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

190
CapMachine.Wpf/PPCalculation/REFPROP/FLUIDS/R410A.PPF Normal file
View File

@@ -0,0 +1,190 @@
R410A !Short name
410A-410A !CAS number
50% R32/50% R125 !Full name
R410A !Chemical formula
R410A !Synonym
72.5854 !Molar mass [g/mol]
200.0 !Triple point temperature [K]
221.71 !Normal boiling point [K]
344.494 !Critical temperature [K]
4901.2 !Critical pressure [kPa]
6.324 !Critical density [mol/L]
0.296 !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:
410a410a !Hash number from InChI Key :Hash:
! compiled by E.W. Lemmon, NIST Physical and Chemical Properties Division, Boulder, Colorado
! 05-06-02 EWL, original version
! 12-16-02 EWL, add final equation
________________________________________________________________________________
#EOS !---Equation of state---
FEQ !Helmholtz equation of state for R-410A 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]
19.51 !Maximum density [mol/L]
CPP !Pointer to Cp0 model
72.5854 !Molar mass [g/mol]
200.0 !Triple point temperature [K]
29.16 !Pressure at triple point [kPa]
19.51 !Density at triple point [mol/L]
221.71 !Normal boiling point temperature [K]
0.296 !Acentric factor
344.494 4901.2 6.324 !Tc [K], pc [kPa], rhoc [mol/L]
344.494 6.324 !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
0.987252 0.44 1. 0. !a(i),t(i),d(i),l(i)
-1.03017 1.2 1. 0.
1.17666 2.97 1. 0.
-0.138991 2.95 2. 0.
0.00302373 0.2 5. 0.
-2.53639 1.93 1. 1.
-1.9668 1.78 2. 1.
-0.830480 3.0 3. 1.
0.172477 0.2 5. 1.
-0.261116 0.74 5. 1.
-0.0745473 3.0 5. 1.
0.679757 2.1 1. 2.
-0.652431 4.3 1. 2.
0.0553849 0.25 4. 2.
-0.0710970 7.0 4. 2.
-0.000875332 4.7 9. 2.
0.0200760 13.0 2. 3.
-0.0139761 16.0 2. 3.
-0.0185110 25.0 4. 3.
0.0171939 17.0 5. 3.
-0.00482049 7.4 6. 3.
#AUX !---Auxiliary function for Cp0
CPP !Ideal gas heat capacity function for R410A 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
2.8749 0.1
2.0623 697.0
5.9751 1723.0
1.5612 3875.0
#AUX !---Auxiliary function for PH0
PH0 !Ideal gas Helmholtz form for R410A.
?
?```````````````````````````````````````````````````````````````````````````````
?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
36.8871 0.0 !aj, ti for [ai*tau**ti] terms
7.15807 1.0
-46.87575 -0.1
2.0623 -2.02326 !aj, ti for [ai*log(1-exp(ti*tau)] terms
5.9751 -5.00154
1.5612 -11.2484
~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~
#STN !---Surface tension---
ST1 !Surface tension model for R410A of Lemmon (2003).
?
?```````````````````````````````````````````````````````````````````````````````
?Lemmon, E.W., preliminary equation, 2003.
?
!```````````````````````````````````````````````````````````````````````````````
0. !
10000. !
0. !
0. !
1 !Number of terms in surface tension model
344.494 !Critical temperature used in fit (dummy)
0.06443 1.245 !Sigma0 and n
#PS !---Vapor pressure---
PS5 !Vapor pressure equation for R410A 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. !
344.494 4901.2 !Reducing parameters
4 0 0 0 0 0 !Number of terms in equation
-7.4411 1.0
1.9883 1.6
-2.4925 2.4
-3.2633 5.0
#PL !---Liquid pressure---
PL5 !Liquid pressure equation for R410A 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. !
344.494 4901.2 !Reducing parameters
4 0 0 0 0 0 !Number of terms in equation
-7.2818 1.0
2.5093 1.8
-3.2695 2.4
-2.8022 4.9
@END
c 1 2 3 4 5 6 7 8
c2345678901234567890123456789012345678901234567890123456789012345678901234567890