VC1 0.95816702 -6.0907761 20.133423 -41.272914 43.087084 -17.710643 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Decane [CO2/C10]
?Kunz and Wagner (2012)
77c8bee0/111888d0
KW0 1.02002879 1.145512213 1.000151132 1.183394668 0. 0. 0. 0. 0. 0. 0. 0.
TC1 342.6571 1404.5778 -6377.3233 18832.606 -23324.739 10112.902 0. 0. 0. 0. 0. 0.
VC1 1.2201135 -8.1227045 28.783465 -58.389569 58.044045 -22.198418 0. 0. 0. 0. 0. 0.
PR1 0.1141 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Undecane [CO2/C11]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.25% from 42 bubble-point pressures
77c8bee0/62f46c40
XR0 1.0061476 1.19119 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 386.98708 384.82053 962.71781 -3282.0315 6583.2342 -4426.7128 0. 0. 0. 0. 0. 0.
VC1 1.3523211 -9.1145211 30.998647 -62.027512 62.564324 -24.911492 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Dodecane [CO2/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
77c8bee0/8bc8dec0
KW0 1. 1.258 1. 1. -1.539 0. 0. 0. 0. 0. 0. 0.
TC1 627.13524 -1577.5707 13169.286 -33894.934 40473.224 -17754.108 0. 0. 0. 0. 0. 0.
VC1 1.9005197 -11.332664 39.10756 -85.354904 93.898603 -39.627362 0. 0. 0. 0. 0. 0.
!
?Carbon dioxide/Methyl stearate [CO2/MSTRT]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.01% from 26 bubble-point pressures
77c8bee0/81403130
XR0 0.90151 1.45262 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 435.61703 2384.3501 -8547.2965 14009.818 -5170.5571 0. 0. 0. 0. 0. 0. 0.
VC2 1.742734 -17.781646 50.706394 -55.112882 18.778695 0. 0. 0. 0. 0. 0. 0.
!
?R41/R40 [R41/R40]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.48% from 11 bubble-point pressures
8ee31230/2b938200
XR0 1.004843344923 0.9981 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 30.796016 1.0372895 8.4032484 -30.025009 25.912839 -9.8522457 0. 0. 0. 0. 0. 0.
VC1 -0.025848495 0.0095768773 -0.078702453 0.20665132 -0.27071667 0.14202927 0. 0. 0. 0. 0. 0.
!
?R41/Toluene [R41/TOL]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.19% from 9 bubble-point pressures
8ee31230/a49b8b50
XR0 0.975390031650 1.09707 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 297.00563 9.3929526 -10.718479 365.72359 -87.071847 -34.762836 0. 0. 0. 0. 0. 0.
VC1 0.34020768 -3.5353914 14.177116 -29.636496 30.640111 -12.564784 0. 0. 0. 0. 0. 0.
!
?R116/Propylene [R116/PRY]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.25% from 13 bubble-point pressures
04997260/56d778b0
XR0 0.986183568209 0.87937 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 8.4975331 -275.34918 536.44886 -900.59909 858.8047 -302.16133 0. 0. 0. 0. 0. 0.
VC1 -0.014410172 -0.8216747 3.074005 -5.5502263 5.3155202 -1.9965267 0. 0. 0. 0. 0. 0.
!
?R116/R143a [R116/R143A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.38% from 78 bubble-point pressures
04997260/0deae990
XR0 1.01003 0.93499 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.2885043 -53.49343 25.291004 -83.530554 73.194643 -9.4476087 0. 0. 0. 0. 0. 0.
VC1 -0.0083126298 -0.34421814 1.3406891 -2.9811878 3.3141999 -1.3182122 0. 0. 0. 0. 0. 0.
!
?R116/Propane [R116/C3]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.7% from 61 bubble-point pressures
04997260/70c6aac0
XR0 0.983661384405 0.89173 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 18.303631 -250.59657 410.27764 -603.56106 550.71817 -191.48342 0. 0. 0. 0. 0. 0.
VC1 -0.005036463 -0.80352892 2.4983271 -3.5098433 2.6392126 -0.82094811 0. 0. 0. 0. 0. 0.
!
?R116/R22 [R116/R22]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.58% from 12 bubble-point pressures
04997260/57716470
XR0 0.996709960093 0.91302 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 1.8873198 -121.29734 121.22956 -166.6943 148.57695 -43.136364 0. 0. 0. 0. 0. 0.
VC1 -0.056778866 -0.074853328 -0.090202332 0.67209656 -0.95508238 0.51035882 0. 0. 0. 0. 0. 0.
!
?R116/R134a [R116/R134A]
?E.W. Lemmon, NIST (2002)
04997260/ff1c0560
XR0 1. 0.9428520 1. 1.0010759 0. 0. 0. 0. 0. 0. 0. 0.
TC1 21.339961 -66.150972 -17.584772 47.975901 -29.979616 7.9695752 0. 0. 0. 0. 0. 0.
VC1 0.0089586636 -0.63026086 1.8016924 -2.7356533 2.1896558 -0.6903768 0. 0. 0. 0. 0. 0.
!
?Sulfur hexafluoride/R32 [SF6/R32]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.48% from 12 bubble-point pressures
7a75e610/7b05bb60
XR0 1.0017029 0.86502 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 -41.212559 -115.82245 -18.910452 125.20551 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.059208094 -0.16506803 0.66348643 -0.43344043 0. 0. 0. 0. 0. 0. 0. 0.
!
?Sulfur hexafluoride/Propane [SF6/C3]
?E.W. Lemmon, NIST (2008)
7a75e610/70c6aac0
XR0 0.990884850262 0.89338144 1.007559212995 1.0150842 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -5.0284792 -189.81255 309.1569 -474.68575 428.05391 -135.27851 0. 0. 0. 0. 0. 0.
VC1 0.016151485 -0.48354094 1.3536696 -1.2431276 0.41006 -0.061672576 0. 0. 0. 0. 0. 0.
!
?Sulfur hexafluoride/Pentane [SF6/C5]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7a75e610/76bc0290
XR0 1.041666666667 0.9293 1. 1.0605 0. 0. 0. 0. 0. 0. 0. 0.
TC1 128.31981 -568.86918 3676.3879 -9705.2045 10252.072 -3831.6525 0. 0. 0. 0. 0. 0.
VC1 0.21138734 -2.2682187 9.8506735 -23.995943 25.624861 -9.3311607 0. 0. 0. 0. 0. 0.
!
?Sulfur hexafluoride/R113 [SF6/R113]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.14% from 22 bubble-point pressures
7a75e610/d2a09ee0
XR0 0.9296359 1.06961 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 131.83286 60.607899 -1219.5738 3990.7908 -4816.4471 2272.4024 0. 0. 0. 0. 0. 0.
VC1 0.13042527 -2.8638234 13.384068 -28.919806 30.37022 -12.645903 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Carbonyl sulfide [H2S/COS]
?I. Cullimore and E.W. Lemmon, NIST (2010)
c6c03020/e7f902e0
XR0 1. 0.9442 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -26.150072 -27.557928 -8.3371949 29.508219 -5.1532332 -4.0298351 0. 0. 0. 0. 0. 0.
VC1 0.020301087 -0.10506938 0.30438244 -0.44107231 0.28138815 -0.063593106 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Propane [H2S/C3]
?Kunz and Wagner (2012)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
c6c03020/70c6aac0
KW0 1.007482008719 0.905829247 1.067450922575 1.010593999 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -24.030729 -110.44448 229.74459 -494.15645 475.62281 -149.59468 0. 0. 0. 0. 0. 0.
VC1 0.11490218 -0.73821456 2.4556853 -3.9417142 2.8617302 -0.79832959 0. 0. 0. 0. 0. 0.
PR1 0.0878 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Isobutane [H2S/C4I]
?Kunz and Wagner (2012)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
c6c03020/47ade7e0
KW0 1.026114040008 0.937130844 0.987172258206 0.988591117 0. 0. 0. 0. 0. 0. 0. 0.
TC1 30.944788 -87.143027 164.02585 -351.07443 202.86918 -16.392898 0. 0. 0. 0. 0. 0.
VC1 0.27852708 -2.4896149 9.55885 -18.421834 17.405579 -6.3521805 0. 0. 0. 0. 0. 0.
PR1 0.0474 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Butane [H2S/C4]
?Kunz and Wagner (2012)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
c6c03020/7b3b4080
KW0 1.014236959828 0.926156602 1.101184346559 1.033366041 0. 0. 0. 0. 0. 0. 0. 0.
TC1 17.203555 -26.127722 -3.7955167 59.188035 -221.99002 114.21677 0. 0. 0. 0. 0. 0.
VC1 0.23763208 -1.6790565 6.1256978 -11.669595 10.912851 -3.9568455 0. 0. 0. 0. 0. 0.
PR1 0.063 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Neopentane [H2S/C5A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.85% from 60 bubble-point pressures
c6c03020/5a410790
XR0 1.025479998987 0.93089 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 49.456848 -24.352993 21.651884 -202.93621 106.79302 5.8039199 0. 0. 0. 0. 0. 0.
VC1 0.4476222 -3.5816601 12.947433 -24.255612 22.524484 -8.0869594 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Isopentane [H2S/C5I]
?Kunz and Wagner (2012)
c6c03020/86ee46a0
KW0 1. 0.982651529 1. 0.835763343 0. 0. 0. 0. 0. 0. 0. 0.
TC1 100.79812 -5.0958874 -13.916441 16.336031 -31.488959 -19.09259 0. 0. 0. 0. 0. 0.
VC1 0.46371661 -4.2731574 15.624727 -29.097766 26.32154 -9.1670615 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Pentane [H2S/C5]
?Kunz and Wagner (2012)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
c6c03020/76bc0290
KW0 1.039493852730 0.959065662 1.015627250328 1.076539234 0. 0. 0. 0. 0. 0. 0. 0.
TC1 70.765149 18.262554 231.86261 -549.24857 206.01376 38.044355 0. 0. 0. 0. 0. 0.
VC1 0.2526479 -1.1775955 3.5634901 -7.0647943 7.1116392 -2.6209458 0. 0. 0. 0. 0. 0.
PR1 0.063 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Acetone [H2S/ACT]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.01% from 2 bubble-point pressures
c6c03020/342481e0
XR0 1.042122595302 1.04871 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 126.30176 152.66283 -258.76138 1230.5668 -2093.4778 981.4661 0. 0. 0. 0. 0. 0.
VC1 0.33503677 -2.3447104 8.4197095 -16.07665 14.460502 -4.8745143 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Methanol [H2S/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c6c03020/c41aa690
XR0 1. 1.042 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 105.26876 136.62787 -397.28454 484.67673 -196.09959 0. 0. 0. 0. 0. 0. 0.
VC2 0.24192933 -1.0860251 1.3501564 -0.47419877 -0.13461321 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Hexane [H2S/C6]
?Kunz and Wagner (2012)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
c6c03020/cb03ba40
KW0 1.014310796409 0.956075596 1.325426794917 1.339283552 0. 0. 0. 0. 0. 0. 0. 0.
TC1 73.220993 -151.90236 1481.8145 -3003.787 2862.9372 -1150.4409 0. 0. 0. 0. 0. 0.
VC1 0.25043466 -0.2833749 1.9862926 -6.7493919 7.8376031 -3.0728025 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Benzene [H2S/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c6c03020/f2cfb460
XR0 0.994 1.06 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 176.14608 -35.526737 361.18724 -206.5172 -185.12715 225.37428 0. 0. 0. 0. 0. 0.
VC1 0.18306099 -1.4294576 5.5346374 -11.697018 12.024181 -4.8341424 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Cyclohexane [H2S/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
c6c03020/6e225350
XR0 1.011 1.0138 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 147.94852 176.51923 -333.35903 649.36465 -780.7265 370.40736 0. 0. 0. 0. 0. 0.
VC1 0.26946893 -1.6560741 4.4806209 -7.5005448 6.7248352 -2.4373679 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Heptane [H2S/C7]
?Kunz and Wagner (2012)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
c6c03020/b398a3b0
KW0 1.011186332734 1.013453092 1.206320398959 1.087956749 0. 0. 0. 0. 0. 0. 0. 0.
TC1 178.35502 -100.3981 1189.5163 -2446.972 2813.9272 -1365.9656 0. 0. 0. 0. 0. 0.
VC1 0.57849897 -3.8616958 14.157254 -27.807007 26.151813 -9.4922049 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Isooctane [H2S/C8I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.81% from 19 bubble-point pressures
c6c03020/c2dd9ef0
XR0 1.022960031008 1.01015 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 164.88428 207.6418 -84.502546 414.08928 -1098.8472 713.15424 0. 0. 0. 0. 0. 0.
VC1 0.78788876 -5.2567033 16.860771 -30.749639 28.369537 -10.141303 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Water [H2S/H2O]
?Kunz and Wagner (2012)
c6c03020/b43a7600
KW0 1. 0.940587083 1. 1.014832832 0. 0. 0. 0. 0. 0. 0. 0.
TC5 238.58338 -517.99629 266.11354 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 0.00055598344 -0.38142953 0.26399479 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.04 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Methylcyclohexane [H2S/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c6c03020/0429edd0
XR0 1.012 1.017 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 145.09323 237.11221 -95.105604 336.46631 -897.03499 578.09933 0. 0. 0. 0. 0. 0.
VC1 0.089885319 0.51849461 -2.9957411 4.0187259 -1.7573956 -0.017320014 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Toluene [H2S/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c6c03020/a49b8b50
XR0 1. 1.075 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 222.82623 196.99318 -569.5918 1961.7922 -2406.3954 1043.6056 0. 0. 0. 0. 0. 0.
VC1 0.31757775 -2.6055003 9.7493976 -19.571463 19.301866 -7.4991042 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Octane [H2S/C8]
?Mixing rules of nonane/Hydrogen sulfide used as an estimate.
c6c03020/f174a9b0
GG0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
XR0 1. 1.086557826 1. 1.082905109 0. 0. 0. 0. 0. 0. 0. 0.
TC1 199.89753 304.08774 -860.81245 2710.977 -3364.2036 1692.5691 0. 0. 0. 0. 0. 0.
VC1 0.8013395 -5.8567167 20.953775 -40.02032 37.93758 -14.055635 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/m-Xylene [H2S/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.33% from 30 bubble-point pressures
c6c03020/0f99ff70
XR0 0.972370008958 1.10582 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 320.4291 -385.37401 1655.0708 -2565.6668 2467.6512 -802.91806 0. 0. 0. 0. 0. 0.
VC1 0.58744495 -5.4810405 22.236917 -45.431012 45.094603 -17.483858 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Nonane [H2S/C9]
?Kunz and Wagner (2012)
c6c03020/7f94dc20
KW0 1. 1.086557826 1. 1.082905109 0. 0. 0. 0. 0. 0. 0. 0.
TC1 228.3432 432.50092 -1167.4288 3564.6835 -4512.2862 2243.8126 0. 0. 0. 0. 0. 0.
VC1 0.73134518 -4.4799713 15.059407 -29.375299 28.898323 -11.095746 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Propylcyclohexane [H2S/C3CC6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.4% from 35 bubble-point pressures
c6c03020/206f01b0
XR0 0.995767986059 1.10114 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 223.05366 417.67747 -417.12791 1256.2743 -1316.1813 573.55233 0. 0. 0. 0. 0. 0.
VC1 0.17828137 0.32519971 -1.8973397 -0.18105047 4.476508 -3.3202141 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Decane [H2S/C10]
?Kunz and Wagner (2012)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
c6c03020/111888d0
KW0 1.027652681588 1.103693489 1.025443545197 1.171714677 0. 0. 0. 0. 0. 0. 0. 0.
TC1 256.91719 587.89839 -1815.6851 6792.3525 -9575.4624 4674.1681 0. 0. 0. 0. 0. 0.
VC1 0.89268488 -5.3089214 19.965388 -42.787094 43.638304 -16.653424 0. 0. 0. 0. 0. 0.
PR1 0.0333 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Ethylene glycol [H2S/EGLY]
?I. Cullimore and E.W. Lemmon, NIST (2010)
c6c03020/7d1768e0
XR0 0.9877 1.1981 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC5 248.61001 212.30144 -6.5418828 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.1847079 0.46633841 -0.75871675 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen sulfide/Dodecane [H2S/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
c6c03020/8bc8dec0
KW0 1. 1.214 1. 1. -1.808 0. 0. 0. 0. 0. 0. 0.
TC1 491.78046 -199.34419 3144.6338 -5212.4477 4044.9486 -708.23681 0. 0. 0. 0. 0. 0.
VC1 1.4388667 -8.9586685 34.719361 -78.9006 86.014773 -35.226973 0. 0. 0. 0. 0. 0.
!
?R32/R125 [R32/R125]
?E.W. Lemmon and R.T Jacobsen, J. Phys. Chem. Ref. Data, 33(2):593-620, 2004.
7b05bb60/25c5a3a0
KWR 1. 1.0420901 1. 1.0050934 1. 0. 0. 0. 0. 0. 0. 0.
TC1 -11.566079 4.0218636 34.221971 -134.14745 128.37804 -45.181648 0. 0. 0. 0. 0. 0.
VC1 0.1214775 -0.36100107 -0.34839302 2.9351907 -4.1655762 2.0164084 0. 0. 0. 0. 0. 0.
TRN 0. 0. 0. 0. 0. -0.15 0.16 0. 0. 0. 0. 0.
!
?R32/Propylene [R32/PRY]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.36% from 80 bubble-point pressures
7b05bb60/56d778b0
XR0 1.003673444808 0.90627 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 -25.649706 -80.463964 -12.220367 58.057772 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.057236416 -0.4713871 1.1781818 -0.87909036 0. 0. 0. 0. 0. 0. 0. 0.
!
?R32/R143a [R32/R143A]
?E.W. Lemmon, NIST (2002)
7b05bb60/0deae990
XR0 1. 0.9748252 1. 1.0178106 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -13.456033 -6.5073042 0.54255739 4.0029255 -2.3371672 0.36184696 0. 0. 0. 0. 0. 0.
VC1 0.032856941 -0.069228442 0.17847639 -0.25546696 0.19186406 -0.060422208 0. 0. 0. 0. 0. 0.
!
?R32/Propane [R32/C3]
?E.W. Lemmon, NIST (2006)
7b05bb60/70c6aac0
XR0 1. 0.8616194 1. 1.0198058 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -16.052002 -278.73842 713.91667 -1705.1962 2010.8509 -812.94023 0. 0. 0. 0. 0. 0.
VC1 0.037566168 -0.18208024 -1.3916158 7.5056426 -10.910205 4.8638956 0. 0. 0. 0. 0. 0.
TRN 0.2857 -0.4346 0. 0. 0.18 -0.08 0.09 0. 0. 0. 0. 0.
!
?R32/R22 [R32/R22]
?E.W. Lemmon, NIST (2002)
7b05bb60/57716470
XR0 1. 0.9933028 1. 1.0073196 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -0.21716899 -1.8849269 -0.0023411869 0.66392322 -0.37908511 0.011875531 0. 0. 0. 0. 0. 0.
VC1 0.018569246 -0.063529253 0.15289279 -0.17048337 0.073158249 0.0087549466 0. 0. 0. 0. 0. 0.
!
?R32/R115 [R32/R115]
?E.W. Lemmon, NIST (2002)
7b05bb60/f7285250
XR0 1. 0.8807734 1. 1.0424065 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -37.909738 -80.680379 -25.447368 -21.151698 220.15164 -134.83467 0. 0. 0. 0. 0. 0.
VC1 0.094538867 -0.50912916 0.29444178 3.9889388 -7.8967078 3.9374152 0. 0. 0. 0. 0. 0.
!
?R32/R161 [R32/R161]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.68% from 96 bubble-point pressures
7b05bb60/edb53660
XR0 0.9976157 0.98909 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -2.8659324 -1.8450712 0.72917196 2.7277366 -1.6235954 0.45586463 0. 0. 0. 0. 0. 0.
VC1 -0.0018288484 0.014966934 -0.078308474 0.22749239 -0.28973824 0.13981107 0. 0. 0. 0. 0. 0.
!
?R32/R12 [R32/R12]
?E.W. Lemmon, NIST (2002)
7b05bb60/98829b70
XR0 1. 0.9032201 1. 1.0256397 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -8.8903308 -117.32443 118.37145 -243.66481 278.44046 -98.653638 0. 0. 0. 0. 0. 0.
VC1 0.031913591 -0.48802337 2.1002128 -4.434622 5.0096599 -2.2521456 0. 0. 0. 0. 0. 0.
!
?R32/R1234yf [R32/R1234YF]
?R. Akasaka, FPE, 2013, DOI:10.1016/j.fluid.2013.07.057
7b05bb60/40377b40
KW4 1.00052 0.948538 0.993346 1.02211 -0.277708 0. 0. 0. 0. 0. 0. 0.
TC1 4.1246157 -66.279199 100.35723 -142.91371 126.74397 -42.404493 0. 0. 0. 0. 0. 0.
VC1 0.10157531 -0.93223961 3.6183152 -7.0365843 6.688079 -2.4884845 0. 0. 0. 0. 0. 0.
!
?R32/R134a [R32/R134A]
?E.W. Lemmon and R.T Jacobsen, J. Phys. Chem. Ref. Data, 33(2):593-620, 2004.
7b05bb60/ff1c0560
KWS 1. 1.0114076 1. 1.0137207 1. 0. 0. 0. 0. 0. 0. 0.
TC1 5.2640593 -9.8183454 40.506497 -85.66996 84.068307 -31.654943 0. 0. 0. 0. 0. 0.
VC1 0.013377049 0.10869078 -0.28895079 0.6199192 -0.76841354 0.41036702 0. 0. 0. 0. 0. 0.
TRN 0.0437 -0.4678 -0.0645 -0.0305 0.06 -0.09 0.1 0. 0. 0. 0. 0.
!
?R32/Dimethyl ether [R32/DME]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7b05bb60/8f27e300
XR0 1. 1.0255 1. 0.8321 0. 0. 0. 0. 0. 0. 0. 0.
TC1 33.227697 7.0173808 -6.3641301 4.3952049 -18.185698 13.600002 0. 0. 0. 0. 0. 0.
VC1 -0.010017317 -0.23003375 0.91568616 -2.2289798 2.6065307 -1.1744165 0. 0. 0. 0. 0. 0.
!
?R32/R152a [R32/R152A]
?E.W. Lemmon, NIST (2002)
7b05bb60/63f364b0
XR0 1. 0.9975547 1. 1.0120247 0. 0. 0. 0. 0. 0. 0. 0.
TC1 7.671267 3.659595 -1.773994 2.2638266 -0.97185494 1.2706599 0. 0. 0. 0. 0. 0.
VC1 0.019011621 0.026767103 -0.26696633 0.73010336 -0.87632925 0.40063212 0. 0. 0. 0. 0. 0.
!
?R32/R1234ze(E) [R32/R1234ZEE]
?R. Akasaka, FPE, 2013, DOI:10.1016/j.fluid.2013.07.057
7b05bb60/9905ef70
KW2 1.00343 0.977857 1.00586 0.982707 -0.265419 0. 0. 0. 0. 0. 0. 0.
TC2 36.144318 -64.279946 134.18412 -151.98534 68.036556 0. 0. 0. 0. 0. 0. 0.
VC2 0.22814375 -1.4682101 4.016084 -4.9161734 2.2102819 0. 0. 0. 0. 0. 0. 0.
!
?R32/R227ea [R32/R227EA]
?E.W. Lemmon, NIST (2002)
7b05bb60/40091ee0
XR0 1. 0.9573075 1. 1.0589568 0. 0. 0. 0. 0. 0. 0. 0.
TC1 3.7568111 -57.297746 83.926085 -108.31329 83.97329 -20.652604 0. 0. 0. 0. 0. 0.
VC1 0.0065013896 0.13877515 -0.96721423 3.0929648 -3.994706 1.8932769 0. 0. 0. 0. 0. 0.
!
?R32/Isobutane [R32/C4I]
?E.W. Lemmon, NIST (2002)
7b05bb60/47ade7e0
XR0 1. 0.8573096 1. 1.0454476 0. 0. 0. 0. 0. 0. 0. 0.
TC1 41.78135 -338.55159 608.0883 -1173.8575 1111.1603 -358.88211 0. 0. 0. 0. 0. 0.
VC1 0.21901816 -2.844219 11.709575 -23.313019 23.244915 -9.0440592 0. 0. 0. 0. 0. 0.
!
?R32/Sulfur dioxide [R32/SO2]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.2% from 52 bubble-point pressures
7b05bb60/7fad4b80
XR0 1.002379950717 0.99968 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 16.119822 0.41258569 -4.4306283 8.1965627 -11.366856 6.2259194 0. 0. 0. 0. 0. 0.
VC1 -0.013518256 -0.11251242 0.70991178 -2.0015193 2.4950549 -1.1596348 0. 0. 0. 0. 0. 0.
!
?R32/R142b [R32/R142B]
?E.W. Lemmon, NIST (2002)
7b05bb60/f2a8b2e0
XR0 1. 0.9718126 1. 1.0305781 0. 0. 0. 0. 0. 0. 0. 0.
TC1 14.482048 -6.5227559 -32.679086 55.166249 -43.890713 17.005352 0. 0. 0. 0. 0. 0.
VC1 0.064869432 -0.33949694 0.74639163 -0.52488008 -0.23102749 0.35015169 0. 0. 0. 0. 0. 0.
!
?R32/Butene [R32/1BE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.31% from 35 bubble-point pressures
7b05bb60/cd7a06d0
XR0 1.020262411492 0.85398 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 25.444636 -74.265662 -248.49738 253.32997 -328.08303 249.77697 0. 0. 0. 0. 0. 0.
VC1 0.14319149 -1.939552 8.1577794 -18.489471 21.205389 -9.1886369 0. 0. 0. 0. 0. 0.
!
?R32/R236fa [R32/R236FA]
?E.W. Lemmon, NIST (2002)
7b05bb60/77fa2150
XR0 1. 0.9881848 1. 1.0540041 0. 0. 0. 0. 0. 0. 0. 0.
TC1 25.519122 -21.836336 30.558361 8.9878841 -49.509361 43.168421 0. 0. 0. 0. 0. 0.
VC1 0.14019018 -0.81377425 2.4524727 -3.4683861 2.1376023 -0.34162015 0. 0. 0. 0. 0. 0.
!
?R32/Butane [R32/C4]
?E.W. Lemmon, NIST (2006)
7b05bb60/7b3b4080
XR0 1. 0.8997516 1. 0.7952703 0. 0. 0. 0. 0. 0. 0. 0.
TC1 60.901384 -69.026664 -234.51963 287.44655 -316.09904 190.42486 0. 0. 0. 0. 0. 0.
VC1 0.20193392 -2.5593687 8.8131323 -16.21128 15.315051 -5.6527752 0. 0. 0. 0. 0. 0.
!
?R32/R236ea [R32/R236EA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.38% from 25 bubble-point pressures
7b05bb60/93fd5d40
XR0 1.0018835 1.01165 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 45.08736 -15.632875 57.663749 -26.749042 -21.620122 31.200116 0. 0. 0. 0. 0. 0.
VC1 0.21444067 -1.6865652 6.12565 -11.187849 9.8755662 -3.3410471 0. 0. 0. 0. 0. 0.
!
?R32/R123 [R32/R123]
?E.W. Lemmon, NIST (2002)
7b05bb60/efdfede0
XR0 1. 0.9720610 1. 1.0550886 0. 0. 0. 0. 0. 0. 0. 0.
TC1 56.742136 30.897888 -217.67965 437.71268 -442.43864 196.31673 0. 0. 0. 0. 0. 0.
VC1 0.20057083 -1.4817015 4.6548252 -7.6016435 6.2658952 -2.0142006 0. 0. 0. 0. 0. 0.
!
?R32/Isopentane [R32/C5I]
?E.W. Lemmon, NIST (2006)
7b05bb60/86ee46a0
XR0 1. 0.8885477 1. 1.0683958 0. 0. 0. 0. 0. 0. 0. 0.
TC1 103.05135 -161.21595 -54.241633 -102.09318 300.63445 -147.988 0. 0. 0. 0. 0. 0.
VC1 0.31483089 -3.0155412 9.7728762 -15.670137 12.609423 -3.8741913 0. 0. 0. 0. 0. 0.
!
?R32/Methanol [R32/MEO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.41% from 17 bubble-point pressures
7b05bb60/c41aa690
XR0 1.007049345418 1.01175 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 99.826177 78.771917 -135.08638 -92.758141 147.67879 0. 0. 0. 0. 0. 0. 0.
VC2 -0.037557768 0.068605749 -0.70357078 1.1179368 -0.61893471 0. 0. 0. 0. 0. 0. 0.
!
?R32/Ethanol [R32/ETO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.97% from 22 bubble-point pressures
7b05bb60/3d5f67e0
XR0 1.025031263454 1.01657 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 158.79231 -400.78255 2832.2165 -7198.1473 7235.7787 -2517.1029 0. 0. 0. 0. 0. 0.
VC1 0.12006654 -1.206203 5.3543698 -13.57975 14.882472 -5.7267019 0. 0. 0. 0. 0. 0.
!
?R32/Toluene [R32/TOL]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.49% from 9 bubble-point pressures
7b05bb60/a49b8b50
XR0 1.015980045339 0.98173 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 275.67072 -182.43754 744.60079 -615.11658 -1274.1206 1280.7583 0. 0. 0. 0. 0. 0.
VC1 0.32129176 -3.2462172 12.046161 -23.860486 22.497442 -8.03123 0. 0. 0. 0. 0. 0.
!
?Carbonyl sulfide/Propane [COS/C3]
?I. Cullimore and E.W. Lemmon, NIST (2010)
e7f902e0/70c6aac0
XR0 1. 0.9929 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -3.814776 -1.4297828 0.6362257 0.22653866 -0.49279857 0.24651301 0. 0. 0. 0. 0. 0.
VC1 0.02083728 -0.071689748 0.18136733 -0.27613628 0.21734555 -0.068574085 0. 0. 0. 0. 0. 0.
PR1 -0.0189 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Carbonyl sulfide/Methanol [COS/MEO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
e7f902e0/c41aa690
XR0 1. 1.0122 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 76.840919 -1.5467776 -41.395812 27.206416 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.14320098 -1.0732885 1.8987164 -1.0983566 0. 0. 0. 0. 0. 0. 0. 0.
!
?R125/Propylene [R125/PRY]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.34% from 47 bubble-point pressures
25c5a3a0/56d778b0
XR0 0.992723337933 0.92944 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -31.823508 -66.040309 88.210857 -94.827601 121.63515 -58.77432 0. 0. 0. 0. 0. 0.
VC1 -0.024907883 0.054481264 -0.45289046 1.2447736 -1.0848631 0.27001781 0. 0. 0. 0. 0. 0.
!
?R125/R143a [R125/R143A]
?E.W. Lemmon and R.T Jacobsen, J. Phys. Chem. Ref. Data, 33(2):593-620, 2004.
25c5a3a0/0deae990
KWT 1. 1.0081513 1. 0.9993132 1.1697 0. 0. 0. 0. 0. 0. 0.
TC1 2.4640832 0.93168725 -2.3137366 6.5415036 -7.7437986 3.4586984 0. 0. 0. 0. 0. 0.
VC1 0.0035224626 -0.0021474269 -0.015013669 0.060784657 -0.085077597 0.041231275 0. 0. 0. 0. 0. 0.
TRN 0. 0. 0. 0. 0. -0.15 0.16 0. 0. 0. 0. 0.
!
?R125/Propane [R125/C3]
?E.W. Lemmon, NIST (2002)
25c5a3a0/70c6aac0
XR0 1. 0.8993018 1. 1.0001703 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -27.232574 -144.38407 313.42022 -708.37286 847.02075 -343.11993 0. 0. 0. 0. 0. 0.
VC1 0.00010170369 -0.28590357 0.86556975 -1.0075885 0.67348988 -0.25379026 0. 0. 0. 0. 0. 0.
TRN -0.21 0.3776 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R125/R22 [R125/R22]
?E.W. Lemmon, NIST (2002)
25c5a3a0/57716470
XR0 1. 0.9775661 1. 1.0046832 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -12.354709 -6.2447776 1.0367082 1.9986545 -2.4073083 1.6123422 0. 0. 0. 0. 0. 0.
VC1 -0.033940772 0.10605615 -0.31220428 0.49853037 -0.38811306 0.12947257 0. 0. 0. 0. 0. 0.
!
?R125/R115 [R125/R115]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.16% from 60 bubble-point pressures
25c5a3a0/f7285250
XR0 1.000280078422 0.96147 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -16.959229 -14.638169 -2.1736411 4.5201162 4.3049821 -1.8721579 0. 0. 0. 0. 0. 0.
VC1 0.010474751 -0.034084678 0.032283954 0.17897715 -0.33161728 0.14062163 0. 0. 0. 0. 0. 0.
!
?R125/R161 [R125/R161]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.27% from 63 bubble-point pressures
25c5a3a0/edb53660
XR0 1.01043 0.99311 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 2.9099235 -8.9976786 -4.2263392 5.4672912 -18.399423 10.95846 0. 0. 0. 0. 0. 0.
VC1 -0.0096402501 -0.011466825 -0.039482199 0.12530275 -0.16522893 0.084072018 0. 0. 0. 0. 0. 0.
!
?R125/Ammonia [R125/NH3]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2% from 230 bubble-point pressures
25c5a3a0/e9847540
XR0 0.956498450473 0.96866 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -46.652185 -26.465656 250.51946 -306.27083 135.13834 6.8359909 0. 0. 0. 0. 0. 0.
VC1 -0.014684207 -0.31485335 1.141951 -0.86610472 -0.65584969 0.59930597 0. 0. 0. 0. 0. 0.
!
?R125/Cyclopropane [R125/CC3]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.37% from 34 bubble-point pressures
25c5a3a0/bc9f5400
XR0 0.985008175568 0.91039 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -38.39106 -55.519406 -18.558888 92.136716 -30.555716 -6.3560311 0. 0. 0. 0. 0. 0.
VC1 -0.064670793 0.0013112736 0.074883151 0.15915332 -0.25965008 0.10487551 0. 0. 0. 0. 0. 0.
!
?R125/R1234yf [R125/R1234YF]
?E.W. Lemmon, NIST (2013)
25c5a3a0/40377b40
XR0 1. 0.999 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 5.8338929 -1.2922015 -0.60358991 4.6840411 -6.3807961 2.8779543 0. 0. 0. 0. 0. 0.
VC1 0.034653221 -0.18596521 0.54735835 -0.86652592 0.68531297 -0.20631724 0. 0. 0. 0. 0. 0.
!
?R125/R134a [R125/R134A]
?E.W. Lemmon and R.T Jacobsen, J. Phys. Chem. Ref. Data, 33(2):593-620, 2004.
25c5a3a0/ff1c0560
KWT 1. 1.0005991 1. 0.9992977 1. 0. 0. 0. 0. 0. 0. 0.
TC1 3.830512 -9.0999441 32.653786 -61.735199 55.843599 -19.20876 0. 0. 0. 0. 0. 0.
VC1 -0.0028715286 -0.0089197682 0.0083971738 -0.0090764025 0.00833958 -0.0090637346 0. 0. 0. 0. 0. 0.
TRN -0.0045 0.0038 -0.0829 -0.0106 0. 0. 0. 0. 0. 0. 0. 0.
!
?R125/Dimethyl ether [R125/DME]
?E.W. Lemmon, NIST (2006)
25c5a3a0/8f27e300
XR0 1. 1.0529664 1. 1.0039379 0. 0. 0. 0. 0. 0. 0. 0.
TC1 36.538408 9.2321723 -5.5399025 76.249493 -103.3405 60.176793 0. 0. 0. 0. 0. 0.
VC1 0.0046342446 -0.15647437 0.86668852 -2.4130392 3.0422134 -1.4802113 0. 0. 0. 0. 0. 0.
!
?R125/R152a [R125/R152A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.4% from 93 bubble-point pressures
25c5a3a0/63f364b0
XR0 0.99429 1.00282 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 3.4736765 4.8315405 -0.90637151 18.856135 -22.732386 12.487586 0. 0. 0. 0. 0. 0.
VC1 -0.022398902 -0.012842603 0.18855319 -0.59188434 0.76568849 -0.37888151 0. 0. 0. 0. 0. 0.
!
?R125/RE143a [R125/RE143A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.23% from 21 bubble-point pressures
25c5a3a0/bf6c1a00
XR0 1.00105 1.00517 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 10.460265 1.069903 2.5476226 -2.7452275 0.41285537 0.75638686 0. 0. 0. 0. 0. 0.
VC1 -0.0052787335 0.0044584155 -0.021043825 0.024870289 -0.018181578 0.0037156145 0. 0. 0. 0. 0. 0.
!
?R125/R1234ze(E) [R125/R1234ZEE]
?E.W. Lemmon, NIST (2015); fit of data from Honeywell
25c5a3a0/9905ef70
XR0 1.003 1.0071 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 16.462433 -1.8778443 4.1582447 -3.6877402 -0.76361202 0.59145319 0. 0. 0. 0. 0. 0.
VC1 0.12776123 -1.1258322 4.2941427 -8.1990093 7.5649086 -2.6898164 0. 0. 0. 0. 0. 0.
!
?R125/R227ea [R125/R227EA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.47% from 38 bubble-point pressures
25c5a3a0/40091ee0
XR0 1.00101 1.00302 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 15.132568 -3.7693312 11.466643 -15.098209 11.830937 -4.0801852 0. 0. 0. 0. 0. 0.
VC1 -0.013165979 0.12455957 -0.55865257 1.2779077 -1.4143679 0.61678452 0. 0. 0. 0. 0. 0.
!
?R125/Isobutane [R125/C4I]
?E.W. Lemmon, NIST (2002)
25c5a3a0/47ade7e0
XR0 1. 0.9053808 1. 1.0036183 0. 0. 0. 0. 0. 0. 0. 0.
TC1 22.894906 -196.63032 310.97422 -525.22646 425.5327 -110.70833 0. 0. 0. 0. 0. 0.
VC1 0.10989795 -1.5795442 5.9342337 -11.027456 10.432726 -3.8720779 0. 0. 0. 0. 0. 0.
!
?R125/R236fa [R125/R236FA]
?E.W. Lemmon, NIST (2002)
25c5a3a0/77fa2150
XR0 1. 1.0094115 1. 1.0063437 0. 0. 0. 0. 0. 0. 0. 0.
TC1 28.576581 -4.2035868 18.950312 -10.977458 -0.54711296 5.2358039 0. 0. 0. 0. 0. 0.
VC1 0.079815926 -0.52929066 1.732846 -3.0706156 2.6946121 -0.92365111 0. 0. 0. 0. 0. 0.
!
?R125/Butane [R125/C4]
?E.W. Lemmon, NIST (2002)
25c5a3a0/7b3b4080
XR0 1. 0.9013212 1. 1.0032460 0. 0. 0. 0. 0. 0. 0. 0.
TC1 22.492431 -90.192002 -135.96385 273.39315 -260.72121 112.54742 0. 0. 0. 0. 0. 0.
VC1 0.083945698 -1.5238893 5.2576339 -9.1858433 8.5280638 -3.1543577 0. 0. 0. 0. 0. 0.
!
?R125/R236ea [R125/R236EA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.06% from 23 bubble-point pressures
25c5a3a0/93fd5d40
XR0 0.99947 1.01046 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 39.827562 -28.006408 80.991608 -96.896137 62.117352 -11.034263 0. 0. 0. 0. 0. 0.
VC1 0.13019639 -1.0813276 3.8960003 -7.3571873 6.8326422 -2.4856987 0. 0. 0. 0. 0. 0.
!
?R125/R245fa [R125/R245FA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.17% from 17 bubble-point pressures
25c5a3a0/5c322280
XR0 0.99836 1.01325 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 40.66267 19.08007 -51.934809 126.96036 -142.66754 69.876671 0. 0. 0. 0. 0. 0.
VC1 0.24909925 -2.2079558 8.270686 -15.913417 14.948707 -5.4722182 0. 0. 0. 0. 0. 0.
!
?R125/Isopentane [R125/C5I]
?E.W. Lemmon, NIST (2006)
25c5a3a0/86ee46a0
XR0 1. 0.9155196 1. 1.0119468 0. 0. 0. 0. 0. 0. 0. 0.
TC1 87.785051 -113.47204 -51.199611 -186.13436 446.33898 -238.78358 0. 0. 0. 0. 0. 0.
VC1 0.21134507 -2.3286461 7.5216988 -13.167888 11.9732 -4.2032758 0. 0. 0. 0. 0. 0.
!
?R125/Ethanol [R125/ETO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.47% from 11 bubble-point pressures
25c5a3a0/3d5f67e0
XR0 0.995401246242 1.05044 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 114.8257 26.886558 -96.122035 400.78484 -790.05692 550.75887 0. 0. 0. 0. 0. 0.
VC1 0.045118707 -0.8775088 3.8430301 -10.039506 11.770809 -5.226898 0. 0. 0. 0. 0. 0.
!
?Propylene/Propane [PRY/C3]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
56d778b0/70c6aac0
XR0 1.001001001001 0.995 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -2.0299905 -1.810103 -0.48360356 0.025022071 0.06230641 0.041621098 0. 0. 0. 0. 0. 0.
VC1 0.0054220918 -0.0045975308 0.0080583694 -0.0042282618 0.001991655 0.0011365041 0. 0. 0. 0. 0. 0.
PR1 0.0074 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propylene/R22 [PRY/R22]
?E.W. Lemmon, NIST (2002)
56d778b0/57716470
XR0 1. 0.9784013 1. 1.0009101 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -14.720749 -4.0885061 2.8034877 1.7516616 -0.0085393757 -0.43304841 0. 0. 0. 0. 0. 0.
VC1 -0.0074742016 0.035512702 -0.15886274 0.43583697 -0.51454835 0.22552796 0. 0. 0. 0. 0. 0.
!
?Propylene/R115 [PRY/R115]
?E.W. Lemmon, NIST (2002)
56d778b0/f7285250
XR0 1. 0.9428297 1. 1.0082859 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -32.925536 -19.535425 -8.1334785 41.308526 -19.227049 0.81712293 0. 0. 0. 0. 0. 0.
VC1 0.047552728 -0.30563006 1.5383661 -3.4358921 3.1410352 -1.0432684 0. 0. 0. 0. 0. 0.
!
?Propylene/Ammonia [PRY/NH3]
?I. Cullimore and E.W. Lemmon, NIST (2010)
56d778b0/e9847540
XR0 0.9721 0.8483 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 -66.339608 -327.16745 584.9612 -248.02358 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.082770475 0.17466443 -0.0062579084 -0.054933776 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propylene/R1216 [PRY/R1216]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.57% from 127 bubble-point pressures
56d778b0/edc3a7b0
XR0 1.01903 0.93686 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 -24.799148 -11.864807 -86.611996 72.295538 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.058303262 -0.28974917 0.79235944 -0.69331112 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propylene/R12 [PRY/R12]
?E.W. Lemmon, NIST (2002)
56d778b0/98829b70
XR0 1. 0.9887079 1. 1.0020049 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -2.7485355 -3.6254229 -0.46759254 0.86648372 -0.029967901 -0.1994145 0. 0. 0. 0. 0. 0.
VC1 0.0018896904 0.037265536 -0.22978097 0.66345487 -0.8398071 0.40364404 0. 0. 0. 0. 0. 0.
!
?Propylene/R134a [PRY/R134A]
?E.W. Lemmon, NIST (2002)
56d778b0/ff1c0560
XR0 1. 0.9364605 1. 1.0007007 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -27.912991 -46.107922 25.423554 -31.633435 75.739599 -38.923629 0. 0. 0. 0. 0. 0.
VC1 0.028801011 -0.19683442 0.35427585 0.49359242 -1.6538542 0.96145234 0. 0. 0. 0. 0. 0.
!
?Propylene/Dimethyl ether [PRY/DME]
?I. Cullimore and E.W. Lemmon, NIST (2010)
56d778b0/8f27e300
XR0 1. 0.9924 1. 0.975 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0.18633344 -4.756171 -0.8713256 2.4502608 -1.6335069 0.46178036 0. 0. 0. 0. 0. 0.
VC1 -0.0080043552 -0.033708472 0.13802371 -0.34317291 0.41675883 -0.19535202 0. 0. 0. 0. 0. 0.
!
?Propylene/R152a [PRY/R152A]
?E.W. Lemmon, NIST (2002)
56d778b0/63f364b0
XR0 1. 0.9499507 1. 1.0000359 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -23.320751 -22.229611 -12.401987 24.91894 -2.1776831 -1.9679056 0. 0. 0. 0. 0. 0.
VC1 -0.010771042 0.010581135 -0.056264148 0.31879764 -0.42169061 0.15078095 0. 0. 0. 0. 0. 0.
!
?Propylene/Isobutane [PRY/C4I]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
56d778b0/47ade7e0
XR0 0.971817298348 1.014 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 12.283769 -3.9763146 -13.965704 261.73462 -386.54499 208.76424 0. 0. 0. 0. 0. 0.
VC1 0.13297459 -0.98444561 3.4634997 -5.9420381 4.8866691 -1.5329342 0. 0. 0. 0. 0. 0.
PR1 -0.0144 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propylene/R142b [PRY/R142B]
?E.W. Lemmon, NIST (2002)
56d778b0/f2a8b2e0
XR0 1. 0.9913727 1. 1.0035574 0. 0. 0. 0. 0. 0. 0. 0.
TC1 7.5478224 1.8748593 -15.54653 24.867517 -21.612644 9.50206 0. 0. 0. 0. 0. 0.
VC1 0.016542303 0.0019865587 -0.34111995 1.177437 -1.5508385 0.74259848 0. 0. 0. 0. 0. 0.
!
?Propylene/Butene [PRY/1BE]
?I. Cullimore and E.W. Lemmon, NIST (2010)
56d778b0/cd7a06d0
XR0 1. 1.0075 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 18.769281 12.859976 -26.293377 66.943311 -80.734099 41.500685 0. 0. 0. 0. 0. 0.
VC1 0.018875519 0.0097320291 -0.37476358 1.1576598 -1.4661259 0.68325457 0. 0. 0. 0. 0. 0.
PR1 0.0004 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propylene/Butane [PRY/C4]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
56d778b0/7b3b4080
XR0 1. 1.02 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 28.539138 27.443646 -69.155626 189.91907 -229.18406 111.64692 0. 0. 0. 0. 0. 0.
VC1 0.061807667 -0.17175501 -0.030698768 0.86609782 -1.4341522 0.73287867 0. 0. 0. 0. 0. 0.
!
?Propylene/R114 [PRY/R114]
?E.W. Lemmon, NIST (2002)
56d778b0/b1698aa0
XR0 1. 0.9744438 1. 1.0187337 0. 0. 0. 0. 0. 0. 0. 0.
TC1 10.547167 0.53379407 -51.853924 96.121025 -91.886034 40.776104 0. 0. 0. 0. 0. 0.
VC1 0.014966948 0.10117222 -1.0384388 3.1436687 -3.928751 1.80017 0. 0. 0. 0. 0. 0.
!
?Propylene/Isopentane [PRY/C5I]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
56d778b0/86ee46a0
XR0 1. 1.035 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 60.527977 80.082404 -290.98736 802.17315 -973.39528 455.78909 0. 0. 0. 0. 0. 0.
VC1 0.22773553 -1.6526889 5.5553144 -9.7629528 8.3669249 -2.7927568 0. 0. 0. 0. 0. 0.
!
?Propylene/Pentane [PRY/C5]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
56d778b0/76bc0290
XR0 1. 1.04 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 62.285451 102.70757 -346.15971 959.23267 -1180.0433 557.46411 0. 0. 0. 0. 0. 0.
VC1 0.092588485 -0.31536912 0.37577037 -0.1369422 -0.24955994 0.16432465 0. 0. 0. 0. 0. 0.
!
?Propylene/Acetone [PRY/ACT]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.4% from 33 bubble-point pressures
56d778b0/342481e0
XR0 1.019919 0.99014 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 102.75327 -34.348703 222.71368 -675.30379 550.91677 -127.37176 0. 0. 0. 0. 0. 0.
VC1 0.26267809 -2.223865 7.702155 -14.483359 13.042127 -4.3610257 0. 0. 0. 0. 0. 0.
!
?Propylene/Methanol [PRY/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
56d778b0/c41aa690
XR0 1. 0.979 1. 1.086 0. 0. 0. 0. 0. 0. 0. 0.
TC1 50.600464 5.8185271 -1.224499 -303.55352 466.02649 -189.49217 0. 0. 0. 0. 0. 0.
VC1 -0.048019152 -0.082453356 0.5112872 -1.8749368 2.4857605 -1.0675814 0. 0. 0. 0. 0. 0.
!
?Propylene/Hexane [PRY/C6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
56d778b0/cb03ba40
XR0 1.021450459653 1.068 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 110.84696 195.16978 -769.75201 2403.0884 -3121.3332 1422.0398 0. 0. 0. 0. 0. 0.
VC1 0.15097547 -0.92088167 3.0109031 -5.7422559 4.8814164 -1.5736813 0. 0. 0. 0. 0. 0.
!
?Propylene/Ethanol [PRY/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
56d778b0/3d5f67e0
XR0 1.011 1.022 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 102.26009 -43.048942 445.30652 -1314.4378 1349.939 -444.34395 0. 0. 0. 0. 0. 0.
VC1 0.043067605 -0.50774335 1.7819046 -4.7901619 5.4828334 -2.1502065 0. 0. 0. 0. 0. 0.
!
?Propylene/Benzene [PRY/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
56d778b0/f2cfb460
XR0 1. 1.03 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 141.77205 -54.514941 83.413698 433.21831 -1130.4237 737.52651 0. 0. 0. 0. 0. 0.
VC1 0.10074098 -1.1383502 4.2754142 -8.9834577 8.987936 -3.5211698 0. 0. 0. 0. 0. 0.
!
?Propylene/Cyclohexane [PRY/CC6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.57% from 12 bubble-point pressures
56d778b0/6e225350
XR0 0.999011 1.04089 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 111.92461 233.10608 -992.5814 2555.9304 -3085.7519 1428.3373 0. 0. 0. 0. 0. 0.
VC1 0.099794066 -0.83154844 2.3040719 -4.3931614 4.4455358 -1.9035821 0. 0. 0. 0. 0. 0.
!
?Propylene/Heptane [PRY/C7]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
56d778b0/b398a3b0
XR0 1.008064516129 1.082 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 156.2611 295.1116 -1257.6264 3711.044 -4608.4676 2070.3835 0. 0. 0. 0. 0. 0.
VC1 0.43332597 -3.4156144 12.587204 -24.697061 23.455374 -8.7644716 0. 0. 0. 0. 0. 0.
!
?Propylene/Isooctane [PRY/C8I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.36% from 7 bubble-point pressures
56d778b0/c2dd9ef0
XR0 0.964534081812 1.11387 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 131.19653 348.52053 -1464.5568 4045.5119 -4639.0573 2142.7384 0. 0. 0. 0. 0. 0.
VC1 0.45921041 -3.5708716 13.606201 -27.97993 28.939502 -12.028693 0. 0. 0. 0. 0. 0.
!
?Propylene/Water [PRY/H2O]
?I. Cullimore and E.W. Lemmon, NIST (2010)
56d778b0/b43a7600
KW8 0.931 0.8775 1. 1. 0.7604 0. 0. 0. 0. 0. 0. 0.
TC5 446.59498 -1280.639 904.01855 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.080134126 1.0216944 -1.1487909 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propylene/Toluene [PRY/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
56d778b0/a49b8b50
XR0 1.021450459653 1.039 1. 1.024 0. 0. 0. 0. 0. 0. 0. 0.
TC1 182.12738 241.38744 -1261.2581 4223.394 -6167.7343 3056.5334 0. 0. 0. 0. 0. 0.
VC1 0.20172842 -1.6433534 5.3840978 -10.023472 8.4406588 -2.6922928 0. 0. 0. 0. 0. 0.
!
?Propylene/Octane [PRY/C8]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
56d778b0/f174a9b0
XR0 0.979431929481 1.097 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 188.75662 337.7395 -1504.5526 4133.2585 -4727.0261 2099.6307 0. 0. 0. 0. 0. 0.
VC1 0.77156766 -6.6046735 24.897266 -49.022953 47.753273 -18.447761 0. 0. 0. 0. 0. 0.
!
?Propylene/p-Xylene [PRY/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.66% from 16 bubble-point pressures
56d778b0/01b0e650
XR0 0.99082 1.09426 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 267.08539 -88.644008 -137.30161 2380.3523 -4214.7384 2273.8013 0. 0. 0. 0. 0. 0.
VC1 0.48483729 -4.1934502 16.404068 -34.504991 35.366716 -14.307195 0. 0. 0. 0. 0. 0.
!
?Propylene/m-Xylene [PRY/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.3% from 16 bubble-point pressures
56d778b0/0f99ff70
XR0 0.9934926 1.09811 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 256.79425 66.022329 -1048.604 4587.5992 -6491.0487 3117.665 0. 0. 0. 0. 0. 0.
VC1 0.51250268 -5.1380541 21.315521 -44.777511 45.118337 -17.808724 0. 0. 0. 0. 0. 0.
!
?Propylene/Nonane [PRY/C9]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
56d778b0/7f94dc20
XR0 0.970873786408 1.117 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 214.78872 476.04739 -1924.4134 4927.9832 -5247.8446 2206.8257 0. 0. 0. 0. 0. 0.
VC1 0.65955878 -5.1882387 19.338446 -39.544222 40.747669 -16.860566 0. 0. 0. 0. 0. 0.
!
?Propylene/Decane [PRY/C10]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
56d778b0/111888d0
XR0 0.956937799043 1.191 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 281.18895 101.8352 591.04016 -1567.7304 2949.6199 -1473.1335 0. 0. 0. 0. 0. 0.
VC1 0.89773663 -7.6189822 31.384294 -67.676752 71.823511 -30.097499 0. 0. 0. 0. 0. 0.
!
?R143a/Propane [R143A/C3]
?E.W. Lemmon, NIST (2002)
0deae990/70c6aac0
XR0 1. 0.9130538 1. 1.0000536 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -30.061076 -103.07405 186.63473 -395.13052 494.78735 -208.44525 0. 0. 0. 0. 0. 0.
VC1 0.0017964865 -0.18049618 0.41311804 -0.039399492 -0.42506205 0.22482226 0. 0. 0. 0. 0. 0.
!
?R143a/R22 [R143A/R22]
?E.W. Lemmon, NIST (2002)
0deae990/57716470
XR0 1. 0.9990265 1. 1.0023121 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -0.57215615 0.1065861 -0.01543537 -0.0079466452 0.011887057 -0.0034261632 0. 0. 0. 0. 0. 0.
VC1 -0.010790998 0.0088514809 -0.014627516 0.0076513443 0.00092708766 -0.0022078235 0. 0. 0. 0. 0. 0.
!
?R143a/R161 [R143A/R161]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.55% from 109 bubble-point pressures
0deae990/edb53660
XR0 0.99931 0.99556 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -2.7804387 0.24778313 0.27233689 0.10792704 -0.09851552 0.054775581 0. 0. 0. 0. 0. 0.
VC1 -0.0079172686 -0.0019395145 0.0085716123 -0.031264746 0.040195485 -0.022562692 0. 0. 0. 0. 0. 0.
!
?R143a/R12 [R143A/R12]
?E.W. Lemmon, NIST (2002)
0deae990/98829b70
XR0 1. 0.9484400 1. 1.0007214 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -13.955434 -42.248688 28.767781 -45.801266 51.099581 -16.512623 0. 0. 0. 0. 0. 0.
VC1 -0.033592623 0.057108955 -0.13395697 0.21776776 -0.069489269 -0.03871582 0. 0. 0. 0. 0. 0.
!
?R143a/R1234yf [R143A/R1234YF]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.2% from 35 bubble-point pressures
0deae990/40377b40
XR0 0.9997601 0.99523 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 2.0217429 -2.672901 1.0921635 0.126198 -0.64951518 0.2585253 0. 0. 0. 0. 0. 0.
VC1 0.03299167 -0.17085472 0.52074063 -0.8578802 0.72372715 -0.24000974 0. 0. 0. 0. 0. 0.
!
?R143a/R134a [R143A/R134A]
?E.W. Lemmon and R.T Jacobsen, J. Phys. Chem. Ref. Data, 33(2):593-620, 2004.
0deae990/ff1c0560
KWT 1. 1.0040047 1. 1.0016349 0.5557 0. 0. 0. 0. 0. 0. 0.
TC1 5.0739149 -8.057009 34.87285 -67.53301 62.981626 -22.427388 0. 0. 0. 0. 0. 0.
VC1 -0.00025724381 -0.0021249835 -0.0049281519 0.0074985363 -0.0028094542 -0.0029332642 0. 0. 0. 0. 0. 0.
!
?R143a/Dimethyl ether [R143A/DME]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.46% from 54 bubble-point pressures
0deae990/8f27e300
XR0 0.999880014398 0.99059 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0.48256917 -5.2465985 3.3438493 -2.7055631 0.90489006 0.031187324 0. 0. 0. 0. 0. 0.
VC1 -0.010139872 -0.02478572 0.086981454 -0.23430309 0.29149832 -0.14863749 0. 0. 0. 0. 0. 0.
!
?R143a/R152a [R143A/R152A]
?E.W. Lemmon, NIST (2002)
0deae990/63f364b0
XR0 1. 0.9889541 1. 1.0005720 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.9862369 -3.4009511 -0.22875175 -0.43574059 0.66849071 -0.23019648 0. 0. 0. 0. 0. 0.
VC1 -0.020936274 0.018002771 -0.023910503 0.021542427 -0.0078913868 -0.0020886353 0. 0. 0. 0. 0. 0.
!
?R143a/Isobutane [R143A/C4I]
?E.W. Lemmon, NIST (2002)
0deae990/47ade7e0
XR0 1. 0.9254452 1. 1.0064788 0. 0. 0. 0. 0. 0. 0. 0.
TC1 14.090547 -144.9927 224.52509 -356.15513 280.06196 -74.89312 0. 0. 0. 0. 0. 0.
VC1 0.10191215 -1.2550325 4.6760955 -8.547908 7.8746629 -2.8460916 0. 0. 0. 0. 0. 0.
!
?R143a/Isobutene [R143A/IBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.31% from 54 bubble-point pressures
0deae990/d287e4b0
XR0 0.997804829375 0.94375 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 6.0161305 -45.57043 -32.890044 66.033213 -50.531679 18.066641 0. 0. 0. 0. 0. 0.
VC1 -0.014005546 -0.20951351 0.6137884 -0.83553041 0.66690905 -0.21964863 0. 0. 0. 0. 0. 0.
!
?R143a/R236fa [R143A/R236FA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.12% from 21 bubble-point pressures
0deae990/77fa2150
XR0 0.99911 1.01834 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 27.368116 6.5421339 3.7897719 14.839649 -19.384762 11.898541 0. 0. 0. 0. 0. 0.
VC1 0.065832893 -0.38346089 1.1970454 -2.0650131 1.7814191 -0.6073656 0. 0. 0. 0. 0. 0.
!
?R143a/Butane [R143A/C4]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.87% from 112 bubble-point pressures
0deae990/7b3b4080
XR0 0.999070864096 0.91912 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 16.131456 -87.848235 -33.918397 97.553338 -105.67272 51.442766 0. 0. 0. 0. 0. 0.
VC1 0.075685912 -1.2328909 4.2555646 -7.230049 6.4027273 -2.2662985 0. 0. 0. 0. 0. 0.
!
?Propane/R22 [C3/R22]
?E.W. Lemmon, NIST (2002)
70c6aac0/57716470
XR0 1. 0.9412329 1. 1.0030692 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -39.142686 -15.935908 -17.224596 110.57285 -99.463398 31.218577 0. 0. 0. 0. 0. 0.
VC1 -0.020136715 0.015367254 0.13346736 0.12284337 -0.7609339 0.54953883 0. 0. 0. 0. 0. 0.
TRN -0.1284 0.3331 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/R115 [C3/R115]
?E.W. Lemmon, NIST (2002)
70c6aac0/f7285250
XR0 1. 0.9432827 1. 1.0043338 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -35.953487 -16.443836 -8.9658252 64.102968 -51.563509 14.974345 0. 0. 0. 0. 0. 0.
VC1 0.024639524 -0.13521233 0.81106674 -2.4113857 2.7748613 -1.0973745 0. 0. 0. 0. 0. 0.
TRN -0.2744 0.414 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/Ammonia [C3/NH3]
?I. Cullimore and E.W. Lemmon, NIST (2010)
70c6aac0/e9847540
XR0 0.9599 0.7905 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 -70.77828 -605.76938 1139.1464 -516.59562 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.12893242 0.20235362 0.14478321 -0.21082602 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/Cyclopropane [C3/CC3]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.85% from 13 bubble-point pressures
70c6aac0/bc9f5400
XR0 1.0024359 0.98041 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 -11.327514 -6.312881 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC2 -0.011260695 0.0081343006 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/R1216 [C3/R1216]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.29% from 35 bubble-point pressures
70c6aac0/edc3a7b0
XR0 1.01214 0.92233 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -36.381643 -39.748855 -6.9775534 -48.146077 165.27167 -84.186467 0. 0. 0. 0. 0. 0.
VC1 0.058931326 -0.69120196 3.5031391 -7.3463702 6.3351488 -1.8815305 0. 0. 0. 0. 0. 0.
!
?Propane/R134a [C3/R134A]
?E.W. Lemmon, NIST (2002)
70c6aac0/ff1c0560
XR0 1. 0.9002394 1. 1.0000015 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -45.044894 -68.249378 -62.296069 198.47718 -42.982107 -34.801617 0. 0. 0. 0. 0. 0.
VC1 0.031138746 -0.59314888 2.5861065 -4.4256266 3.0626537 -0.64885987 0. 0. 0. 0. 0. 0.
TRN 0. 0. 0. 0. 0.08 -0.04 0.2 0. 0. 0. 0. 0.
!
?Propane/Dimethyl ether [C3/DME]
?I. Cullimore and E.W. Lemmon, NIST (2010)
70c6aac0/8f27e300
XR0 1. 0.9658 1. 0.9857 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -17.592029 -18.012564 6.5823691 -3.2033032 9.3631464 -3.8162569 0. 0. 0. 0. 0. 0.
VC1 -0.011711072 -0.019839712 0.064462213 -0.068771157 0.026466998 0.0081497263 0. 0. 0. 0. 0. 0.
!
?Propane/R152a [C3/R152A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.86% from 133 bubble-point pressures
70c6aac0/63f364b0
XR0 1.01223 0.92009 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -35.516009 -48.480953 46.535466 -215.41021 327.63835 -130.29975 0. 0. 0. 0. 0. 0.
VC1 -0.032710402 0.17119835 -1.045138 3.1428063 -3.8926372 1.6719845 0. 0. 0. 0. 0. 0.
!
?Propane/R13I1 [C3/CF3I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.26% from 24 bubble-point pressures
70c6aac0/d26ca240
XR0 1.0055102 0.98807 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0.70091278 -4.4247229 -8.3039497 0.6743164 -1.5269051 1.5104616 0. 0. 0. 0. 0. 0.
VC1 0.015517626 -0.011444929 -0.050582543 0.13136194 -0.11186377 0.040922906 0. 0. 0. 0. 0. 0.
!
?Propane/R227ea [C3/R227EA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.55% from 188 bubble-point pressures
70c6aac0/40091ee0
XR0 1.02125 0.91449 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -19.009526 -93.782703 181.29428 -549.69903 633.79472 -220.02072 0. 0. 0. 0. 0. 0.
VC1 -0.055789093 0.83310483 -5.0523234 13.365197 -15.136407 5.9915321 0. 0. 0. 0. 0. 0.
!
?Propane/Isobutane [C3/C4I]
?Kunz and Wagner (2007)
70c6aac0/47ade7e0
KW0 0.998012298 1.005250774 0.999243146 1.001156119 -0.0551609771024 0. 0. 0. 0. 0. 0. 0.
TC1 19.056985 -0.21987686 -6.1349223 45.171536 -61.408226 32.510488 0. 0. 0. 0. 0. 0.
VC1 0.10656859 -0.72730584 2.3989609 -4.0280226 3.2881491 -1.0201133 0. 0. 0. 0. 0. 0.
PR1 -0.0078 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/Sulfur dioxide [C3/SO2]
?I. Cullimore and E.W. Lemmon, NIST (2010)
70c6aac0/7fad4b80
XR0 1. 0.8738 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -48.745034 -136.36594 206.77696 -597.1912 862.27863 -368.49432 0. 0. 0. 0. 0. 0.
VC1 -0.099219415 0.32416654 -1.8171208 4.8810031 -5.1208284 1.8856348 0. 0. 0. 0. 0. 0.
!
?Propane/Isobutene [C3/IBE]
?I. Cullimore and E.W. Lemmon, NIST (2010)
70c6aac0/d287e4b0
XR0 1. 0.9927 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 7.6714605 0.34196963 -11.034178 18.575213 -16.746956 7.6016906 0. 0. 0. 0. 0. 0.
VC1 0.0040407453 -0.0010331121 -0.13372094 0.46383409 -0.60687424 0.29501696 0. 0. 0. 0. 0. 0.
!
?Propane/RC318 [C3/RC318]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.17% from 55 bubble-point pressures
70c6aac0/9e4d8e90
XR0 1.02377 0.9232 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -15.670894 -28.664105 -42.556323 -54.432402 43.639732 26.165588 0. 0. 0. 0. 0. 0.
VC1 0.046497238 -0.13218557 -0.057083607 0.37733822 0.30245133 -0.62378381 0. 0. 0. 0. 0. 0.
!
?Propane/Perfluorobutane [C3/C4F10]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.45% from 37 bubble-point pressures
70c6aac0/a8f85e00
XR0 1.0256515 0.90987 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -16.818308 -29.506684 -48.643241 -103.28125 117.91645 -2.6319014 0. 0. 0. 0. 0. 0.
VC1 0.082530048 -0.26909755 0.073633599 0.49526999 0.2816462 -0.77381303 0. 0. 0. 0. 0. 0.
!
?Propane/R236fa [C3/R236FA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.68% from 43 bubble-point pressures
70c6aac0/77fa2150
XR0 1.02204 0.91493 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.7967715 -95.34517 109.14898 -332.80047 292.56015 -47.480739 0. 0. 0. 0. 0. 0.
VC1 0.11663917 -0.98645082 3.3267056 -6.1662399 6.4817377 -2.8638435 0. 0. 0. 0. 0. 0.
!
?Propane/Butane [C3/C4]
?Kunz and Wagner (2007)
70c6aac0/7b3b4080
KW0 1.000310289 1.007392782 0.999795868 1.003264179 0.0312572600489 0. 0. 0. 0. 0. 0. 0.
TC1 16.346732 10.935815 -22.158164 54.741092 -63.033142 31.131507 0. 0. 0. 0. 0. 0.
VC1 0.034782696 -0.064172049 -0.17263926 0.84216107 -1.1912666 0.58500671 0. 0. 0. 0. 0. 0.
TRN 0.0825 -0.3471 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0033 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/R114 [C3/R114]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.17% from 12 bubble-point pressures
70c6aac0/b1698aa0
XR0 1.00332 0.98055 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 9.2168176 -1.3264367 -22.96173 23.042027 -20.838404 10.686229 0. 0. 0. 0. 0. 0.
VC1 0.0075325301 0.039837087 -0.47365966 1.3940623 -1.7019521 0.78302217 0. 0. 0. 0. 0. 0.
!
?Propane/R236ea [C3/R236EA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.5% from 37 bubble-point pressures
70c6aac0/93fd5d40
XR0 1.02233 0.92015 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 11.861004 -117.62545 150.38132 -311.89085 172.644 17.339442 0. 0. 0. 0. 0. 0.
VC1 0.1566483 -1.4384807 5.3278584 -10.665028 11.185725 -4.6238349 0. 0. 0. 0. 0. 0.
!
?Propane/Neopentane [C3/C5A]
?I. Cullimore and E.W. Lemmon, NIST (2010)
70c6aac0/5a410790
XR0 1. 1.004 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 27.848273 23.640967 -89.246903 213.85898 -242.16246 110.9857 0. 0. 0. 0. 0. 0.
VC1 0.17054245 -0.98833812 2.7984822 -4.1176469 2.8811661 -0.7094346 0. 0. 0. 0. 0. 0.
!
?Propane/R245fa [C3/R245FA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.55% from 28 bubble-point pressures
70c6aac0/5c322280
XR0 1.02121 0.92286 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 11.189329 -24.830636 -152.58256 113.93357 -99.026337 72.727868 0. 0. 0. 0. 0. 0.
VC1 0.28482148 -2.6061528 9.5052466 -18.374818 18.158058 -7.0023304 0. 0. 0. 0. 0. 0.
!
?Propane/Isopentane [C3/C5I]
?Kunz and Wagner (2007)
70c6aac0/86ee46a0
KW0 0.994364425 1.0032695 1.040459289 0.999432118 0. 0. 0. 0. 0. 0. 0. 0.
TC1 43.482441 24.020199 -105.19733 327.62281 -414.2205 191.89804 0. 0. 0. 0. 0. 0.
VC1 0.19191863 -1.3493627 4.4236938 -7.6228897 6.3000968 -1.9853446 0. 0. 0. 0. 0. 0.
PR1 0.0111 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/Pentane [C3/C5]
?Kunz and Wagner (2007)
70c6aac0/76bc0290
KW0 0.996484021 1.008344412 1.044919431 1.019921513 0. 0. 0. 0. 0. 0. 0. 0.
TC1 42.661282 52.787476 -150.04154 435.04348 -554.37767 258.80385 0. 0. 0. 0. 0. 0.
VC1 0.073968563 -0.1476056 -0.11503387 0.73924454 -1.2181534 0.63094307 0. 0. 0. 0. 0. 0.
PR1 0.0267 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/R113 [C3/R113]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.22% from 11 bubble-point pressures
70c6aac0/d2a09ee0
XR0 1.0047 1.01447 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 70.918992 47.316667 -213.57911 593.58402 -753.19299 360.39314 0. 0. 0. 0. 0. 0.
VC1 0.082593758 -0.87896873 2.8491471 -4.8809282 4.0058742 -1.2369159 0. 0. 0. 0. 0. 0.
!
?Propane/Acetone [C3/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
70c6aac0/342481e0
XR0 1.003109639884 1.0191 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 83.392888 46.588301 -245.4848 634.56652 -802.25759 389.24533 0. 0. 0. 0. 0. 0.
VC1 0.21156485 -1.7428935 5.9242379 -10.804454 9.5911163 -3.3072744 0. 0. 0. 0. 0. 0.
!
?Propane/Isohexane [C3/C6I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.4% from 62 bubble-point pressures
70c6aac0/faa2db70
XR0 0.9988813 1.03496 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 79.859535 128.00658 -473.20963 1278.2389 -1552.6199 720.67164 0. 0. 0. 0. 0. 0.
VC1 0.11459973 -0.59203783 1.4110434 -2.2119484 1.7830954 -0.6221916 0. 0. 0. 0. 0. 0.
!
?Propane/Methanol [C3/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
70c6aac0/c41aa690
KW0 0.992 0.922 1. 1. 2.715 0. 0. 0. 0. 0. 0. 0.
TC2 -233.35375 1884.6616 -7323.1822 10251.322 -4633.3996 0. 0. 0. 0. 0. 0. 0.
VC2 -0.6206779 4.0484043 -16.344431 27.199971 -15.924218 0. 0. 0. 0. 0. 0. 0.
!
?Propane/Hexane [C3/C6]
?Kunz and Wagner (2007)
70c6aac0/cb03ba40
KW0 1. 1.025657518 1. 1.057872566 0. 0. 0. 0. 0. 0. 0. 0.
TC1 94.244749 43.85511 -265.795 1000.0482 -1376.393 691.69637 0. 0. 0. 0. 0. 0.
VC1 0.13353163 -0.95917398 3.295615 -6.1364 5.5512586 -1.9714446 0. 0. 0. 0. 0. 0.
PR1 0.0007 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/Ethanol [C3/ETO]
?E.W. Lemmon, NIST (2015)
70c6aac0/3d5f67e0
KW0 1.016 0.998 1.064 0.964 1.15 0. 0. 0. 0. 0. 0. 0.
TC4 -40.378667 224.8016 -370.23198 62.682906 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.18690165 -0.34807447 0.75923041 -0.68798217 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0315 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/Benzene [C3/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
70c6aac0/f2cfb460
XR0 1. 1.018 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 130.91252 -105.13182 305.08711 -230.52988 -266.92931 333.00808 0. 0. 0. 0. 0. 0.
VC1 0.083020069 -1.0481489 3.8676536 -8.050344 7.9708707 -3.0716965 0. 0. 0. 0. 0. 0.
PR1 0.0233 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/Cyclohexane [C3/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
70c6aac0/6e225350
XR0 1.0023 1.035 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 103.84036 171.23765 -677.45102 1766.6491 -2199.2133 1045.637 0. 0. 0. 0. 0. 0.
VC1 0.066512696 -0.57162377 1.3528985 -2.5613569 2.6061491 -1.1474649 0. 0. 0. 0. 0. 0.
!
?Propane/Heptane [C3/C7]
?Kunz and Wagner (2007)
70c6aac0/b398a3b0
KW0 1. 1.050044169 1. 1.079648053 0. 0. 0. 0. 0. 0. 0. 0.
TC1 145.3681 139.93931 -709.12361 2234.2263 -2846.8889 1350.878 0. 0. 0. 0. 0. 0.
VC1 0.42231783 -3.2247933 11.873237 -23.03296 21.844536 -8.1313128 0. 0. 0. 0. 0. 0.
PR1 0.0056 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/Water [C3/H2O]
?Kunz and Wagner (2007)
70c6aac0/b43a7600
KW0 1. 0.600340961 1. 1.011759763 0. 0. 0. 0. 0. 0. 0. 0.
TC6 301.94718 -682.53913 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 -0.11373541 -0.75868454 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Propane/Methylcyclohexane [C3/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
70c6aac0/0429edd0
XR0 1. 1.06 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 109.94372 283.76446 -1052.653 3020.334 -3859.4942 1814.3735 0. 0. 0. 0. 0. 0.
VC1 0.01354179 -0.061545649 0.49392698 -2.886998 4.3627477 -2.3146009 0. 0. 0. 0. 0. 0.
!
?Propane/Toluene [C3/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
70c6aac0/a49b8b50
XR0 1. 1.049 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 174.90219 187.7017 -1046.8878 3136.1388 -4129.2906 1974.788 0. 0. 0. 0. 0. 0.
VC1 0.18928375 -1.8061783 6.4681246 -13.094562 12.948214 -5.1489512 0. 0. 0. 0. 0. 0.
!
?Propane/Octane [C3/C8]
?Kunz and Wagner (2007)
70c6aac0/f174a9b0
KW0 1. 1.063694129 1. 1.102764612 0. 0. 0. 0. 0. 0. 0. 0.
TC1 164.84979 291.76437 -1245.632 3577.3649 -4426.8684 2059.4978 0. 0. 0. 0. 0. 0.
VC1 0.65428465 -4.9061592 17.802606 -34.494167 32.983404 -12.423711 0. 0. 0. 0. 0. 0.
!
?Propane/m-Xylene [C3/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.88% from 25 bubble-point pressures
70c6aac0/0f99ff70
XR0 0.9965519 1.08363 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 246.52247 12.973158 -780.61115 3819.2443 -5671.7589 2808.9765 0. 0. 0. 0. 0. 0.
VC1 0.4681266 -4.6182891 18.711731 -38.894659 38.835151 -15.228163 0. 0. 0. 0. 0. 0.
!
?Propane/Nonane [C3/C9]
?Kunz and Wagner (2012)
70c6aac0/7f94dc20
KW0 1. 1.109973833 1. 1.199769134 0. 0. 0. 0. 0. 0. 0. 0.
TC1 168.12627 457.16806 -1746.0375 5118.0876 -6126.0544 2758.2229 0. 0. 0. 0. 0. 0.
VC1 0.45929971 -2.298998 9.1142825 -20.626784 22.533842 -9.6862015 0. 0. 0. 0. 0. 0.
!
?Propane/Propylcyclohexane [C3/C3CC6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.97% from 27 bubble-point pressures
70c6aac0/206f01b0
XR0 0.9948665 1.10943 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 173.24013 665.00683 -2614.1302 7133.0315 -8476.0996 3659.3774 0. 0. 0. 0. 0. 0.
VC1 0.11784363 -0.50075387 2.8996153 -10.962991 15.658005 -8.0913272 0. 0. 0. 0. 0. 0.
!
?Propane/Decane [C3/C10]
?Kunz and Wagner (2012)
70c6aac0/111888d0
KW0 0.985331233 1.140905252 0.984104227 1.053040574 0. 0. 0. 0. 0. 0. 0. 0.
TC1 251.70098 407.14988 -1255.699 3505.8023 -3716.2542 1517.6352 0. 0. 0. 0. 0. 0.
VC1 0.83652869 -6.255098 23.95884 -50.009739 51.764969 -21.275098 0. 0. 0. 0. 0. 0.
!
?Propane/Dodecane [C3/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
70c6aac0/8bc8dec0
XR0 1. 1.19 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 267.76365 670.27455 -2171.4937 5922.8868 -5497.1941 1524.6492 0. 0. 0. 0. 0. 0.
VC1 1.3240983 -12.229374 51.986207 -110.97978 112.83318 -44.618723 0. 0. 0. 0. 0. 0.
!
?Propane/Methyl palmitate [C3/MPLMT]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.01% from 83 bubble-point pressures
70c6aac0/27c9ec60
XR0 0.9215401 1.21332 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 544.48962 259.21364 790.11681 -9315.0323 20215.537 -11524.749 0. 0. 0. 0. 0. 0.
VC1 2.2494554 -27.868277 97.96153 -165.4451 142.04442 -51.274527 0. 0. 0. 0. 0. 0.
!
?R22/R115 [R22/R115]
?E.W. Lemmon, NIST (2002)
57716470/f7285250
KWT 1. 0.9453230 1. 1.0146614 -1.082 0. 0. 0. 0. 0. 0. 0.
TC1 -31.545042 -14.561094 -5.2798935 34.504147 -19.777808 2.1118255 0. 0. 0. 0. 0. 0.
VC1 0.053651059 -0.28892241 1.7002077 -4.3155015 4.3123777 -1.5055034 0. 0. 0. 0. 0. 0.
PR1 0.0874 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R22/R218 [R22/R218]
?E.W. Lemmon, NIST (2002)
57716470/00bd3610
XR0 1. 0.8866968 1. 1.0293533 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -56.770877 -38.12295 -206.48534 568.82132 -457.9155 123.48825 0. 0. 0. 0. 0. 0.
VC1 0.10124385 -1.2710267 7.3133538 -17.670551 18.109234 -6.7064464 0. 0. 0. 0. 0. 0.
!
?R22/R1216 [R22/R1216]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.7% from 69 bubble-point pressures
57716470/edc3a7b0
XR0 1.0040866 0.96186 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -19.461658 -14.441793 -3.1063825 1.823159 10.511114 -5.4903979 0. 0. 0. 0. 0. 0.
VC1 0.058748446 -0.16943221 0.2541055 0.20978445 -0.92316014 0.54393944 0. 0. 0. 0. 0. 0.
!
?R22/R12 [R22/R12]
?E.W. Lemmon, NIST (2002)
57716470/98829b70
XR0 1. 0.9701504 1. 1.0056117 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -12.137267 -14.568073 2.9506946 -0.84425405 3.5946769 -1.2980849 0. 0. 0. 0. 0. 0.
VC1 0.0098200095 -0.033502569 0.11708603 -0.16273931 0.14618542 -0.066937713 0. 0. 0. 0. 0. 0.
TRN -0.0213 0.0698 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0522 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R22/R134a [R22/R134A]
?E.W. Lemmon, NIST (2002)
57716470/ff1c0560
XR0 1. 0.9907541 1. 1.0032063 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -3.6557722 -10.460641 34.431777 -66.904731 62.764884 -22.462101 0. 0. 0. 0. 0. 0.
VC1 0.015618996 -0.0083393571 -0.016520064 0.067718091 -0.077515446 0.030826862 0. 0. 0. 0. 0. 0.
!
?R22/Dimethyl ether [R22/DME]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.85% from 57 bubble-point pressures
57716470/8f27e300
XR0 0.985309042181 1.07125 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 42.026565 29.487567 -58.531643 199.7955 -237.05471 131.16897 0. 0. 0. 0. 0. 0.
VC1 0.0026979736 -0.054884408 0.3555061 -1.0009411 1.3188081 -0.66976415 0. 0. 0. 0. 0. 0.
!
?R22/R152a [R22/R152A]
?E.W. Lemmon, NIST (2002)
57716470/63f364b0
KWT 1. 1.0167222 1. 0.9961647 1.717 0. 0. 0. 0. 0. 0. 0.
TC1 9.4278193 1.488518 1.3584469 -0.41662767 1.4222366 -0.6249063 0. 0. 0. 0. 0. 0.
VC1 0.0030900319 0.002565335 -0.035283549 0.13277317 -0.18254155 0.093196923 0. 0. 0. 0. 0. 0.
TRN -0.1382 0.4355 0. 0. -0.48 0. 0. 0. 0. 0. 0. 0.
!
?R22/R124 [R22/R124]
?E.W. Lemmon, NIST (2002)
57716470/36953260
XR0 1. 1.0004273 1. 1.0126149 0. 0. 0. 0. 0. 0. 0. 0.
TC1 9.1213608 1.8745047 2.2159003 -3.5300205 5.9636689 -2.3304047 0. 0. 0. 0. 0. 0.
VC1 0.056625254 -0.16004618 0.2477062 0.028619448 -0.43050447 0.31651285 0. 0. 0. 0. 0. 0.
!
?R22/R142b [R22/R142B]
?E.W. Lemmon, NIST (2002)
57716470/f2a8b2e0
XR0 1. 1.0050317 1. 1.0080566 0. 0. 0. 0. 0. 0. 0. 0.
TC1 13.265825 6.7563803 -1.9460589 6.1707106 -5.9298403 3.9725224 0. 0. 0. 0. 0. 0.
VC1 0.026506982 -0.012680301 -0.16989468 0.58555497 -0.76353116 0.3653293 0. 0. 0. 0. 0. 0.
TRN 0. 0. 0. 0. -0.75 0. 0. 0. 0. 0. 0. 0.
!
?R22/RC318 [R22/RC318]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.24% from 6 bubble-point pressures
57716470/9e4d8e90
XR0 1.05268 0.96966 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 18.953955 -27.230756 0.7228808 88.537589 -393.09581 252.74414 0. 0. 0. 0. 0. 0.
VC1 0.031832975 0.092830414 0.24400875 -2.6021198 4.4403826 -2.1682951 0. 0. 0. 0. 0. 0.
!
?R22/R114 [R22/R114]
?E.W. Lemmon, NIST (2002)
57716470/b1698aa0
KWT 1. 0.9712526 1. 1.0175958 -1.011 0. 0. 0. 0. 0. 0. 0.
TC1 9.4576333 -0.47408539 -28.36759 34.719589 -20.955028 8.1106748 0. 0. 0. 0. 0. 0.
VC1 0.022324174 0.051669858 -0.63973146 1.9583943 -2.4442423 1.1304013 0. 0. 0. 0. 0. 0.
!
?R22/R11 [R22/R11]
?E.W. Lemmon, NIST (2002)
57716470/6f9b71e0
XR0 1. 0.9751865 1. 1.0137561 0. 0. 0. 0. 0. 0. 0. 0.
TC1 31.050083 6.9281061 -72.671384 113.59722 -95.547698 36.869776 0. 0. 0. 0. 0. 0.
VC1 0.013308507 -0.24255598 0.55931898 -0.5593624 0.21571727 0.015197186 0. 0. 0. 0. 0. 0.
!
?R22/R123 [R22/R123]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.67% from 56 bubble-point pressures
57716470/efdfede0
XR0 1.005207 1.01277 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 45.774362 42.092997 -71.16395 148.51625 -180.72398 88.104388 0. 0. 0. 0. 0. 0.
VC1 0.11822781 -0.5339171 1.0984091 -1.3449991 0.81327497 -0.16249869 0. 0. 0. 0. 0. 0.
!
?R22/Pentane [R22/C5]
?E.W. Lemmon, NIST (2002)
57716470/76bc0290
XR0 1. 0.9569485 1. 1.0331871 0. 0. 0. 0. 0. 0. 0. 0.
TC1 50.696088 6.1041133 -159.43608 207.19164 -134.26476 44.272025 0. 0. 0. 0. 0. 0.
VC1 0.14487902 -0.94097064 2.2289639 -2.4692474 1.1312338 -0.026977868 0. 0. 0. 0. 0. 0.
!
?R22/R113 [R22/R113]
?E.W. Lemmon, NIST (2002)
57716470/d2a09ee0
XR0 1. 0.9774450 1. 1.0412243 0. 0. 0. 0. 0. 0. 0. 0.
TC1 76.656112 -28.944998 -49.307257 182.1874 -234.53937 125.50127 0. 0. 0. 0. 0. 0.
VC1 0.10572537 -1.2403029 4.418994 -7.711387 6.5771924 -2.1398734 0. 0. 0. 0. 0. 0.
!
?R22/Acetone [R22/ACT]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.51% from 40 bubble-point pressures
57716470/342481e0
XR0 0.955511389696 1.07981 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 89.71099 142.40898 -888.76404 2736.5903 -3310.3014 1585.9111 0. 0. 0. 0. 0. 0.
VC1 0.27547284 -2.5509504 10.425354 -21.557184 21.890115 -8.7647269 0. 0. 0. 0. 0. 0.
!
?R22/Methanol [R22/MEO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.44% from 19 bubble-point pressures
57716470/c41aa690
XR0 0.997386846462 1.03751 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 66.200013 44.403859 -91.771091 287.36981 -403.11544 226.05665 0. 0. 0. 0. 0. 0.
VC1 -0.012086914 -0.38425664 1.9313838 -4.808578 5.4164802 -2.3365757 0. 0. 0. 0. 0. 0.
!
?R22/Hexane [R22/C6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.9% from 56 bubble-point pressures
57716470/cb03ba40
XR0 1.010866818297 0.99579 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 115.88444 -59.333017 314.39909 -526.3865 263.28518 9.4176406 0. 0. 0. 0. 0. 0.
VC1 0.18170924 -1.4970691 5.0486032 -9.6068444 8.9303424 -3.1273068 0. 0. 0. 0. 0. 0.
!
?R22/Ethanol [R22/ETO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.59% from 76 bubble-point pressures
57716470/3d5f67e0
XR0 1.006309560947 1.05058 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 94.737633 68.176248 -86.384807 287.30001 -510.37929 307.97109 0. 0. 0. 0. 0. 0.
VC1 0.034539322 -0.30311412 1.1493316 -3.2174077 3.827008 -1.6772289 0. 0. 0. 0. 0. 0.
!
?R22/Benzene [R22/BEN]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.64% from 29 bubble-point pressures
57716470/f2cfb460
XR0 0.989511181476 1.03496 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 140.7006 -47.140767 59.46704 434.69774 -936.67913 601.77398 0. 0. 0. 0. 0. 0.
VC1 0.10719394 -1.1642997 4.6015082 -9.9213536 10.418726 -4.3074637 0. 0. 0. 0. 0. 0.
!
?R22/Cyclohexane [R22/CC6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.75% from 77 bubble-point pressures
57716470/6e225350
XR0 1.009142834077 0.97638 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 122.67522 70.595791 -135.59122 -126.43742 199.44675 -33.480288 0. 0. 0. 0. 0. 0.
VC1 0.14914557 -1.3795478 3.769792 -6.3519395 5.6692913 -1.9662295 0. 0. 0. 0. 0. 0.
!
?R115/R114 [R115/R114]
?E.W. Lemmon, NIST (2002)
f7285250/b1698aa0
XR0 1. 1.0008497 1. 1.0021192 0. 0. 0. 0. 0. 0. 0. 0.
TC1 15.338319 2.5121535 -5.1638479 10.340705 -11.419487 5.5916538 0. 0. 0. 0. 0. 0.
VC1 -0.007296398 -0.048704947 0.15566868 -0.43220784 0.55241183 -0.27621064 0. 0. 0. 0. 0. 0.
!
?R161/R1234yf [R161/R1234YF]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.23% from 50 bubble-point pressures
edb53660/40377b40
XR0 1.0021948 0.98828 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -5.4597471 -4.048354 -2.3112617 3.2436436 -2.6711698 1.12921 0. 0. 0. 0. 0. 0.
VC1 0.031321908 -0.14978451 0.40984158 -0.66747535 0.55883231 -0.18568352 0. 0. 0. 0. 0. 0.
!
?R161/R134a [R161/R134A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.29% from 31 bubble-point pressures
edb53660/ff1c0560
XR0 0.998991019071 1.00619 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 4.9972641 -7.0475348 36.108235 -69.679788 65.465167 -23.398252 0. 0. 0. 0. 0. 0.
VC1 0.0061068668 -0.0077298678 0.0018439672 0.014283693 -0.021312799 0.0090897452 0. 0. 0. 0. 0. 0.
!
?R161/R227ea [R161/R227EA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.85% from 57 bubble-point pressures
edb53660/40091ee0
XR0 1.00966 1.02456 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 25.865937 -16.714148 42.683913 -58.947849 40.489921 -13.350939 0. 0. 0. 0. 0. 0.
VC1 -0.010352277 0.19150247 -0.6239332 0.93736776 -0.66978295 0.18271417 0. 0. 0. 0. 0. 0.
!
?R218/R134a [R218/R134A]
?E.W. Lemmon, NIST (2005)
00bd3610/ff1c0560
XR0 1. 0.9201114 1. 1.0132426 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -40.229727 -55.686994 69.698487 -125.61568 190.22824 -89.076851 0. 0. 0. 0. 0. 0.
VC1 -0.10001958 0.43659782 -2.0663307 5.6258907 -6.4118654 2.5418291 0. 0. 0. 0. 0. 0.
!
?R218/Isobutane [R218/C4I]
?E.W. Lemmon, NIST (2005)
00bd3610/47ade7e0
XR0 1. 0.8968592 1. 1.0018693 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -7.964172 -193.51167 368.51932 -719.77206 731.7252 -256.4118 0. 0. 0. 0. 0. 0.
VC1 0.017376535 -1.0275638 3.9675367 -7.7228822 8.1203553 -3.388402 0. 0. 0. 0. 0. 0.
!
?R218/RC318 [R218/RC318]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.47% from 47 bubble-point pressures
00bd3610/9e4d8e90
XR0 1.00386 1.04248 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 33.47966 2.9972574 9.9828615 9.7371319 -16.808363 9.7847139 0. 0. 0. 0. 0. 0.
VC1 0.00081332101 -0.025046479 0.098262772 -0.36707944 0.4680435 -0.25511652 0. 0. 0. 0. 0. 0.
!
?Ammonia/R134a [NH3/R134A]
?I.H. Bell, NIST (2018)
e9847540/ff1c0560
XR0 1.055547 0.935232 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 -6.8709632 -91.102716 217.26067 -502.97754 303.26933 0. 0. 0. 0. 0. 0. 0.
VC2 0.052002349 0.025403706 -0.55479328 1.0220409 -0.60558101 0. 0. 0. 0. 0. 0. 0.
!
?Ammonia/Dimethyl ether [NH3/DME]
?E.W. Lemmon, NIST (2011), estimated from P-x plot of Krauss, D. and Schenk, J., Ammonia+dimethyl ether (R723) as a new refrigerant blend, Schick + Co., Wernerstr. 28, D-70469 Stuttgart, Germany, ILK Institut fuer Luft- und Kaeltetechnik gGmbH, Bertolt-Brecht-Allee 20, D-01309 Dresden, Germany
e9847540/8f27e300
KW3 0.9603 0.9724 0.8083 0.521 -1.206 0. 0. 0. 0. 0. 0. 0.
TC1 58.324178 -104.45798 -66.187862 456.65631 -467.80946 210.41736 0. 0. 0. 0. 0. 0.
VC1 -0.020516649 -0.84231109 2.9327243 -5.5762243 5.4185407 -2.0507226 0. 0. 0. 0. 0. 0.
!
?Ammonia/Propyne [NH3/PPY]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.78% from 32 bubble-point pressures
e9847540/3cbb9620
XR0 1.006960006871 0.94154 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -24.50771 -10.208016 -69.034829 99.444806 -66.328281 20.448312 0. 0. 0. 0. 0. 0.
VC1 0.040418698 -0.11338756 0.15508082 -0.15632318 0.11841581 -0.057527017 0. 0. 0. 0. 0. 0.
!
?Ammonia/Isobutane [NH3/C4I]
?I. Cullimore and E.W. Lemmon, NIST (2010) (estimated from propane/ammonia and butane/ammonia)
e9847540/47ade7e0
XR0 1.048657718121 0.7986 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 5.427693 -255.21333 374.26774 -1154.8232 897.66156 0. 0. 0. 0. 0. 0. 0.
VC2 0.22966515 -1.9401097 5.1256043 -5.2288205 1.689992 0. 0. 0. 0. 0. 0. 0.
!
?Ammonia/Butane [NH3/C4]
?I. Cullimore and E.W. Lemmon, NIST (2010)
e9847540/7b3b4080
XR0 1.055631795630 0.8067 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 4.2652447 -140.98951 225.9161 -1140.9262 894.92708 0. 0. 0. 0. 0. 0. 0.
VC2 0.2227993 -1.5805117 3.2513331 -2.1731823 0.15699834 0. 0. 0. 0. 0. 0. 0.
!
?Ammonia/Isopentane [NH3/C5I]
?I. Cullimore and E.W. Lemmon, NIST (2010) (estimated from butane/ammonia and pentane/ammonia)
e9847540/86ee46a0
XR0 1.106194690265 0.8385 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 67.80621 -316.36117 1877.8019 -4281.9903 2697.1289 -238.25012 0. 0. 0. 0. 0. 0.
VC1 0.43628886 -3.8847976 16.23873 -37.051038 41.112918 -17.038169 0. 0. 0. 0. 0. 0.
!
?Ammonia/Pentane [NH3/C5]
?I. Cullimore and E.W. Lemmon, NIST (2010)
e9847540/76bc0290
XR0 1.161980013944 0.8702 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 83.632398 -524.5317 3237.1618 -5572.6669 1727.8143 861.92615 0. 0. 0. 0. 0. 0.
VC1 0.27876678 -2.2212835 13.774724 -41.431844 51.764553 -22.332316 0. 0. 0. 0. 0. 0.
!
?Ammonia/Methanol [NH3/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
e9847540/c41aa690
XR0 0.987 1.117 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 86.029201 299.07997 -1225.1153 3406.9101 -3985.7328 1789.2912 0. 0. 0. 0. 0. 0.
VC1 0.16914854 -1.0420434 3.4580343 -5.6972447 4.435765 -1.4127645 0. 0. 0. 0. 0. 0.
!
?Ammonia/Hexane [NH3/C6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
e9847540/cb03ba40
XR0 1.130454442686 0.8776 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 146.89638 -843.75516 5386.1099 -11157.598 8113.8399 -1792.6909 0. 0. 0. 0. 0. 0.
VC1 0.29244771 -2.4062258 14.474821 -43.573 54.407195 -23.305793 0. 0. 0. 0. 0. 0.
!
?Ammonia/Ethanol [NH3/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
e9847540/3d5f67e0
XR0 1. 1.101 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 95.844877 239.01018 -848.48519 2545.179 -3066.6231 1392.5349 0. 0. 0. 0. 0. 0.
VC1 0.020214098 -0.018800724 0.60920884 -2.1263283 2.5063624 -1.0705829 0. 0. 0. 0. 0. 0.
!
?Ammonia/Benzene [NH3/BEN]
?I. Cullimore and E.W. Lemmon, NIST (2010)
e9847540/f2cfb460
XR0 1.029654036244 0.9299 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 161.57852 -205.47232 1207.9778 -2605.1793 1829.5827 -351.46434 0. 0. 0. 0. 0. 0.
VC1 0.18979052 -1.3194818 4.2714173 -8.6882866 8.9331288 -3.3872031 0. 0. 0. 0. 0. 0.
!
?Ammonia/Cyclohexane [NH3/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
e9847540/6e225350
KW0 1.107297087809 0.8395 1. 1.3341 -0.08997 0. 0. 0. 0. 0. 0. 0.
TC1 120.14785 -531.75217 4104.7189 -10725.906 10179.498 -3297.2724 0. 0. 0. 0. 0. 0.
VC1 0.28140806 -1.920742 9.5278981 -28.411717 37.369772 -16.766411 0. 0. 0. 0. 0. 0.
!
?Ammonia/Heptane [NH3/C7]
?I. Cullimore and E.W. Lemmon, NIST (2010) (estimated from hexane/ammonia and octane/ammonia)
e9847540/b398a3b0
XR0 1.178828244725 0.9726 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 182.0761 -123.18394 737.49759 4258.3233 -11929.978 6951.0043 0. 0. 0. 0. 0. 0.
VC1 0.4745975 -4.3776556 23.923264 -61.245564 66.294591 -25.024726 0. 0. 0. 0. 0. 0.
!
?Ammonia/Water [NH3/H2O]
?#Note: The TR1 model shows up first below, but the program uses the last set of parameters,
?# which in this case is the model of Bell et al.
?I.H. Bell, K. Gao, J. Wu, and E.W. Lemmon (2018)
e9847540/b43a7600
TR1 0.9648407 1.2395117 1.125455 0.8978069 0.5248379 0. 0. 0. 0. 0. 0. 0.
BAW 0.933585 1.015826 1.044759 1.189754 1. 0. 0. 0. 0. 0. 0. 0.
TC1 148.15952 -281.38211 -466.86772 3933.5643 -6208.8526 3352.3341 0. 0. 0. 0. 0. 0.
VC1 0.16069238 -1.3325703 4.6259404 -8.3849305 7.7375498 -2.9196346 0. 0. 0. 0. 0. 0.
!
?Ammonia/Octane [NH3/C8]
?I. Cullimore and E.W. Lemmon, NIST (2010)
e9847540/f174a9b0
XR0 1.231678778175 1.0676 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 237.72503 739.61384 -7235.964 32088.068 -48852.659 23450.73 0. 0. 0. 0. 0. 0.
VC1 0.39091008 -3.062217 22.654005 -64.667243 70.374189 -25.583724 0. 0. 0. 0. 0. 0.
!
?Ammonia/m-Xylene [NH3/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.7% from 138 bubble-point pressures
e9847540/0f99ff70
XR0 1.042500015116 0.95719 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 316.8403 -695.88211 3301.2219 -5469.049 3109.0826 -311.4185 0. 0. 0. 0. 0. 0.
VC1 0.56558092 -4.9999954 19.863171 -41.083249 40.293031 -14.73155 0. 0. 0. 0. 0. 0.
!
?Cyclopropane/R134a [CC3/R134A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.32% from 31 bubble-point pressures
bc9f5400/ff1c0560
XR0 1.01623 0.91325 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -46.537201 -46.126208 -23.482052 43.218341 72.779363 -58.512713 0. 0. 0. 0. 0. 0.
VC1 0.04589513 -0.3356646 1.4442295 -3.1142504 2.8402346 -0.92353148 0. 0. 0. 0. 0. 0.
!
?R1216/R12 [R1216/R12]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.89% from 15 bubble-point pressures
edc3a7b0/98829b70
XR0 1.000360129647 0.97942 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -12.398159 -5.1123726 -0.23673777 2.9293505 -2.6284864 1.4662325 0. 0. 0. 0. 0. 0.
VC1 -0.027309814 0.022102673 -0.01320996 -0.028346518 0.088555497 -0.043342111 0. 0. 0. 0. 0. 0.
!
?R1216/Butene [R1216/1BE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.46% from 34 bubble-point pressures
edc3a7b0/cd7a06d0
XR0 0.982965212861 0.92312 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -21.192957 -74.391994 -23.989044 161.94888 -117.9612 26.239734 0. 0. 0. 0. 0. 0.
VC1 -0.068618882 -0.10926664 0.38397123 -0.17130617 -0.12685508 0.087874631 0. 0. 0. 0. 0. 0.
!
?R1216/RC318 [R1216/RC318]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.85% from 31 bubble-point pressures
edc3a7b0/9e4d8e90
XR0 1.00387 1.00433 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 10.032156 0.60310926 0.062868533 -3.4543388 0.33497417 0.15357985 0. 0. 0. 0. 0. 0.
VC1 0.0047893016 0.0086509191 -0.052782364 0.058710246 -0.042956223 0.019352209 0. 0. 0. 0. 0. 0.
!
?R1216/R123 [R1216/R123]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.75% from 11 bubble-point pressures
edc3a7b0/efdfede0
XR0 1.004939983477 0.97467 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 26.537719 -5.8187377 -42.62184 19.907238 -1.2964548 -2.0514627 0. 0. 0. 0. 0. 0.
VC1 -0.0080589185 -0.3904525 1.4111507 -3.279387 3.7609183 -1.6532246 0. 0. 0. 0. 0. 0.
!
?R12/R134a [R12/R134A]
?E.W. Lemmon, NIST (2002)
98829b70/ff1c0560
XR0 1. 0.9404374 1. 1.0003354 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -39.582492 -28.560299 28.12108 32.031683 -31.08274 6.5273124 0. 0. 0. 0. 0. 0.
VC1 -0.00080887857 -0.10973149 0.81103862 -2.012679 1.9973635 -0.70826813 0. 0. 0. 0. 0. 0.
!
?R12/R152a [R12/R152A]
?E.W. Lemmon, NIST (2002)
98829b70/63f364b0
XR0 1. 0.9425830 1. 1.0025770 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -38.807533 -18.181755 -5.2973904 55.044034 -32.4398 4.4018693 0. 0. 0. 0. 0. 0.
VC1 -0.01733035 -0.0075306912 0.27315071 -0.46509735 0.16032557 0.051088095 0. 0. 0. 0. 0. 0.
!
?R12/R142b [R12/R142B]
?E.W. Lemmon, NIST (2002)
98829b70/f2a8b2e0
XR0 1. 0.9777321 1. 1.0002214 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -10.175384 -8.6561646 -1.5979301 3.6869893 -0.88245542 0.14744084 0. 0. 0. 0. 0. 0.
VC1 -0.0045902792 -0.011449619 0.045187368 -0.043786779 0.026563486 -0.010618459 0. 0. 0. 0. 0. 0.
!
?R12/RC318 [R12/RC318]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.76% from 61 bubble-point pressures
98829b70/9e4d8e90
XR0 1.00226 0.96907 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -14.43518 -11.019637 -4.9563698 3.2066887 3.9042409 -2.0885728 0. 0. 0. 0. 0. 0.
VC1 0.023411393 -0.026323593 0.019980464 0.039060823 -0.079554233 0.02676488 0. 0. 0. 0. 0. 0.
!
?R12/R114 [R12/R114]
?E.W. Lemmon, NIST (2002)
98829b70/b1698aa0
XR0 1. 0.9983405 1. 1.0085162 0. 0. 0. 0. 0. 0. 0. 0.
TC1 7.4224269 2.4495384 -0.82994591 2.6043301 -2.1298054 1.4810649 0. 0. 0. 0. 0. 0.
VC1 0.0080380398 0.0028968159 -0.037548312 0.10680981 -0.13119701 0.063522686 0. 0. 0. 0. 0. 0.
!
?R12/R11 [R12/R11]
?E.W. Lemmon, NIST (2002)
98829b70/6f9b71e0
XR0 1. 1.0044593 1. 1.0018062 0. 0. 0. 0. 0. 0. 0. 0.
TC1 22.743309 8.9392649 -12.051672 34.391178 -41.527618 22.684755 0. 0. 0. 0. 0. 0.
VC1 -0.023055311 -0.09035813 0.51934506 -1.4142892 1.7386615 -0.81614375 0. 0. 0. 0. 0. 0.
!
?R12/Diethyl ether [R12/DEE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.83% from 36 bubble-point pressures
98829b70/46a701e0
XR0 1.004328656510 1.02787 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 43.174855 24.746826 -15.914969 63.607287 -94.899278 51.401253 0. 0. 0. 0. 0. 0.
VC1 0.0016780173 -0.10162083 0.48782806 -1.4398916 1.8107973 -0.85321144 0. 0. 0. 0. 0. 0.
!
?R12/R113 [R12/R113]
?E.W. Lemmon, NIST (2002)
98829b70/d2a09ee0
XR0 1. 1.0301898 1. 1.0165841 0. 0. 0. 0. 0. 0. 0. 0.
TC1 57.232411 36.944257 -67.520249 225.71279 -284.72704 147.97372 0. 0. 0. 0. 0. 0.
VC1 0.065929731 -0.62942489 2.4230292 -5.1067377 5.3022067 -2.1833265 0. 0. 0. 0. 0. 0.
!
?R12/Cyclohexane [R12/CC6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.03% from 2 bubble-point pressures
98829b70/6e225350
XR0 1.038507871890 0.989 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 95.075636 -35.842386 609.11521 -1681.5485 1533.2475 -499.52579 0. 0. 0. 0. 0. 0.
VC1 0.05192311 -0.53418882 1.622228 -4.377639 4.8431723 -1.7362419 0. 0. 0. 0. 0. 0.
!
?R12/Heptane [R12/C7]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.43% from 4 bubble-point pressures
98829b70/b398a3b0
XR0 1.011920422578 1.03388 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 137.02244 73.61538 -196.10583 698.91672 -1075.5812 558.07583 0. 0. 0. 0. 0. 0.
VC1 0.37720949 -3.0128257 10.814728 -21.14456 20.156424 -7.4687211 0. 0. 0. 0. 0. 0.
!
?R12/Octane [R12/C8]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.02% from 2 bubble-point pressures
98829b70/f174a9b0
XR0 1.003482082827 1.06084 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 157.11433 248.32502 -899.00397 2570.9002 -3295.2576 1557.3761 0. 0. 0. 0. 0. 0.
VC1 0.63910672 -5.0898194 18.382986 -35.747718 34.227611 -12.896507 0. 0. 0. 0. 0. 0.
!
?R1234yf/R134a [R1234YF/R134A]
?E.W. Lemmon, NIST (2013)
40377b40/ff1c0560
XR0 1. 0.985 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -9.9853692 -9.5430775 34.128183 -62.871803 59.248474 -21.306207 0. 0. 0. 0. 0. 0.
VC1 -0.0083129694 0.023137893 -0.046892213 0.12833899 -0.14875803 0.06357655 0. 0. 0. 0. 0. 0.
!
?R1234yf/R152a [R1234YF/R152A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.13% from 50 bubble-point pressures
40377b40/63f364b0
XR0 0.996300040539 0.98112 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -15.787637 0.34244368 5.6604042 -1.9003625 0.5890511 -0.49678279 0. 0. 0. 0. 0. 0.
VC1 -0.019284179 0.034173927 -0.039881389 0.0835224 -0.090228033 0.036542275 0. 0. 0. 0. 0. 0.
!
?R1234yf/R1234ze(E) [R1234YF/R1234ZEE]
?E.W. Lemmon, NIST (2015); fit of data from Honeywell
40377b40/9905ef70
XR0 1. 0.987 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -7.1434447 -4.9702253 2.8323449 -1.4755042 1.3431936 -0.43993195 0. 0. 0. 0. 0. 0.
VC1 0.033731321 -0.32571815 1.2166965 -2.2685455 2.0656689 -0.7261691 0. 0. 0. 0. 0. 0.
!
?R1234yf/R227ea [R1234YF/R227EA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.27% from 40 bubble-point pressures
40377b40/40091ee0
XR0 0.999379984658 0.99916 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0.37516255 0.20090577 0.98689713 -0.9708925 0.93350497 -0.32922441 0. 0. 0. 0. 0. 0.
VC1 0.0023052604 0.01194061 -0.020192302 0.04951049 -0.055142787 0.027270546 0. 0. 0. 0. 0. 0.
!
?R1234yf/Isobutane [R1234YF/C4I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.16% from 49 bubble-point pressures
40377b40/47ade7e0
XR0 0.992752903802 0.93536 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -15.276409 -93.745405 128.11178 -173.66419 174.9122 -66.205399 0. 0. 0. 0. 0. 0.
VC1 0.062014261 -0.80045102 2.9966383 -5.23089 4.512602 -1.550659 0. 0. 0. 0. 0. 0.
!
?R134a/Dimethyl ether [R134A/DME]
?E.W. Lemmon, NIST (2006)
ff1c0560/8f27e300
XR0 1. 1.0134905 1. 1.0025949 0. 0. 0. 0. 0. 0. 0. 0.
TC1 9.8761163 3.230271 -15.268122 46.33363 -55.678522 25.263479 0. 0. 0. 0. 0. 0.
VC1 0.0012738249 -0.015251734 0.055218602 -0.1630051 0.20348635 -0.10313228 0. 0. 0. 0. 0. 0.
!
?R134a/R152a [R134A/R152A]
?E.W. Lemmon and R.T Jacobsen, J. Phys. Chem. Ref. Data, 33(2):593-620, 2004.
ff1c0560/63f364b0
KWT 1. 1.0056547 1. 1.0121687 2. 0. 0. 0. 0. 0. 0. 0.
TC1 -0.54296638 2.571249 -15.000584 40.116354 -48.999523 22.347244 0. 0. 0. 0. 0. 0.
VC1 0.0035286957 0.0076523695 -0.014090133 0.025391376 -0.023609821 0.011633437 0. 0. 0. 0. 0. 0.
!
?R134a/RE143a [R134A/RE143A]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.06% from 24 bubble-point pressures
ff1c0560/bf6c1a00
XR0 0.99957 0.99594 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -2.5929148 0.99959153 -9.2573927 29.778911 -39.289526 18.785912 0. 0. 0. 0. 0. 0.
VC1 0.0033086907 -0.004194953 0.022092987 -0.050419197 0.052962264 -0.021317867 0. 0. 0. 0. 0. 0.
!
?R134a/R1234ze(E) [R134A/R1234ZEE]
?E.W. Lemmon, NIST (2015); fit of data from Honeywell
ff1c0560/9905ef70
XR0 1. 0.992 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -3.6537383 -0.66158053 -14.544807 42.74642 -52.267112 23.681845 0. 0. 0. 0. 0. 0.
VC1 0.10856663 -0.8791067 3.2991192 -6.1823073 5.6013068 -1.9553393 0. 0. 0. 0. 0. 0.
!
?R134a/R227ea [R134A/R227EA]
?E.W. Lemmon, NIST (2002)
ff1c0560/40091ee0
XR0 1. 0.9855694 1. 1.0104107 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -7.118998 -3.1509722 -11.039191 37.726338 -47.606983 21.9644 0. 0. 0. 0. 0. 0.
VC1 0.01437687 0.0029932609 0.041420152 -0.064268614 0.026360706 -0.0048549393 0. 0. 0. 0. 0. 0.
!
?R134a/R124 [R134A/R124]
?E.W. Lemmon, NIST (2002)
ff1c0560/36953260
XR0 1. 0.9874736 1. 1.0031148 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -2.868016 -4.3218748 -11.142295 35.100518 -44.61036 20.890433 0. 0. 0. 0. 0. 0.
VC1 0.023648048 -0.096270899 0.28134978 -0.44322272 0.37707792 -0.13148104 0. 0. 0. 0. 0. 0.
!
?R134a/Isobutane [R134A/C4I]
?E.W. Lemmon, NIST (2002)
ff1c0560/47ade7e0
XR0 1. 0.8937027 1. 1.0051783 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -13.072421 -194.97232 385.23896 -851.7578 968.16165 -370.89502 0. 0. 0. 0. 0. 0.
VC1 0.10187767 -1.0927892 3.3039248 -4.1098147 2.385602 -0.65915514 0. 0. 0. 0. 0. 0.
!
?R134a/R142b [R134A/R142B]
?E.W. Lemmon, NIST (2002)
ff1c0560/f2a8b2e0
XR0 1. 0.9869325 1. 1.0011016 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.8252636 -2.3419558 -15.97733 41.182179 -49.767495 22.613522 0. 0. 0. 0. 0. 0.
VC1 -0.0048050616 -0.0014838485 0.013141608 -0.015289093 0.019175273 -0.0072585944 0. 0. 0. 0. 0. 0.
!
?R134a/R236fa [R134A/R236FA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.03% from 15 bubble-point pressures
ff1c0560/77fa2150
XR0 0.99958 1.00198 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 8.3318701 2.202577 -11.713633 36.971641 -45.378168 20.427345 0. 0. 0. 0. 0. 0.
VC1 0.043225677 -0.15430748 0.42219819 -0.62353476 0.47699916 -0.13146801 0. 0. 0. 0. 0. 0.
!
?R134a/Butane [R134A/C4]
?E.W. Lemmon, NIST (2006)
ff1c0560/7b3b4080
XR0 1. 0.8929711 1. 1.0047311 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -11.989595 -124.24248 80.900465 -237.5113 317.73425 -107.54662 0. 0. 0. 0. 0. 0.
VC1 0.072571991 -1.062979 3.4203771 -5.1585027 4.4553389 -1.7846406 0. 0. 0. 0. 0. 0.
!
?R134a/R245fa [R134A/R245FA]
?E.W. Lemmon, NIST (2016)
ff1c0560/5c322280
XR0 1. 1.0060512 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 18.892586 7.2285272 -15.779064 41.254097 -50.017668 23.75287 0. 0. 0. 0. 0. 0.
VC1 0.26210887 -2.2541459 8.6363312 -16.374812 14.932612 -5.2254786 0. 0. 0. 0. 0. 0.
!
?R134a/R123 [R134A/R123]
?E.W. Lemmon, NIST (2002)
ff1c0560/efdfede0
XR0 1. 0.9787038 1. 1.0087988 0. 0. 0. 0. 0. 0. 0. 0.
TC1 23.885052 -0.22970259 -55.137248 82.629886 -68.792041 25.180153 0. 0. 0. 0. 0. 0.
VC1 0.053268359 -0.39357704 0.97279501 -1.2810048 0.84471922 -0.18314104 0. 0. 0. 0. 0. 0.
!
?R134a/Isopentane [R134A/C5I]
?E.W. Lemmon, NIST (2006)
ff1c0560/86ee46a0
XR0 1. 0.8993586 1. 1.0146590 0. 0. 0. 0. 0. 0. 0. 0.
TC1 43.830617 -121.37579 -118.2638 169.40634 -105.79796 47.509837 0. 0. 0. 0. 0. 0.
VC1 0.20084541 -2.1896719 7.7572748 -14.43102 13.961418 -5.260541 0. 0. 0. 0. 0. 0.
!
?R134a/R141b [R134A/R141B]
?E.W. Lemmon, NIST (2002)
ff1c0560/ba322c10
XR0 1. 0.9692334 1. 1.0047490 0. 0. 0. 0. 0. 0. 0. 0.
TC1 26.817218 -9.0119357 -61.062554 86.733888 -66.712326 22.330087 0. 0. 0. 0. 0. 0.
VC1 0.019987004 -0.39086477 1.1181278 -1.79812 1.531631 -0.50776191 0. 0. 0. 0. 0. 0.
!
?R134a/Methanol [R134A/MEO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.08% from 14 bubble-point pressures
ff1c0560/c41aa690
XR0 0.992270215025 0.98889 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 40.992823 6.4432214 -151.6368 259.46334 -179.19489 59.32595 0. 0. 0. 0. 0. 0.
VC1 -0.066633182 -0.19481595 1.2438223 -3.6614392 4.6452113 -2.1861404 0. 0. 0. 0. 0. 0.
!
?R134a/Ethanol [R134A/ETO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.85% from 15 bubble-point pressures
ff1c0560/3d5f67e0
XR0 1.029039494536 0.98183 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 91.521562 -268.5649 1860.975 -5329.0884 6028.4702 -2415.5757 0. 0. 0. 0. 0. 0.
VC1 0.050625287 -0.96063837 5.1103333 -14.913318 17.866007 -7.2889821 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/R40 [DME/R40]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.11% from 65 bubble-point pressures
8f27e300/2b938200
XR0 0.99969 1.01217 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 9.9027072 0.62454959 -5.3926214 15.206544 -15.333285 5.9791348 0. 0. 0. 0. 0. 0.
VC1 0.0053540436 0.0012972215 -0.0006210396 0.0064245922 -0.011605281 0.0079139344 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/R227ea [DME/R227EA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.73% from 34 bubble-point pressures
8f27e300/40091ee0
XR0 1.01575 1.05765 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 74.354537 -151.27532 335.80459 -438.33503 323.64954 -103.59065 0. 0. 0. 0. 0. 0.
VC1 -0.19568286 1.3759521 -4.5961264 8.6057347 -8.1777779 3.0287972 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Isobutane [DME/C4I]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8f27e300/47ade7e0
XR0 1. 0.9671 1. 0.969 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -10.139711 -27.505561 16.818213 -21.575347 24.517221 -8.5183134 0. 0. 0. 0. 0. 0.
VC1 0.12794979 -0.99891577 3.457068 -6.1046707 5.2566207 -1.7623152 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Sulfur dioxide [DME/SO2]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8f27e300/7fad4b80
XR0 0.972478848585 1.1053 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 70.423423 65.593275 -253.11829 653.37339 -748.28307 378.45409 0. 0. 0. 0. 0. 0.
VC1 0.0062711924 -0.089185676 0.73153217 -2.2527723 2.8032889 -1.2636261 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Butene [DME/1BE]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8f27e300/cd7a06d0
XR0 1. 0.9802 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -6.3911564 -6.1861532 -5.0461826 7.0464457 -4.0242508 1.1327359 0. 0. 0. 0. 0. 0.
VC1 0.024336919 -0.073448179 0.16100717 -0.20401491 0.1417835 -0.043091417 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Perfluorobutane [DME/C4F10]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.16% from 92 bubble-point pressures
8f27e300/a8f85e00
XR0 1.0495933 0.86921 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -36.503681 -132.51826 510.81065 -1822.0419 2183.2133 -814.06441 0. 0. 0. 0. 0. 0.
VC1 0.052941442 0.76463969 -7.2769137 22.163622 -27.783763 12.067188 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/R236fa [DME/R236FA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.27% from 31 bubble-point pressures
8f27e300/77fa2150
XR0 0.98997 1.04344 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 26.279203 17.58404 -12.139313 65.645971 -70.377348 41.533482 0. 0. 0. 0. 0. 0.
VC1 -0.013423718 0.047611698 0.077255774 -0.19701905 0.10759832 0.0037898746 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Butane [DME/C4]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8f27e300/7b3b4080
XR0 1. 0.9645 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -9.0390343 -17.561051 -15.564223 28.989791 -21.040861 7.2885639 0. 0. 0. 0. 0. 0.
VC1 0.078621513 -0.46398483 1.4314974 -2.308085 1.88587 -0.61997274 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/R236ea [DME/R236EA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.64% from 34 bubble-point pressures
8f27e300/93fd5d40
XR0 0.98075 1.06804 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 37.777848 46.41461 -92.853474 305.94667 -360.08549 190.83799 0. 0. 0. 0. 0. 0.
VC1 -0.0049314584 0.080042987 0.015074104 -0.29456921 0.38163678 -0.16326518 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Pentane [DME/C5]
?S.L. Outcalt and E.W. Lemmon, NIST (2014)
8f27e300/76bc0290
KW2 1.037021673753 0.9892 1.033698573496 1.0372 0.2666 0. 0. 0. 0. 0. 0. 0.
TC1 16.56431 0.77530109 -25.614628 277.14386 -591.08268 269.59453 0. 0. 0. 0. 0. 0.
VC1 -0.10492638 -0.11892541 3.4225803 -10.018906 11.007238 -4.1741292 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Methanol [DME/MEO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8f27e300/c41aa690
KW0 1.004318569850 0.9862 1. 1.072 0.736 0. 0. 0. 0. 0. 0. 0.
TC5 -69.324146 127.22985 -136.86464 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.045494958 0.39985319 -0.097966157 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Hexane [DME/C6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.92% from 48 bubble-point pressures
8f27e300/cb03ba40
XR0 1.009839981766 0.99219 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 80.028395 -29.802078 128.66298 -179.96876 31.844075 41.800679 0. 0. 0. 0. 0. 0.
VC1 0.15410909 -1.1326087 3.5820432 -6.1848194 5.1946433 -1.6061845 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Ethanol [DME/ETO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8f27e300/3d5f67e0
KW0 1.005025125628 1.0417 1. 1.1286 -1.2836 0. 0. 0. 0. 0. 0. 0.
TC1 185.16421 -95.285021 -34.267104 903.08627 -1480.3148 789.85126 0. 0. 0. 0. 0. 0.
VC1 0.086772669 -0.22025437 0.98349695 -2.779452 3.4206518 -1.6183898 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Benzene [DME/BEN]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8f27e300/f2cfb460
XR0 1. 1.0297 1. 1.0203 0. 0. 0. 0. 0. 0. 0. 0.
TC1 105.07458 -31.731639 86.46291 242.13313 -597.46018 373.70816 0. 0. 0. 0. 0. 0.
VC1 0.086399785 -0.72500137 2.5417355 -4.8195274 4.3640872 -1.558307 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Dimethyl carbonate [DME/DMC]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8f27e300/859e6f80
KW0 1. 0.9794 1. 1. 1. 0. 0. 0. 0. 0. 0. 0.
TC1 57.89311 -332.69676 631.97527 -778.90943 413.12307 -83.470123 0. 0. 0. 0. 0. 0.
VC1 -0.15748937 -0.64845299 1.5006822 -0.15568264 -2.2105906 1.4028977 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Toluene [DME/TOL]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8f27e300/a49b8b50
XR0 1. 1.044 1. 1.032 0. 0. 0. 0. 0. 0. 0. 0.
TC1 144.17758 143.13655 -640.20133 1959.8685 -2475.0358 1151.8753 0. 0. 0. 0. 0. 0.
VC1 0.17805757 -1.3555261 4.5997104 -8.6218832 7.9611438 -2.9634319 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Decane [DME/C10]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8f27e300/111888d0
XR0 1. 1.0921 1. 1.0064 0. 0. 0. 0. 0. 0. 0. 0.
TC1 226.55692 407.18587 -1275.9216 3865.1913 -4717.9894 2104.1358 0. 0. 0. 0. 0. 0.
VC1 0.78429162 -5.5497915 19.719821 -38.783672 37.594253 -14.299368 0. 0. 0. 0. 0. 0.
!
?Dimethyl ether/Dodecane [DME/C12]
?I. Cullimore and E.W. Lemmon, NIST (2010)
8f27e300/8bc8dec0
XR0 0.987361769352 1.1448 1. 0.9576 0. 0. 0. 0. 0. 0. 0. 0.
TC1 270.37864 289.66045 -453.43873 1851.4548 -1720.5802 630.54982 0. 0. 0. 0. 0. 0.
VC1 1.3328491 -12.549087 51.260296 -104.74184 102.50016 -38.882765 0. 0. 0. 0. 0. 0.
!
?R152a/R13I1 [R152A/CF3I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.3% from 28 bubble-point pressures
63f364b0/d26ca240
XR0 1.001251564456 0.96404 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -19.264324 -16.4311 0.083389829 6.0314795 3.5135869 -2.806087 0. 0. 0. 0. 0. 0.
VC1 0.017530607 -0.076563249 0.16495586 -0.15498762 0.037523316 0.0052573574 0. 0. 0. 0. 0. 0.
!
?R152a/R227ea [R152A/R227EA]
?E.W. Lemmon, NIST (2002)
63f364b0/40091ee0
XR0 1. 0.9934671 1. 1.0180486 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -4.4685798 -0.44622738 0.49876052 0.1357124 -0.30785446 0.2800481 0. 0. 0. 0. 0. 0.
VC1 0.018209853 -0.011109777 0.016667405 -0.013244724 0.0089600809 -0.0021976586 0. 0. 0. 0. 0. 0.
!
?R152a/R124 [R152A/R124]
?E.W. Lemmon, NIST (2002)
63f364b0/36953260
XR0 1. 0.9906777 1. 1.0077824 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -3.6725538 -4.0033189 3.8751054 -5.5890066 5.0552226 -1.752983 0. 0. 0. 0. 0. 0.
VC1 0.022227055 -0.056340819 0.13914509 -0.1915343 0.13863739 -0.042013073 0. 0. 0. 0. 0. 0.
!
?R152a/Isobutane [R152A/C4I]
?E.W. Lemmon, NIST (2002)
63f364b0/47ade7e0
XR0 1. 0.9227117 1. 1.0108869 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -20.70177 -105.76668 149.2726 -275.86596 321.40325 -128.91049 0. 0. 0. 0. 0. 0.
VC1 0.10909479 -0.92484195 2.9508943 -4.0408759 2.430732 -0.55124863 0. 0. 0. 0. 0. 0.
!
?R152a/R142b [R152A/R142B]
?E.W. Lemmon, NIST (2002)
63f364b0/f2a8b2e0
XR0 1. 0.9901133 1. 1.0043071 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -2.4195627 -3.4209313 -0.12023372 0.51224399 -0.39789635 0.18448482 0. 0. 0. 0. 0. 0.
VC1 0.0064154482 -0.016161306 0.038808216 -0.043699415 0.030171627 -0.0096606893 0. 0. 0. 0. 0. 0.
!
?R152a/Isobutene [R152A/IBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.41% from 67 bubble-point pressures
63f364b0/d287e4b0
XR0 0.999200639488 0.93949 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -20.846651 -46.472125 7.9091947 -11.660276 43.024818 -20.573592 0. 0. 0. 0. 0. 0.
VC1 -0.0017958341 -0.089762123 0.16690047 0.16689286 -0.41478082 0.1657716 0. 0. 0. 0. 0. 0.
!
?R152a/Butane [R152A/C4]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.47% from 112 bubble-point pressures
63f364b0/7b3b4080
XR0 0.997575890586 0.91179 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -18.298379 -98.548073 56.797707 -128.55283 207.51165 -88.798158 0. 0. 0. 0. 0. 0.
VC1 0.073257784 -0.83025179 2.5297257 -3.246621 2.0298303 -0.58435223 0. 0. 0. 0. 0. 0.
!
?R152a/R114 [R152A/R114]
?E.W. Lemmon, NIST (2002)
63f364b0/b1698aa0
XR0 1. 0.9504005 1. 1.0203986 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -13.381189 -27.464622 -11.993439 14.623398 2.4224052 -2.6027619 0. 0. 0. 0. 0. 0.
VC1 0.011708774 -0.065108043 0.19119603 -0.16787028 0.097532855 -0.039520882 0. 0. 0. 0. 0. 0.
!
?R152a/Pentane [R152A/C5]
?E.W. Lemmon, NIST (2002)
63f364b0/76bc0290
XR0 1. 0.9210153 1. 1.0250359 0. 0. 0. 0. 0. 0. 0. 0.
TC1 25.528204 -52.70662 -151.64548 187.31679 -91.98628 21.084594 0. 0. 0. 0. 0. 0.
VC1 0.09938948 -1.0160221 3.1619557 -5.3444682 5.0829453 -1.9289922 0. 0. 0. 0. 0. 0.
!
?R152a/R113 [R152A/R113]
?E.W. Lemmon, NIST (2002)
63f364b0/d2a09ee0
XR0 1. 0.9460750 1. 1.0320957 0. 0. 0. 0. 0. 0. 0. 0.
TC1 51.804256 -98.023255 69.608836 -125.78717 133.49847 -53.76334 0. 0. 0. 0. 0. 0.
VC1 0.039157799 -0.96762731 3.6323429 -6.4796448 5.750193 -1.9208065 0. 0. 0. 0. 0. 0.
!
?R152a/Methanol [R152A/MEO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.76% from 15 bubble-point pressures
63f364b0/c41aa690
XR0 0.988660069008 0.98828 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 36.106958 -9.2501879 -150.38529 318.57214 -247.73599 79.205787 0. 0. 0. 0. 0. 0.
VC1 -0.054568601 -0.20887737 1.1374222 -2.927565 3.4906962 -1.6207031 0. 0. 0. 0. 0. 0.
!
?R152a/Ethanol [R152A/ETO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.94% from 13 bubble-point pressures
63f364b0/3d5f67e0
XR0 1.031502073319 0.97677 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 75.690818 -120.90007 878.64259 -2669.214 2926.2284 -1137.2507 0. 0. 0. 0. 0. 0.
VC1 0.032867724 -0.51685116 2.4044954 -7.5904986 9.4874481 -3.9011504 0. 0. 0. 0. 0. 0.
!
?R40/Isobutene [R40/IBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.4% from 18 bubble-point pressures
2b938200/d287e4b0
XR0 0.999480270259 0.97922 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -9.7514705 -4.5955232 -7.3114054 17.146123 -13.371402 4.1949687 0. 0. 0. 0. 0. 0.
VC1 0.064332242 -0.24941574 0.66208978 -1.0328838 0.83873091 -0.27249511 0. 0. 0. 0. 0. 0.
!
?R13I1/Isobutane [CF3I/C4I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.06% from 28 bubble-point pressures
d26ca240/47ade7e0
XR0 1.001999991984 0.98459 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -7.1216486 -7.4733708 0.38842308 -2.7729495 4.7419043 -1.738916 0. 0. 0. 0. 0. 0.
VC1 0.034079861 -0.17583513 0.52877598 -0.87275328 0.71908541 -0.23340361 0. 0. 0. 0. 0. 0.
!
?R1234ze(E)/Pentane [R1234ZEE/C5]
?S.L. Outcalt and E.W. Lemmon, NIST (2012)
9905ef70/76bc0290
XR0 1.007049345418 0.937 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 21.757495 -22.989908 -124.83178 112.66593 -51.270478 10.451629 0. 0. 0. 0. 0. 0.
VC1 0.03161885 -0.29454631 -0.27624781 2.369112 -3.4080992 1.704055 0. 0. 0. 0. 0. 0.
!
?R227ea/Isobutane [R227EA/C4I]
?E.W. Lemmon, NIST (2002)
40091ee0/47ade7e0
XR0 1. 0.9078054 1. 1.0009088 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -33.049563 -117.33692 221.05609 -519.24083 655.35973 -268.35043 0. 0. 0. 0. 0. 0.
VC1 0.010618961 -0.57575232 2.3430945 -4.7762166 5.372628 -2.4574927 0. 0. 0. 0. 0. 0.
!
?R227ea/Isobutene [R227EA/IBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.41% from 60 bubble-point pressures
40091ee0/d287e4b0
XR0 0.987215558517 0.92836 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -37.781215 -50.307958 15.490865 39.319699 3.9441968 -17.824786 0. 0. 0. 0. 0. 0.
VC1 -0.086296541 0.099216231 0.057808587 -0.3557547 0.7306772 -0.44476197 0. 0. 0. 0. 0. 0.
!
?R227ea/Butane [R227EA/C4]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.77% from 60 bubble-point pressures
40091ee0/7b3b4080
XR0 0.985794698396 0.90171 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -33.44746 -109.69255 76.05883 -110.56864 229.7047 -118.20801 0. 0. 0. 0. 0. 0.
VC1 -0.024411728 -0.74049933 3.3976339 -6.6257521 6.5669516 -2.6043647 0. 0. 0. 0. 0. 0.
!
?R124/R142b [R124/R142B]
?E.W. Lemmon, NIST (2002)
36953260/f2a8b2e0
XR0 1. 1.0025158 1. 1.0005123 0. 0. 0. 0. 0. 0. 0. 0.
TC1 2.0863566 0.48243865 -1.2055001 3.7439554 -4.5782014 2.1029524 0. 0. 0. 0. 0. 0.
VC1 -0.0028272205 -0.00071129698 -0.003006447 0.0060824894 -0.0051785184 0.0012346467 0. 0. 0. 0. 0. 0.
!
?Isobutane/Isobutene [C4I/IBE]
?I. Cullimore and E.W. Lemmon, NIST (2010)
47ade7e0/d287e4b0
XR0 1. 0.9947 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -4.2127853 0.41700412 -5.2092949 14.731489 -18.400113 8.5414809 0. 0. 0. 0. 0. 0.
VC1 -0.0045643101 0.040784767 -0.24710211 0.67964863 -0.84034478 0.3822952 0. 0. 0. 0. 0. 0.
!
?Isobutane/Butene [C4I/1BE]
?I. Cullimore and E.W. Lemmon, NIST (2010)
47ade7e0/cd7a06d0
XR0 1. 0.996 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -3.0868383 -0.16463745 -0.9859224 2.8409042 -3.4375523 1.5292982 0. 0. 0. 0. 0. 0.
VC1 -0.0034514517 0.0097448231 -0.047951046 0.12334701 -0.14476668 0.06259816 0. 0. 0. 0. 0. 0.
!
?Isobutane/Butane [C4I/C4]
?Kunz and Wagner (2007)
?#The values of betaT and betaV are reciprocals of the published values, but deviations are expected to be less than 1 ppb.
47ade7e0/7b3b4080
KW0 0.999922459 1.001432824 0.999120311 1.00041444 -0.0551240293009 0. 0. 0. 0. 0. 0. 0.
TC1 6.7379337 1.1994762 -0.45359839 2.3910622 -2.313984 1.3988509 0. 0. 0. 0. 0. 0.
VC1 0.01503062 -0.016776314 -0.047437409 0.23636241 -0.34078302 0.17334852 0. 0. 0. 0. 0. 0.
PR1 -0.0004 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Isobutane/R245fa [C4I/R245FA]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.58% from 78 bubble-point pressures
47ade7e0/5c322280
XR0 1.01357 0.90803 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -35.363015 -79.911119 75.284131 -357.52216 569.81005 -241.79633 0. 0. 0. 0. 0. 0.
VC1 0.10692493 -1.0367345 2.4911711 -1.1687144 -1.9775605 1.6107105 0. 0. 0. 0. 0. 0.
!
?Isobutane/Isopentane [C4I/C5I]
?Kunz and Wagner (2007)
47ade7e0/86ee46a0
KW0 1. 1.001835788 1. 1.002284353 0. 0. 0. 0. 0. 0. 0. 0.
TC1 14.738235 4.4868956 -9.4314279 17.976226 -16.305693 7.6724738 0. 0. 0. 0. 0. 0.
VC1 0.068313853 -0.32124263 0.71857784 -0.64864052 -0.022355691 0.26289915 0. 0. 0. 0. 0. 0.
!
?Isobutane/Pentane [C4I/C5]
?Kunz and Wagner (2007)
47ade7e0/76bc0290
KW0 1. 1.002495889 1. 1.002779804 0. 0. 0. 0. 0. 0. 0. 0.
TC1 18.834498 4.9336115 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0.009199126 -0.0040288827 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Isobutane/Acetone [C4I/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
47ade7e0/342481e0
XR0 1.016363451570 0.9358 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 24.558348 -39.857186 -158.0681 209.84293 -221.06386 108.12602 0. 0. 0. 0. 0. 0.
VC1 0.13536487 -1.3916834 4.6530613 -8.8921902 8.8533057 -3.3717786 0. 0. 0. 0. 0. 0.
!
?Isobutane/Methanol [C4I/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
47ade7e0/c41aa690
XR0 1.048 0.89 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -13.409163 -44.537643 213.72832 -1259.0123 1317.6539 -337.83717 0. 0. 0. 0. 0. 0.
VC1 -0.10740706 -0.030104138 1.3576088 -7.8156904 12.651046 -5.9376648 0. 0. 0. 0. 0. 0.
!
?Isobutane/Hexane [C4I/C6]
?Kunz and Wagner (2007)
47ade7e0/cb03ba40
KW0 1. 1.006018054 1. 1.010493989 0. 0. 0. 0. 0. 0. 0. 0.
TC1 52.017041 -2.7616908 -14.208379 110.92542 -175.90744 102.73486 0. 0. 0. 0. 0. 0.
VC1 0.055273344 -0.34916572 0.61855276 -0.21674334 -0.69149877 0.60780071 0. 0. 0. 0. 0. 0.
!
?Isobutane/Ethanol [C4I/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
47ade7e0/3d5f67e0
XR0 1.018 0.965 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 26.977166 -16.645849 -67.487587 -13.641855 15.403615 5.5019481 0. 0. 0. 0. 0. 0.
VC1 -0.021311449 -0.13534494 0.22375208 -1.3442551 2.561925 -1.3473522 0. 0. 0. 0. 0. 0.
!
?Isobutane/Benzene [C4I/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
47ade7e0/f2cfb460
XR0 1. 0.992 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 70.598868 -118.4687 329.1467 -550.10899 433.82105 -110.04306 0. 0. 0. 0. 0. 0.
VC1 0.027572641 -0.6370715 2.1460561 -4.0779572 3.7166578 -1.2865426 0. 0. 0. 0. 0. 0.
!
?Isobutane/Cyclohexane [C4I/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
47ade7e0/6e225350
XR0 1. 1.0167 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 58.497455 61.370494 -213.04411 536.60866 -654.41419 323.3187 0. 0. 0. 0. 0. 0.
VC1 -0.015530744 -0.0090514725 -0.51321062 1.2719493 -1.4112063 0.55703395 0. 0. 0. 0. 0. 0.
!
?Isobutane/Heptane [C4I/C7]
?Kunz and Wagner (2007)
47ade7e0/b398a3b0
KW0 1. 1.00988576 1. 1.021668316 0. 0. 0. 0. 0. 0. 0. 0.
TC1 100.01272 18.944341 -209.33273 648.43991 -839.16062 414.14907 0. 0. 0. 0. 0. 0.
VC1 0.3042402 -2.2310358 6.9143079 -11.245288 8.796145 -2.5822893 0. 0. 0. 0. 0. 0.
!
?Isobutane/Water [C4I/H2O]
?Kunz and Wagner (2007)
47ade7e0/b43a7600
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -21.500364 136.13803 -310.10398 681.74472 -798.23021 382.75377 0. 0. 0. 0. 0. 0.
VC1 -0.10621519 0.15374355 -0.33272876 -1.0141195 2.3339844 -1.448778 0. 0. 0. 0. 0. 0.
!
?Isobutane/Methylcyclohexane [C4I/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
47ade7e0/0429edd0
XR0 1. 1.03 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 70.668588 121.14799 -385.32236 1075.4661 -1390.3929 688.13443 0. 0. 0. 0. 0. 0.
VC1 -0.025649409 0.14323741 -0.81074476 1.21204 -0.9528127 0.23974802 0. 0. 0. 0. 0. 0.
!
?Isobutane/Toluene [C4I/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
47ade7e0/a49b8b50
XR0 1. 1.01 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 115.79318 22.878949 -262.65642 739.23106 -975.69386 501.41559 0. 0. 0. 0. 0. 0.
VC1 0.097315996 -1.0259816 2.9974331 -5.2248694 4.4479375 -1.5073738 0. 0. 0. 0. 0. 0.
!
?Isobutane/Octane [C4I/C8]
?Kunz and Wagner (2007)
47ade7e0/f174a9b0
KW0 1. 1.013945424 1. 1.032807063 0. 0. 0. 0. 0. 0. 0. 0.
TC1 126.01577 111.48632 -548.56723 1416.675 -1743.5396 836.01624 0. 0. 0. 0. 0. 0.
VC1 0.53092407 -4.0760793 13.235821 -22.805982 19.356444 -6.3871314 0. 0. 0. 0. 0. 0.
!
?Isobutane/Nonane [C4I/C9]
?Kunz and Wagner (2012)
47ade7e0/7f94dc20
KW0 1. 1.017817492 1. 1.047298475 0. 0. 0. 0. 0. 0. 0. 0.
TC1 152.0641 235.14953 -959.0441 2340.9293 -2871.1502 1367.9523 0. 0. 0. 0. 0. 0.
VC1 0.46972931 -3.070319 8.7111739 -14.357763 12.072687 -4.0547899 0. 0. 0. 0. 0. 0.
!
?Isobutane/Decane [C4I/C10]
?Kunz and Wagner (2012)
47ade7e0/111888d0
KW0 1. 1.021624748 1. 1.060243344 0. 0. 0. 0. 0. 0. 0. 0.
TC1 224.40785 235.63918 -1104.4348 2868.5451 -3694.4623 1804.0369 0. 0. 0. 0. 0. 0.
VC1 0.86718364 -6.4735702 21.372961 -38.694599 34.986501 -12.436694 0. 0. 0. 0. 0. 0.
!
?Isobutane/Dodecane [C4I/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010) (estimated from propane and pentane mixed with dodecane)
47ade7e0/8bc8dec0
XR0 1. 1.16 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 211.64654 687.47075 -2744.9424 7641.6014 -8425.8649 3333.6587 0. 0. 0. 0. 0. 0.
VC1 1.1929099 -10.813457 44.753554 -93.635965 93.955847 -36.951354 0. 0. 0. 0. 0. 0.
!
?Sulfur dioxide/Isobutene [SO2/IBE]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7fad4b80/d287e4b0
XR0 1.0136 0.9405 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -25.949086 -32.287815 6.4305862 -96.222106 136.75006 -48.896795 0. 0. 0. 0. 0. 0.
VC1 0.046612292 -0.15680436 0.2565275 -0.0026630228 -0.44141955 0.27311934 0. 0. 0. 0. 0. 0.
!
?Sulfur dioxide/Diethyl ether [SO2/DEE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.7% from 22 bubble-point pressures
7fad4b80/46a701e0
XR0 1.012268696603 1.04115 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 52.09389 12.39713 34.717847 3.384798 -9.7676794 -4.4282891 0. 0. 0. 0. 0. 0.
VC1 0.003437104 0.055970252 -0.04764184 -0.097491212 0.12549967 -0.038783547 0. 0. 0. 0. 0. 0.
!
?Sulfur dioxide/Acetone [SO2/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7fad4b80/342481e0
XR0 0.990197049213 1.0959 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 83.341926 78.87499 -87.774773 386.83107 -421.2576 219.75835 0. 0. 0. 0. 0. 0.
VC1 0.14370122 -0.80712001 3.0595915 -6.3721916 6.6219247 -2.7737543 0. 0. 0. 0. 0. 0.
!
?Sulfur dioxide/Methanol [SO2/MEO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7fad4b80/c41aa690
XR0 1.038637307852 1.0124 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 51.774288 26.910992 -103.22609 315.57444 -597.60506 292.63081 0. 0. 0. 0. 0. 0.
VC1 -0.032782998 1.1471746 -6.1876262 12.796154 -12.042168 4.3332588 0. 0. 0. 0. 0. 0.
!
?Sulfur dioxide/Ethanol [SO2/ETO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7fad4b80/3d5f67e0
XR0 1.015537727227 1.0224 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 57.391967 29.753406 32.851009 -75.576829 -24.088672 27.747244 0. 0. 0. 0. 0. 0.
VC1 0.017559227 0.047487092 -0.27635165 0.21862869 -0.053978942 0.019777879 0. 0. 0. 0. 0. 0.
!
?Sulfur dioxide/Benzene [SO2/BEN]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7fad4b80/f2cfb460
XR0 1.015847216579 1. 1. 1.0266 0. 0. 0. 0. 0. 0. 0. 0.
TC1 98.889326 -97.045066 496.29863 -815.76999 536.02419 -136.58393 0. 0. 0. 0. 0. 0.
VC1 0.13279512 -1.0116364 3.9066172 -7.8862823 7.4770022 -2.6676703 0. 0. 0. 0. 0. 0.
PR1 0.0015 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Sulfur dioxide/Water [SO2/H2O]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7fad4b80/b43a7600
XR0 1.030502885408 0.9424 1. 0.7 0. 0. 0. 0. 0. 0. 0. 0.
TC1 184.41121 -489.04513 3459.6971 -16967.444 26777.689 -13254.898 0. 0. 0. 0. 0. 0.
VC1 0.012564911 -1.2680286 5.7985611 -15.14967 17.887824 -7.4376249 0. 0. 0. 0. 0. 0.
!
?Sulfur dioxide/Toluene [SO2/TOL]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.74% from 27 bubble-point pressures
7fad4b80/a49b8b50
XR0 1.011330031476 1.02114 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 140.49151 76.857373 -75.855146 422.39041 -695.86366 332.24128 0. 0. 0. 0. 0. 0.
VC1 0.22199562 -1.6430909 5.7455118 -11.039397 10.381802 -3.8134681 0. 0. 0. 0. 0. 0.
!
?Sulfur dioxide/Ethylene glycol [SO2/EGLY]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7fad4b80/7d1768e0
XR0 1. 1.148 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 147.80538 1141.8087 -6804.0307 19106.03 -23178.209 10139.856 0. 0. 0. 0. 0. 0.
VC1 -0.049418526 -0.60221896 3.2154441 -8.5620963 10.446359 -5.1556445 0. 0. 0. 0. 0. 0.
!
?R142b/R141b [R142B/R141B]
?E.W. Lemmon, NIST (2002)
f2a8b2e0/ba322c10
XR0 1. 0.9945438 1. 1.0012780 0. 0. 0. 0. 0. 0. 0. 0.
TC1 10.722322 -1.659318 -3.9862066 6.0564399 -5.4326011 2.3131211 0. 0. 0. 0. 0. 0.
VC1 -0.0070373946 -0.054336989 0.12663693 -0.22817991 0.22644583 -0.10064988 0. 0. 0. 0. 0. 0.
!
?R142b/R113 [R142B/R113]
?E.W. Lemmon, NIST (2002)
f2a8b2e0/d2a09ee0
XR0 1. 0.9839683 1. 1.0129894 0. 0. 0. 0. 0. 0. 0. 0.
TC1 25.357857 -21.583609 10.179021 -12.489156 12.309566 -5.329995 0. 0. 0. 0. 0. 0.
VC1 0.017659835 -0.34116429 1.1857934 -2.0160692 1.702955 -0.54329645 0. 0. 0. 0. 0. 0.
!
?Isobutene/Butane [IBE/C4]
?I. Cullimore and E.W. Lemmon, NIST (2010)
d287e4b0/7b3b4080
XR0 1. 0.997 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.8548507 -0.45823475 0.11657958 -0.20994195 0.28922063 -0.13540116 0. 0. 0. 0. 0. 0.
VC1 0.0027093656 -0.0036841152 0.002818554 -4.3895285e-05 -0.0022047783 0.0013852192 0. 0. 0. 0. 0. 0.
!
?Isobutene/Acetone [IBE/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
d287e4b0/342481e0
XR0 1.013890297070 0.9602 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 22.896837 -35.88727 -25.709441 -46.097503 25.684626 10.88212 0. 0. 0. 0. 0. 0.
VC1 0.12384182 -1.1287789 3.7660845 -6.9988033 6.4780495 -2.2564462 0. 0. 0. 0. 0. 0.
!
?Isobutene/Methanol [IBE/MEO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
d287e4b0/c41aa690
XR0 1.026061974143 0.9209 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -12.313505 -58.384801 104.62184 -547.81542 554.03201 -134.96174 0. 0. 0. 0. 0. 0.
VC1 -0.083231842 -0.048421489 0.62627312 -3.0125483 4.7775509 -2.2500821 0. 0. 0. 0. 0. 0.
!
?Isobutene/Ethanol [IBE/ETO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
d287e4b0/3d5f67e0
XR0 1.022913256956 0.9627 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 23.843135 -26.806821 -7.499373 -153.47156 96.977883 8.7188642 0. 0. 0. 0. 0. 0.
VC1 -0.014182495 -0.12253799 0.19571713 -1.1733053 2.0461335 -0.95272476 0. 0. 0. 0. 0. 0.
!
?Isobutene/Benzene [IBE/BEN]
?I. Cullimore and E.W. Lemmon, NIST (2010)
d287e4b0/f2cfb460
XR0 1. 1.0028 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 68.445868 -100.0024 315.09962 -530.87686 437.79169 -132.89932 0. 0. 0. 0. 0. 0.
VC1 0.046440887 -0.78031322 3.1461522 -6.813408 7.0971177 -2.8938404 0. 0. 0. 0. 0. 0.
!
?Isobutene/Cyclohexane [IBE/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
d287e4b0/6e225350
XR0 1. 1.0101 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 55.382144 26.163069 -54.765276 118.22409 -135.58421 69.326751 0. 0. 0. 0. 0. 0.
VC1 0.0082491663 -0.28224192 0.97362006 -2.3948953 2.875685 -1.3532391 0. 0. 0. 0. 0. 0.
!
?Isobutene/Octane [IBE/C8]
?I. Cullimore and E.W. Lemmon, NIST (2010)
d287e4b0/f174a9b0
XR0 0.992418911932 1.0536 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 119.90235 101.06614 -243.8928 772.97809 -923.07264 443.11557 0. 0. 0. 0. 0. 0.
VC1 0.51846534 -4.0125072 14.73396 -28.969263 28.212238 -10.860759 0. 0. 0. 0. 0. 0.
!
?Butene/Perfluorobutane [1BE/C4F10]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.3% from 36 bubble-point pressures
cd7a06d0/a8f85e00
XR0 1.06345 0.86402 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 -60.531572 5.8036718 -378.42244 302.48913 71.379174 0. 0. 0. 0. 0. 0. 0.
VC2 0.14223243 -1.7393549 7.8441475 -13.358805 7.0398533 0. 0. 0. 0. 0. 0. 0.
!
?Butene/Butane [1BE/C4]
?I. Cullimore and E.W. Lemmon, NIST (2010)
cd7a06d0/7b3b4080
XR0 1. 0.9977 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.4572363 -0.28703068 -0.061521159 0.25225473 -0.29216504 0.13064136 0. 0. 0. 0. 0. 0.
VC1 0.0019824277 -0.0025432073 0.00357412 -0.0057763973 0.0060055847 -0.002555705 0. 0. 0. 0. 0. 0.
PR1 0.0011 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Butene/Acetone [1BE/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
cd7a06d0/342481e0
XR0 1.014610389610 0.9565 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 20.955603 -38.910766 -27.840544 -51.443458 32.842007 10.913361 0. 0. 0. 0. 0. 0.
VC1 0.12447999 -1.1346594 3.778466 -7.0301959 6.5464558 -2.2973936 0. 0. 0. 0. 0. 0.
!
?Butene/Methanol [1BE/MEO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
cd7a06d0/c41aa690
XR0 1.026377912347 0.9185 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -13.568927 -60.560224 109.40373 -578.86525 601.25329 -154.07296 0. 0. 0. 0. 0. 0.
VC1 -0.085051655 -0.0029334337 0.34781055 -2.219737 3.8117783 -1.8338607 0. 0. 0. 0. 0. 0.
!
?Butene/Ethanol [1BE/ETO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
cd7a06d0/3d5f67e0
XR0 1.024275325207 0.9615 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 22.688882 -26.380865 -7.3200493 -159.39764 92.956078 16.736626 0. 0. 0. 0. 0. 0.
VC1 -0.014645071 -0.10262698 0.10043509 -0.94731578 1.8104894 -0.86563918 0. 0. 0. 0. 0. 0.
!
?Butene/Benzene [1BE/BEN]
?I. Cullimore and E.W. Lemmon, NIST (2010)
cd7a06d0/f2cfb460
XR0 1. 1.0044 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 66.997801 -93.510371 293.75455 -488.316 398.72387 -119.84444 0. 0. 0. 0. 0. 0.
VC1 0.045926373 -0.77145155 3.1541965 -6.8950412 7.2458708 -2.9773108 0. 0. 0. 0. 0. 0.
!
?Butene/Cyclohexane [1BE/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
cd7a06d0/6e225350
XR0 1. 1.0122 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 54.716077 25.977043 -50.374424 114.21226 -133.2176 68.054677 0. 0. 0. 0. 0. 0.
VC1 0.0062660526 -0.26859279 0.98912726 -2.5088753 3.0521287 -1.4427007 0. 0. 0. 0. 0. 0.
!
?Perfluorobutane/R365mfc [C4F10/R365MFC]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.65% from 75 bubble-point pressures
a8f85e00/9d316cb0
XR0 0.99786 0.93067 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 12.260259 -159.68864 150.02607 -167.12963 166.10839 -61.715406 0. 0. 0. 0. 0. 0.
VC1 0.13470212 -2.2369894 8.6990509 -17.099353 16.681174 -6.2113388 0. 0. 0. 0. 0. 0.
!
?Butane/trans-Butene [C4/T2B]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7b3b4080/b28337f0
XR0 1. 0.9962 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -3.2310422 -0.066736025 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 -0.00084405797 0.0016042411 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Butane/cis-Butene [C4/C2B]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7b3b4080/411c4500
XR0 1. 0.9953 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -3.9119823 -0.25619003 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 -0.0027784657 0.0026347022 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Butane/R245fa [C4/R245FA]
?S.L. Outcalt and E.W. Lemmon, NIST (2012)
7b3b4080/5c322280
XR0 1.02 0.904 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -46.489824 -71.533356 48.824323 -317.20872 596.90872 -280.59001 0. 0. 0. 0. 0. 0.
VC1 0.10208727 -1.1359316 3.6550888 -4.2991397 1.0980901 0.58794111 0. 0. 0. 0. 0. 0.
!
?Butane/Isopentane [C4/C5I]
?Kunz and Wagner (2007)
7b3b4080/86ee46a0
KW0 1. 1.000792201 1. 1.002728434 0. 0. 0. 0. 0. 0. 0. 0.
TC1 8.0328485 0.74337294 -2.210597 3.5217481 -2.2536412 0.46384565 0. 0. 0. 0. 0. 0.
VC1 0.053969766 -0.2398294 0.69258976 -1.1120313 0.91717577 -0.29230269 0. 0. 0. 0. 0. 0.
PR1 0.00292 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Butane/Pentane [C4/C5]
?Kunz and Wagner (2007)
7b3b4080/76bc0290
KW0 1. 1.00214364 1. 1.01815965 0. 0. 0. 0. 0. 0. 0. 0.
TC1 10.261647 2.75632 2.0096283 -3.3615215 4.6594926 -1.7765709 0. 0. 0. 0. 0. 0.
VC1 0.015461085 0.020285146 -0.10142417 0.26104758 -0.31893416 0.16183221 0. 0. 0. 0. 0. 0.
PR1 0.0174 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Butane/R113 [C4/R113]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.17% from 12 bubble-point pressures
7b3b4080/d2a09ee0
XR0 1.0029 0.99168 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 16.722958 -7.5726568 -2.5385118 -7.9375098 9.7286735 -4.9690006 0. 0. 0. 0. 0. 0.
VC1 0.0050443646 -0.10740461 0.26861798 -0.33570899 0.20474571 -0.0089055359 0. 0. 0. 0. 0. 0.
!
?Butane/Acetone [C4/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7b3b4080/342481e0
XR0 1.016156894625 0.9452 1. 0.8906 0. 0. 0. 0. 0. 0. 0. 0.
TC1 26.763623 -51.686373 -150.44892 108.54761 -19.320126 17.851637 0. 0. 0. 0. 0. 0.
VC1 0.14650062 -1.7826432 5.9264534 -11.125817 10.789309 -4.0250521 0. 0. 0. 0. 0. 0.
!
?Butane/Methanol [C4/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
7b3b4080/c41aa690
KW0 1.037 0.872 1. 1. 1.068 0. 0. 0. 0. 0. 0. 0.
TC2 -191.51542 532.58859 -1607.2512 1397.4924 -334.77689 0. 0. 0. 0. 0. 0. 0.
VC2 -0.37016293 1.4864021 -5.5247672 8.4521213 -4.7392949 0. 0. 0. 0. 0. 0. 0.
!
?Butane/Hexane [C4/C6]
?Kunz and Wagner (2007)
7b3b4080/cb03ba40
KW0 1. 1.00915706 1. 1.034995284 0. 0. 0. 0. 0. 0. 0. 0.
TC1 38.347382 -1.1768503 21.35265 -7.533577 -5.9415656 11.560115 0. 0. 0. 0. 0. 0.
VC1 0.052528806 -0.15499667 0.12940089 0.43779391 -1.0612523 0.65198694 0. 0. 0. 0. 0. 0.
PR1 -0.0056 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Butane/Ethanol [C4/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
7b3b4080/3d5f67e0
XR0 1.03 0.95 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 12.377533 -30.398523 -21.300731 -140.25565 39.054862 64.503948 0. 0. 0. 0. 0. 0.
VC1 -0.021577609 -0.10260437 0.29825759 -2.0660335 3.7790557 -1.9006014 0. 0. 0. 0. 0. 0.
!
?Butane/Benzene [C4/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
7b3b4080/f2cfb460
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 56.220374 -85.277644 244.17756 -401.42895 328.10074 -97.341317 0. 0. 0. 0. 0. 0.
VC1 0.026882683 -0.53735893 1.8584906 -3.6196456 3.3752137 -1.2311434 0. 0. 0. 0. 0. 0.
!
?Butane/Cyclohexane [C4/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
7b3b4080/6e225350
XR0 1. 1.0267 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 53.106092 36.708022 -68.960449 205.45868 -264.44261 138.12982 0. 0. 0. 0. 0. 0.
VC1 -0.0093884417 -0.026369486 -0.10743253 0.030184855 0.10251311 -0.13616776 0. 0. 0. 0. 0. 0.
!
?Butane/Heptane [C4/C7]
?Kunz and Wagner (2007)
7b3b4080/b398a3b0
KW0 1. 1.021283378 1. 1.019174227 0. 0. 0. 0. 0. 0. 0. 0.
TC1 80.958126 19.81017 -67.098078 245.19989 -320.58102 160.10592 0. 0. 0. 0. 0. 0.
VC1 0.27208228 -1.8312449 5.8110316 -9.7605684 7.8982515 -2.4406021 0. 0. 0. 0. 0. 0.
PR1 0.0033 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Butane/Water [C4/H2O]
?Kunz and Wagner (2007)
7b3b4080/b43a7600
KW0 1. 0.615512682 1. 1.223638763 0. 0. 0. 0. 0. 0. 0. 0.
TC4 -112.55902 -1405.324 6364.7792 -4826.6248 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.091471078 -0.75548385 0.9495178 -0.39544982 0. 0. 0. 0. 0. 0. 0. 0.
!
?Butane/Methylcyclohexane [C4/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
7b3b4080/0429edd0
XR0 1. 1.02 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 59.797417 56.174606 -102.24541 294.66438 -403.84591 214.71653 0. 0. 0. 0. 0. 0.
VC1 -0.021344538 0.064033438 -0.41106343 0.49614595 -0.33674669 0.050163214 0. 0. 0. 0. 0. 0.
!
?Butane/Toluene [C4/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
7b3b4080/a49b8b50
XR0 1. 1.02 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 96.471021 17.567237 -120.11576 377.30938 -511.32802 263.1704 0. 0. 0. 0. 0. 0.
VC1 0.076846975 -0.74288834 2.2068251 -4.1454134 3.8607339 -1.5036039 0. 0. 0. 0. 0. 0.
!
?Butane/Octane [C4/C8]
?Kunz and Wagner (2007)
7b3b4080/f174a9b0
KW0 1. 1.033180106 1. 1.046905515 0. 0. 0. 0. 0. 0. 0. 0.
TC1 102.82493 85.246528 -261.74857 784.73631 -998.34392 486.28141 0. 0. 0. 0. 0. 0.
VC1 0.44487883 -2.954263 9.6391186 -17.008312 14.798961 -5.080464 0. 0. 0. 0. 0. 0.
!
?Butane/Nonane [C4/C9]
?Kunz and Wagner (2012)
7b3b4080/7f94dc20
KW0 1. 1.014096448 1. 1.049219137 0. 0. 0. 0. 0. 0. 0. 0.
TC1 131.90162 141.39686 -493.1818 1144.1728 -1383.4716 665.41963 0. 0. 0. 0. 0. 0.
VC1 0.40685809 -2.4300211 6.4942575 -10.117003 8.0366021 -2.5578853 0. 0. 0. 0. 0. 0.
!
?Butane/Decane [C4/C10]
?Kunz and Wagner (2012)
7b3b4080/111888d0
KW0 0.993688386 1.076466918 0.976951968 1.027845529 0. 0. 0. 0. 0. 0. 0. 0.
TC1 177.74911 276.30335 -1029.7167 2832.5547 -3330.7968 1493.6748 0. 0. 0. 0. 0. 0.
VC1 0.63591826 -4.4299778 15.581386 -30.656086 30.423714 -12.1703 0. 0. 0. 0. 0. 0.
PR1 0.0078 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Butane/Dodecane [C4/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010) (estimated from propane and pentane mixed with dodecane)
7b3b4080/8bc8dec0
XR0 1. 1.15 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 207.41187 404.2569 -1154.968 3426.9983 -3527.9883 1268.6669 0. 0. 0. 0. 0. 0.
VC1 1.1456952 -10.048519 40.884201 -84.467848 84.072299 -32.950264 0. 0. 0. 0. 0. 0.
!
?Butane/Methyl palmitate [C4/MPLMT]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.43% from 76 bubble-point pressures
7b3b4080/27c9ec60
XR0 0.93827 1.21149 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 379.78655 -370.04519 3933.6501 -11767.942 17061.993 -8161.0309 0. 0. 0. 0. 0. 0.
VC1 0.42210838 -6.9302276 28.557301 -60.157254 65.443871 -29.726768 0. 0. 0. 0. 0. 0.
!
?trans-Butene/cis-Butene [T2B/C2B]
?I. Cullimore and E.W. Lemmon, NIST (2010)
b28337f0/411c4500
XR0 0.9667 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -25.055149 16.959396 134.80324 -179.8972 78.662904 7.8240978 0. 0. 0. 0. 0. 0.
VC1 -0.012835799 0.10866424 -0.32528715 0.40754269 -0.15927518 -0.030175354 0. 0. 0. 0. 0. 0.
!
?trans-Butene/Acetone [T2B/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
b28337f0/342481e0
XR0 1.015228426396 0.9504 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 11.058303 -43.171924 -25.7945 -58.74324 44.52015 10.322636 0. 0. 0. 0. 0. 0.
VC1 0.11350166 -1.0584809 3.614648 -6.9385296 6.7082345 -2.4454565 0. 0. 0. 0. 0. 0.
!
?trans-Butene/Methanol [T2B/MEO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
b28337f0/c41aa690
XR0 1.022808632505 0.9061 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -24.533242 -84.065469 163.95992 -776.20743 941.7219 -320.51475 0. 0. 0. 0. 0. 0.
VC1 -0.088302825 -0.018954991 0.51292171 -2.7333357 4.7591759 -2.4154066 0. 0. 0. 0. 0. 0.
!
?trans-Butene/Ethanol [T2B/ETO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
b28337f0/3d5f67e0
XR0 1.026272577997 0.9517 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 12.884486 -36.679445 4.2266724 -194.83332 121.11274 21.966781 0. 0. 0. 0. 0. 0.
VC1 -0.01512249 -0.11883417 0.25601602 -1.3862858 2.4388664 -1.1781841 0. 0. 0. 0. 0. 0.
!
?R114/R21 [R114/R21]
?E.W. Lemmon, NIST (2002)
b1698aa0/79ff2f80
XR0 1. 0.9609090 1. 1.0139360 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -32.132679 -7.1030971 4.4126235 -6.0223342 14.644693 -6.8150537 0. 0. 0. 0. 0. 0.
VC1 -0.020432447 0.031132323 -0.0076826259 0.066033227 -0.10905919 0.04755057 0. 0. 0. 0. 0. 0.
PR1 0.022 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R114/Pentane [R114/C5]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.12% from 12 bubble-point pressures
b1698aa0/76bc0290
XR0 1.003552576119 0.97011 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -3.4894593 -15.382371 -41.041548 67.57659 -59.580206 23.411504 0. 0. 0. 0. 0. 0.
VC1 -0.051859488 0.48685191 -2.2282142 4.6082215 -4.3462894 1.5402601 0. 0. 0. 0. 0. 0.
!
?R114/R113 [R114/R113]
?E.W. Lemmon, NIST (2002)
b1698aa0/d2a09ee0
XR0 1. 1.0031258 1. 1.0013426 0. 0. 0. 0. 0. 0. 0. 0.
TC1 19.1067 -3.3039507 5.1236358 -4.4749211 3.2769543 -0.94534428 0. 0. 0. 0. 0. 0.
VC1 -0.021777524 0.022274148 -0.089103166 0.15075897 -0.13138965 0.045641417 0. 0. 0. 0. 0. 0.
!
?R114/Hexane [R114/C6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.2% from 12 bubble-point pressures
b1698aa0/cb03ba40
XR0 1.003723815355 0.98179 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 34.903208 -48.965782 76.089401 -141.43834 113.47646 -36.722256 0. 0. 0. 0. 0. 0.
VC1 0.027151935 -0.43239937 1.3706703 -2.4778604 2.3144955 -0.8193989 0. 0. 0. 0. 0. 0.
!
?R114/Ethanol [R114/ETO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.63% from 6 bubble-point pressures
b1698aa0/3d5f67e0
XR0 1.048646721406 0.93497 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 9.6449932 -46.402725 85.885713 -454.67215 230.08888 76.314908 0. 0. 0. 0. 0. 0.
VC1 -0.022943803 -0.46137734 3.2017434 -12.094123 17.580256 -8.2675132 0. 0. 0. 0. 0. 0.
!
?R114/Benzene [R114/BEN]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.38% from 12 bubble-point pressures
b1698aa0/f2cfb460
XR0 0.998821390759 0.95788 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 46.767297 -191.30222 461.58051 -860.9793 809.58635 -294.51452 0. 0. 0. 0. 0. 0.
VC1 -0.0043958943 -0.62049634 2.1003449 -4.0926739 4.0263812 -1.4802778 0. 0. 0. 0. 0. 0.
!
?R114/Heptane [R114/C7]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.24% from 12 bubble-point pressures
b1698aa0/b398a3b0
XR0 1.007912110064 0.99663 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 84.481981 -44.557101 118.39289 -260.70839 204.31439 -62.377136 0. 0. 0. 0. 0. 0.
VC1 0.24313909 -1.9179034 6.2797856 -11.354765 10.045245 -3.3699836 0. 0. 0. 0. 0. 0.
!
?cis-Butene/Acetone [C2B/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
411c4500/342481e0
XR0 1.014713343480 0.9521 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 8.31138 -40.930675 -25.81429 -54.032825 44.557908 7.9770215 0. 0. 0. 0. 0. 0.
VC1 0.11793627 -1.0596228 3.6536202 -7.0282548 6.8248419 -2.5145893 0. 0. 0. 0. 0. 0.
!
?cis-Butene/Methanol [C2B/MEO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
411c4500/c41aa690
XR0 1.023646227864 0.9065 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -27.284393 -95.095542 222.79639 -917.04481 1112.8483 -394.11791 0. 0. 0. 0. 0. 0.
VC1 -0.082152027 -0.03400777 0.62218011 -3.0609361 5.2957658 -2.7452451 0. 0. 0. 0. 0. 0.
!
?cis-Butene/Ethanol [C2B/ETO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
411c4500/3d5f67e0
XR0 1.027010372805 0.9489 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 9.0834257 -43.002658 28.293538 -261.82476 197.14728 -3.477727 0. 0. 0. 0. 0. 0.
VC1 -0.011092628 -0.14554965 0.45675283 -1.9041687 3.0901301 -1.4881943 0. 0. 0. 0. 0. 0.
!
?R21/Methanol [R21/MEO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.74% from 4 bubble-point pressures
79ff2f80/c41aa690
XR0 0.969208253777 0.91282 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -29.424836 -97.91139 -637.58448 2181.738 -2295.5 824.13174 0. 0. 0. 0. 0. 0.
VC1 -0.06370682 -0.34020185 1.7154417 -2.1204249 0.63414509 0.17925463 0. 0. 0. 0. 0. 0.
!
?R21/Ethanol [R21/ETO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.41% from 4 bubble-point pressures
79ff2f80/3d5f67e0
XR0 1.020543541490 0.90692 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 6.3959413 -134.92682 110.0025 -664.11648 956.51917 -375.31622 0. 0. 0. 0. 0. 0.
VC1 -0.003866966 0.030581261 -1.8823455 5.5604936 -5.3739885 1.6432334 0. 0. 0. 0. 0. 0.
!
?Neopentane/Pentane [C5A/C5]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.22% from 50 bubble-point pressures
5a410790/76bc0290
XR0 1.000500049925 1.00236 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 5.7085509 0.44319637 0.087261592 -0.72959589 0.73285854 -0.32951065 0. 0. 0. 0. 0. 0.
VC1 -0.0065326649 0.0030517776 -0.0050748679 0.012506748 -0.016817086 0.0095818725 0. 0. 0. 0. 0. 0.
!
?R245fa/Isopentane [R245FA/C5I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.01% from 71 bubble-point pressures
5c322280/86ee46a0
XR0 1.011756611829 0.90433 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 -28.353226 -66.072994 -90.939941 55.135013 48.886517 0. 0. 0. 0. 0. 0. 0.
VC2 0.030011895 0.03687868 -1.9398396 5.245899 -3.6999643 0. 0. 0. 0. 0. 0. 0.
!
?R245fa/Pentane [R245FA/C5]
?S.L. Outcalt and E.W. Lemmon, NIST (2012)
5c322280/76bc0290
XR0 1. 0.9 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -27.763718 -95.728508 10.823341 -169.5464 354.82234 -157.94854 0. 0. 0. 0. 0. 0.
VC1 -0.0087255796 -0.27976718 0.96026723 -2.5529569 4.9159097 -3.3131073 0. 0. 0. 0. 0. 0.
!
?R123/Water [R123/H2O]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.05% from 4 bubble-point pressures
efdfede0/b43a7600
XR0 1.099959961457 0.95847 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 63.510402 -550.58258 1793.8429 -2883.6373 1702.2046 -289.12559 0. 0. 0. 0. 0. 0.
VC1 0.1318671 -2.2897781 8.5138788 -14.373131 8.3490599 -0.23957325 0. 0. 0. 0. 0. 0.
!
?Isopentane/Pentane [C5I/C5]
?Kunz and Wagner (2007)
86ee46a0/76bc0290
KW0 1. 1.000050537 1. 1.000024335 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0.36049227 0.039923455 0.052719194 -0.11810139 0.14117139 -0.062913542 0. 0. 0. 0. 0. 0.
VC1 -0.00024362985 0.00016583523 0.00060093415 -0.00028361882 -7.1072205e-05 0.00049022859 0. 0. 0. 0. 0. 0.
!
?Isopentane/R365mfc [C5I/R365MFC]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.31% from 47 bubble-point pressures
86ee46a0/9d316cb0
XR0 1.01335 0.9238 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -41.010888 -64.697472 10.489788 -90.908425 265.46478 -139.99853 0. 0. 0. 0. 0. 0.
VC1 0.15652965 -1.4665378 5.144038 -8.2018106 5.7771961 -1.4281322 0. 0. 0. 0. 0. 0.
!
?Isopentane/Acetone [C5I/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
86ee46a0/342481e0
XR0 1. 0.9177 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -41.20016 -87.272141 18.014784 -14.298502 123.82848 -72.234057 0. 0. 0. 0. 0. 0.
VC1 0.0048342528 -0.57153928 2.2412545 -4.9273836 5.9390381 -2.6735318 0. 0. 0. 0. 0. 0.
!
?Isopentane/Methanol [C5I/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
86ee46a0/c41aa690
KWT 1. 0.8541581 1. 1.2935310 43.215000 0. 0. 0. 0. 0. 0. 0.
TC1 -188.94445 -163.15082 1443.1788 -6207.5756 9274.7896 -4305.943 0. 0. 0. 0. 0. 0.
VC1 -0.015868124 1.14741 -6.6374447 18.14208 -21.756595 9.3085328 0. 0. 0. 0. 0. 0.
!
?Isopentane/Hexane [C5I/C6]
?Kunz and Wagner (2007)
86ee46a0/cb03ba40
KW0 1. 1.001204174 1. 1.002995876 0. 0. 0. 0. 0. 0. 0. 0.
TC1 12.588196 -0.7523494 4.2662487 -5.3317237 5.4908943 -2.3901597 0. 0. 0. 0. 0. 0.
VC1 0.010650508 -0.018204905 -0.047363233 0.30628353 -0.48278708 0.26362731 0. 0. 0. 0. 0. 0.
!
?Isopentane/Ethanol [C5I/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
86ee46a0/3d5f67e0
XR0 1.016 0.934 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -30.985813 -64.952956 95.811746 -381.81563 503.65395 -190.63753 0. 0. 0. 0. 0. 0.
VC1 -0.042332398 -0.013112237 -0.12316224 0.14660718 0.33829061 -0.20824783 0. 0. 0. 0. 0. 0.
!
?Isopentane/Benzene [C5I/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
86ee46a0/f2cfb460
XR0 1. 0.99 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 15.072835 -33.620972 68.57429 -98.843938 75.708227 -23.741683 0. 0. 0. 0. 0. 0.
VC1 -0.010597487 -0.27996106 1.3341924 -3.3363048 3.9374144 -1.7981543 0. 0. 0. 0. 0. 0.
!
?Isopentane/Cyclohexane [C5I/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010) (estimated from pentane/cyclohexane)
86ee46a0/6e225350
XR0 1. 0.9961 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 14.548975 0.77249651 -4.3872786 9.8669816 -10.475121 5.5284125 0. 0. 0. 0. 0. 0.
VC1 -0.032278449 -0.090437559 0.59252606 -1.6911217 2.1330504 -1.0134325 0. 0. 0. 0. 0. 0.
!
?Isopentane/Heptane [C5I/C7]
?Kunz and Wagner (2007)
86ee46a0/b398a3b0
KW0 1. 1.003194615 1. 1.009928206 0. 0. 0. 0. 0. 0. 0. 0.
TC1 39.335653 -0.028881314 -3.8914406 16.293365 -15.023214 6.2438266 0. 0. 0. 0. 0. 0.
VC1 0.16619194 -0.97915768 2.9548 -4.6702471 3.5723455 -1.0028795 0. 0. 0. 0. 0. 0.
!
?Isopentane/Water [C5I/H2O]
?Kunz and Wagner (2007)
86ee46a0/b43a7600
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 3.805435 -266.69378 1282.1786 -2496.6358 2291.0814 -797.02664 0. 0. 0. 0. 0. 0.
VC1 0.2085604 -3.3065172 13.955396 -29.348131 29.799615 -11.869163 0. 0. 0. 0. 0. 0.
!
?Isopentane/Methylcyclohexane [C5I/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
86ee46a0/0429edd0
XR0 1. 1.005 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 28.87341 16.618135 -9.3060955 35.375803 -49.089559 29.032063 0. 0. 0. 0. 0. 0.
VC1 -0.022305934 -0.088240216 0.60805836 -1.771308 2.2084244 -1.0298496 0. 0. 0. 0. 0. 0.
!
?Isopentane/Toluene [C5I/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
86ee46a0/a49b8b50
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 48.705899 -9.5700346 -2.8152528 17.272002 -23.190725 14.959623 0. 0. 0. 0. 0. 0.
VC1 0.016563964 -0.40200583 1.6354453 -3.9214826 4.5377699 -2.0391441 0. 0. 0. 0. 0. 0.
!
?Isopentane/Octane [C5I/C8]
?Kunz and Wagner (2007)
86ee46a0/f174a9b0
KW0 1. 1.00564748 1. 1.017880545 0. 0. 0. 0. 0. 0. 0. 0.
TC1 62.529263 14.095451 -11.603752 27.570917 -34.31727 25.084944 0. 0. 0. 0. 0. 0.
VC1 0.24126551 -1.4053296 4.0706887 -6.4480978 5.087173 -1.5313135 0. 0. 0. 0. 0. 0.
!
?Isopentane/Nonane [C5I/C9]
?Kunz and Wagner (2012)
86ee46a0/7f94dc20
KW0 1. 1.008191499 1. 1.028994325 0. 0. 0. 0. 0. 0. 0. 0.
TC1 84.936226 64.994391 -132.56474 251.74115 -272.79915 135.74134 0. 0. 0. 0. 0. 0.
VC1 0.24943251 -1.1735882 2.8026068 -4.0579829 3.0850301 -0.92460978 0. 0. 0. 0. 0. 0.
!
?Isopentane/Decane [C5I/C10]
?Kunz and Wagner (2012)
86ee46a0/111888d0
KW0 1. 1.010825138 1. 1.039372957 0. 0. 0. 0. 0. 0. 0. 0.
TC1 135.23028 79.369593 -229.8333 478.65722 -546.13619 269.34181 0. 0. 0. 0. 0. 0.
VC1 0.56921146 -3.6415063 11.403132 -19.827214 17.433134 -6.0304782 0. 0. 0. 0. 0. 0.
!
?Isopentane/Dodecane [C5I/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010) (estimated from propane and pentane mixed with dodecane)
86ee46a0/8bc8dec0
XR0 1. 1.13 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 168.54383 346.3666 -1047.0981 3222.8467 -3695.6114 1613.9537 0. 0. 0. 0. 0. 0.
VC1 1.0241193 -8.6275533 34.883848 -71.789334 71.29246 -27.710811 0. 0. 0. 0. 0. 0.
!
?Perfluoropentane/Pentane [C5F12/C5]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.76% from 78 bubble-point pressures
053a8820/76bc0290
XR0 0.973039981240 0.8914 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -62.633797 -101.2133 -164.34861 749.4267 -678.69532 189.31539 0. 0. 0. 0. 0. 0.
VC1 -0.31705108 1.816629 -9.1984778 24.195906 -27.409977 10.988443 0. 0. 0. 0. 0. 0.
!
?R141b/Pentane [R141B/C5]
?S.L. Outcalt and E.W. Lemmon, NIST (2012)
ba322c10/76bc0290
XR0 1. 0.977 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -19.416145 -6.9534999 5.3097184 -1.724756 2.9099118 -1.5031302 0. 0. 0. 0. 0. 0.
VC1 0.0078348575 -0.0063499224 0.010220586 -0.048534464 0.028859927 -0.0052743806 0. 0. 0. 0. 0. 0.
!
?RE347mcc/Pentane [RE347MCC/C5]
?S.L. Outcalt and E.W. Lemmon, NIST (2012)
12934ef0/76bc0290
XR0 1. 0.928 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -47.118589 -47.62259 41.570325 -107.01263 191.87189 -87.659204 0. 0. 0. 0. 0. 0.
VC1 -0.10170689 0.39438063 -1.6596369 4.2706675 -4.7737837 1.9519095 0. 0. 0. 0. 0. 0.
!
?RE347mcc/Novec649 [RE347MCC/N649]
?S.L. Outcalt and E.W. Lemmon, NIST (2012)
12934ef0/a9e22c00
XR0 1.011122345804 0.98 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -4.8154288 -12.915384 -8.4592405 -11.308386 3.1928159 7.389243 0. 0. 0. 0. 0. 0.
VC1 0.21707235 -0.96383737 2.5864826 -3.7315928 2.6973906 -0.82947056 0. 0. 0. 0. 0. 0.
!
?Diethyl ether/Acetone [DEE/ACT]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.02% from 156 bubble-point pressures
46a701e0/342481e0
XR0 1.010090807164 0.97127 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -11.375919 -21.516884 0.8667452 -42.820024 51.896877 -15.120261 0. 0. 0. 0. 0. 0.
VC1 0.0256026 -0.24896577 0.73769566 -1.220223 1.1522898 -0.44577254 0. 0. 0. 0. 0. 0.
!
?Diethyl ether/Methanol [DEE/MEO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2% from 141 bubble-point pressures
46a701e0/c41aa690
XR0 1.004170016829 0.94684 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -45.395323 -14.432913 -8.5337744 -2.5287613 48.245382 -26.884327 0. 0. 0. 0. 0. 0.
VC1 -0.058336774 0.095142368 -0.53447822 1.9797418 -2.5502902 1.0747915 0. 0. 0. 0. 0. 0.
!
?Diethyl ether/Hexane [DEE/C6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.19% from 30 bubble-point pressures
46a701e0/cb03ba40
XR0 0.997729964784 0.99035 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 4.8779412 -11.338647 11.907389 -7.5381845 4.9036254 -1.3934697 0. 0. 0. 0. 0. 0.
VC1 0.038022196 -0.23727018 0.73308436 -1.203859 1.0059161 -0.33430717 0. 0. 0. 0. 0. 0.
!
?Diethyl ether/Ethanol [DEE/ETO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.25% from 461 bubble-point pressures
46a701e0/3d5f67e0
XR0 1.008970046404 0.97226 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -14.311317 -19.394373 -1.7564711 -34.738251 49.874513 -15.542993 0. 0. 0. 0. 0. 0.
VC1 -0.025923707 -0.0022997689 -0.063184443 0.13844414 0.014065539 -0.067127391 0. 0. 0. 0. 0. 0.
!
?Diethyl ether/Benzene [DEE/BEN]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.6% from 104 bubble-point pressures
46a701e0/f2cfb460
XR0 0.999080845622 1.00226 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 21.107577 -19.753002 51.59938 -66.884233 50.768262 -14.692339 0. 0. 0. 0. 0. 0.
VC1 0.0046112453 -0.22632229 0.70840448 -1.2899121 1.1305207 -0.40310063 0. 0. 0. 0. 0. 0.
!
?Diethyl ether/Water [DEE/H2O]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.02% from 64 bubble-point pressures
46a701e0/b43a7600
XR0 0.96917 0.84219 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -144.47358 -115.5898 129.07025 -41.483522 -34.880653 60.325615 0. 0. 0. 0. 0. 0.
VC1 -0.17158503 0.74327842 -5.2505766 11.650667 -9.4338035 2.4124087 0. 0. 0. 0. 0. 0.
!
?Pentane/Novec649 [C5/N649]
?S.L. Outcalt and E.W. Lemmon, NIST (2012)
76bc0290/a9e22c00
XR0 1. 0.894 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -59.33501 -71.445688 -279.08324 876.29769 -780.83193 234.87576 0. 0. 0. 0. 0. 0.
VC1 0.73368774 -7.7266876 36.145141 -79.689549 79.719798 -29.499942 0. 0. 0. 0. 0. 0.
!
?Pentane/Acetone [C5/ACT]
?I. Cullimore and E.W. Lemmon, NIST (2010)
76bc0290/342481e0
XR0 1.005833836250 0.9221 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -45.815138 -73.801493 52.299537 -134.7512 242.221 -111.93926 0. 0. 0. 0. 0. 0.
VC1 -0.042792364 0.065985769 -1.1339577 3.9007245 -4.4146313 1.6274903 0. 0. 0. 0. 0. 0.
!
?Pentane/Methanol [C5/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
76bc0290/c41aa690
KWT 1. 0.9168380 1. 0.6340970 10.487000 0. 0. 0. 0. 0. 0. 0.
TC1 -32.651469 87.09655 -2726.97 7699.9036 -7905.7047 2841.3039 0. 0. 0. 0. 0. 0.
VC1 -0.1404394 -1.1941722 5.5668792 -9.4528143 6.3845158 -1.0520395 0. 0. 0. 0. 0. 0.
!
?Pentane/Hexane [C5/C6]
?Kunz and Wagner (2007)
76bc0290/cb03ba40
KW0 1. 1.000761237 1. 1.002480637 0. 0. 0. 0. 0. 0. 0. 0.
TC1 8.5223831 -1.2902653 1.7838181 -1.3272759 0.63145839 -0.19895291 0. 0. 0. 0. 0. 0.
VC1 0.0093314092 -0.041524904 0.11025947 -0.17536283 0.14690016 -0.049548426 0. 0. 0. 0. 0. 0.
!
?Pentane/Ethanol [C5/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
76bc0290/3d5f67e0
XR0 1.028 0.923 1. 1.025 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -37.983865 -85.850581 234.03582 -847.13138 1069.2427 -411.87905 0. 0. 0. 0. 0. 0.
VC1 -0.042679156 0.24780211 -1.647577 3.7499421 -3.0628195 0.78400574 0. 0. 0. 0. 0. 0.
!
?Pentane/Benzene [C5/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
76bc0290/f2cfb460
XR0 1. 0.976 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 2.5353219 -50.436666 85.826115 -129.74125 102.07835 -31.884493 0. 0. 0. 0. 0. 0.
VC1 -0.024396197 -0.12698041 0.35205177 -0.56148019 0.42034417 -0.11510395 0. 0. 0. 0. 0. 0.
PR1 0.0174 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Pentane/Cyclohexane [C5/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
76bc0290/6e225350
XR0 1. 0.9961 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 10.177716 -1.8249474 -1.3616204 3.436253 -3.4832378 1.9051169 0. 0. 0. 0. 0. 0.
VC1 -0.033667454 -0.013286066 0.048320156 -0.17116269 0.22441508 -0.12203863 0. 0. 0. 0. 0. 0.
PR1 0.0037 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Pentane/Heptane [C5/C7]
?Kunz and Wagner (2007)
76bc0290/b398a3b0
KW0 1. 1.002441051 1. 1.008972412 0. 0. 0. 0. 0. 0. 0. 0.
TC1 31.614492 -4.2210707 -1.2423747 13.092946 -16.374402 6.877969 0. 0. 0. 0. 0. 0.
VC1 0.1407399 -0.86055596 2.7816343 -4.8670489 4.2589114 -1.4674455 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0205 -0.1068 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0074 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Pentane/Water [C5/H2O]
?Kunz and Wagner (2007)
76bc0290/b43a7600
KW0 1. 0.447666011 1. 0.95667731 0. 0. 0. 0. 0. 0. 0. 0.
TC6 -9.2340206 -143.50648 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 -0.42932218 0.96434896 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Pentane/Methylcyclohexane [C5/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
76bc0290/0429edd0
XR0 1. 1.003 0.995 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 23.635117 9.9141679 -12.939167 32.488028 -35.96643 18.80503 0. 0. 0. 0. 0. 0.
VC1 -0.024873826 -0.061742259 0.33345905 -0.96629646 1.2237279 -0.59786874 0. 0. 0. 0. 0. 0.
!
?Pentane/Toluene [C5/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
76bc0290/a49b8b50
XR0 1. 0.992 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 38.141612 -25.724215 10.36213 -8.9389253 2.9047987 2.3621979 0. 0. 0. 0. 0. 0.
VC1 0.0016509661 -0.27742703 0.84799251 -1.7545342 1.825312 -0.77804353 0. 0. 0. 0. 0. 0.
!
?Pentane/Octane [C5/C8]
?Kunz and Wagner (2007)
76bc0290/f174a9b0
KW0 1. 1.016422347 1. 1.069223964 0. 0. 0. 0. 0. 0. 0. 0.
TC1 51.305846 19.069368 -1.790112 57.766921 -78.573671 45.546214 0. 0. 0. 0. 0. 0.
VC1 0.18242569 -0.77050806 2.5427079 -4.7426189 4.4955641 -1.7111311 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0892 -0.1474 0. 0. 0. 0. 0. 0. 0. 0.
!
?Pentane/Nonane [C5/C9]
?Kunz and Wagner (2012)
76bc0290/7f94dc20
KW0 1. 1.103421755 1. 1.034910633 0. 0. 0. 0. 0. 0. 0. 0.
TC1 110.57489 103.17397 -143.95584 641.12608 -708.46181 321.82183 0. 0. 0. 0. 0. 0.
VC1 0.10663506 -0.28442324 2.614145 -8.4593228 11.161309 -5.5653611 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.1195 -0.161 0. 0. 0. 0. 0. 0. 0. 0.
!
?Pentane/Decane [C5/C10]
?Kunz and Wagner (2012)
76bc0290/111888d0
KW0 1. 1.049035838 1. 1.016370338 0. 0. 0. 0. 0. 0. 0. 0.
TC1 117.60904 115.42807 -224.66332 694.30983 -833.67458 365.98909 0. 0. 0. 0. 0. 0.
VC1 0.39584033 -2.2108669 7.5951945 -15.300099 15.477352 -6.2973226 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0965 -0.2775 0. 0. 0. 0. 0. 0. 0. 0.
!
?Pentane/Dodecane [C5/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
76bc0290/8bc8dec0
XR0 1. 1.114 1. 1.047 0. 0. 0. 0. 0. 0. 0. 0.
TC1 157.43934 230.22378 -501.49023 1632.6379 -1707.2986 696.51805 0. 0. 0. 0. 0. 0.
VC1 0.92842797 -7.6126399 31.099998 -64.167094 64.126942 -25.248406 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.1188 -0.4911 0. 0. 0. 0. 0. 0. 0. 0.
!
?Pentane/Hexadecane [C5/C16]
?I.H. Bell, NIST (2017)
76bc0290/8cf1f140
XR0 0.9833 1.1486 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 206.35993 476.2924 -1291.0697 3571.2933 -3336.3726 1136.0445 0. 0. 0. 0. 0. 0.
VC1 1.0392448 -6.4804393 25.418801 -57.006168 62.72603 -27.439071 0. 0. 0. 0. 0. 0.
ST1 0.11 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R113/Acetone [R113/ACT]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.51% from 44 bubble-point pressures
d2a09ee0/342481e0
XR0 1.003713740841 0.95086 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -40.252225 -23.587785 9.4925132 -12.742903 46.564478 -24.32269 0. 0. 0. 0. 0. 0.
VC1 -0.061864149 0.20201168 -1.3511779 4.4935468 -5.5593962 2.3060195 0. 0. 0. 0. 0. 0.
!
?R113/Hexane [R113/C6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.27% from 50 bubble-point pressures
d2a09ee0/cb03ba40
XR0 1.000600360216 0.98509 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -7.3423793 -8.8486178 1.2218338 -1.2222572 2.0621096 -0.61036254 0. 0. 0. 0. 0. 0.
VC1 0.0064044037 -0.0373483 0.11471487 -0.16967628 0.1567877 -0.06180296 0. 0. 0. 0. 0. 0.
!
?R113/Ethanol [R113/ETO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.78% from 6 bubble-point pressures
d2a09ee0/3d5f67e0
XR0 1.011940902651 0.90301 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -66.597637 -65.768616 -41.586942 -41.143058 417.45983 -272.93587 0. 0. 0. 0. 0. 0.
VC1 -0.076549649 0.507043 -3.8952303 12.17459 -15.040487 6.4278617 0. 0. 0. 0. 0. 0.
!
?R113/Benzene [R113/BEN]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.51% from 69 bubble-point pressures
d2a09ee0/f2cfb460
XR0 0.996293787112 0.97215 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -12.450678 -38.659132 63.609109 -83.678442 68.847707 -22.81384 0. 0. 0. 0. 0. 0.
VC1 -0.033696417 -0.047595009 0.033850658 0.13668064 -0.34351939 0.17969027 0. 0. 0. 0. 0. 0.
!
?R113/Heptane [R113/C7]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.34% from 12 bubble-point pressures
d2a09ee0/b398a3b0
XR0 1.004247968908 0.99057 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 18.100197 -7.3246926 -15.691836 8.347592 -11.691709 5.8990808 0. 0. 0. 0. 0. 0.
VC1 0.12423604 -0.71549663 2.0749115 -3.3890691 2.7873815 -0.86789085 0. 0. 0. 0. 0. 0.
!
?Cyclopentane/Ethanol [CC5/ETO]
?I. Cullimore and E.W. Lemmon, NIST (2010)
43ab1810/3d5f67e0
XR0 1.087665869045 0.9055 1. 0.9916 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -4.4750316 -413.08818 1890.5576 -5466.4912 6435.2554 -2523.5199 0. 0. 0. 0. 0. 0.
VC1 -0.063531509 1.0056674 -6.6100414 17.189052 -19.022684 7.4489091 0. 0. 0. 0. 0. 0.
!
?Cyclopentane/Benzene [CC5/BEN]
?I. Cullimore and E.W. Lemmon, NIST (2010)
43ab1810/f2cfb460
XR0 1. 0.9859 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.7607604 -20.802744 24.922594 -33.345452 25.648911 -7.7806853 0. 0. 0. 0. 0. 0.
VC1 0.010092946 -0.14264128 0.45491044 -0.7791988 0.68373287 -0.23471631 0. 0. 0. 0. 0. 0.
!
?Cyclopentane/Cyclohexane [CC5/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
43ab1810/6e225350
XR0 1. 1.0014 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 8.1432952 1.2646535 -0.4359005 0.6802444 -0.45267019 0.18622878 0. 0. 0. 0. 0. 0.
VC1 0.0038617001 -0.019245835 0.015323059 -0.014575837 0.008564856 -0.0031536371 0. 0. 0. 0. 0. 0.
!
?Cyclopentane/D4 [CC5/D4]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.39% from 33 bubble-point pressures
43ab1810/b6895470
XR0 0.99608 1.03293 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 62.232827 95.778357 -185.41608 620.82135 -743.14085 390.9044 0. 0. 0. 0. 0. 0.
VC1 0.62848955 -2.570459 7.0996701 -12.525148 11.69655 -4.4319408 0. 0. 0. 0. 0. 0.
!
?Acetone/Methanol [ACT/MEO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
342481e0/c41aa690
XR0 1. 0.97 1. 1.007 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -30.341699 1.0720946 19.8562 -17.299953 15.124274 -7.3363215 0. 0. 0. 0. 0. 0.
VC1 -0.027761208 0.7943081 -3.497909 7.3386511 -7.3104491 2.8388759 0. 0. 0. 0. 0. 0.
!
?Acetone/Hexane [ACT/C6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
342481e0/cb03ba40
XR0 1. 0.9194 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -43.161119 -91.402251 64.168558 -132.75483 252.14342 -126.17294 0. 0. 0. 0. 0. 0.
VC1 0.037145078 -0.22613845 0.24281469 1.997175 -4.6668818 2.5480513 0. 0. 0. 0. 0. 0.
!
?Acetone/Ethanol [ACT/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
342481e0/3d5f67e0
XR0 1.005 0.975 1. 0.997 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -20.201369 -12.138277 1.7382574 -2.3629458 20.261534 -11.105364 0. 0. 0. 0. 0. 0.
VC1 -0.0081058307 0.063244464 -0.37203714 1.066217 -1.3374713 0.64772459 0. 0. 0. 0. 0. 0.
!
?Acetone/Benzene [ACT/BEN]
?I. Cullimore and E.W. Lemmon, NIST (2010)
342481e0/f2cfb460
XR0 1. 0.984 1. 0.9826 0. 0. 0. 0. 0. 0. 0. 0.
TC1 1.2069589 -25.31738 32.434021 -45.41509 31.967677 -8.7268799 0. 0. 0. 0. 0. 0.
VC1 0.013835177 -0.17827935 0.60472644 -1.0318498 0.88541947 -0.29179764 0. 0. 0. 0. 0. 0.
!
?Acetone/Cyclohexane [ACT/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
342481e0/6e225350
KW0 1. 0.9335 1. 0.9903 -0.5274 0. 0. 0. 0. 0. 0. 0.
TC1 15.733272 -23.442879 -95.503129 216.17154 -198.80402 95.194306 0. 0. 0. 0. 0. 0.
VC1 0.1162116 -0.61275166 1.3790275 -1.2800872 0.1403989 0.31177524 0. 0. 0. 0. 0. 0.
!
?Acetone/Dimethyl carbonate [ACT/DMC]
?I. Cullimore and E.W. Lemmon, NIST (2010)
342481e0/859e6f80
XR0 1. 1.00016 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 9.6789166 -1.8503878 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0.0078538345 -0.0021733739 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Acetone/Heptane [ACT/C7]
?I. Cullimore and E.W. Lemmon, NIST (2010)
342481e0/b398a3b0
XR0 1. 0.9146 1. 1.0198 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -2.030469 -137.731 46.134514 -127.18169 238.37097 -107.77885 0. 0. 0. 0. 0. 0.
VC1 0.2742951 -2.2409877 8.0570516 -14.217148 12.863343 -4.7418565 0. 0. 0. 0. 0. 0.
!
?Acetone/Isooctane [ACT/C8I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.53% from 83 bubble-point pressures
342481e0/c2dd9ef0
XR0 1.004510049219 0.93534 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -13.918389 -33.705997 -51.595306 13.103114 20.56078 -3.3069448 0. 0. 0. 0. 0. 0.
VC1 0.13326905 -0.54840682 1.2720886 -1.0706172 0.13413759 0.20101855 0. 0. 0. 0. 0. 0.
!
?Acetone/Water [ACT/H2O]
?I.H. Bell, NIST (2017) - autofitting code based on data from TDE
342481e0/b43a7600
XR0 0.98882 0.925278 1.008091 0.923029 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -82.135302 -58.594845 203.83657 -414.78817 432.50598 -162.2449 0. 0. 0. 0. 0. 0.
VC1 -0.089357179 -0.10329993 1.0677174 -3.2934594 3.6763356 -1.1883946 0. 0. 0. 0. 0. 0.
ST1 0.350 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Acetone/Methylcyclohexane [ACT/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
342481e0/0429edd0
XR0 1. 0.919 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -27.943184 -45.039548 -41.29282 -41.445622 96.293565 -28.865194 0. 0. 0. 0. 0. 0.
VC1 -0.034329005 0.080397733 -0.26418211 0.8271834 -0.85998849 0.27352537 0. 0. 0. 0. 0. 0.
!
?Acetone/Toluene [ACT/TOL]
?I. Cullimore and E.W. Lemmon, NIST (2010)
342481e0/a49b8b50
XR0 1. 0.98 1. 0.9962 0. 0. 0. 0. 0. 0. 0. 0.
TC1 22.577537 -24.206565 8.8915075 -20.34925 21.887632 -10.005188 0. 0. 0. 0. 0. 0.
VC1 0.037840193 -0.18238171 0.19714857 0.50979467 -1.2534471 0.78353908 0. 0. 0. 0. 0. 0.
!
?Acetone/Octane [ACT/C8]
?I. Cullimore and E.W. Lemmon, NIST (2010)
342481e0/f174a9b0
XR0 1.0196 0.9277 1. 1.0352 0. 0. 0. 0. 0. 0. 0. 0.
TC1 20.812162 -48.380903 1.4878995 -198.30254 139.03417 -4.1162878 0. 0. 0. 0. 0. 0.
VC1 0.31653954 -1.9206411 5.7817219 -9.2285427 7.7385847 -2.4601203 0. 0. 0. 0. 0. 0.
!
?Acetone/p-Xylene [ACT/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.27% from 26 bubble-point pressures
342481e0/01b0e650
XR0 1.0007 0.9752 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 99.739968 -459.17352 1635.1555 -3096.3046 2848.7479 -1015.2879 0. 0. 0. 0. 0. 0.
VC1 0.35730853 -3.0944165 11.645538 -21.350515 18.586749 -6.032684 0. 0. 0. 0. 0. 0.
!
?Acetone/Nonane [ACT/C9]
?I. Cullimore and E.W. Lemmon, NIST (2010)
342481e0/7f94dc20
XR0 1.0246 0.9409 1. 1.0466 0. 0. 0. 0. 0. 0. 0. 0.
TC1 44.265789 -0.76073756 70.822645 -412.34763 286.05359 -42.220645 0. 0. 0. 0. 0. 0.
VC1 0.24470584 -0.70038433 0.14069097 2.6492666 -4.5291183 2.5581329 0. 0. 0. 0. 0. 0.
!
?Acetone/Decane [ACT/C10]
?I. Cullimore and E.W. Lemmon, NIST (2010)
342481e0/111888d0
XR0 1.044 0.9779 1. 1.0563 0. 0. 0. 0. 0. 0. 0. 0.
TC1 86.28104 62.25056 152.84308 -157.32506 -476.57353 357.90624 0. 0. 0. 0. 0. 0.
VC1 0.3484932 -0.78625669 -0.017426951 2.8949869 -5.4297648 3.4036714 0. 0. 0. 0. 0. 0.
!
?Acetone/Undecane [ACT/C11]
?I. Cullimore and E.W. Lemmon, NIST (2010) (estimated from decane and dodecane)
342481e0/62f46c40
XR0 1.044 0.98 1. 1.075 0. 0. 0. 0. 0. 0. 0. 0.
TC1 91.712327 57.449359 233.15376 -299.21697 -326.58542 320.52518 0. 0. 0. 0. 0. 0.
VC1 0.3596347 -0.7198269 -0.3421186 2.9591202 -4.8020501 2.9779203 0. 0. 0. 0. 0. 0.
!
?Acetone/Ethylene glycol [ACT/EGLY]
?I. Cullimore and E.W. Lemmon, NIST (2010)
342481e0/7d1768e0
XR0 0.9975 1.0468 1. 0.9108 0. 0. 0. 0. 0. 0. 0. 0.
TC1 94.958395 -38.311821 12.73087 236.71122 -457.34195 322.31007 0. 0. 0. 0. 0. 0.
VC1 -0.19160541 0.25059331 -0.40125047 -0.83001381 2.2352298 -1.4078025 0. 0. 0. 0. 0. 0.
!
?Acetone/Dodecane [ACT/C12]
?I. Cullimore and E.W. Lemmon, NIST (2010)
342481e0/8bc8dec0
XR0 1.044 0.995 1. 1.0915 0. 0. 0. 0. 0. 0. 0. 0.
TC1 120.77825 104.60384 -92.261912 905.67934 -1885.0285 1038.5315 0. 0. 0. 0. 0. 0.
VC1 0.90824246 -6.827784 25.380817 -47.703964 42.150936 -13.567042 0. 0. 0. 0. 0. 0.
!
?Isohexane/Methanol [C6I/MEO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.97% from 5 bubble-point pressures
faa2db70/c41aa690
XR0 1.00691 0.88008 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -113.38617 23.04544 -390.13443 1082.3125 -879.20929 222.73064 0. 0. 0. 0. 0. 0.
VC1 -0.054149911 -0.64635242 3.9972359 -6.3953099 3.2307935 0.0010245605 0. 0. 0. 0. 0. 0.
!
?Isohexane/Hexane [C6I/C6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.11% from 53 bubble-point pressures
faa2db70/cb03ba40
XR0 1.000460211697 0.9986 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -0.42963261 -1.5806452 2.7041103 -6.7537639 7.2787058 -2.8977678 0. 0. 0. 0. 0. 0.
VC1 -0.00015626611 -0.0035035505 0.013037216 -0.020217531 0.014745957 -0.0038882402 0. 0. 0. 0. 0. 0.
!
?Isohexane/Ethanol [C6I/ETO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.82% from 21 bubble-point pressures
faa2db70/3d5f67e0
XR0 1.0146413 0.90538 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -75.725188 -35.008173 -98.649554 141.23595 201.09133 -194.68799 0. 0. 0. 0. 0. 0.
VC1 -0.053075171 0.077357853 -0.7666399 3.7670559 -5.7017955 2.7793319 0. 0. 0. 0. 0. 0.
!
?Isohexane/Benzene [C6I/BEN]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.53% from 54 bubble-point pressures
faa2db70/f2cfb460
XR0 0.9936111 0.97119 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -25.718 -23.475166 48.47552 -48.645106 37.256998 -13.333406 0. 0. 0. 0. 0. 0.
VC1 -0.052292285 0.082651022 -0.23539751 0.48943846 -0.44905657 0.14803948 0. 0. 0. 0. 0. 0.
!
?Isohexane/Heptane [C6I/C7]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.13% from 42 bubble-point pressures
faa2db70/b398a3b0
XR0 0.9990309 1.00472 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 13.278817 0.74104222 1.6328798 0.96302055 -0.63377353 0.29328605 0. 0. 0. 0. 0. 0.
VC1 0.047543395 -0.22268862 0.60992047 -0.97571648 0.80229519 -0.26559858 0. 0. 0. 0. 0. 0.
!
?Methanol/Hexane [MEO/C6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c41aa690/cb03ba40
KWT 1. 0.8780631 1. 0.9683251 11.089885 0. 0. 0. 0. 0. 0. 0.
TC1 -23.61183 -321.95963 709.62412 -2457.6002 3563.0871 -1628.2252 0. 0. 0. 0. 0. 0.
VC1 0.15618146 -2.0009916 7.4455734 -12.629513 9.9525265 -3.0333184 0. 0. 0. 0. 0. 0.
ST1 0.1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methanol/Ethanol [MEO/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c41aa690/3d5f67e0
XR0 1. 0.999 1. 1.012 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -0.013455912 0.55791296 -0.92403449 2.6625274 -2.372638 0.897343 0. 0. 0. 0. 0. 0.
VC1 0.0015400039 0.00099950601 0.016948491 -0.054484426 0.077497449 -0.033556216 0. 0. 0. 0. 0. 0.
!
?Methanol/Benzene [MEO/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c41aa690/f2cfb460
XR0 0.978473581213 0.901 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 4.5012217 -276.01227 477.02205 -950.22449 1129.0332 -472.89185 0. 0. 0. 0. 0. 0.
VC1 0.10513178 -1.0743097 3.9417083 -6.5665342 5.5757583 -1.9659213 0. 0. 0. 0. 0. 0.
ST1 0.030 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methanol/Cyclohexane [MEO/CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c41aa690/6e225350
KWT 1. 0.8680742 1. 1.0530481 15.061 0. 0. 0. 0. 0. 0. 0.
TC1 -14.448891 -308.42547 559.65376 -2121.3306 2973.9636 -1277.7103 0. 0. 0. 0. 0. 0.
VC1 0.092285569 -1.2125197 4.2601065 -6.4392243 4.5742159 -1.3114311 0. 0. 0. 0. 0. 0.
!
?Methanol/Dimethyl carbonate [MEO/DMC]
?I. Cullimore and E.W. Lemmon, NIST (2010)
c41aa690/859e6f80
XR0 1. 0.9369 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC2 -5.5023352 -66.270361 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC2 -0.015120781 0.082536101 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methanol/Heptane [MEO/C7]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c41aa690/b398a3b0
KWT 1. 0.8586313 1. 1.0533466 9.577000 0. 0. 0. 0. 0. 0. 0.
TC1 50.968727 -415.48487 764.66049 -2981.5212 4313.1173 -1924.3197 0. 0. 0. 0. 0. 0.
VC1 0.43297536 -4.2232872 14.461457 -23.00105 17.41344 -5.1451769 0. 0. 0. 0. 0. 0.
!
?Methanol/Water [MEO/H2O]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c41aa690/b43a7600
XR0 0.995024875622 0.961 1. 1.034 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -18.287756 -108.50304 372.41635 -668.12262 579.26871 -194.96908 0. 0. 0. 0. 0. 0.
VC1 -0.037438374 0.20615296 -0.8822719 1.6736589 -1.4830841 0.48499329 0. 0. 0. 0. 0. 0.
PR1 -0.0778 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
ST1 0.150 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methanol/MM [MEO/MM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.54% from 15 bubble-point pressures
c41aa690/78082e80
XR0 1.02619 0.90636 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -10.782146 -67.372381 108.69525 -404.35777 284.09206 -11.472248 0. 0. 0. 0. 0. 0.
VC1 0.11463065 -0.32627987 0.67031902 0.40293534 -2.5554753 1.9029833 0. 0. 0. 0. 0. 0.
!
?Methanol/Methylcyclohexane [MEO/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c41aa690/0429edd0
XR0 1.01 0.864 0.978 1.041 0. 0. 0. 0. 0. 0. 0. 0.
TC2 -19.340749 -108.92351 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC2 -0.13890507 0.76947907 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methanol/Toluene [MEO/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c41aa690/a49b8b50
KW0 0.947867298578 0.764 1. 1.183 5.902 0. 0. 0. 0. 0. 0. 0.
TC5 -147.08348 420.78332 -783.78096 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -1.1766153 3.3777066 -3.5325793 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methanol/Octane [MEO/C8]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c41aa690/f174a9b0
XR0 1.074113856069 0.881 1. 1.124 0. 0. 0. 0. 0. 0. 0. 0.
TC1 12.249731 273.97229 -1683.668 5364.4073 -8465.8199 4394.0813 0. 0. 0. 0. 0. 0.
VC1 0.42238124 -1.6804707 5.5579786 -12.064642 13.381185 -5.395303 0. 0. 0. 0. 0. 0.
!
?Methanol/Ethylbenzene [MEO/EBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.04% from 20 bubble-point pressures
c41aa690/a4c64370
XR0 0.9989112 0.89432 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 90.398388 -216.80492 707.19272 -2052.7983 2120.3567 -746.97705 0. 0. 0. 0. 0. 0.
VC1 0.37736736 -2.4909097 7.1041218 -9.5413746 5.8315817 -1.044417 0. 0. 0. 0. 0. 0.
!
?Methanol/m-Xylene [MEO/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.08% from 11 bubble-point pressures
c41aa690/0f99ff70
XR0 0.99745 0.88973 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 115.92986 -176.48471 -78.473616 30.496646 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.24862501 -1.1540136 1.8094532 -0.76122326 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methanol/Nonane [MEO/C9]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c41aa690/7f94dc20
XR0 1.074113856069 0.893 1. 1.118 0. 0. 0. 0. 0. 0. 0. 0.
TC1 68.038399 -283.88859 2029.2427 -3403.4362 717.74958 737.99571 0. 0. 0. 0. 0. 0.
VC1 0.28757844 -0.065437563 0.55890907 -5.7014805 9.4650533 -4.2052548 0. 0. 0. 0. 0. 0.
!
?Methanol/Decane [MEO/C10]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
c41aa690/111888d0
KW0 1.095290251917 1.047 1. 0.957 -7.124 0. 0. 0. 0. 0. 0. 0.
TC1 1201.5218 -5797.8077 25684.94 -46963.18 38570.177 -11515.377 0. 0. 0. 0. 0. 0.
VC1 -0.86906516 13.761826 -46.65669 56.570512 -20.118599 -3.4421852 0. 0. 0. 0. 0. 0.
!
?Methanol/Undecane [MEO/C11]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.17% from 9 bubble-point pressures
c41aa690/62f46c40
XR0 1.105729892302 0.95529 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 136.53166 -214.63211 947.92661 3769.5359 -10212.88 5600.9539 0. 0. 0. 0. 0. 0.
VC1 0.44633687 -2.852231 22.232873 -66.420117 77.181297 -30.363343 0. 0. 0. 0. 0. 0.
!
?Methanol/Ethylene glycol [MEO/EGLY]
?I. Cullimore and E.W. Lemmon, NIST (2010)
c41aa690/7d1768e0
KW0 0.9942 1.0691 1.0723 0.8637 -1.703 0. 0. 0. 0. 0. 0. 0.
TC1 207.71811 48.697777 -71.842026 1843.4254 -3583.0924 2098.9888 0. 0. 0. 0. 0. 0.
VC1 0.13212061 -1.55506 7.6280957 -18.507001 20.2006 -8.3254235 0. 0. 0. 0. 0. 0.
!
?Methanol/Dodecane [MEO/C12]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.6% from 52 bubble-point pressures
c41aa690/8bc8dec0
XR0 1.109742428782 0.79118 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC5 64.605847 1752.3189 -2409.0703 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 1.7266116 -6.1707488 4.7520182 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hexane/Ethanol [C6/ETO]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
cb03ba40/3d5f67e0
XR0 1.013 0.901 1.022 1.026 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -88.496876 19.87608 -351.28893 784.78439 -480.04637 70.798651 0. 0. 0. 0. 0. 0.
VC1 -0.01506835 -0.079293135 -0.077653736 2.7203805 -5.5510341 3.1320707 0. 0. 0. 0. 0. 0.
!
?Hexane/Benzene [C6/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
cb03ba40/f2cfb460
KW0 1. 0.991 1. 0.999 -0.92 0. 0. 0. 0. 0. 0. 0.
TC1 115.14438 -236.98097 637.85272 -940.37085 691.82392 -171.25107 0. 0. 0. 0. 0. 0.
VC1 0.060325851 -0.51013756 2.5429962 -6.2227935 7.1654406 -3.1544335 0. 0. 0. 0. 0. 0.
PR1 0.0093 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hexane/Cyclohexane [C6/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
cb03ba40/6e225350
KW0 1. 1.002 1. 0.9979 -0.3672 0. 0. 0. 0. 0. 0. 0.
TC1 39.921042 -1.2943395 -19.84859 72.390959 -87.059849 44.757958 0. 0. 0. 0. 0. 0.
VC1 0.038256553 -0.25037937 1.0463928 -2.5107046 2.9247048 -1.3383313 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.12 0.2243 0. 0. 0. 0. 0. 0. 0. 0.
PR1 -0.003 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hexane/Dimethyl carbonate [C6/DMC]
?I. Cullimore and E.W. Lemmon, NIST (2010)
cb03ba40/859e6f80
KW0 1. 0.9365 1. 1. -0.382 0. 0. 0. 0. 0. 0. 0.
TC1 3.7783599 -212.14127 598.84148 -995.40664 880.76427 -297.74612 0. 0. 0. 0. 0. 0.
VC1 0.034631109 -0.55978683 2.3127819 -4.2426403 3.7391018 -1.2556073 0. 0. 0. 0. 0. 0.
!
?Hexane/Heptane [C6/C7]
?Kunz and Wagner (2007)
cb03ba40/b398a3b0
KW0 1. 0.999762786 1. 1.001508227 0. 0. 0. 0. 0. 0. 0. 0.
TC1 6.6221448 -0.16080914 -2.4819357 4.4978102 -3.71841 1.3011548 0. 0. 0. 0. 0. 0.
VC1 0.036537223 -0.12926392 0.28167868 -0.38327684 0.27726049 -0.080873657 0. 0. 0. 0. 0. 0.
PR1 -0.0078 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hexane/Isooctane [C6/C8I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.83% from 6 bubble-point pressures
cb03ba40/c2dd9ef0
XR0 1.00668 1.00427 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 15.562086 -2.422711 -0.31671251 -4.8790023 -4.1409033 2.284342 0. 0. 0. 0. 0. 0.
VC1 0.016917552 0.0031010246 -0.10829614 0.16361232 -0.11596882 0.048055753 0. 0. 0. 0. 0. 0.
!
?Hexane/Water [C6/H2O]
?Kunz and Wagner (2007)
cb03ba40/b43a7600
KW0 1. 0.569681333 1. 1.170217596 0. 0. 0. 0. 0. 0. 0. 0.
TC6 -536.28235 838.8773 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC6 -0.18794271 -0.43584138 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hexane/MM [C6/MM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.13% from 18 bubble-point pressures
cb03ba40/78082e80
XR0 0.995 1.00697 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 6.2873245 11.433919 -4.7142123 24.586787 -22.256525 11.475781 0. 0. 0. 0. 0. 0.
VC1 0.031585949 -0.039699162 0.14925432 -0.1992242 0.085864791 0.023343988 0. 0. 0. 0. 0. 0.
!
?Hexane/Methylcyclohexane [C6/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
cb03ba40/0429edd0
XR0 1. 0.998 1. 0.998 0. 0. 0. 0. 0. 0. 0. 0.
TC1 3.9621027 3.2679844 -5.0881121 11.78482 -12.033995 5.3293147 0. 0. 0. 0. 0. 0.
VC1 -0.017076598 -0.028627868 0.15025809 -0.42307147 0.52405858 -0.25567305 0. 0. 0. 0. 0. 0.
!
?Hexane/Toluene [C6/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
cb03ba40/a49b8b50
KW0 1. 0.988 1. 1. -0.213 0. 0. 0. 0. 0. 0. 0.
TC1 31.761645 -27.705192 18.897371 1.9040184 -16.767573 12.935099 0. 0. 0. 0. 0. 0.
VC1 0.010603964 -0.24805756 1.0445257 -2.5387125 2.9638483 -1.3545238 0. 0. 0. 0. 0. 0.
!
?Hexane/Octane [C6/C8]
?Kunz and Wagner (2007)
cb03ba40/f174a9b0
KW0 1. 1.001633952 1. 1.006268954 0. 0. 0. 0. 0. 0. 0. 0.
TC1 21.508979 3.5933937 -6.3062353 13.365818 -13.363272 7.1136197 0. 0. 0. 0. 0. 0.
VC1 0.089929838 -0.41970687 1.1038419 -1.7472792 1.4456283 -0.48092406 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0519 -0.001 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hexane/Ethylbenzene [C6/EBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.09% from 33 bubble-point pressures
cb03ba40/a4c64370
XR0 1.0002601 0.99383 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 31.262671 -40.93652 87.932786 -133.41313 106.77459 -32.36485 0. 0. 0. 0. 0. 0.
VC1 0.1145208 -1.2060626 4.3647471 -8.4456068 8.1034934 -3.068577 0. 0. 0. 0. 0. 0.
!
?Hexane/p-Xylene [C6/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.28% from 27 bubble-point pressures
cb03ba40/01b0e650
XR0 1.00071 0.99711 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 63.620285 -244.11485 815.12595 -1457.796 1292.3067 -445.72766 0. 0. 0. 0. 0. 0.
VC1 0.31542764 -3.0640294 12.127149 -24.029555 22.943217 -8.4595218 0. 0. 0. 0. 0. 0.
!
?Hexane/m-Xylene [C6/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.42% from 11 bubble-point pressures
cb03ba40/0f99ff70
XR0 1.01308 0.99672 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 47.469272 -35.959083 52.074089 -94.196305 45.445717 -12.053966 0. 0. 0. 0. 0. 0.
VC1 0.21064741 -1.9912621 7.489888 -14.579881 13.63373 -4.894524 0. 0. 0. 0. 0. 0.
!
?Hexane/o-Xylene [C6/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.3% from 12 bubble-point pressures
cb03ba40/32008e80
XR0 1.00096 1.00154 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 76.65925 -308.20722 1091.3704 -1986.8986 1777.5287 -613.8071 0. 0. 0. 0. 0. 0.
VC1 0.17486827 -1.875606 7.5954584 -15.610713 15.445252 -5.9259972 0. 0. 0. 0. 0. 0.
!
?Hexane/Nonane [C6/C9]
?Kunz and Wagner (2012)
cb03ba40/7f94dc20
KW0 1. 1.055369591 1. 1.02076168 0. 0. 0. 0. 0. 0. 0. 0.
TC1 65.934389 58.699273 -101.04706 393.14681 -497.67365 247.80517 0. 0. 0. 0. 0. 0.
VC1 0.067753695 -0.10862813 0.97585513 -3.3951747 4.4958795 -2.2175853 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0263 -0.0738 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hexane/Decane [C6/C10]
?Kunz and Wagner (2012)
cb03ba40/111888d0
KW0 0.99764101 1.028939539 1.001516371 1.013511439 0. 0. 0. 0. 0. 0. 0. 0.
TC1 72.715104 69.915598 -173.2834 477.90245 -566.11959 266.09285 0. 0. 0. 0. 0. 0.
VC1 0.25635734 -1.2071824 3.6337616 -6.8863909 6.7797899 -2.753121 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.055 -0.131 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hexane/Dodecane [C6/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
cb03ba40/8bc8dec0
KW0 0.991 1.027 1. 1.038 1.14 0. 0. 0. 0. 0. 0. 0.
TC4 5.2168719 -19.838202 11.259152 -2.8656085 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -2.0106694 7.9561573 -14.935508 9.4503215 0. 0. 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0168 -0.2999 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethanol/Benzene [ETO/BEN]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
3d5f67e0/f2cfb460
KW0 0.981354268891 0.92 0.997008973081 0.97 -0.162 0. 0. 0. 0. 0. 0. 0.
TC1 7.100421 -196.65673 319.45386 -594.7373 724.80815 -311.38057 0. 0. 0. 0. 0. 0.
VC1 0.082665178 -0.80668422 2.7499502 -4.5833277 3.7219197 -1.1885579 0. 0. 0. 0. 0. 0.
!
?Ethanol/Cyclohexane [ETO/CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
3d5f67e0/6e225350
KWB 0.989119683482 0.961 0.994035785288 1.2 1. 0. 0. 0. 0. 0. 0. 0.
TC4 -88.215861 -771.33321 869.26884 -339.83867 0. 0. 0. 0. 0. 0. 0. 0.
VC4 -0.374825 1.1218106 5.9283191 -6.9462599 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethanol/Dimethyl carbonate [ETO/DMC]
?I. Cullimore and E.W. Lemmon, NIST (2010)
3d5f67e0/859e6f80
XR0 0.9977 0.9414 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -16.160812 -55.539675 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0.0040456715 -0.0032286824 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethanol/Heptane [ETO/C7]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.97% from 597 bubble-point pressures
3d5f67e0/b398a3b0
XR0 0.980959959569 0.8981 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 19.159566 -176.02922 -142.48886 115.02143 367.56798 -274.29456 0. 0. 0. 0. 0. 0.
VC1 0.39621488 -3.4415323 11.588166 -18.083162 13.184583 -3.6878584 0. 0. 0. 0. 0. 0.
!
?Ethanol/Isooctane [ETO/C8I]
?E.W. Lemmon, NIST (2013)
3d5f67e0/c2dd9ef0
KW4 0.997008973081 0.871 0.987166831194 1.058 -1.223 0. 0. 0. 0. 0. 0. 0.
TC1 23.17454 -14.787652 -493.22738 467.50138 107.07192 -154.67856 0. 0. 0. 0. 0. 0.
VC1 0.37606584 -3.1711007 9.8432946 -14.900726 11.028775 -3.2593284 0. 0. 0. 0. 0. 0.
!
?Ethanol/Water [ETO/H2O]
?E.W. Lemmon, NIST (2008)
3d5f67e0/b43a7600
KW8 0.971761 0.93996768 1.0624092 0.8687762 0.3285109 0. 0. 0. 0. 0. 0. 0.
TC1 177.49034 -1348.7708 4283.669 -6995.9244 5814.4018 -1859.9303 0. 0. 0. 0. 0. 0.
VC1 0.013987335 -0.47489283 1.6853516 -2.7457151 2.0880301 -0.5474048 0. 0. 0. 0. 0. 0.
ST1 0.15 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethanol/MM [ETO/MM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.9% from 85 bubble-point pressures
3d5f67e0/78082e80
XR0 0.99498 0.91176 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -16.919067 -83.735495 -49.066013 -34.868057 226.15192 -122.90921 0. 0. 0. 0. 0. 0.
VC1 0.12281234 -0.64103614 0.28835461 4.6799613 -8.9899344 4.5194111 0. 0. 0. 0. 0. 0.
!
?Ethanol/Methylcyclohexane [ETO/C1CC6]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 4.44% from 103 bubble-point pressures
3d5f67e0/0429edd0
XR0 0.9749534 0.9013 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -32.114371 14.435694 -377.24846 339.71873 136.67157 -162.26407 0. 0. 0. 0. 0. 0.
VC1 -0.0079723911 0.14515876 -1.2690421 3.9555104 -4.8277613 2.0061661 0. 0. 0. 0. 0. 0.
!
?Ethanol/Toluene [ETO/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
3d5f67e0/a49b8b50
KW0 0.982318271120 0.904 1. 1. 0.282 0. 0. 0. 0. 0. 0. 0.
TC2 3.242217 -61.089613 -576.69634 840.5467 -326.95767 0. 0. 0. 0. 0. 0. 0.
VC2 0.029607516 -0.2147158 -0.35510781 1.1265711 0.32662142 0. 0. 0. 0. 0. 0. 0.
!
?Ethanol/Octane [ETO/C8]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
3d5f67e0/f174a9b0
XR0 0.985221674877 0.887 0.986193293886 1.036 0. 0. 0. 0. 0. 0. 0. 0.
TC1 47.791969 -19.165921 -832.66532 1164.1494 -517.23041 58.559045 0. 0. 0. 0. 0. 0.
VC1 0.60014382 -4.9238537 15.511649 -23.390705 17.85685 -5.6908064 0. 0. 0. 0. 0. 0.
!
?Ethanol/Ethylbenzene [ETO/EBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.38% from 32 bubble-point pressures
3d5f67e0/a4c64370
XR0 0.9898638 0.90463 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 73.177757 -145.37002 116.52877 -700.22257 936.74958 -369.82063 0. 0. 0. 0. 0. 0.
VC1 0.34431368 -2.7062083 8.4932867 -14.004919 12.209846 -4.3577729 0. 0. 0. 0. 0. 0.
!
?Ethanol/p-Xylene [ETO/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.86% from 190 bubble-point pressures
3d5f67e0/01b0e650
XR0 0.97813 0.9059 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 136.5638 -625.69963 1811.1798 -3996.5213 4222.7875 -1622.2458 0. 0. 0. 0. 0. 0.
VC1 0.44999192 -3.7385469 12.687256 -21.933444 19.234002 -6.7277967 0. 0. 0. 0. 0. 0.
!
?Ethanol/o-Xylene [ETO/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.93% from 14 bubble-point pressures
3d5f67e0/32008e80
XR0 0.98697 0.90681 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 145.78327 -715.52347 2391.3065 -5105.2605 5044.8389 -1844.4131 0. 0. 0. 0. 0. 0.
VC1 0.22833362 -1.9812753 6.4992246 -11.139777 9.9569933 -3.5710965 0. 0. 0. 0. 0. 0.
!
?Ethanol/Nonane [ETO/C9]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
3d5f67e0/7f94dc20
XR0 1.021450459653 0.9 1. 1.048 0. 0. 0. 0. 0. 0. 0. 0.
TC1 58.678499 18.926343 160.91363 -1062.513 843.67405 -136.0334 0. 0. 0. 0. 0. 0.
VC1 0.45560738 -2.5368705 8.0786484 -16.540347 18.293659 -7.7637129 0. 0. 0. 0. 0. 0.
!
?Ethanol/Decane [ETO/C10]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
3d5f67e0/111888d0
XR0 1.004016064257 0.894 1. 1.059 0. 0. 0. 0. 0. 0. 0. 0.
TC1 142.66112 168.0325 -799.51922 18.099102 806.25627 -413.69171 0. 0. 0. 0. 0. 0.
VC1 0.94718521 -6.6784769 20.543634 -34.734269 31.557006 -11.582298 0. 0. 0. 0. 0. 0.
!
?Ethanol/Ethylene glycol [ETO/EGLY]
?I. Cullimore and E.W. Lemmon, NIST (2010)
3d5f67e0/7d1768e0
KW0 1. 1.0174 1. 0.9095 0.3312 0. 0. 0. 0. 0. 0. 0.
TC1 96.379231 -313.02767 1306.5234 -2913.545 2947.962 -1013.5758 0. 0. 0. 0. 0. 0.
VC1 -0.22889481 0.37909923 -0.69385737 0.19978241 -0.094281838 0.35912907 0. 0. 0. 0. 0. 0.
!
?Benzene/Cyclohexane [BEN/CC6]
?I. Cullimore and E.W. Lemmon, NIST (2010)
f2cfb460/6e225350
KW0 1. 0.9933 1. 1. -0.6475 0. 0. 0. 0. 0. 0. 0.
TC1 59.518991 4.235858 -112.91226 394.51788 -514.17828 254.92551 0. 0. 0. 0. 0. 0.
VC1 0.050213182 -0.17292177 0.46533533 -0.63985353 0.3988619 -0.071522593 0. 0. 0. 0. 0. 0.
!
?Benzene/Dimethyl carbonate [BEN/DMC]
?I. Cullimore and E.W. Lemmon, NIST (2010)
f2cfb460/859e6f80
XR0 1. 0.9858 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -16.290571 1.2683634 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0.00010974854 0.00078105913 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Benzene/Heptane [BEN/C7]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
f2cfb460/b398a3b0
KW0 1. 0.987 1. 1.007 -0.675 0. 0. 0. 0. 0. 0. 0.
TC1 78.355108 -90.031773 112.04952 102.53945 -314.63707 199.03488 0. 0. 0. 0. 0. 0.
VC1 0.0525876 -0.16278509 0.43654713 -0.64116814 0.43097659 -0.087233575 0. 0. 0. 0. 0. 0.
PR1 0.0011 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Benzene/Isooctane [BEN/C8I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.36% from 103 bubble-point pressures
f2cfb460/c2dd9ef0
XR0 1.008609999259 0.96998 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -18.692153 -12.059894 -25.064898 22.303343 -17.90086 9.1429004 0. 0. 0. 0. 0. 0.
VC1 0.078896794 -0.0028171157 -0.44546367 1.0282459 -0.96962269 0.30396564 0. 0. 0. 0. 0. 0.
!
?Benzene/Methylcyclohexane [BEN/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
f2cfb460/0429edd0
XR0 1.003 0.98 1. 1.014 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -13.764098 -6.1794416 -7.6969664 6.8972267 -6.240114 2.7651906 0. 0. 0. 0. 0. 0.
VC1 0.010256356 0.010709268 0.0087229153 -0.013270617 -0.0034641245 0.012463756 0. 0. 0. 0. 0. 0.
!
?Benzene/Toluene [BEN/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
f2cfb460/a49b8b50
KW0 1. 1. 1. 1.004 0.068 0. 0. 0. 0. 0. 0. 0.
TC1 -3.2079675 -0.050268269 -2.440687 10.348136 -13.040548 5.2757894 0. 0. 0. 0. 0. 0.
VC1 0.0074191257 0.012371891 0.11091201 -0.08726908 -0.022211335 0.0051129287 0. 0. 0. 0. 0. 0.
!
?Benzene/Octane [BEN/C8]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
f2cfb460/f174a9b0
KW0 1. 0.994 1. 1.016 -0.924 0. 0. 0. 0. 0. 0. 0.
TC1 107.54617 -50.160344 -33.33408 494.41007 -787.54302 421.74665 0. 0. 0. 0. 0. 0.
VC1 0.18534799 -0.97153141 3.1975665 -5.7116161 5.0626366 -1.7533006 0. 0. 0. 0. 0. 0.
PR1 0.003 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Benzene/Ethylbenzene [BEN/EBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 3.88% from 54 bubble-point pressures
f2cfb460/a4c64370
XR0 0.99807 1.01425 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 29.147564 14.945791 -19.439647 79.103179 -97.520296 50.688215 0. 0. 0. 0. 0. 0.
VC1 0.12452395 -0.58579165 1.5634586 -2.1587582 1.3661241 -0.26599954 0. 0. 0. 0. 0. 0.
!
?Benzene/p-Xylene [BEN/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.8% from 79 bubble-point pressures
f2cfb460/01b0e650
XR0 1.00112 1.00639 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 46.277305 -106.75379 358.25585 -610.57155 523.30061 -174.03142 0. 0. 0. 0. 0. 0.
VC1 0.33410381 -2.8746154 11.229351 -21.428309 19.53252 -6.7742928 0. 0. 0. 0. 0. 0.
!
?Benzene/m-Xylene [BEN/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.82% from 53 bubble-point pressures
f2cfb460/0f99ff70
XR0 0.99896 1.00464 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 30.858419 -11.23761 19.187972 11.82329 -36.089628 23.948324 0. 0. 0. 0. 0. 0.
VC1 0.35673074 -3.084681 11.970437 -22.72915 20.649167 -7.1472757 0. 0. 0. 0. 0. 0.
!
?Benzene/o-Xylene [BEN/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.58% from 30 bubble-point pressures
f2cfb460/32008e80
XR0 1.01414 1.00329 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 62.643732 -146.50076 472.47074 -847.73715 715.63264 -244.83429 0. 0. 0. 0. 0. 0.
VC1 0.1800394 -1.4884411 5.6352059 -10.547149 9.3900463 -3.1355366 0. 0. 0. 0. 0. 0.
!
?Benzene/Nonane [BEN/C9]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
f2cfb460/7f94dc20
KW0 1.005025125628 1. 1. 1. -1.193 0. 0. 0. 0. 0. 0. 0.
TC1 152.68369 -29.853763 -136.26595 855.68739 -1285.2084 660.17503 0. 0. 0. 0. 0. 0.
VC1 0.24773459 -1.3039384 4.33512 -8.2327895 7.7448361 -2.8385569 0. 0. 0. 0. 0. 0.
!
?Benzene/Decane [BEN/C10]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
f2cfb460/111888d0
KW0 1.008064516129 1.052 1. 1. -2.444 0. 0. 0. 0. 0. 0. 0.
TC1 396.70979 -462.78505 850.75467 359.64608 -1719.025 1116.2578 0. 0. 0. 0. 0. 0.
VC1 0.14956037 -0.41610334 2.6658543 -8.4926472 10.771384 -4.9433358 0. 0. 0. 0. 0. 0.
!
?Benzene/D4 [BEN/D4]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.33% from 40 bubble-point pressures
f2cfb460/b6895470
XR0 1.01222 0.98954 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 19.424113 88.609396 -381.12613 1031.5554 -1314.5634 643.8836 0. 0. 0. 0. 0. 0.
VC1 0.47567023 -0.55305109 -2.4637284 8.9614293 -10.979953 4.8022344 0. 0. 0. 0. 0. 0.
!
?Benzene/Dodecane [BEN/C12]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.5% from 61 bubble-point pressures
f2cfb460/8bc8dec0
XR0 1.007170043540 1.02547 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 82.124535 138.37192 -439.78024 1273.1637 -1542.532 703.01972 0. 0. 0. 0. 0. 0.
VC1 0.93411491 -7.1751037 26.247482 -48.586474 43.527716 -14.963785 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/Dimethyl carbonate [CC6/DMC]
?I. Cullimore and E.W. Lemmon, NIST (2010)
6e225350/859e6f80
XR0 1.0091 0.9299 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -55.456385 -64.150706 14.192892 31.638455 66.296294 -58.322801 0. 0. 0. 0. 0. 0.
VC1 -0.0032668017 -0.22391434 0.68543884 0.0069249633 -1.3474441 0.88797885 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/Heptane [CC6/C7]
?I. Cullimore and E.W. Lemmon, NIST (2010)
6e225350/b398a3b0
KW0 1. 1. 1. 1.0015 -0.2539 0. 0. 0. 0. 0. 0. 0.
TC1 35.676547 -29.863478 61.393987 -80.738732 63.508489 -21.22608 0. 0. 0. 0. 0. 0.
VC1 0.022014729 -0.030186808 0.063276048 -0.047988399 -0.0048068864 0.024450653 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/Isooctane [CC6/C8I]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.21% from 113 bubble-point pressures
6e225350/c2dd9ef0
XR0 1.001900003166 0.99375 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -3.1523068 -1.1849892 -9.3113384 15.503186 -14.008947 4.883189 0. 0. 0. 0. 0. 0.
VC1 0.037324899 -0.041911744 0.045061851 -0.060448661 0.043218465 -0.011867908 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/Methylcyclohexane [CC6/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
6e225350/0429edd0
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 1.9389587 1.7293131 -4.4335003 8.9340495 -8.3486228 2.9892663 0. 0. 0. 0. 0. 0.
VC1 0.0018215151 -0.0065831872 0.035195017 -0.067494351 0.063322129 -0.022095318 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/Toluene [CC6/TOL]
?I. Cullimore and E.W. Lemmon, NIST (2010)
6e225350/a49b8b50
KW0 1. 1. 1. 0.9979 0.5865 0. 0. 0. 0. 0. 0. 0.
TC1 -88.558854 202.04825 -585.57535 1013.5987 -1036.1405 435.21862 0. 0. 0. 0. 0. 0.
VC1 -0.59382796 1.9242438 -5.7603982 12.548005 -16.203966 8.2113915 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/Octane [CC6/C8]
?I. Cullimore and E.W. Lemmon, NIST (2010)
6e225350/f174a9b0
KW0 1. 1.008 1. 1.0069 -0.358 0. 0. 0. 0. 0. 0. 0.
TC1 56.846534 -21.76019 69.765543 -87.584971 69.375424 -21.492044 0. 0. 0. 0. 0. 0.
VC1 0.11541729 -0.49793393 1.5541629 -2.6830506 2.3140911 -0.77820153 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/Ethylbenzene [CC6/EBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.99% from 51 bubble-point pressures
6e225350/a4c64370
XR0 1.0043 0.99414 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 18.327488 -17.254473 12.413644 -24.811448 8.8369414 0.30312621 0. 0. 0. 0. 0. 0.
VC1 0.1179602 -0.77248962 2.5042568 -4.4019584 3.8692225 -1.3245226 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/p-Xylene [CC6/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.87% from 79 bubble-point pressures
6e225350/01b0e650
XR0 1.00184 0.99198 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 38.524338 -164.71948 502.44183 -883.40197 762.85774 -258.19816 0. 0. 0. 0. 0. 0.
VC1 0.31888227 -2.7946419 10.938085 -21.146232 19.670318 -7.0249604 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/m-Xylene [CC6/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.8% from 53 bubble-point pressures
6e225350/0f99ff70
XR0 1.00315 0.99328 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 24.747423 -40.096782 63.375815 -100.00149 70.235454 -19.305835 0. 0. 0. 0. 0. 0.
VC1 0.27571463 -2.3710632 9.074163 -17.2988 15.905422 -5.6149115 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/o-Xylene [CC6/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.73% from 39 bubble-point pressures
6e225350/32008e80
XR0 1.00392 0.99006 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 49.997808 -224.65711 701.29084 -1239.1159 1065.4418 -359.66461 0. 0. 0. 0. 0. 0.
VC1 0.15774387 -1.3281659 4.9260183 -9.2725733 8.5063852 -3.011292 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/Nonane [CC6/C9]
?I. Cullimore and E.W. Lemmon, NIST (2010) (estimated from octane/cyclohexane and dodecane/cyclohexane)
6e225350/7f94dc20
KW0 1. 1.015 1. 1.009 -0.358 0. 0. 0. 0. 0. 0. 0.
TC1 69.384018 6.5857579 22.962701 2.7486678 -13.684685 10.893073 0. 0. 0. 0. 0. 0.
VC1 0.15811695 -0.62547531 1.8193462 -3.1044408 2.6941499 -0.93286982 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/Decane [CC6/C10]
?I. Cullimore and E.W. Lemmon, NIST (2010) (estimated from octane/cyclohexane and dodecane/cyclohexane)
6e225350/111888d0
KW0 1. 1.025 1. 1.012 -0.358 0. 0. 0. 0. 0. 0. 0.
TC1 99.799265 2.4080505 58.142038 -10.678272 -23.702437 21.35442 0. 0. 0. 0. 0. 0.
VC1 0.27273998 -1.3607622 4.3886001 -7.9282494 7.1695698 -2.5744667 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/Undecane [CC6/C11]
?I. Cullimore and E.W. Lemmon, NIST (2010) (estimated from octane/cyclohexane and dodecane/cyclohexane)
6e225350/62f46c40
KW0 1. 1.04 1. 1.014 -0.358 0. 0. 0. 0. 0. 0. 0.
TC1 103.25552 56.280223 -17.060854 176.59447 -215.02373 108.4755 0. 0. 0. 0. 0. 0.
VC1 0.33893965 -1.5516689 4.9036027 -9.1617398 8.6554847 -3.2885565 0. 0. 0. 0. 0. 0.
!
?Cyclohexane/Dodecane [CC6/C12]
?I. Cullimore and E.W. Lemmon, NIST (2010)
6e225350/8bc8dec0
KW0 1. 1.0548 1. 1.0167 -0.358 0. 0. 0. 0. 0. 0. 0.
TC1 132.16207 73.812516 -64.514844 409.94478 -488.04119 232.187 0. 0. 0. 0. 0. 0.
VC1 0.7856126 -6.2789267 24.733907 -48.879271 46.413721 -17.045015 0. 0. 0. 0. 0. 0.
!
?Dimethyl carbonate/Heptane [DMC/C7]
?I. Cullimore and E.W. Lemmon, NIST (2010)
859e6f80/b398a3b0
XR0 1. 0.9256 1. 1.0133 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -45.205987 -80.795869 -10.18701 62.643736 51.086152 -51.665875 0. 0. 0. 0. 0. 0.
VC1 0.19943632 -1.1444669 2.5233612 0.24468028 -5.6736561 3.7557474 0. 0. 0. 0. 0. 0.
!
?Dimethyl carbonate/Water [DMC/H2O]
?I. Cullimore and E.W. Lemmon, NIST (2010)
859e6f80/b43a7600
XR0 0.949487276870 0.8581 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC5 -204.31254 5.5868234 138.2648 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.16028203 0.44547218 -0.24578992 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Dimethyl carbonate/Toluene [DMC/TOL]
?I. Cullimore and E.W. Lemmon, NIST (2010)
859e6f80/a49b8b50
XR0 1. 0.9766 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -8.736679 -11.05054 -27.843033 49.937403 -38.168182 11.680951 0. 0. 0. 0. 0. 0.
VC1 0.015032922 0.13128099 -1.1992387 3.6022134 -4.5614537 2.1244791 0. 0. 0. 0. 0. 0.
!
?Dimethyl carbonate/Octane [DMC/C8]
?I. Cullimore and E.W. Lemmon, NIST (2010)
859e6f80/f174a9b0
XR0 1.013479274349 0.9247 1. 1.0273 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -21.748013 -61.119335 -62.724662 14.949497 20.47068 12.603315 0. 0. 0. 0. 0. 0.
VC1 0.37142296 -3.1026382 13.502133 -30.055703 32.854777 -13.74039 0. 0. 0. 0. 0. 0.
!
?Dimethyl carbonate/Nonane [DMC/C9]
?I. Cullimore and E.W. Lemmon, NIST (2010)
859e6f80/7f94dc20
XR0 1.021346134205 0.9302 1. 1.0357 0. 0. 0. 0. 0. 0. 0. 0.
TC1 1.3380347 -12.28903 -98.833008 -155.25377 243.93589 -78.785126 0. 0. 0. 0. 0. 0.
VC1 0.21143455 -0.430528 -1.5101475 7.3285808 -10.053227 4.7617356 0. 0. 0. 0. 0. 0.
!
?Dimethyl carbonate/Decane [DMC/C10]
?I. Cullimore and E.W. Lemmon, NIST (2010)
859e6f80/111888d0
XR0 1.017293997965 0.9217 1. 1.0432 0. 0. 0. 0. 0. 0. 0. 0.
TC1 46.415154 -41.309702 -97.38515 -409.92297 674.25065 -267.58468 0. 0. 0. 0. 0. 0.
VC1 0.5096429 -2.8149188 6.2655631 -5.8219992 1.2360382 0.93745739 0. 0. 0. 0. 0. 0.
!
?Dimethyl carbonate/Ethylene glycol [DMC/EGLY]
?I. Cullimore and E.W. Lemmon, NIST (2010)
859e6f80/7d1768e0
XR0 0.9876 0.9898 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 21.796919 -84.757392 66.567286 229.51619 -414.11685 226.45101 0. 0. 0. 0. 0. 0.
VC1 -0.23901549 0.94529646 -3.4400964 6.3662076 -5.534241 1.7741997 0. 0. 0. 0. 0. 0.
!
?Heptane/Water [C7/H2O]
?Kunz and Wagner (2007)
b398a3b0/b43a7600
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 241.0252 -1976.3664 6921.9847 -12440.381 11062.749 -3831.4351 0. 0. 0. 0. 0. 0.
VC1 0.12231461 -0.75440993 0.99771238 1.5358111 -4.8145511 2.7137341 0. 0. 0. 0. 0. 0.
!
?Heptane/Methylcyclohexane [C7/C1CC6]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
b398a3b0/0429edd0
XR0 1. 0.998 1. 1.003 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -2.3778342 1.9573009 -7.1986121 14.526578 -13.657983 4.8842828 0. 0. 0. 0. 0. 0.
VC1 -0.0026949681 -0.017128548 0.073517956 -0.17252193 0.18926434 -0.083452149 0. 0. 0. 0. 0. 0.
!
?Heptane/Toluene [C7/TOL]
?E.W. Lemmon, NIST (2012)
b398a3b0/a49b8b50
KW1 0.998329 0.9832346 1.0019167 1.0026789 -0.6281548 0. 0. 0. 0. 0. 0. 0.
TC1 40.228323 -58.066334 99.30064 -76.262624 19.843351 14.980036 0. 0. 0. 0. 0. 0.
VC1 0.0073455575 -0.11376142 0.61687877 -1.6185138 1.9679001 -0.90432976 0. 0. 0. 0. 0. 0.
!
?Heptane/Octane [C7/C8]
?Kunz and Wagner (2007)
b398a3b0/f174a9b0
KW0 1. 0.998793111 1. 1.006767176 0. 0. 0. 0. 0. 0. 0. 0.
TC1 3.3898885 0.35217114 0.42929159 -0.60370082 0.88883585 -0.44495588 0. 0. 0. 0. 0. 0.
VC1 0.020750361 -0.0095143379 0.011613495 0.015262534 -0.034774608 0.025952974 0. 0. 0. 0. 0. 0.
!
?Heptane/Ethylbenzene [C7/EBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.52% from 151 bubble-point pressures
b398a3b0/a4c64370
XR0 0.9996002 0.98665 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0.26091067 -17.634055 22.574941 -28.49757 19.891961 -5.9749171 0. 0. 0. 0. 0. 0.
VC1 0.027225353 -0.37680164 1.2489197 -2.212353 1.9821151 -0.72183641 0. 0. 0. 0. 0. 0.
!
?Heptane/p-Xylene [C7/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.25% from 124 bubble-point pressures
b398a3b0/01b0e650
XR0 0.99936 0.98957 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 19.047255 -107.28233 310.71705 -518.71534 438.15058 -146.59708 0. 0. 0. 0. 0. 0.
VC1 0.24345633 -2.2188817 8.5447325 -16.383672 15.215777 -5.4796256 0. 0. 0. 0. 0. 0.
!
?Heptane/m-Xylene [C7/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.37% from 48 bubble-point pressures
b398a3b0/0f99ff70
XR0 0.99846 0.9896 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 7.0093056 -28.383481 48.346893 -60.222493 44.169698 -13.334375 0. 0. 0. 0. 0. 0.
VC1 0.10967495 -1.1580884 4.4479822 -8.5162295 7.8711095 -2.8219613 0. 0. 0. 0. 0. 0.
!
?Heptane/o-Xylene [C7/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.27% from 71 bubble-point pressures
b398a3b0/32008e80
XR0 0.99904 0.98672 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 28.506529 -180.64839 565.46838 -976.66886 844.12594 -287.29782 0. 0. 0. 0. 0. 0.
VC1 0.12668219 -1.2463259 4.7640637 -9.2114422 8.7272732 -3.2429445 0. 0. 0. 0. 0. 0.
!
?Heptane/Nonane [C7/C9]
?Kunz and Wagner (2012)
b398a3b0/7f94dc20
KW0 1. 1.001150096 1. 1.001370076 0. 0. 0. 0. 0. 0. 0. 0.
TC1 15.587026 5.9515466 -0.87659929 -1.3983883 4.0435256 -1.5954262 0. 0. 0. 0. 0. 0.
VC1 0.032639176 0.012993007 -0.24623507 0.70462788 -0.86479441 0.41356199 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0704 -0.0117 0. 0. 0. 0. 0. 0. 0. 0.
!
?Heptane/Decane [C7/C10]
?Kunz and Wagner (2012)
b398a3b0/111888d0
KW0 1. 1.002229938 1. 1.002972346 0. 0. 0. 0. 0. 0. 0. 0.
TC1 36.379749 15.159594 -24.737563 32.999965 -23.235413 8.8408417 0. 0. 0. 0. 0. 0.
VC1 0.15570267 -0.47671666 0.70176926 -0.24238634 -0.52316887 0.45632221 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0374 -0.0677 0. 0. 0. 0. 0. 0. 0. 0.
!
?Heptane/Dodecane [C7/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
b398a3b0/8bc8dec0
XR0 1. 1.019 1. 1.02 0. 0. 0. 0. 0. 0. 0. 0.
TC1 73.141833 45.503626 -58.368274 228.22014 -289.77857 153.6074 0. 0. 0. 0. 0. 0.
VC1 0.5955248 -4.8346213 18.165018 -34.136509 30.919014 -10.739346 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0716 -0.16 0. 0. 0. 0. 0. 0. 0. 0.
!
?Isooctane/Toluene [C8I/TOL]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.59% from 438 bubble-point pressures
c2dd9ef0/a49b8b50
XR0 0.99502 0.9779 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -27.833725 -2.4691749 21.304426 -25.808203 25.181737 -11.014242 0. 0. 0. 0. 0. 0.
VC1 -0.045215339 0.0068804396 0.1260098 -0.24664499 0.27012229 -0.11917875 0. 0. 0. 0. 0. 0.
!
?Isooctane/Octane [C8I/C8]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.15% from 40 bubble-point pressures
c2dd9ef0/f174a9b0
XR0 1.001289961858 1.00412 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 7.7368252 -0.83359945 -0.39233668 -1.4535335 1.2280292 -0.50893619 0. 0. 0. 0. 0. 0.
VC1 0.0051172005 -0.010613495 -0.0079827605 0.00061231063 0.0035042953 -0.0012284633 0. 0. 0. 0. 0. 0.
!
?Isooctane/Ethylbenzene [C8I/EBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.4% from 63 bubble-point pressures
c2dd9ef0/a4c64370
XR0 0.9990409 0.98599 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -5.3625707 -17.945721 23.010031 -27.158251 20.425882 -6.4716245 0. 0. 0. 0. 0. 0.
VC1 -0.0029671657 -0.26569317 0.71750841 -1.1697901 0.93613084 -0.30255979 0. 0. 0. 0. 0. 0.
!
?Isooctane/p-Xylene [C8I/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.29% from 34 bubble-point pressures
c2dd9ef0/01b0e650
XR0 0.99929 0.99104 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 10.801462 -78.606012 217.1575 -357.50027 302.19716 -100.96111 0. 0. 0. 0. 0. 0.
VC1 0.20398765 -1.8654311 6.8885695 -12.977076 11.750499 -4.1255162 0. 0. 0. 0. 0. 0.
!
?Isooctane/m-Xylene [C8I/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.19% from 22 bubble-point pressures
c2dd9ef0/0f99ff70
XR0 0.99628 1.0016 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 7.1163307 -8.8281138 28.63027 -26.70145 16.755778 -3.2913549 0. 0. 0. 0. 0. 0.
VC1 0.015933107 -0.50257026 1.9545732 -4.0487119 4.0005254 -1.5856078 0. 0. 0. 0. 0. 0.
!
?Isooctane/o-Xylene [C8I/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.15% from 37 bubble-point pressures
c2dd9ef0/32008e80
XR0 0.99859 0.98905 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 18.950957 -141.56659 433.11647 -739.38024 634.86996 -213.68368 0. 0. 0. 0. 0. 0.
VC1 0.11055541 -1.1084783 3.9965301 -7.478868 6.7704592 -2.4474587 0. 0. 0. 0. 0. 0.
!
?Water/Heavy water [H2O/D2O]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.52% from 70 bubble-point pressures
b43a7600/3e131610
XR0 1.004248 1.00379 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 11.260404 -17.135775 15.492572 -17.000377 7.2404203 -0.41463478 0. 0. 0. 0. 0. 0.
VC1 0.00011212139 -0.0044154276 0.023565928 -0.048947193 0.045074884 -0.01541108 0. 0. 0. 0. 0. 0.
!
?Water/Octane [H2O/C8]
?Kunz and Wagner (2007)
b43a7600/f174a9b0
KW0 1. 0.662072469 1. 0.599484191 0. 0. 0. 0. 0. 0. 0. 0.
TC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC7 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Water/Nonane [H2O/C9]
?Kunz and Wagner (2012)
b43a7600/7f94dc20
KW0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -31.083753 680.52717 -4204.2833 11890.301 -15033.219 7198.6641 0. 0. 0. 0. 0. 0.
VC1 -0.054265336 0.36959312 -1.1830384 2.0553339 -1.5929529 0.60221149 0. 0. 0. 0. 0. 0.
!
?Water/Decane [H2O/C10]
?Kunz and Wagner (2012)
b43a7600/111888d0
KW0 1.114625565149 0.740416402 1. 0.551405318 0. 0. 0. 0. 0. 0. 0. 0.
TC2 75.995653 523.11441 -159.79463 -4641.3563 3929.1277 0. 0. 0. 0. 0. 0. 0.
VC2 1.0601614 -5.0121733 1.8790757 9.6615887 -8.4182848 0. 0. 0. 0. 0. 0. 0.
!
?Water/Ethylene glycol [H2O/EGLY]
?I.H. Bell and E.W. Lemmon, NIST (2018)
b43a7600/7d1768e0
XR0 1.006062026742 0.9986637 1.009003234965 1.066166 0. 0. 0. 0. 0. 0. 0. 0.
TC1 27.47687 101.00904 -689.46201 2015.8754 -2557.1204 1244.7708 0. 0. 0. 0. 0. 0.
VC1 0.05547963 -0.49970394 1.7985497 -2.8526099 2.0666297 -0.50120741 0. 0. 0. 0. 0. 0.
!
?Water/Dodecane [H2O/C12]
?I. Cullimore and E.W. Lemmon, NIST (2010)
b43a7600/8bc8dec0
XR0 1.080146899978 0.7908 1. 0.5514 0. 0. 0. 0. 0. 0. 0. 0.
TC1 128.19174 -370.56457 3559.2268 -12020.579 13897.358 -5623.8182 0. 0. 0. 0. 0. 0.
VC1 1.4866278 -11.106468 35.102535 -66.770112 68.879278 -28.389901 0. 0. 0. 0. 0. 0.
!
?MM/Toluene [MM/TOL]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.75% from 54 bubble-point pressures
78082e80/a49b8b50
XR0 0.999100010710 0.97446 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -29.485666 6.4422265 -28.925739 64.430884 -74.244941 33.129912 0. 0. 0. 0. 0. 0.
VC1 -0.08177179 -0.0034678589 -0.13449943 0.47083301 -0.58383785 0.28723417 0. 0. 0. 0. 0. 0.
!
?Methylcyclohexane/Toluene [C1CC6/TOL]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
0429edd0/a49b8b50
XR0 1. 0.987 1. 1.006 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -14.233458 -1.7723212 -7.4633184 29.489288 -38.688644 17.516462 0. 0. 0. 0. 0. 0.
VC1 -0.0040867649 0.014348146 0.0048315359 -0.061841906 0.10048669 -0.050259384 0. 0. 0. 0. 0. 0.
!
?Methylcyclohexane/Octane [C1CC6/C8]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
0429edd0/f174a9b0
XR0 1. 1.01 1. 1.01 0. 0. 0. 0. 0. 0. 0. 0.
TC1 12.24005 -6.2199046 37.267406 -74.861803 73.221828 -27.11221 0. 0. 0. 0. 0. 0.
VC1 0.013185426 0.049687531 -0.2511095 0.54457983 -0.54427123 0.20386744 0. 0. 0. 0. 0. 0.
!
?Methylcyclohexane/Ethylbenzene [C1CC6/EBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.34% from 81 bubble-point pressures
0429edd0/a4c64370
XR0 1.001039980436 0.99289 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 1.1705199 -12.672015 10.256957 -15.45065 13.431593 -4.7506265 0. 0. 0. 0. 0. 0.
VC1 0.035869798 -0.25709284 0.76169653 -1.2360016 1.0265682 -0.33621402 0. 0. 0. 0. 0. 0.
!
?Methylcyclohexane/p-Xylene [C1CC6/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.25% from 60 bubble-point pressures
0429edd0/01b0e650
XR0 1.001329966461 0.99463 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 12.337717 -60.054387 148.70698 -243.15292 203.52799 -67.435767 0. 0. 0. 0. 0. 0.
VC1 0.19842952 -1.6736521 6.2392739 -11.696651 10.627443 -3.71731 0. 0. 0. 0. 0. 0.
!
?Methylcyclohexane/o-Xylene [C1CC6/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.21% from 44 bubble-point pressures
0429edd0/32008e80
XR0 1.001320040209 0.99508 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 21.73664 -106.64854 304.15409 -516.02096 438.61952 -146.5231 0. 0. 0. 0. 0. 0.
VC1 0.11739579 -0.9602735 3.4612964 -6.3639068 5.6907977 -1.9645109 0. 0. 0. 0. 0. 0.
!
?Methylcyclohexane/Nonane [C1CC6/C9]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
0429edd0/7f94dc20
XR0 1. 1.02 1. 1.02 0. 0. 0. 0. 0. 0. 0. 0.
TC1 25.677065 8.8363154 3.8273048 2.1070003 -0.22092752 0.19956226 0. 0. 0. 0. 0. 0.
VC1 0.036240308 0.01495293 -0.06568991 0.12341687 -0.12886212 0.045486138 0. 0. 0. 0. 0. 0.
!
?Methylcyclohexane/Decane [C1CC6/C10]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
0429edd0/111888d0
XR0 1. 1.035 1. 1.03 0. 0. 0. 0. 0. 0. 0. 0.
TC1 46.646748 22.52847 5.7894672 19.34207 -17.760537 7.8946188 0. 0. 0. 0. 0. 0.
VC1 0.07305087 0.012432996 -0.070045277 0.075348709 -0.06480969 -0.0076442999 0. 0. 0. 0. 0. 0.
!
?Toluene/Octane [TOL/C8]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
a49b8b50/f174a9b0
KW0 1. 0.996 1. 1. -0.704 0. 0. 0. 0. 0. 0. 0.
TC1 81.982655 -57.984097 135.83905 -118.37994 43.00224 19.722091 0. 0. 0. 0. 0. 0.
VC1 0.033569332 -0.12955234 0.62051445 -1.5485433 1.7616835 -0.75604218 0. 0. 0. 0. 0. 0.
!
?Toluene/Ethylbenzene [TOL/EBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.97% from 78 bubble-point pressures
a49b8b50/a4c64370
XR0 0.9971283 1.00252 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 4.169563 3.4656237 5.6541624 -2.9927062 3.089872 -0.71943171 0. 0. 0. 0. 0. 0.
VC1 0.037026677 -0.12639442 0.3124869 -0.46162134 0.36695992 -0.12140062 0. 0. 0. 0. 0. 0.
!
?Toluene/p-Xylene [TOL/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.54% from 53 bubble-point pressures
a49b8b50/01b0e650
XR0 1.0008507 0.99999 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 11.580143 -24.916534 64.676105 -108.71492 91.716808 -30.911293 0. 0. 0. 0. 0. 0.
VC1 0.22841515 -1.8149617 6.8127865 -12.763717 11.584036 -4.0579557 0. 0. 0. 0. 0. 0.
!
?Toluene/m-Xylene [TOL/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.35% from 70 bubble-point pressures
a49b8b50/0f99ff70
XR0 1.0035123 0.99601 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 6.0679025 -6.7857544 -4.4304266 -0.79176712 -1.406484 1.4070079 0. 0. 0. 0. 0. 0.
VC1 0.23202014 -1.966948 7.6114033 -14.566729 13.424469 -4.7510871 0. 0. 0. 0. 0. 0.
!
?Toluene/o-Xylene [TOL/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 1.16% from 67 bubble-point pressures
a49b8b50/32008e80
XR0 1.001743 1.00209 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 21.464354 -50.137566 140.27946 -231.36475 191.41896 -64.081744 0. 0. 0. 0. 0. 0.
VC1 0.12274286 -0.91678422 3.3446535 -6.1744016 5.5800919 -1.9598073 0. 0. 0. 0. 0. 0.
!
?Toluene/Nonane [TOL/C9]
?T.M. Blackham and E.W. Lemmon, NIST (2010) (estimated from trend found in C1-C10)
a49b8b50/7f94dc20
KW0 1. 1. 1. 1. -1.06 0. 0. 0. 0. 0. 0. 0.
TC1 127.51298 -53.759261 54.333139 212.5748 -395.9875 238.86616 0. 0. 0. 0. 0. 0.
VC1 0.12166028 -0.62368575 2.3591742 -5.0725081 5.3512819 -2.2045255 0. 0. 0. 0. 0. 0.
!
?Toluene/Decane [TOL/C10]
?T.M. Blackham and E.W. Lemmon, NIST (2010)
a49b8b50/111888d0
KW0 1. 1.026 1. 1. -1.395 0. 0. 0. 0. 0. 0. 0.
TC1 230.85685 -215.17178 437.9055 -62.811615 -446.61233 376.26368 0. 0. 0. 0. 0. 0.
VC1 0.14580098 -0.70355413 2.969135 -7.1425984 8.1507548 -3.5822099 0. 0. 0. 0. 0. 0.
!
?Toluene/Dodecane [TOL/C12]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.82% from 19 bubble-point pressures
a49b8b50/8bc8dec0
XR0 1.004944326084 1.01727 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 54.966373 42.834867 -17.517953 95.675823 -111.56786 56.303036 0. 0. 0. 0. 0. 0.
VC1 0.77701798 -5.5863968 19.806377 -35.897997 31.61038 -10.652463 0. 0. 0. 0. 0. 0.
!
?Octane/Ethylbenzene [C8/EBE]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.52% from 76 bubble-point pressures
f174a9b0/a4c64370
XR0 0.9992206 0.98584 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -14.906638 -1.0386485 -16.553917 52.177673 -64.348572 28.882964 0. 0. 0. 0. 0. 0.
VC1 -0.02743963 -0.0087521059 -0.0043235902 0.059228402 -0.096380157 0.055719532 0. 0. 0. 0. 0. 0.
!
?Octane/p-Xylene [C8/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.2% from 51 bubble-point pressures
f174a9b0/01b0e650
XR0 0.99788 0.98651 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -10.62441 -23.080096 47.295986 -45.752261 19.739491 -1.1320179 0. 0. 0. 0. 0. 0.
VC1 0.15043514 -1.3851523 5.1144017 -9.6795009 8.8838642 -3.1258212 0. 0. 0. 0. 0. 0.
!
?Octane/m-Xylene [C8/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.56% from 24 bubble-point pressures
f174a9b0/0f99ff70
XR0 0.9996901 0.99296 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -6.5584188 -2.4362375 2.3319344 -2.115757 1.36628 -0.38855168 0. 0. 0. 0. 0. 0.
VC1 -0.13262411 0.84839918 -3.221047 6.0145223 -5.4423758 1.9044523 0. 0. 0. 0. 0. 0.
!
?Octane/o-Xylene [C8/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.84% from 36 bubble-point pressures
f174a9b0/32008e80
XR0 0.99933 0.99245 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -0.28154845 -34.438153 93.976882 -149.28912 122.88805 -40.207129 0. 0. 0. 0. 0. 0.
VC1 0.074442282 -0.68585907 2.3818789 -4.3227008 3.7535455 -1.274497 0. 0. 0. 0. 0. 0.
!
?Octane/Nonane [C8/C9]
?Kunz and Wagner (2012)
f174a9b0/7f94dc20
KW0 1. 1.000235044 1. 1.001357085 0. 0. 0. 0. 0. 0. 0. 0.
TC1 3.4676684 1.1994604 -2.4061828 4.6065919 -4.224038 1.5119187 0. 0. 0. 0. 0. 0.
VC1 0.006266866 0.011092335 -0.046519819 0.094228536 -0.089733254 0.034368182 0. 0. 0. 0. 0. 0.
!
?Octane/Decane [C8/C10]
?Kunz and Wagner (2012)
f174a9b0/111888d0
KW0 1. 1.007186267 1. 1.002553544 0. 0. 0. 0. 0. 0. 0. 0.
TC1 19.119921 7.0362976 -3.1778701 7.774737 -8.0080088 3.6090333 0. 0. 0. 0. 0. 0.
VC1 0.051769424 -0.052698115 0.037391067 -0.034439875 0.029941435 -0.01775395 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0299 -0.0488 0. 0. 0. 0. 0. 0. 0. 0.
!
?Octane/Dodecane [C8/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
f174a9b0/8bc8dec0
XR0 0.99884 1.025 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 52.372114 34.41304 -27.627699 114.47255 -128.57641 61.535743 0. 0. 0. 0. 0. 0.
VC1 0.47134609 -3.6312524 13.441895 -25.468119 23.583618 -8.5228552 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0802 -0.116 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethylbenzene/p-Xylene [EBE/XYP]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.38% from 204 bubble-point pressures
a4c64370/01b0e650
XR0 0.999479970571 0.99905 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.5200659 1.0135193 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0.0068514759 -0.0095035806 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethylbenzene/m-Xylene [EBE/XYM]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.35% from 125 bubble-point pressures
a4c64370/0f99ff70
XR0 1.000120014402 0.99939 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -0.56464025 -0.18877019 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0.0018469848 -0.0021036727 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ethylbenzene/o-Xylene [EBE/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.57% from 48 bubble-point pressures
a4c64370/32008e80
XR0 1.001530037438 0.99924 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 2.6847497 -13.350099 38.152723 -75.815962 70.087648 -24.533198 0. 0. 0. 0. 0. 0.
VC1 0.036753967 -0.23651388 0.8285386 -1.5272613 1.372856 -0.47624518 0. 0. 0. 0. 0. 0.
!
?Ethylbenzene/Nonane [EBE/C9]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.21% from 50 bubble-point pressures
a4c64370/7f94dc20
XR0 1.003750010038 0.98564 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -12.09355 -6.2187604 -17.065945 36.122855 -40.344886 17.915557 0. 0. 0. 0. 0. 0.
VC1 0.01031378 -0.02594321 0.21909908 -0.6677548 0.79863592 -0.35575417 0. 0. 0. 0. 0. 0.
!
?p-Xylene/Nonane [XYP/C9]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.22% from 11 bubble-point pressures
01b0e650/7f94dc20
XR0 0.999390371873 0.99387 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -7.9184529 3.7548794 -13.534491 33.912054 -37.291832 15.79881 0. 0. 0. 0. 0. 0.
VC1 -0.0083899135 0.23010043 -1.4383078 4.0131705 -5.0357303 2.3757612 0. 0. 0. 0. 0. 0.
!
?p-Xylene/Decane [XYP/C10]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.89% from 57 bubble-point pressures
01b0e650/111888d0
XR0 1.001011021131 0.99262 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.196566 5.5915371 -23.652054 60.90122 -77.700311 40.915826 0. 0. 0. 0. 0. 0.
VC1 0.011715035 0.76188062 -4.5468158 11.95294 -14.361746 6.4901983 0. 0. 0. 0. 0. 0.
!
?p-Xylene/Undecane [XYP/C11]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.14% from 12 bubble-point pressures
01b0e650/62f46c40
XR0 1.000190036107 1.0018 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 8.764032 22.946642 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0.06867552 0.027630509 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?m-Xylene/o-Xylene [XYM/XYO]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.25% from 78 bubble-point pressures
0f99ff70/32008e80
XR0 1.00073 0.99997 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 1.5277022 -2.2244601 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0.013538563 -0.0045124443 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?m-Xylene/Nonane [XYM/C9]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.26% from 12 bubble-point pressures
0f99ff70/7f94dc20
XR0 1.002270041417 0.98031 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -19.245176 -8.1532994 -1.732987 4.3225074 -7.5476556 6.6447714 0. 0. 0. 0. 0. 0.
VC1 0.0099109031 0.093873094 -0.53305844 1.2439472 -1.3059352 0.45323721 0. 0. 0. 0. 0. 0.
!
?m-Xylene/Decane [XYM/C10]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 2.15% from 44 bubble-point pressures
0f99ff70/111888d0
XR0 0.999650122457 0.99369 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.3961487 1.2003083 0.96558798 -0.96055321 2.8276708 -0.30966089 0. 0. 0. 0. 0. 0.
VC1 0.0081669989 0.79300832 -4.8646811 13.227189 -16.215947 7.4358384 0. 0. 0. 0. 0. 0.
!
?m-Xylene/Undecane [XYM/C11]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.1% from 13 bubble-point pressures
0f99ff70/62f46c40
XR0 0.999100809272 1.00198 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 10.960944 12.707803 -12.059998 60.326361 -84.884386 49.166965 0. 0. 0. 0. 0. 0.
VC1 0.031589715 0.90880365 -5.4268311 14.416732 -17.521726 7.9908365 0. 0. 0. 0. 0. 0.
!
?o-Xylene/Nonane [XYO/C9]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.15% from 40 bubble-point pressures
32008e80/7f94dc20
XR0 1.002908434460 0.98501 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -15.156263 -7.1697504 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0.005879356 -0.022936241 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?o-Xylene/Decane [XYO/C10]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.41% from 16 bubble-point pressures
32008e80/111888d0
XR0 1.001351824964 0.99471 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 -1.9095448 6.5014741 -32.815237 95.574487 -125.04606 63.586739 0. 0. 0. 0. 0. 0.
VC1 0.012452335 0.3838121 -2.1502866 5.4312489 -6.4337754 2.9073527 0. 0. 0. 0. 0. 0.
!
?o-Xylene/Undecane [XYO/C11]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.14% from 13 bubble-point pressures
32008e80/62f46c40
XR0 1.001903616872 0.99825 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 5.737749 35.312533 -174.75182 489.3929 -612.62882 291.2962 0. 0. 0. 0. 0. 0.
VC1 0.04475752 0.56073469 -3.330724 8.0650696 -9.1199003 3.964098 0. 0. 0. 0. 0. 0.
!
?Nonane/Decane [C9/C10]
?Kunz and Wagner (2012)
7f94dc20/111888d0
KW0 1. 1.000182392 1. 1.00081052 0. 0. 0. 0. 0. 0. 0. 0.
TC1 3.380577 -0.15180499 -0.2725307 -0.34029361 1.1561101 -0.74990283 0. 0. 0. 0. 0. 0.
VC1 0.013571625 -0.017222143 0.028030614 -0.0556765 0.063276374 -0.028394635 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0671 -0.0241 0. 0. 0. 0. 0. 0. 0. 0.
!
?Nonane/Dodecane [C9/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010) (estimated from octane and decane mixed with dodecane)
7f94dc20/8bc8dec0
KW0 0.999 1.01 1. 1.005 0.15 0. 0. 0. 0. 0. 0. 0.
TC1 9.2361645 8.4862262 2.2559343 2.533067 0.471163 -0.49928203 0. 0. 0. 0. 0. 0.
VC1 0.083790929 0.6614902 -3.4210609 7.0330484 -6.7243661 2.4311419 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0634 -0.0803 0. 0. 0. 0. 0. 0. 0. 0.
!
?MDM/D4 [MDM/D4]
?I.H. Bell and E.W. Lemmon, JCED, 2016. DOI:10.1021/acs.jced.6b00257; MAPD: 0.94% from 29 bubble-point pressures
4be67b80/b6895470
XR0 0.998263 0.99969 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC4 -0.20286244 4.3138029 -3.59171 3.9681204 0. 0. 0. 0. 0. 0. 0. 0.
VC4 0.002249348 -0.014360397 0.048286732 -0.038797379 0. 0. 0. 0. 0. 0. 0. 0.
!
?Decane/Dodecane [C10/C12]
?J. Watanasiri and E.W. Lemmon, NIST (2010)
111888d0/8bc8dec0
KW0 1. 0.998 1. 1.005 0.35 0. 0. 0. 0. 0. 0. 0.
TC1 -30.972795 -33.98309 172.8817 -441.44924 457.56983 -186.91113 0. 0. 0. 0. 0. 0.
VC1 -2.1669296 16.119348 -66.259809 138.21209 -141.71238 56.280961 0. 0. 0. 0. 0. 0.
TRN 0. 0. -0.0499 -0.0614 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methyl palmitate/Methyl oleate [MPLMT/MOLEA]
?No reference (2008) set to ideal
27c9ec60/f300b9e0
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 2.6114766 0.2984313 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 -0.013003757 -0.002968705 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methyl palmitate/Methyl linoleate [MPLMT/MLNLT]
?No reference (2008) set to ideal
27c9ec60/b61b9eb0
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 2.828995 9.121835 -34.125225 71.989723 -70.01972 25.854963 0. 0. 0. 0. 0. 0.
VC1 -0.034394309 0.020190533 -0.080377045 0.13900972 -0.13627359 0.047648534 0. 0. 0. 0. 0. 0.
!
?Methyl palmitate/Methyl linolenate [MPLMT/MLNLNT]
?No reference (2008) set to ideal
27c9ec60/298c8c80
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0.68810194 -0.048657489 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 -0.0095155722 0.00045082295 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methyl palmitate/Methyl stearate [MPLMT/MSTRT]
?No reference (2008) set to ideal
27c9ec60/81403130
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 1.7522819 0.14268336 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 -0.0095151232 0.00020316476 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methyl oleate/Methyl linoleate [MOLEA/MLNLT]
?No reference (2008) set to ideal
f300b9e0/b61b9eb0
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 1.1095339 -1.0441972 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 -0.022452939 0.028898073 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methyl oleate/Methyl linolenate [MOLEA/MLNLNT]
?No reference (2008) set to ideal
f300b9e0/298c8c80
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0.62214823 0.12823793 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 -0.0016397442 -0.0072178597 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methyl oleate/Methyl stearate [MOLEA/MSTRT]
?No reference (2008) set to ideal
f300b9e0/81403130
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0.72879061 -0.26646588 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0.016433059 -0.0026772181 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methyl linoleate/Methyl linolenate [MLNLT/MLNLNT]
?No reference (2008) set to ideal
b61b9eb0/298c8c80
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 2.1223588 -0.76448687 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 -0.01582831 0.0053511749 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methyl linoleate/Methyl stearate [MLNLT/MSTRT]
?No reference (2008) set to ideal
b61b9eb0/81403130
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0.60181009 0.94731358 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 -0.00056715804 -0.031089639 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Methyl linolenate/Methyl stearate [MLNLNT/MSTRT]
?No reference (2008) set to ideal
298c8c80/81403130
XR0 1. 1. 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC5 0.40045785 -0.35675251 0.18851515 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC5 -0.035738329 0.099368037 -0.087364948 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Water/Propylene glycol [H2O/PGLY]
?E.W. Lemmon, NIST (2012)
b43a7600/b7273ed0
KW1 1.0196 0.9385 1.0065 1.2113 8.59 0. 0. 0. 0. 0. 0. 0.
TC1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ammonia/Hydrazine [NH3/N2H4]
?E.W. Lemmon, NIST (2012)
e9847540/506609c0
XR0 1.014 1.053 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ammonia/Monomethylhydrazine [NH3/MMH]
?E.W. Lemmon, NIST (2012)
e9847540/fa4584a0
XR0 1. 1.049 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrazine/Monomethylhydrazine [N2H4/MMH]
?E.W. Lemmon, NIST (2012)
506609c0/fa4584a0
XR0 1. 0.9695 1. 1. 0. 0. 0. 0. 0. 0. 0. 0.
TC1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
VC1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
#MXM !Mixture model specification
XR0 Reducing functions only
?
?```````````````````````````````````````````````````````````````````````````````
?Mixture model for binaries that are based on mixing rules for the reducing
? parameters only. Excess functions cannot be included in this model.
?
?The mixing rules are based on those of Kunz and Wagner (2008), but all binaries
? that use the XR0 rules were developed by others.
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV not used not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
0 0 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
#MXM !Mixture model specification
KWR Lemmon and Jacobsen model for the R32-125 mixture
?
?```````````````````````````````````````````````````````````````````````````````
?E.W. Lemmon and R.T Jacobsen
? "Equations of State for Mixtures of R-32, R-125, R-134a, R-143a, and R-152a,"
? J. Phys. Chem. Ref. Data, Volume 33, Number 2, pp. 593-620, 2004.
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
8 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-0.0072955 4.5 2. 1. !a(i),t(i),d(i),e(i)
0.078035 0.57 5. 1.
0.61007 1.9 1. 2.
0.64246 1.2 3. 2.
0.014965 0.5 9. 2.
-0.34049 2.6 2. 3.
0.085658 11.4 3. 3.
-0.064429 4.5 6. 3.
#MXM !Mixture model specification
KWS Lemmon and Jacobsen model for the R32-134a mixture
?
?```````````````````````````````````````````````````````````````````````````````
?E.W. Lemmon and R.T Jacobsen
? "Equations of State for Mixtures of R-32, R-125, R-134a, R-143a, and R-152a,"
? J. Phys. Chem. Ref. Data, Volume 33, Number 2, pp. 593-620, 2004.
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
4 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
0.22909 1.9 1. 1. !a(i),t(i),d(i),e(i)
0.094074 0.25 3. 1.
0.00039876 0.07 8. 1.
0.021133 2.0 1. 2.
#MXM !Mixture model specification
KWT Lemmon and Jacobsen model for refrigerant mixtures
?
?```````````````````````````````````````````````````````````````````````````````
?E.W. Lemmon and R.T Jacobsen
? "Equations of State for Mixtures of R-32, R-125, R-134a, R-143a, and R-152a,"
? J. Phys. Chem. Ref. Data, Volume 33, Number 2, pp. 593-620, 2004.
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
4 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-0.013073 7.4 1. 1. !a(i),t(i),d(i),e(i)
0.018259 0.35 3. 1.
0.81299e-5 10.0 11. 2.
0.0078496 5.3 2. 3.
#MXM !Mixture model specification
KWQ Thol et al. (2018) model for methane + pentane
?
?```````````````````````````````````````````````````````````````````````````````
?Thol, M., Span, R., May, E., Lemmon, E., and Richter, M.
? EOS-LNG: A Fundamental Equation of State for the Calculation of Thermodynamic
? Properties of Liquefied Natural Gases.
? to be published, 2017.
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
2 4 0 4 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
0.03711 1.54 2. 0. !a(i),t(i),d(i),e(i)
-0.12154 0.95 3. 0.
27.086 0.47 1. 0.6 0.7 0.916 0.5 !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
-13.614 0.90 1. 0.43 0.61 0.87 0.5
-14.450 0.22 1. 0.7 0.7 0.86 0.5
-0.46867 2.65 2. 1.4 0.46 2.8 0.5
#MXM !Mixture model specification
KWI Thol et al. (2018) model for methane + isopentane
?
?```````````````````````````````````````````````````````````````````````````````
?Thol, M., Span, R., May, E., Lemmon, E., and Richter, M.
? EOS-LNG: A Fundamental Equation of State for the Calculation of Thermodynamic
? Properties of Liquefied Natural Gases.
? to be published, 2017.
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
2 4 0 4 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
0.051 0.2 2. 0. !a(i),t(i),d(i),e(i)
-0.1580 0.53 3. 0.
-67.49 1.79 1. 0.64 0.5 1.56 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
-88.27 2.1 1. 0.39 0.5 1.33 0.
154.9 2.0 1. 0.48 0.5 1.46 0.
3.725 0.2 2. 1. 0.5 2.7 0.
#MXM !Mixture model specification
KWK Thol et al. (2018) model for methane + butane
?
?```````````````````````````````````````````````````````````````````````````````
?Thol, M., Span, R., May, E., Lemmon, E., and Richter, M.
? EOS-LNG: A Fundamental Equation of State for the Calculation of Thermodynamic
? Properties of Liquefied Natural Gases.
? to be published, 2017.
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
3 4 0 5 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
0.7588 1.02 1. 0. !a(i),t(i),d(i),e(i)
-0.4386 0.71 2. 0.
-0.02273 1.57 3. 0.
45.05 3.41 1. 1.34 0.59 1.07 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
-2.291 2.12 1. 1.45 1.9 1.06 0.
-62.51 3.28 1. 0.96 0.87 1.11 0.
33.32 3.37 2. 1.33 1.12 1.2 0.
-12.14 3.40 1. 1.9 1.43 1.23 0.
#MXM !Mixture model specification
KWE Thol et al. (2018) model for methane + isobutane
?
?```````````````````````````````````````````````````````````````````````````````
?Thol, M., Span, R., May, E., Lemmon, E., and Richter, M.
? EOS-LNG: A Fundamental Equation of State for the Calculation of Thermodynamic
? Properties of Liquefied Natural Gases.
? to be published, 2017.
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
3 4 0 5 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
0.9396 1.43 1. 0. !a(i),t(i),d(i),e(i)
-0.1439 0.30 2. 0.
-0.1413 1.20 3. 0.
35.32 3.10 1. 1.87 1.73 1.67 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
-4.216 1.78 1. 1.05 0.78 1.76 0.
59.17 3.36 1. 1.78 1.75 1.02 0.
-76.68 2.70 2. 1.19 1.84 1.76 0.
-41.39 3.70 1. 2. 1.71 1.06 0.
#MXM !Mixture model specification
KW0 Kunz and Wagner model for hydrocarbon mixtures
?
?```````````````````````````````````````````````````````````````````````````````
?Kunz, O., Klimeck, R., Wagner, W., Jaeschke, M.
? The GERG-2004 Wide-Range Equation of State for Natural Gases and Other Mixtures.
? GERG Technical Monograph 15. Fortschr.-Ber. VDI, VDI-Verlag, Duesseldorf, 2007.
?
?Kunz, O. and Wagner, W.
? The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures:
? An Expansion of GERG-2004.
? J. Chem. Eng. Data, 57(11):3032-3091, 2012.
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
10 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
2.5574776844118 1.0 1. 0. !a(i),t(i),d(i)
-7.9846357136353 1.55 1. 0.
4.7859131465806 1.7 1. 0.
-0.73265392369587 0.25 2. 0.
1.3805471345312 1.35 2. 0.
0.28349603476365 0.0 3. 0.
-0.49087385940425 1.25 3. 0.
-0.10291888921447 0.0 4. 0.
0.11836314681968 0.7 4. 0.
0.000055527385721943 5.4 4. 0.
#MXM !Mixture model specification
KW1 Kunz and Wagner model for the methane-ethane mixture
?
?```````````````````````````````````````````````````````````````````````````````
?Kunz, O., Klimeck, R., Wagner, W., Jaeschke, M.
? The GERG-2004 Wide-Range Equation of State for Natural Gases and Other Mixtures.
? GERG Technical Monograph 15. Fortschr.-Ber. VDI, VDI-Verlag, Duesseldorf, 2007.
?
?Kunz, O. and Wagner, W.
? The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures:
? An Expansion of GERG-2004.
? J. Chem. Eng. Data, 57(11):3032-3091, 2012.
?
?Methane-Ethane
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
2 4 0 10 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-0.00080926050298746 0.65 3. 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
-0.00075381925080059 1.55 4. 0.
-0.041618768891219 3.1 1. 1.0 0.5 1.0 0.5
-0.23452173681569 5.9 2. 1.0 0.5 1.0 0.5
0.14003840584586 7.05 2. 1.0 0.5 1.0 0.5
0.063281744807738 3.35 2. 0.875 0.5 1.25 0.5
-0.034660425848809 1.2 2. 0.75 0.5 1.5 0.5
-0.23918747334251 5.8 2. 0.5 0.5 2.0 0.5
0.0019855255066891 2.7 2. 0.0 0.5 3.0 0.5
6.1777746171555 0.45 3. 0.0 0.5 3.0 0.5
-6.9575358271105 0.55 3. 0.0 0.5 3.0 0.5
1.0630185306388 1.95 3. 0.0 0.5 3.0 0.5
#MXM !Mixture model specification
KW2 Kunz and Wagner model for the methane-propane mixture
?
?```````````````````````````````````````````````````````````````````````````````
?Kunz, O., Klimeck, R., Wagner, W., Jaeschke, M.
? The GERG-2004 Wide-Range Equation of State for Natural Gases and Other Mixtures.
? GERG Technical Monograph 15. Fortschr.-Ber. VDI, VDI-Verlag, Duesseldorf, 2007.
?
?Kunz, O. and Wagner, W.
? The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures:
? An Expansion of GERG-2004.
? J. Chem. Eng. Data, 57(11):3032-3091, 2012.
?
?Methane-Propane
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
5 4 0 4 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
0.013746429958576 1.85 3. 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
-0.0074425012129552 3.95 3. 0.
-0.0045516600213685 0.0 4. 0.
-0.0054546603350237 1.85 4. 0.
0.0023682016824471 3.85 4. 0.
0.18007763721438 5.25 1. 0.25 0.5 0.75 0.5
-0.44773942932486 3.85 1. 0.25 0.5 1.0 0.5
0.019327374888200 0.2 1. 0.0 0.5 2.0 0.5
-0.30632197804624 6.5 2. 0.0 0.5 3.0 0.5
#MXM !Mixture model specification
KW3 Kunz and Wagner model for the methane-nitrogen mixture
?
?```````````````````````````````````````````````````````````````````````````````
?Kunz, O., Klimeck, R., Wagner, W., Jaeschke, M.
? The GERG-2004 Wide-Range Equation of State for Natural Gases and Other Mixtures.
? GERG Technical Monograph 15. Fortschr.-Ber. VDI, VDI-Verlag, Duesseldorf, 2007.
?
?Kunz, O. and Wagner, W.
? The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures:
? An Expansion of GERG-2004.
? J. Chem. Eng. Data, 57(11):3032-3091, 2012.
?
?Methane-Nitrogen
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
2 4 0 7 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-0.0098038985517335 0.0 1. 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
0.00042487270143005 1.85 4. 0.
-0.034800214576142 7.85 1. 1.0 0.5 1.0 0.5
-0.13333813013896 5.4 2. 1.0 0.5 1.0 0.5
-0.011993694974627 0.0 2. 0.25 0.5 2.5 0.5
0.069243379775168 0.75 2. 0.0 0.5 3.0 0.5
-0.31022508148249 2.8 2. 0.0 0.5 3.0 0.5
0.24495491753226 4.45 2. 0.0 0.5 3.0 0.5
0.22369816716981 4.25 3. 0.0 0.5 3.0 0.5
#MXM !Mixture model specification
KW4 Kunz and Wagner model for the methane-CO2 mixture
?
?```````````````````````````````````````````````````````````````````````````````
?Kunz, O., Klimeck, R., Wagner, W., Jaeschke, M.
? The GERG-2004 Wide-Range Equation of State for Natural Gases and Other Mixtures.
? GERG Technical Monograph 15. Fortschr.-Ber. VDI, VDI-Verlag, Duesseldorf, 2007.
?
?Kunz, O. and Wagner, W.
? The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures:
? An Expansion of GERG-2004.
? J. Chem. Eng. Data, 57(11):3032-3091, 2012.
?
?Methane-Carbon dioxide
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
3 4 0 3 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-0.10859387354942 2.6 1. 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
0.080228576727389 1.95 2. 0.
-0.0093303985115717 0.0 3. 0.
0.040989274005848 3.95 1. 1.0 0.5 1.0 0.5
-0.24338019772494 7.95 2. 0.5 0.5 2.0 0.5
0.23855347281124 8.0 3. 0.0 0.5 3.0 0.5
#MXM !Mixture model specification
KW5 Kunz and Wagner model for the nitrogen-CO2 mixture
?
?```````````````````````````````````````````````````````````````````````````````
?Kunz, O., Klimeck, R., Wagner, W., Jaeschke, M.
? The GERG-2004 Wide-Range Equation of State for Natural Gases and Other Mixtures.
? GERG Technical Monograph 15. Fortschr.-Ber. VDI, VDI-Verlag, Duesseldorf, 2007.
?
?Kunz, O. and Wagner, W.
? The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures:
? An Expansion of GERG-2004.
? J. Chem. Eng. Data, 57(11):3032-3091, 2012.
?
?Nitrogen-Carbon dioxide
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
2 4 0 4 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
0.28661625028399 1.85 2. 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
-0.10919833861247 1.4 3. 0.
-1.1374032082270 3.2 1. 0.25 0.5 0.75 0.5
0.76580544237358 2.5 1. 0.25 0.5 1.0 0.5
0.0042638000926819 8.0 1. 0.0 0.5 2.0 0.5
0.17673538204534 3.75 2. 0.0 0.5 3.0 0.5
#MXM !Mixture model specification
KW6 Kunz and Wagner model for the nitrogen-ethane mixture
?
?```````````````````````````````````````````````````````````````````````````````
?Kunz, O., Klimeck, R., Wagner, W., Jaeschke, M.
? The GERG-2004 Wide-Range Equation of State for Natural Gases and Other Mixtures.
? GERG Technical Monograph 15. Fortschr.-Ber. VDI, VDI-Verlag, Duesseldorf, 2007.
?
?Kunz, O. and Wagner, W.
? The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures:
? An Expansion of GERG-2004.
? J. Chem. Eng. Data, 57(11):3032-3091, 2012.
?
?Nitrogen-Ethane
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
3 4 0 3 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-0.47376518126608 0.0 2. 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
0.48961193461001 0.05 2. 0.
-0.0057011062090535 0.0 3. 0.
-0.19966820041320 3.65 1. 1.0 0.5 1.0 0.5
-0.69411103101723 4.9 2. 1.0 0.5 1.0 0.5
0.69226192739021 4.45 2. 0.875 0.5 1.25 0.5
#MXM !Mixture model specification
KW7 Kunz and Wagner model for the methane-hydrogen mixture
?
?```````````````````````````````````````````````````````````````````````````````
?Kunz, O., Klimeck, R., Wagner, W., Jaeschke, M.
? The GERG-2004 Wide-Range Equation of State for Natural Gases and Other Mixtures.
? GERG Technical Monograph 15. Fortschr.-Ber. VDI, VDI-Verlag, Duesseldorf, 2007.
?
?Kunz, O. and Wagner, W.
? The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures:
? An Expansion of GERG-2004.
? J. Chem. Eng. Data, 57(11):3032-3091, 2012.
?
?Methane-Hydrogen
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
4 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-0.25157134971934 2.0 1. 0. !a(i),t(i),d(i)
-0.0062203841111983 -1.0 3. 0.
0.088850315184396 1.75 3. 0.
-0.035592212573239 1.4 4. 0.
#MXM !Mixture model specification
KW8 Lemmon model for the ethanol/water mixture
?
?```````````````````````````````````````````````````````````````````````````````
?E.W. Lemmon, preliminary equation fit to PVT, VLE, and HE, 2008.
?
?Ethanol-Water
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
6 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
1.09765 0.26 2. 1. !a(i),t(i),d(i),e(i)
1.94679 7.3 3. 2.
-2.16809 5.3 5. 2.
-0.137077 2.3 5. 1.
0.0486690 0.7 7. 1.
1.04024 3.3 6. 2.
#MXM !Mixture model specification
KWB Blackham and Lemmon model for ethanol/hydrocarbon mixtures
?
?```````````````````````````````````````````````````````````````````````````````
?T.M. Blackham and E.W. Lemmon, NIST (2010) Preliminary equation fit to PVT, VLE, and HE.
?
?Ethanol-Hydrocarbon mixtures
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
7 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-2.05560 4.5 1. 2. !a(i),t(i),d(i),e(i)
1.94512 4.7 1. 0.
-0.196687 4.68 2. 0.
0.425412 2.5 3. 1.
-1.01883 4.68 4. 1.
-0.786737 5.5 4. 2.
-0.229943 8.2 5. 2.
#MXM !Mixture model specification
KWC Gernert model for the CO2-Ar mixture
?
?```````````````````````````````````````````````````````````````````````````````
?Gernert, J. and Span, R.
? EOS-CG: A Helmholtz Energy Mixture Model for Humid Gases and CCS Mixtures
? J. Chem. Thermodyn., 93:274-293, 2016.
? DOI:10.1016/j.jct.2015.05.015
?
?Carbon dioxide-Argon
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
2 4 0 4 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
0.20483577 2.194 2. 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
-0.11465124 1.743 3. 0.
-2.3151700 2.470 1. 0.25 0.5 0.75 0.5
2.3523617 1.977 1. 0.25 0.5 1.00 0.5
-0.66835959 1.207 1. 0.0 0.5 1.05 0.5
-0.053016558 0.796 2. 0.0 0.5 3.00 0.5
#MXM !Mixture model specification
KWD Gernert model for water mixtures
?
?```````````````````````````````````````````````````````````````````````````````
?Gernert, J. and Span, R.
? EOS-CG: A Helmholtz Energy Mixture Model for Humid Gases and CCS Mixtures
? J. Chem. Thermodyn., 93:274-293, 2016.
? DOI:10.1016/j.jct.2015.05.015
?
?Departure function for H2O/N2, H2O/O2, and H2O/CO
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
5 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
4.01420713 0.547 1. 0. !a(i),t(i),d(i),e(i)
-1.15739394 0.055 1. 1.
-7.21024248 1.925 1. 1.
-5.32512228 0.552 2. 1.
-2.21558667 1.0 4. 1.
#MXM !Mixture model specification
KWG Gernert model for the CO2-water mixture
?
?```````````````````````````````````````````````````````````````````````````````
?Gernert, J. and Span, R.
? EOS-CG: A Helmholtz Energy Mixture Model for Humid Gases and CCS Mixtures
? J. Chem. Thermodyn., 93:274-293, 2016.
? DOI:10.1016/j.jct.2015.05.015
?
?Carbon dioxide-Water
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
8 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
0.39440467 0.88 1. 0. !a(i),t(i),d(i),e(i)
-1.7634732 2.932 1. 0.
0.14620755 2.433 3. 0.
0.008752232 1.33 0. 1.
2.0349398 4.416 2. 1.
-0.090350250 5.514 3. 1.
-0.21638854 5.203 1. 2.
0.039612170 1.0 5. 2.
#MXM !Mixture model specification
KWL Richardson et al. model for the helium-hydrogen mixture
?
?```````````````````````````````````````````````````````````````````````````````
?Richardson, I.A., Blackham, T.M., Leachman, J.W., and Lemmon, E.W.,
? in preparation, 2018.
?
?Helium-Hydrogen
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
4 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-0.7708 1.8 2. 2. !a(i),t(i),d(i),e(i)
-0.08563 1.0 2. 0.
-0.2624 1.6 1. 1.
0.4731 0.4 1. 2.
#MXM !Mixture model specification
KWN Neumann model for the CO2-argon mixture
?
?```````````````````````````````````````````````````````````````````````````````
?T. Neumann,
? Lehrstuhl Fuer Thermodynamik, Ruhr Universitaet, Bochum, Germany, 2017.
?
?Carbon dioxide-Argon
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
2 4 0 4 7 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-0.0656 3.22 2. 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
0.0237 2.9 3. 0.
3.5217 1.9 1. 1.243 0.65 1.208 0.5
-2.831 1.57 1. 1.072 0.727 0.82 0.5
-1.406 2.73 1. 1.465 0.648 1.527 0.5
0.864 1.08 2. 0.946 0.706 0.86 0.5
#MXM !Mixture model specification
BAA Neumann model for the argon-ammonia mixture
?
?```````````````````````````````````````````````````````````````````````````````
?T. Neumann,
? Lehrstuhl Fuer Thermodynamik, Ruhr Universitaet, Bochum, Germany, 2018.
?
?Argon - Ammonia
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
1 4 0 0 0 2 12 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
0.02350785 2.3 3. 1. !a(i),t(i),d(i),e(i)
-1.913776 1.65 1. 2. 2. -1.3 -0.6 0.9 0.31 0. 0. 0.
1.624062 0.42 1. 2. 2. -1.5 -0.5 1.5 0.39 0. 0. 0.
#MXM !Mixture model specification
BAW Bell et al. model for the ammonia/water mixture
?
?```````````````````````````````````````````````````````````````````````````````
?I.H. Bell, K. Gao, J. Wu, and E.W. Lemmon (2018)
?
?Ammonia-Water
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
2 4 0 0 0 5 12 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-2.00211 0.25 1. 2. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
3.08130 2.0 1. 1.
-1.75352 0.5 1. 2. 2. 0.0 -0.27 2.8 0.0 0. 0. 0.
2.98160 2.0 1. 2. 2. -0.746 -0.86 1.8 2.0 0. 0. 0.
-3.82588 1.0 1. 2. 2. -4.25 -3.0 1.5 -0.25 0. 0. 0.
-1.73850 4.0 1. 2. 2. -0.7 -0.5 0.8 1.85 0. 0. 0.
0.42008 1.0 3. 2. 2. -3.0 -4.0 1.3 0.3 0. 0. 0.
#MXM !Mixture model specification
BCC Souza and Herrig model for the CO2-CO mixture
?
?```````````````````````````````````````````````````````````````````````````````
?L. Souza and S. Herrig, 2018.
?
?Carbon dioxide-Carbon monoxide
?
!```````````````````````````````````````````````````````````````````````````````
BetaT GammaT BetaV GammaV Fij not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 0.0 0.0 !Default values (i.e. ideal-solution)
4 4 0 0 0 2 12 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
1.861 2.82 1. 0. !a(i),t(i),d(i),eta(i),epsilon(i),beta(i),gamma(i)
-4.017 3.26 1. 0.
0.2734 0.94 2. 1.
2.393 3.944 4. 1.
26.46 2.53 1. 2. 2. -0.385 -0.144 5.1 0.109 0. 0. 0.
-1.213 4.38 1. 2. 2. -0.295 -0.31 1.661 2.596 0. 0. 0.
#MXM !Mixture model specification
LJ6 Lemmon and Jacobsen model for refrigerant mixtures
?
?```````````````````````````````````````````````````````````````````````````````
?E.W. Lemmon and R.T Jacobsen
? "Equations of State for Mixtures of R-32, R-125, R-134a, R-143a, and R-152a,"
? J. Phys. Chem. Ref. Data, Volume 33, Number 2, pp. 593-620, 2004.
?
?Refrigerant mixtures
?
!```````````````````````````````````````````````````````````````````````````````
zeta xi Fpq beta gamma not used !Descriptors for binary-specific parameters
0.0 0.0 0.0 1.0 1.0 0.0 !Default values (i.e. ideal-solution)
4 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-0.013073 7.4 1. 1. !a(i),t(i),d(i),e(i)
0.018259 0.35 3. 1.
0.81299e-5 10.0 11. 2.
0.0078496 5.3 2. 3.
#MXM !Mixture model specification
LIN Linear mixing rules modified by Kt and Kv
?
?```````````````````````````````````````````````````````````````````````````````
?McLinden, M.O. and Klein, S.A.,
? "A next generation refrigerant properties database,"
? 6th International Refrigeration Conference at Purdue,
? July 23-26, West Lafayette, IN, 1996.
?
?A mixture Helmholtz free energy (HMX) model for refrigerant mixtures employing
? simple linear mixing rules to define the reducing parameters. The parameter
? Kt is applied to the arithmetic mean of the component critical temperatures:
?
? Treducing = sum(i=1,n) {xi * Tcrit_i}
? + sum(j=i+1,n) sum(i=1,n-1) {(Kt - 1) xi xj 0.5*(Tcrit_i + Tcrit_j)}
?
? The parameter Kv is similarly applied to the arithmetic mean of the
? component critical volumes:
?
? Vreducing = sum(i=1,n) {xi * Vcrit_i}
? + sum(j=i+1,n) sum(i=1,n-1) {(Kv - 1) xi xj 0.5*(Vcrit_i + Vcrit_j)}
?
? rho_reducing = 1/Vreducing.
?
!```````````````````````````````````````````````````````````````````````````````
Kt Kv not used not used not used not used !Descriptors for binary-specific parameters
1.0 1.0 0.0 0.0 0.0 0.0 !Default values (i.e. ideal-solution)
1 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
1.0 0. 1. 0. !a(i),t(i),d(i),e(i)
@MXM !Mixture model specification
i=j Trivial case--identical components
?
?```````````````````````````````````````````````````````````````````````````````
?This represents the trivial mixture case of identical components. It is
? included for use with some of the summations involved in mixture calculations.
? This model should not be specified for any binary pair.
?
!```````````````````````````````````````````````````````````````````````````````
not used not used not used not used not used not used !Descriptors for binary-specific parameters
0.0 0.0 0.0 0.0 0.0 0.0 !Default values (i.e. ideal-solution)
1 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
1.0 0. 1. 0. !a(i),t(i),d(i),e(i)
#MXM !Mixture model specification
TR1 Tillner-Roth model for ammonia-water mixtures
?
?```````````````````````````````````````````````````````````````````````````````
?Tillner-Roth, R. and Friend, D.G.,
? "A Helmholtz free energy formulation of the thermodynamic properties
? of the mixture {water + ammonia},"
? J. Phys. Chem. Ref. Data, 27(1):63-96, 1998.
?
?A fundamental equation of state for the Helmholtz free energy of the mixture
? {ammonia+water} is presented which covers the thermodynamic space between the
? solid-liquid-vapor boundary and the critical locus. It is also valid in the
? vapor and liquid phase for pressures up to 40 MPa. It represents VLS properties
? with an uncertainty of 0.01 of liquid and vapor compositions. Typical uncertainties
? in the single-phase regions are 0.3% for the density and +/- 200 J/mol for enthalpies.
?
!```````````````````````````````````````````````````````````````````````````````
Kt Kv alpha beta gamma not used !Descriptors for binary-specific parameters
1.0 1.0 1.0 1.0 1.0 0.0 !Default values (i.e. ideal solution)
14 4 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Kunz-Wagner terms, and Gaussian terms. 3rd column is not used.
-0.01855822 1.5 4. 0. !a(i),t(i),d(i),e(i)
0.05258010 0.5 5. 1.
3.552874e-10 6.5 15. 1.
5.451379e-6 1.75 12. 1.
-5.998546e-13 15.0 12. 1.
-3.687808e-6 6.0 15. 2.
0.2586192 -1.0 4. 1.
-1.368072e-8 4.0 15. 1.
0.01226146 3.5 4. 1.
-0.07181443 0.0 5. 1.
0.09970849 -1.0 6. 2.
0.0010584086 8.0 10. 2.
-0.1963687 7.5 6. 2.
-0.7777897 4.0 2. 2.
@END
c 1 2 3 4 5 6 7 8
c2345678901234567890123456789012345678901234567890123456789012345678901234567890
?R13/R22
?Only transport interaction parameters are available (2006)
126c90a0/57716470
TRN -0.0332 0.1389 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R13B1/R22
?Only transport interaction parameters are available (2006)
52a67e60/57716470
TRN -0.2505 0.7028 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R14/R22
?Only transport interaction parameters are available (2006)
dba9f950/57716470
TRN 0.0523 -0.1194 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R14/Carbon monoxide
?Only transport interaction parameters are available (2006)
dba9f950/091cb7e0
TRN -0.0421 -0.0638 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?R32/R124
?Only transport interaction parameters are available (2006)
7b05bb60/36953260
TRN 0. 0. -0.0813 -0.1158 0. 0. 0. 0. 0. 0. 0. 0.
!
?Krypton/Carbon monoxide
?Only transport interaction parameters are available (2006)
d7c8c510/091cb7e0
TRN -0.08889 -0.05653 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Ammonia
?Only transport interaction parameters are available (2006)
8d757b40/e9847540
TRN -0.50 0.848 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Ethylene
?Only transport interaction parameters are available (2006)
8d757b40/9c1062b0
TRN -0.634 0.872 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 0.0074 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/Propylene
?Only transport interaction parameters are available (2006)
8d757b40/56d778b0
TRN -0.568 0.786 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
PR1 -0.1037 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Hydrogen/cis-Butene
?Only transport interaction parameters are available (2006)
8d757b40/411c4500
TRN -0.766 0.854 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Xenon/Argon
?Only transport interaction parameters are available (2009)
71fd7fa0/ed016370
TRN -0.16301 0.30637 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Xenon/Helium
?Only transport interaction parameters are available (2009)
71fd7fa0/3b8eed30
TRN -0.2 -4. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ammonia/Nitrous oxide
? Fit 9/17 to Trans. Faraday Soc., 1965, 61, 2422 AAD 1.1%
e9847540/e0647c00
TRN 0.02 -0.37 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Argon/Sulfur dioxide
? Fit 9/17 to Trans. Faraday Soc., 1965, 61, 2422 AAD 1.8%
ed016370/7fad4b80
TRN 0.17 -0.79 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
?Ammonia/Oxygen
? Fit 9/17 to Trautz, M. and Heberling, R., Ann. Physik, 1931, 10, 155 AAD 0.5%
e9847540/edc36840
TRN -0.120 0.17 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.
!
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