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

505
CapMachine.Wpf/PPCalculation/REFPROP/FLUIDS/CYCLOPEN.FLD Normal file
View File

@@ -0,0 +1,505 @@
Cyclopentane !Short name
287-92-3 !CAS number
Cyclopentane !Full name
C5H10 !Chemical formula {C5H10}
C5H10 !Synonym
70.1329 !Molar mass [g/mol]
179.7 !Triple point temperature [K]
322.40 !Normal boiling point [K]
511.72 !Critical temperature [K]
4582.8 !Critical pressure [kPa]
3.92 !Critical density [mol/L]
0.202 !Acentric factor
0.0 !Dipole moment [Debye]; van Arkel, A.E., P. Meerburg, and C.R. van der Handel, Rec. Trav. Chim., 61, 767-770 (1942).
NBP !Default reference state
10.0 !Version number
1146 !UN Number :UN:
naphthene !Family :Family:
3319.59 !Heating value (upper) [kJ/mol] :Heat:
1S/C5H10/c1-2-4-5-3-1/h1-5H2 !Standard InChI String :InChi:
RGSFGYAAUTVSQA-UHFFFAOYSA-N !Standard InChI Key :InChiKey:
76bc0290 (pentane) !Alternative fluid for mixing rules :AltID:
43ab1810 !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
! 09-02-08 EWL, Original version.
! 07-01-10 MLH, Add preliminary transport.
! 08-23-10 IDC, Add ancillary equations.
! 02-22-10 EWL, Add new equation of state.
! 04-17-14 EWL, Add surface tension coefficients of Mulero et al. (2014).
! 04-30-14 EWL, Add final equation of state.
! 06-30-14 MLH, Update critical parameters in TK3 block.
! 04-15-15 MLH, Add new Vassiliou et al. (2015) thermal conductivity formulation.
! 11-21-17 MLH, Revise ECS transport.
________________________________________________________________________________
#EOS !---Equation of state---
FEQ !Helmholtz equation of state for cyclopentane of Gedanitz et al. (2015).
:TRUECRITICALPOINT: 511.72 3.92 !True EOS critical point [K, mol/L] (where dP/dD=0 and d^2P/dD^2=0 at constant T)
:DOI: 10.1021/je5010164
?
?```````````````````````````````````````````````````````````````````````````````
?Gedanitz, H., Dávila, M.J., and Lemmon, E.W.,
? "Speed of Sound Measurements and a Fundamental Equation of State for Cyclopentane,"
? J. Chem. Eng. Data, 60(5):1311-1337, 2015.
?
?The uncertainty in density of the equation of state ranges from 0.2% at low
? temperatures in the liquid to 0.5% at the highest temperatures and in the vapor.
? Between 280 and 315 K, the uncertainty in saturated liquid density decreases to
? 0.05%. The uncertainty in the speed of sound is 0.1% and in heat capacities is
? 1%. The uncertainty in vapor pressure is 0.1% at temperatures between 280 and
? 325 K. This uncertainty increases to possibly 0.5% at other temperatures due to
? a lack of reliable experimental data. In the critical region, the uncertainties
? are higher for all properties.
?
!```````````````````````````````````````````````````````````````````````````````
179.7 !Lower temperature limit [K]
550. !Upper temperature limit [K]
250000. !Upper pressure limit [kPa]
12.11 !Maximum density [mol/L]
CPP !Pointer to Cp0 model
70.1329 !Molar mass [g/mol]
179.7 !Triple point temperature [K]
0.0089 !Pressure at triple point [kPa]
12.1 !Density at triple point [mol/L]
322.40 !Normal boiling point temperature [K]
0.202 !Acentric factor
511.72 4582.8 3.92 !Tc [K], pc [kPa], rhoc [mol/L]
511.72 3.92 !Reducing parameters [K, mol/L]
8.3144598 !Gas constant [J/mol-K]
10 4 5 12 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Gaussian terms, and Gao terms
0.0630928 1.0 4. 0. !a(i),t(i),d(i),l(i)
1.50365 0.29 1. 0.
-2.37099 0.85 1. 0.
-0.484886 1.185 2. 0.
0.191843 0.45 3. 0.
-0.835582 2.28 1. 2.
-0.435929 1.8 3. 2.
0.545607 1.5 2. 1.
-0.209741 2.9 2. 2.
-0.0387635 0.93 7. 1.
0.677674 1.05 1. 2. 2. -0.86 -0.63 1.22 0.684 0. 0. 0.
-0.137043 4.0 1. 2. 2. -0.85 -2.8 0.32 0.7 0. 0. 0.
-0.0852862 2.33 3. 2. 2. -0.86 -0.5 0.22 0.77 0. 0. 0.
-0.128085 1.5 3. 2. 2. -1.53 -0.95 1.94 0.625 0. 0. 0.
-0.00389381 1.0 2. 2. 2. -5.13 -0.23 1.21 0.42 0. 0. 0.
eta beta gamma epsilon
EXP[eta*(delta-epsilon)^2+beta*(tau-gamma)^2]
#AUX !---Auxiliary function for Cp0
CPP !Ideal gas heat capacity function for cyclopentane of Gedanitz et al. (2015).
?
?```````````````````````````````````````````````````````````````````````````````
?Gedanitz, H., Dávila, M.J., and Lemmon, E.W., 2015.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1.0 8.3144598 !Reducing parameters for T, Cp0
1 4 0 0 0 0 0 !Nterms: polynomial, exponential, cosh, sinh
4.0 0.0
1.34 230.0
13.4 1180.0
17.4 2200.0
6.65 5200.0
#AUX !---Auxiliary function for PX0
PX0 !Helmholtz energy ideal-gas function for cyclopentane of Gedanitz et al. (2015).
?
?```````````````````````````````````````````````````````````````````````````````
?Gedanitz, H., Dávila, M.J., and Lemmon, E.W., 2015.
?
!```````````````````````````````````````````````````````````````````````````````
1 2 4 0 0 0 0 0 !Nterms: ai*log(tau**ti); ai*tau**ti; ai*log(1-exp(bi*tau))
3.0 1.0 !ai, ti for [ai*log(tau**ti)] terms
-0.3946228999462562 0.0 !aj, ti for [ai*tau**ti] terms
2.4918907456695547 1.0 !aj, ti for [ai*tau**ti] terms
1.34 230.0 !aj, ti for [ai*log(1-exp(-ti/T)] terms
13.4 1180.0
17.4 2200.0
6.65 5200.0
#AUX !---Auxiliary function for PH0
PH0 !Ideal gas Helmholtz form for cyclopentane of Gedanitz et al. (2015).
?
?```````````````````````````````````````````````````````````````````````````````
?Gedanitz, H., Dávila, M.J., and Lemmon, E.W., 2015.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1 2 4 0 0 0 0 0 !Nterms: ai*log(tau**ti); ai*tau**ti; ai*log(1-exp(bi*tau)); cosh; sinh
3.0 1.0 !ai, ti for [ai*log(tau**ti)] terms
-0.3946233253 0.0 !aj, ti for [ai*tau**ti] terms
2.4918910143 1.0
1.34 -0.4494645509 !aj, ti for [ai*log(1-exp(ti*tau)] terms
13.4 -2.3059485656
17.4 -4.2992261393
6.65 -10.1618072383
--------------------------------------------------------------------------------
@EOS !---Equation of state---
FE1 !Helmholtz equation of state for cyclopentane of Gedanitz et al. (2010).
?
?```````````````````````````````````````````````````````````````````````````````
?Gedanitz, H., Davila, M.J., Lemmon, E.W.
? "Speed of Sound Measurements and a Fundamental Equation of State for Cyclopentane,"
? unpublished equation, 2010.
?
!```````````````````````````````````````````````````````````````````````````````
179.7 !Lower temperature limit [K]
550. !Upper temperature limit [K]
250000. !Upper pressure limit [kPa]
12.11 !Maximum density [mol/L]
CP1 !Pointer to Cp0 model
70.1329 !Molar mass [g/mol]
179.7 !Triple point temperature [K]
0.008854 !Pressure at triple point [kPa]
12.1 !Density at triple point [mol/L]
322.405 !Normal boiling point temperature [K]
0.201 !Acentric factor
511.72 4571.2 3.82 !Tc [K], pc [kPa], rhoc [mol/L]
511.72 3.82 !Reducing parameters [K, mol/L]
8.314472 !Gas constant [J/mol-K]
10 4 4 12 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Gaussian terms, and Gao terms
0.0536938 1.0 4. 0. !a(i),t(i),d(i),l(i)
1.60394 0.29 1. 0.
-2.41244 0.8 1. 0.
-0.474009 1.14 2. 0.
0.203482 0.5 3. 0.
-0.965616 2.0 1. 2.
-0.344543 1.5 3. 2.
0.353975 1.0 2. 1.
-0.231373 3.36 2. 2.
-0.0379099 0.95 7. 1.
0.867586 1.0 1. 2. 2. -0.82 -1.15 1.08 0.68 0. 0. 0.
-0.381827 2.5 1. 2. 2. -1.19 -1.61 0.36 0.97 0. 0. 0.
-0.108741 2.5 3. 2. 2. -0.79 -0.66 0.09 0.84 0. 0. 0.
-0.0976984 1.5 3. 2. 2. -1.52 -2.72 1.48 0.66 0. 0. 0.
@AUX !---Auxiliary function for Cp0
CP1 !Ideal gas heat capacity function for cyclopentane of Gedanitz et al. (2010).
?
?```````````````````````````````````````````````````````````````````````````````
?Gedanitz, H., Davila, M.J., Lemmon, E.W.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1.0 8.314472 !Reducing parameters for T, Cp0
1 4 0 0 0 0 0 !Nterms: polynomial, exponential, cosh, sinh
1.96 0.0
3.34 120.0
18.6 1300.0
13.9 2700.0
4.86 5300.0
@EOS !---Equation of state---
FE2 !Helmholtz equation of state for cyclopentane.
?
?```````````````````````````````````````````````````````````````````````````````
?Lemmon, E.W., unpublished equation, 2008.
?
!```````````````````````````````````````````````````````````````````````````````
179.7 !Lower temperature limit [K]
600. !Upper temperature limit [K]
200000. !Upper pressure limit [kPa]
12.2 !Maximum density [mol/L]
CP2 !Pointer to Cp0 model
70.1329 !Molar mass [g/mol]
179.722 !Triple point temperature [K]
0.0089 !Pressure at triple point [kPa]
12.1 !Density at triple point [mol/L]
322.40 !Normal boiling point temperature [K]
0.195 !Acentric factor
511.69 4515.0 3.82 !Tc [K], pc [kPa], rhoc [mol/L]
511.69 3.82 !Reducing parameters [K, mol/L]
8.314472 !Gas constant [J/mol-K]
10 4 4 12 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Gaussian terms, and Gao terms
0.04909331 1.0 4. 0. !a(i),t(i),d(i),l(i)
1.244679 0.23 1. 0.
-1.990222 0.94 1. 0.
-0.5245596 1.08 2. 0.
0.1764215 0.53 3. 0.
-1.066798 1.67 1. 2.
-0.5028152 1.80 3. 2.
0.8484762 1.30 2. 1.
-0.4547443 2.50 2. 2.
-0.02767817 1.0 7. 1.
0.9455318 0.87 1. 2. 2. -1.023 -1.70 1.10 0.713 0. 0. 0.
-0.3014822 1.40 1. 2. 2. -1.383 -1.55 0.64 0.917 0. 0. 0.
-0.1675668 2.40 3. 2. 2. -0.996 -1.07 0.50 0.688 0. 0. 0.
-0.6377070 1.30 3. 2. 2. -7.038 -87.17 1.26 0.748 0. 0. 0.
@AUX !---Auxiliary function for Cp0
CP2 !Ideal gas heat capacity function for cyclopentane.
?
?```````````````````````````````````````````````````````````````````````````````
?Lemmon, E.W., unpublished equation, 2008.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1.0 8.314472 !Reducing parameters for T, Cp0
1 4 0 0 0 0 0 !Nterms: polynomial, exponential, cosh, sinh
3.263 0.0
2.151 179.0
19.55 1336.0
14.45 2911.0
3.594 6420.0
================================================================================
#TCX !---Thermal conductivity---
TC1 !Pure fluid thermal conductivity model for cyclopentane of Vassiliou 2015.
:DOI: 10.1063/1.4927095
?
?```````````````````````````````````````````````````````````````````````````````
?Vassiliou, C.-M., Assael, M.J., Huber, M.L., and Perkins, R.A.,
? "Reference Correlatons of the Thermal Conductivity
? of Cyclopentane, iso-Pentane, and n-Pentane,"
? J. Phys. Chem. Ref. Data, 44(3), 033102, 2015.
?
?Estimated uncertainty in thermal conductivity is 4% for the liquid over
? 218 K<T<240 K at pressures up to 250 MPa, 3% for the gas, and estimated to be
? 10% in the supercritical region, except near critical where the uncertainties
? are larger.
?
!```````````````````````````````````````````````````````````````````````````````
179.7 !Lower temperature limit [K]
550. !Upper temperature limit [K]
250000. !Upper pressure limit [kPa]
12.11 !Maximum density [mol/L]
4 4 !# terms for dilute gas function: numerator, denominator
511.72 0.001 !Reducing parameters for T, tcx
-8.2523346 0. !Coefficient, power in T
76.336543 1.
-217.6154 2.
312.29877 3.
1.0 0.
0.28341479 1.
2.7890541 2.
0.32645005 3.
10 0 !# terms for background gas function: numerator, denominator
511.72 3.92 1. !Reducing parameters for T, rho, tcx
0.0920536 0. 1. 0.
-0.172699 0. 2. 0.
0.126557 0. 3. 0.
-0.0362296 0. 4. 0.
0.00388718 0. 5. 0.
-0.0435129 1. 1. 0.
0.112636 1. 2. 0.
-0.0908663 1. 3. 0.
0.028095 1. 4. 0.
-0.00280368 1. 5. 0.
TK3 !Pointer to critical enhancement auxiliary function
#AUX !---Auxiliary function for the thermal conductivity critical enhancement
TK3 !Simplified thermal conductivity critical enhancement for cyclopentane 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: 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)
0.216e-9 !Xi0 (amplitude) [m]
0.058 !Gam0 (amplitude) [-]
0.624e-9 !Qd_inverse (modified effective cutoff parameter) [m]
767.58 !Tref (reference temperature) [K]
++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
@TRN !---ECS Transport---
ECS !Extended Corresponding States model (Propane reference) for cyclopentane.
:DOI: 10.6028/NIST.IR.8209
?
?```````````````````````````````````````````````````````````````````````````````
?*** ESTIMATION METHOD *** NOT STANDARD REFERENCE QUALITY ***
?Huber, M.L., (2018) "Models for the Viscosity, Thermal Conductivity, and
? Surface Tension of Selected Pure Fluids as Implemented in REFPROP v10.0",
? NISTIR 8209; doi: 10.6028/NIST.IR.8209
?
?THERMAL CONDUCTIVITY
? Comparisons with liquid data of Assael, M. J., Dalaouti, N. K. "Thermal Conductivity of Toluene+Cyclopentane Mixtures: Measurements and Prediction" Int. J. Thermophys., 2001, 22(3), 659-678
? indicate an estimated uncertainty of 2 % along the saturation boundary and at pressures to 15 MPa
?
?VISCOSITY
? Comparisons with the liquid data of Assael, M. J., Dalaouti, N. K. "Measurement of the viscosity of cyclopentane from 210 to 310 K and pressures up to 25 MPa" High Temp. - High Pressures, 2000, 32, 179-184
? indicate an estimated uncertainty of 2-3 % along the saturation boundary and at pressures to 25 MPa
?
?The Lennard-Jones parameters were estimated with the method of Chung.
?
!```````````````````````````````````````````````````````````````````````````````
179.7 !Lower temperature limit [K]
600.0 !Upper temperature limit [K]
200000.0 !Upper pressure limit [kPa]
12.2 !Maximum density [mol/L]
FEQ PROPANE.FLD
VS1 !Model for reference fluid viscosity
TC1 !Model for reference fluid thermal conductivity
BIG !Large molecule identifier
0.99 0. 0. 0. !Large molecule parameters
1 !Lennard-Jones flag (0 or 1) (0 => use estimates)
0.518 !Lennard-Jones coefficient sigma [nm]
406.33 !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
2 0 0 !Number of terms in psi (visc shape factor): poly,spare1,spare2
1.04775 0. 0. 0. !Coefficient, power of Tr, power of Dr, spare
-8.02057e-4 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
1.01979 0. 0. 0. !Coefficient, power of Tr, power of Dr, spare
0.00432795 0. 1. 0. !Coefficient, power of Tr, power of Dr, spare
TK3 !Pointer to critical enhancement auxiliary function
~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~
#STN !---Surface tension---
ST1 !Surface tension model for cyclopentane of Mulero et al. (2014).
:DOI: 10.1063/1.4878755
?
?```````````````````````````````````````````````````````````````````````````````
?Mulero, A. and Cachadiña, I.,
? "Recommended Correlations for the Surface Tension of Several Fluids
? Included in the REFPROP Program,"
? J. Phys. Chem. Ref. Data, 43, 023104, 2014.
? doi: 10.1063/1.4878755
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1 !Number of terms in surface tension model
511.72 !Critical temperature used in fit (dummy)
0.07348 1.388 !Sigma0 and n
#PS !---Vapor pressure---
PS5 !Vapor pressure equation for cyclopentane of Gedanitz et al. (2015).
?
?```````````````````````````````````````````````````````````````````````````````
?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. !
511.72 4582.8 !Reducing parameters
5 0 0 0 0 0 !Number of terms in equation
-7.42670 1.0
3.31721 1.5
-2.67345 2.0
-2.72910 4.4
-3.17337 20.0
#DL !---Saturated liquid density---
DL1 !Saturated liquid density equation for cyclopentane of Gedanitz et al. (2015).
?
?```````````````````````````````````````````````````````````````````````````````
?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. !
511.72 3.92 !Reducing parameters
5 0 0 0 0 0 !Number of terms in equation
6.98737 0.55
-16.8780 0.94
26.8581 1.35
-20.6403 1.8
6.40338 2.35
#DV !---Saturated vapor density---
DV3 !Saturated vapor density equation for cyclopentane of Gedanitz et al. (2015).
?
?```````````````````````````````````````````````````````````````````````````````
?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. !
511.72 3.92 !Reducing parameters
5 0 0 0 0 0 !Number of terms in equation
-4.36877 0.491
-10.9430 1.9
-34.8856 4.9
-63.2191 10.0
-155.468 20.0
@END
c 1 2 3 4 5 6 7 8
c2345678901234567890123456789012345678901234567890123456789012345678901234567890