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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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R404A !Short name
404A-404A !CAS number
44% R125/4% R134a/52% R143a !Full name
R404A !Chemical formula
R404A !Synonym
97.6038 !Molar mass [g/mol]
200.0 !Triple point temperature [K]
226.93 !Normal boiling point [K]
345.270 !Critical temperature [K]
3734.8 !Critical pressure [kPa]
4.94 !Critical density [mol/L]
0.293 !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:
404a404a !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-404A 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. doi: 10.1023/A:1025048800563
?
?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]
14.21 !Maximum density [mol/L]
CPP !Pointer to Cp0 model
97.6038 !Molar mass [g/mol]
200.0 !Triple point temperature [K]
22.65 !Pressure at triple point [kPa]
14.21 !Density at triple point [mol/L]
226.93 !Normal boiling point temperature [K]
0.293 !Acentric factor
345.27 3734.8 4.94 !Tc [K], pc [kPa], rhoc [mol/L]
345.27 4.94 !Reducing parameters [K, mol/L]
8.314472 !Gas constant [J/mol-K]
22 4 0 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Gaussian terms, and Gao terms
6.10984 0.67 1. 0. !a(i),t(i),d(i),l(i)
-7.79453 0.91 1. 0.
0.0183377 5.96 1. 0.
0.26227 0.7 2. 0.
-0.00351688 6.0 2. 0.
0.0116181 0.3 4. 0.
0.00105992 0.7 6. 0.
0.850922 1.7 1. 1.
-0.520084 3.3 1. 1.
-0.0464225 7.0 1. 1.
0.62119 2.05 2. 1.
-0.195505 4.3 2. 1.
0.336159 2.7 3. 1.
-0.0376062 1.8 4. 1.
-0.00636579 1.25 7. 1.
-0.0758262 12.0 2. 2.
-0.0221041 6.0 3. 2.
0.0310441 8.7 4. 2.
0.0132798 11.6 4. 2.
0.0689437 13.0 2. 3.
-0.0507525 17.0 3. 3.
0.0161382 16.0 5. 3.
#AUX !---Auxiliary function for Cp0
CPP !Ideal gas heat capacity function for R404A 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
1.2744 0.3
0.63078 413.0
3.5979 804.0
5.0335 1727.0
#AUX !---Auxiliary function for PH0
PH0 !Ideal gas Helmholtz form for R404A.
?
?```````````````````````````````````````````````````````````````````````````````
?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
7.00407 0.0 !aj, ti for [ai*tau**ti] terms
7.98695 1.0
-18.8664 -0.3
0.63078 -1.19617 !aj, ti for [ai*log(1-exp(ti*tau)] terms
3.5979 -2.32861
5.0335 -5.00188
~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~
#STN !---Surface tension---
ST1 !Surface tension model for R404A of Lemmon (2003).
?
?```````````````````````````````````````````````````````````````````````````````
?Lemmon, E.W., preliminary equation, 2003.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
2 !Number of terms in surface tension model
345.27 !Critical temperature used in fit (dummy)
0.06868 1.3142 !Sigma0 and n
-0.04576 2.3084
#PS !---Vapor pressure---
PS5 !Vapor pressure equation for R404A 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. !
345.270 3734.8 !Reducing parameters
4 0 0 0 0 0 !Number of terms in equation
-0.00026863 0.1
-6.5757 0.972
-4.1802 3.8
-7.9102 9.0
#PL !---Liquid pressure---
PL5 !Liquid pressure equation for R404A 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. !
345.270 3734.8 !Reducing parameters
4 0 0 0 0 0 !Number of terms in equation
0.061067 0.54
-6.5646 0.965
-3.6162 3.7
-3.9771 9.0
@END
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