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一些优化：CAN和PLC地址的优化

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2025-01-01 13:11:13 +08:00
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R507A !Short name
507A-507A !CAS number
50% R125/50% R143a !Full name
R507A !Chemical formula
R507A !Synonym
98.8592 !Molar mass [g/mol]
200.0 !Triple point temperature [K]
226.41 !Normal boiling point [K]
343.765 !Critical temperature [K]
3704.9 !Critical pressure [kPa]
4.964 !Critical density [mol/L]
0.286 !Acentric factor
-1. !Dipole moment [Debye]
IIR !Default reference state
10.0 !Version number
???? !UN Number :UN:
halocb !Family :Family:
???? !Heating value (upper) at 25 C [kJ/mol] (ISO 6976:2016) :Heat:
???? !IUPAC Int. Chemical Identifier :InChi:
???? !InChi Key :InChiKey:
???? !Alternative fluid for mixing rules :AltID:
507a507a !Hash number from InChI Key :Hash:
! compiled by E.W. Lemmon, NIST Physical and Chemical Properties Division, Boulder, Colorado
! 11-14-02 EWL, original version
________________________________________________________________________________
#EOS !---Equation of state---
FEQ !Helmholtz equation of state for R-507A of Lemmon (2003).
:DOI: 10.1023/A:1025048800563
?
?```````````````````````````````````````````````````````````````````````````````
?Lemmon, E.W.,
? "Pseudo Pure-Fluid Equations of State for the Refrigerant Blends R-410A,
? R-404A, R-507A, and R-407C,"
? Int. J. Thermophys., 24(4):991-1006, 2003.
?
?The estimated uncertainty of density values calculated with the
? equation of state is 0.1%. The estimated uncertainty of calculated
? heat capacities and speed of sound values is 0.5%. Uncertainties of
? bubble and dew point pressures are 0.5%.
?
!```````````````````````````````````````````````````````````````````````````````
200.0 !Lower temperature limit [K]
500.0 !Upper temperature limit [K]
50000.0 !Upper pressure limit [kPa]
14.13 !Maximum density [mol/L]
CPP !Pointer to Cp0 model
98.8592 !Molar mass [g/mol]
200.0 !Triple point temperature [K]
23.23 !Pressure at triple point [kPa]
14.13 !Density at triple point [mol/L]
226.41 !Normal boiling point temperature [K]
0.286 !Acentric factor
343.765 3704.9 4.964 !Tc [K], pc [kPa], rhoc [mol/L]
343.765 4.964 !Reducing parameters [K, mol/L]
8.314472 !Gas constant [J/mol-K]
21 4 0 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Gaussian terms, and Gao terms
6.24982 0.692 1. 0. !a(i),t(i),d(i),l(i)
-8.07855 0.943 1. 0.
0.0264843 5.8 1. 0.
0.286215 0.77 2. 0.
-0.00507076 5.84 2. 0.
0.0109552 0.24 4. 0.
0.00116124 0.69 6. 0.
1.38469 2.0 1. 1.
-0.922473 3.0 1. 1.
-0.0503562 7.0 1. 1.
0.822098 2.2 2. 1.
-0.277727 4.3 2. 1.
0.358172 2.7 3. 1.
-0.0126426 1.2 4. 1.
-0.0060701 1.23 7. 1.
-0.0815653 12.0 2. 2.
-0.0233323 6.0 3. 2.
0.0352952 8.5 4. 2.
0.0159566 11.5 4. 2.
0.0755927 13.0 2. 3.
-0.0542007 17.0 3. 3.
0.0170451 16.2 5. 3.
#AUX !---Auxiliary function for Cp0
CPP !Ideal gas heat capacity function for R507A of Lemmon (2003).
?
?```````````````````````````````````````````````````````````````````````````````
?Lemmon, E.W.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1.0 8.314472 !Reducing parameters for T, Cp0
1 3 0 0 0 0 0 !Nterms: polynomial, exponential, cosh, sinh
1.568 0.25
0.95006 364.0
4.1887 815.0
5.5184 1768.0
#AUX !---Auxiliary function for PH0
PH0 !Ideal gas Helmholtz form for R507A.
?
?```````````````````````````````````````````````````````````````````````````````
?Lemmon, E.W.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1 3 3 0 0 0 0 0 !Nterms: ai*log(tau**ti); ai*tau**ti; ai*log(1-exp(bi*tau))
-1.0 1.0 !ai, ti for [ai*log(tau**ti)] terms
9.93541 0.0 !aj, ti for [ai*tau**ti] terms
7.9985 1.0
-21.6054 -0.25
0.95006 -1.05886 !aj, ti for [ai*log(1-exp(ti*tau)] terms
4.1887 -2.37081
5.5184 -5.14305
~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~
#STN !---Surface tension---
ST1 !Surface tension model for R507A of Lemmon (2003).
?
?```````````````````````````````````````````````````````````````````````````````
?Lemmon, E.W., preliminary equation, 2003.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
2 !Number of terms in surface tension model
343.765 !Critical temperature used in fit (dummy)
0.06701 1.3066 !Sigma0 and n
-0.04297 2.3145
#PS !---Vapor pressure---
PS5 !Vapor pressure equation for R507A of Lemmon (2003)
?
?```````````````````````````````````````````````````````````````````````````````
?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. !
343.765 3704.9 !Reducing parameters
4 0 0 0 0 0 !Number of terms in equation
-7.5459 1.0
2.338 1.5
-2.237 2.1
-4.1535 4.7
#PL !---Liquid pressure---
PL5 !Liquid pressure equation for R507A of Lemmon (2003)
?
?```````````````````````````````````````````````````````````````````````````````
?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. !
343.765 3704.9 !Reducing parameters
4 0 0 0 0 0 !Number of terms in equation
-7.4853 1.0
2.0115 1.5
-2.0141 2.2
-3.7763 4.6
@END
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