TyroneGit/CapMachine
1
0
Fork 0
Code Issues Pull Requests Actions Packages Projects Releases Wiki Activity

一些优化：CAN和PLC地址的优化

Browse Source
This commit is contained in:
Tyrone CT
2025-01-01 13:11:13 +08:00
parent 8b21846424
commit 26569135d3
182 changed files with 87934 additions and 261 deletions
Download Patch File Download Diff File Expand all files Collapse all files

560
CapMachine.Wpf/PPCalculation/REFPROP/FLUIDS/NEON.FLD Normal file
View File

@@ -0,0 +1,560 @@
Neon !Short name
7440-01-9 !CAS number
Neon !Full name
Ne !Chemical formula {Ne}
R-720 !Synonym
20.179 !Molar mass [g/mol]
24.5561 !Triple point temperature [K] (Bedford et al., Metrologia, 33:133, 1996.)
27.1000 !Normal boiling point [K] (all digits are significant!)
44.4 !Critical temperature [K]
2661.63 !Critical pressure [kPa]
24.1 !Critical density [mol/L]
-0.0355 !Acentric factor
0.0 !Dipole moment [Debye]; (exactly zero for monatomic molecules)
NBP !Default reference state
10.0 !Version number
1065, 1913 !UN Number :UN:
cryogen !Family :Family:
0.0 !Heating value (upper) [kJ/mol] :Heat:
A1 !Safety Group (ASHRAE Standard 34, 2010) :Safety:
1S/Ne !Standard InChI String :InChi:
GKAOGPIIYCISHV-UHFFFAOYSA-N !Standard InChI Key :InChiKey:
8d757b40 (hydrogen) !Alternative fluid for mixing rules :AltID:
b912fce0 !Hash number from InChI Key :Hash:
!The fluid files contain general information about the fluid in the first 15 to 20 lines, followed by sections for the
! equations of state, transport equations, and auxiliary equations. Equations of state are listed first. The NIST recommended
! equations begin with a hash mark (#). The secondary equations begin with the @ symbol. These symbols can be swapped to
! select a secondary equation as primary and the primary as secondary. The equation of state section also contains auxiliary
! equations for the ideal gas heat capacity or ideal gas Helmholtz energy. Below the equations of state (both primary and
! secondary) are the transport equations, first viscosity and then thermal conductivity. These are then followed by the
! secondary equations if available. The transport section also contains auxiliary equations required to calculate either the
! dilute gas state or the critical enhancement. At the end of the file are additional but not necessary auxiliary equations,
! including simple equations for the vapor pressure, saturated liquid and vapor densities, melting line (for some fluids), and
! sublimation line (for even fewer fluids). This section also contains the equations for dielectric constant and surface
! tension if available. The sections are divided by different symbols (these being _-+=^*~) to aid the eye in locating a
! particular section. Secondary equations are indented 10 spaces to avoid confusion with the NIST recommended equations. The
! end of the fluid file is marked with @END. Anything below that is ignored.
! compiled by E.W. Lemmon, NIST Physical and Chemical Properties Division, Boulder, Colorado
! 12-03-97 EWL, Original version.
! 03-27-00 EWL, Add viscosity equation of Rabinovich.
! 08-05-04 EWL, Add Harvey and Lemmon dielectric correlation.
! 11-10-04 EWL, Add sublimation line.
! 01-30-07 EWL, Change triple point from 24.562 to 24.556 in accordance with Bedford et al., Metrologia, 33:133, 1996.
! 03-05-10 EWL, Add melting line and increase maximum density.
! 07-13-10 CKL, Add ancillary equations.
! 10-15-10 MLH, Revise lower temp limit on visc and therm. cond.
! 12-06-12 EWL, Add surface tension coefficients of Mulero et al. (2012).
! 07-20-16 MLH, Add ECS fit coefficients, revised LJ par.
! 02-25-17 MLH, Revise ECS.
! 05-15-17 EWL, Change the hard coded VS0 model to the VS7 reverse Polish notation.
! 12-11-17 MLH, Adjust dilute gas ecs viscosity to match ref. value at 25 C from Berg and Moldover, JPCRD 41(4) 043104 (2012).
! 02-13-18 MLH, Adjust dilute k due to adjusted viscosity from the change listed one line up.
! 02-16-18 IHB, Adjust sublimation curve from Brown to match triple point (w/ AHH).
! 03-15-18 MT, Add new equation of state of Thol et al. (2018).
! 04-02-18 MLH, Redo thermal conductivity and viscosity with new EOS of Thol.
________________________________________________________________________________
#EOS !---Equation of state---
FEQ !Helmholtz equation of state for neon of Thol et al. (2018).
:TRUECRITICALPOINT: 44.4 24.1 !True EOS critical point [K, mol/L] (where dP/dD=0 and d^2P/dD^2=0 at constant T)
:DOI:
?
?```````````````````````````````````````````````````````````````````````````````
?Thol, M., Beckmüller, R., Weiss, R., Harvey, A.H., Lemmon, E.W., Jacobsen, R.T, and Span, R.,
? "Thermodynamic Properties for Neon for Temperatures from the Triple
? Point to 700 K at Pressures to 700 MPa,"
? to be submitted to Int. J. Thermophys., 2018.
?
!```````````````````````````````````````````````````````````````````````````````
24.5561 !Lower temperature limit [K]
725.0 !Upper temperature limit [K]
1000000.0 !Upper pressure limit [kPa]
99.62 !Maximum density [mol/L]
CPP !Pointer to Cp0 model
20.179 !Molar mass [g/mol]
24.5561 !Triple point temperature [K]
43.355 !Pressure at triple point [kPa]
61.931 !Density at triple point [mol/L]
27.1000 !Normal boiling point temperature [K] (all digits are significant!)
-0.0355 !Acentric factor
44.4 2661.63 24.1 !Tc [K], pc [kPa], rhoc [mol/L]
44.4 24.1 !Reducing parameters [K, mol/L]
8.3144598 !Gas constant [J/mol-K]
11 4 6 12 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Gaussian terms, and Gao terms
0.031522418 1. 4. 0. !a(i),t(i),d(i),l(i)
3.7716418 0.431 1. 0.
-4.27399448 0.592 1. 0.
-0.756466758 1.105 2. 0.
0.066679921 0.49 3. 0.
-0.356928434 2.3 1. 2.
-0.053124761 3.18 3. 2.
0.9407234 1.36 2. 1.
-0.969302374 2. 2. 2.
0.461243234 0.5 4. 1.
0.008184422 1.12 7. 1.
7.84771604 0.41 1. 2. 2. -0.76 -0.537 1.997 0.5775 0. 0. 0.
6.39604094 0.64 1. 2. 2. -2.126 -0.765 1.782 0.9137 0. 0. 0.
-1.27480579 0.579 3. 2. 2. -2.168 -0.883 1.663 0.7895 0. 0. 0.
-5.51887999 0.6 2. 2. 2. -2.033 -0.751 1.837 0.6229 0. 0. 0.
-8.76652276 0.52 1. 2. 2. -0.743 -0.531 1.953 0.4992 0. 0. 0.
-0.351732709 0.655 2. 2. 2. -4.38 -11.4 1.658 0.869 0. 0. 0.
#AUX !---Auxiliary function for Cp0
CPP !Ideal gas heat capacity function for neon of Thol et al. (2018).
?
?```````````````````````````````````````````````````````````````````````````````
?Thol, M., Beckmüller, R., Weiss, R., Harvey, A.H., Lemmon, E.W., Jacobsen, R.T, and Span, R., 2018.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1.0 8.3144598 !Reducing parameters for T, Cp0
1 0 0 0 0 0 0 !Nterms: polynomial, exponential, cosh, sinh
2.5 0.0
#AUX !---Auxiliary function for PX0
PX0 !Helmholtz energy ideal-gas function for neon of Thol et al. (2018).
?
?```````````````````````````````````````````````````````````````````````````````
?Thol, M., Beckmüller, R., Weiss, R., Harvey, A.H., Lemmon, E.W., Jacobsen, R.T, and Span, R., 2018.
?
!```````````````````````````````````````````````````````````````````````````````
1 2 0 0 0 0 0 0 !Nterms: ai*log(tau**ti); ai*tau**ti; ai*log(1-exp(bi*tau))
1.5 1.0 !ai, ti for [ai*log(tau**ti)] terms
-3.0384719151147275 0.0 !aj, ti for [ai*tau**ti] terms
3.253690479855404 1.0 !aj, ti for [ai*tau**ti] terms
--------------------------------------------------------------------------------
@EOS !---Equation of state---
FE1 !Helmholtz equation of state for neon of Katti et al. (1986).
:DOI: 10.1007/978-1-4613-2213-9_132
?
?```````````````````````````````````````````````````````````````````````````````
?Katti, R.S., Jacobsen, R.T, Stewart, R.B., and Jahangiri, M.,
? "Thermodynamic Properties for Neon for Temperatures from the Triple
? Point to 700 K at Pressures to 700 MPa,"
? Adv. Cryo. Eng., 31:1189-1197, 1986. doi: 10.1007/978-1-4613-2213-9_132
?
?The uncertainties of the equation of state are 0.1% in density, 2% in heat
? capacity, and 1% in the speed of sound, except in the critical region.
? The uncertainty in vapor pressure is 0.2%.
?
!```````````````````````````````````````````````````````````````````````````````
24.556 !Lower temperature limit [K]
700.0 !Upper temperature limit [K]
700000.0 !Upper pressure limit [kPa]
90.56 !Maximum density [mol/L]
CP1 !Pointer to Cp0 model
20.179 !Molar mass [g/mol]
24.556 !Triple point temperature [K]
43.368 !Pressure at triple point [kPa]
62.059 !Density at triple point [mol/L]
27.104 !Normal boiling point temperature [K]
-0.0387 !Acentric factor
44.4918 2678.6 23.882 !Tc [K], pc [kPa], rhoc [mol/L]
44.4918 23.882 !Reducing parameters [K, mol/L]
8.31434 !Gas constant [J/mol-K]
29 4 0 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Gaussian terms, and Gao terms
3.532653449 0.5 1. 0. !a(i),t(i),d(i),l(i)
-4.513954384 0.75 1. 0.
-0.1524027959 3.5 1. 0.
2.188568609 0.5 2. 0.
-7.44299997 0.75 2. 0.
7.755627402 1.0 2. 0.
-3.122553128 1.5 2. 0.
1.014206899 2.5 2. 0.
-0.05289214086 0.25 3. 0.
0.1566849239 0.5 3. 0.
-0.222852705 2.5 3. 0.
-0.01410150942 1.0 4. 0.
0.07036229719 3.0 4. 0.
-0.05882048367 4.0 4. 0.
0.01571172741 5.0 4. 0.
0.001292202769 1.0 6. 0.
0.0007902035603 5.0 6. 0.
-0.0003794403616 6.0 6. 0.
0.04652799333 4.0 1. 3.
0.04524001818 1.0 2. 2.
-0.2383421991 5.0 2. 2.
0.00629359013 8.0 2. 4.
-0.001272313644 12.0 2. 6.
-0.175235256e-6 32.0 2. 6.
0.007188419232 10.0 4. 2.
-0.05403006914 6.0 8. 2.
0.07578222187 7.0 8. 2.
-0.03808588254 8.0 8. 2.
0.006034022431 9.0 8. 2.
@AUX !---Auxiliary function for Cp0
CP1 !Ideal gas heat capacity function for neon of Katti et al. (1986).
?
?```````````````````````````````````````````````````````````````````````````````
?Katti, R.S., Jacobsen, R.T, Stewart, R.B., and Jahangiri, M.,
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1.0 8.31434 !Reducing parameters for T, Cp0
1 0 0 0 0 0 0 !Nterms: polynomial, exponential, cosh, sinh
2.5 0.0
@AUX !---Auxiliary function for PH0
PH1 !Ideal gas Helmholtz form for neon.
?
?```````````````````````````````````````````````````````````````````````````````
?Katti, R.S., Jacobsen, R.T, Stewart, R.B., and Jahangiri, M.,
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1 2 0 0 0 0 0 0 !Nterms: ai*log(tau**ti); ai*tau**ti; ai*log(1-exp(bi*tau)); cosh; sinh
1.5 1.0 !ai, ti for [ai*log(tau**ti)] terms
-3.0597521577 0.0 !aj, ti for [ai*tau**ti] terms
3.2525230449 1.0
++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
#TRN !---ECS Transport---
ECS !Extended Corresponding States model (Nitrogen reference); fit to limited data for neon.
:DOI: 10.6028/NIST.IR.8209
?
?```````````````````````````````````````````````````````````````````````````````
?*** ESTIMATION METHOD *** NOT STANDARD REFERENCE QUALITY ***
?Huber, M.L., "Models for the Viscosity, Thermal Conductivity, and Surface Tension
? of Selected Pure Fluids as Implemented in REFPROP v10.0," NISTIR 8209, 2018.
? doi: 10.6028/NIST.IR.8209
?
?VISCOSITY
? Forster, S., "Viscosity Measurements in Liquid Neon, Argon, and Nitrogen," Cryogenics, 3, 176, 1963.
? Slusar', V.P., Rudenko, N.S., and Tret'yakov, V.M., "Experimental Study of the Viscosity of Simple Substances along the Saturation Curve and under Pressure," Ukr. Fiz. Zh., 18:190-194, 1973. Based on comparisons with data sources above, estimated uncertainty in liquid phase is 10% along the saturation boundary, 10% along the vapor saturation boundary, 3% for atmospheric pressure, and 4% at pressures to 80 MPa.
?
?Data sources for liquid thermal conductivity:
? Bewilogua, L and Yamashira, T., J., Low Temp. Phys., Vol 8, pp. 255-263, 1972. Estimated uncertainty in saturated liquid thermal conductivity is 5%, 3% in the gas phase at atmospheric pressure.
?
?The Lennard-Jones parameters were taken from Kestin, J., Ro, S.T., and Wakeham, W.A., "Viscosity of the Binary Gaseous Mixtures He-Ne and Ne-N2 in the Temperature Range 25-700°C," J. Chem. Phys., 56(12):5837-5842, 1972. doi: 10.1063/1.1677125
?
!```````````````````````````````````````````````````````````````````````````````
24.5561 !Lower temperature limit [K]
725.0 !Upper temperature limit [K]
100000.0 !Upper pressure limit [kPa]
70.0 !Maximum density [mol/L]
FEQ NITROGEN.FLD
VS1 !Model for reference fluid viscosity
TC1 !Model for reference fluid thermal conductivity
BIG !Large molecule identifier
0.989544 0. 0. 0. !Large molecule parameters
1 !Lennard-Jones flag (0 or 1) (0 => use estimates)
0.2707 !Lennard-Jones coefficient sigma [nm] for ECS method
45.58 !Lennard-Jones coefficient epsilon/kappa [K] for ECS method
1 0 0 !Number of terms in f_int term in Eucken correlation, spare1, spare2
0.00132 0. 0. 0. !Coefficient, power of T, spare1, spare2 dummy; this term is zero
2 0 0 !Number of terms in psi (visc shape factor): poly,spare1,spare2
1.12101 0. 0. 0. !Coefficient, power of Tr, power of Dr, spare
-0.0388911 0. 1. 0. !Coefficient, power of Tr, power of Dr, spare
2 0 0 !Number of terms in chi (t.c. shape factor): poly,spare1,spare2
0.83 0. 0. 0. !Coefficient, power of Tr, power of Dr, spare
0.0 0. 1. 0. !Coefficient, power of Tr, power of Dr, spare
TK3 !Pointer to critical enhancement auxiliary function
#AUX !---Auxiliary function for the thermal conductivity critical enhancement
TK3 !Simplified thermal conductivity critical enhancement for neon of Perkins et al. (2013).
?
?```````````````````````````````````````````````````````````````````````````````
?Perkins, R.A., Sengers, J.V., Abdulagatov, I.M., and Huber, M.L.,
? "Simplified Model for the Critical Thermal-Conductivity Enhancement in Molecular Fluids,"
? Int. J. Thermophys., 34(2):191-212, 2013. doi: 10.1007/s10765-013-1409-z
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
9 0 0 0 !# terms: CO2-terms, spare, spare, spare
1.0 1.0 1.0 !Reducing parameters for T, rho, tcx [mW/(m-K)]
0.63 !Nu (universal exponent)
1.239 !Gamma (universal exponent)
1.02 !R0 (universal amplitude)
0.063 !Z (universal exponent--not used for t.c., only viscosity)
1.0 !C (constant in viscosity eqn = 1/[2 - (alpha + gamma)/(2*nu)], but often set to 1)
0.131e-9 !Xi0 (amplitude) [m]
0.060 !Gam0 (amplitude) [-]
0.331e-9 !Qd_inverse (modified effective cutoff parameter) [m]
66.74 !Tref (reference temperature)=1.5*Tc [K]
********************************************************************************
@ETA !---Viscosity---
VS7 !Pure fluid viscosity model for neon of Rabinovich et al. (1988).
?
?```````````````````````````````````````````````````````````````````````````````
?Rabinovich, V.A., Vasserman, A.A., Nedostup, V.I., and Veksler, L.S.,
? "Thermophysical Properties of Neon, Argon, Krypton, and Xenon,"
? Hemisphere Publishing Corp., 1988.
?
?The numbers calculated here do not exactly match those given by Rabinovich.
? The ECS model is currently the preferred model.
?
!```````````````````````````````````````````````````````````````````````````````
24.57 !Lower temperature limit [K]
700.0 !Upper temperature limit [K]
700000.0 !Upper pressure limit [kPa]
62.06 !Maximum density [mol/L]
NUL !Pointer to the viscosity critical enhancement auxiliary function (none used)
!
!Define variables
$VR RED SUM:5 SUM:6 TEMP CNST / LOG10 * - CUBE CNST * DENS * =DEL
!
!Residual function etat----->!
$RF RED SUM:1 LOG10 CNST * SUM:6 + INV CNST * CNST TEMP * SQRT * SUMDEL:6 *
!
!Coefficients
$CF
1.0 1. 82.907973636 0. 0 !Reducing parameters for eta, T, rho
1.03010 0. 0. 0. 0 ! c
-0.99175 0. 1. 0. 0
2.47127 0. 2. 0. 0
-3.11864 0. 3. 0. 0
1.57066 0. 4. 0. 0
0.48148 0. 0. 0. 0 ! b
-1.18732 0. 1. 0. 0
2.80277 0. 2. 0. 0
-5.41058 0. 3. 0. 0
7.04779 0. 4. 0. 0
-3.76608 0. 5. 0. 0
122.1 0. 0. 0. 0
0.035785660797684 0. 0. 0. 0
0.01 0.29944 1. 0. 0 !Reducing parameters for eta, T, rho
1. 1. 0. 0. 0
-2.78751 0. 0. 0. 0 ! a
17.67484 0. 0. 0. 0
311498.7 -2. 0. 0. 0
-48826500. -3. 0. 0. 0
3938774000. -4. 0. 0. 0
-1.654629e+11 -5. 0. 0. 0
2.86561e+12 -6. 0. 0. 0
390.69978483921 0. 0. 0. 0
20.179 0. 0. 0. 0
1.0 0. 0. 0. 0
0.27676 0. 1 0. 0 ! d
0.014355 0. 2 0. 0
2.6480 0. 3 0. 0
-1.9643 0. 4 0. 0
0.89161 0. 5 0. 0
NUL !Pointer to the viscosity critical enhancement auxiliary function (none used)
~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~
#STN !---Surface tension---
ST1 !Surface tension model for neon of Mulero et al. (2012).
:DOI: 10.1063/1.4768782
?
?```````````````````````````````````````````````````````````````````````````````
?Mulero, A., Cachadiña, I., and Parra, M.I.,
? "Recommended Correlations for the Surface Tension of Common Fluids,"
? J. Phys. Chem. Ref. Data, 41(4), 043105, 2012. doi: 10.1063/1.4768782
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
3 !Number of terms in surface tension model
44.4918 !Critical temperature used in fit (dummy)
0.012254 1.4136 !Sigma0 and n
0.02728 1.4517
-0.025715 1.6567
#DE !---Dielectric constant---
DE3 !Dielectric constant model for neon of Harvey and Lemmon (2005).
:DOI: 10.1007/s10765-005-2351-5
?
?```````````````````````````````````````````````````````````````````````````````
?Harvey, A.H. and Lemmon, E.W.,
? "Method for Estimating the Dielectric Constant of Natural Gas Mixtures,"
? Int. J. Thermophys., 26(1):31-46, 2005. doi: 10.1007/s10765-005-2351-5
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
273.16 1000.0 1.0 !Reducing parameters for T and D
0 1 4 0 0 0 !Number of terms in dielectric constant model
0.9969 0. 1. 0. !Coefficient, T exp, D exp
-0.109 0. 2. 0.
0.0708 1. 2. 0.
-2.880 0. 3. 0.
-1.0 1. 3. 0.
#MLT !---Melting line---
ML1 !Melting line model for neon of Lemmon (2010).
:DOI:
?
?```````````````````````````````````````````````````````````````````````````````
?Lemmon, E.W., preliminary equation, 2010.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
24.556 43.36814 !Reducing temperature and pressure
1 1 0 0 0 0 !Number of terms in melting line equation
1.0 0.0 !Coefficients and exponents
4437.0 1.33
#SBL !---Sublimation line---
SB2 !Sublimation line model for neon of Brown and Zeigler (2009).
:DOI: 10.1007/978-1-4613-9856-1_76
?
?```````````````````````````````````````````````````````````````````````````````
?Based on G.N. Brown and W.T. Ziegler, Adv. Cryo. Eng., 25:662-670, 1979.
? Modified to match the triple point of the equation of state.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1.0 1000.0 !Reducing temperature and pressure
5 0 0 0 0 0 !Number of terms in sublimation line equation
8.3071 0.0 !Coefficients and exponents
-3.08555e2 -1.0
9.8602e2 -2.0
-9.0693e3 -3.0
3.5142e4 -4.0
#PS !---Vapor pressure---
PS5 !Vapor pressure equation for neon of Thol et al. (2018)
?
?```````````````````````````````````````````````````````````````````````````````
?Thol, M., Beckmüller, R., Weiss, R., Harvey, A.H., Lemmon, E.W., Jacobsen, R.T, and Span, R., 2018.
?
?Functional Form: P=Pc*EXP[SUM(Ni*Theta^ti)*Tc/T] where Theta=1-T/Tc, Tc and Pc
? are the reducing parameters below, which are followed by rows containing Ni and ti.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
44.4 2661.63 !Reducing parameters
5 0 0 0 0 0 !Number of terms in equation
-5.778 1.0
1.113 1.5
-1.2573 4.76
0.792 14.6
-1.338 17.0
#DL !---Saturated liquid density---
DL1 !Saturated liquid density equation for neon of Thol et al. (2018)
?
?```````````````````````````````````````````````````````````````````````````````
?Thol, M., Beckmüller, R., Weiss, R., Harvey, A.H., Lemmon, E.W., Jacobsen, R.T, and Span, R., 2018.
?
?Functional Form: D=Dc*[1+SUM(Ni*Theta^ti)] where Theta=1-T/Tc, Tc and Dc are
? the reducing parameters below, which are followed by rows containing Ni and ti.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
44.4 24.1 !Reducing parameters
6 0 0 0 0 0 !Number of terms in equation
5.96854 0.53
-17.1 0.9
41.99 1.3
-58.941 1.72
43.481 2.19
-13.246 2.72
#DV !---Saturated vapor density---
DV3 !Saturated vapor density equation for neon of Thol et al. (2018)
?
?```````````````````````````````````````````````````````````````````````````````
?Thol, M., Beckmüller, R., Weiss, R., Harvey, A.H., Lemmon, E.W., Jacobsen, R.T, and Span, R., 2018.
?
?Functional Form: D=Dc*EXP[SUM(Ni*Theta^ti)] where Theta=1-T/Tc, Tc and Dc are
? the reducing parameters below, which are followed by rows containing Ni and ti.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
44.4 24.1 !reducing parameters
6 0 0 0 0 0 !Number of terms in equation
-6.0978 0.536 !coefficients and exponents
14.88 0.94
-43.06 1.367
54.34 1.835
-38.337 2.37
-36.59 7.17
@END
c 1 2 3 4 5 6 7 8
c2345678901234567890123456789012345678901234567890123456789012345678901234567890
@ETA !Viscosity model specification
VS0 pure fluid viscosity model of Rabinovich et al. (1988).
?
?```````````````````````````````````````````````````````````````````````````````
?Rabinovich, V.A., Vasserman, A.A., Nedostup, V.I., and Veksler, L.S.,
? "Thermophysical Properties of Neon, Argon, Krypton, and Xenon,"
? Hemisphere Publishing Corp., 1988.
?
?The numbers calculated here do not exactly match those given by Rabinovich.
? The ECS model is currently the preferred model.
?
!```````````````````````````````````````````````````````````````````````````````
24.57 !Lower temperature limit [K]
700.0 !Upper temperature limit [K]
700000.0 !Upper pressure limit [kPa]
62.06 !Maximum density [mol/L]
NEO !Pointer to hardcoded thermal conductivity model
0 0 0 0 0 0 0 0 !Number of terms for various pieces
NUL !Pointer to the viscosity critical enhancement auxiliary function (none used)