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https://github.com/CoolProp/CoolProp.git
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787 lines
17 KiB
JSON
787 lines
17 KiB
JSON
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"INCHI_STRING": "InChI=1S/CO2/c2-1-3",
|
|
"NAME": "CarbonDioxide",
|
|
"REFPROP_NAME": "CO2",
|
|
"SMILES": "C(=O)=O"
|
|
},
|
|
"STATES": {
|
|
"critical": {
|
|
"T": 304.1282,
|
|
"T_units": "K",
|
|
"hmolar": 14622.609393908302,
|
|
"hmolar_units": "J/mol",
|
|
"p": 7377300.0,
|
|
"p_units": "Pa",
|
|
"rhomolar": 10624.9063,
|
|
"rhomolar_units": "mol/m^3",
|
|
"smolar": 63.09519513382813,
|
|
"smolar_units": "J/mol/K"
|
|
},
|
|
"triple_liquid": {
|
|
"T": 216.592,
|
|
"T_units": "K",
|
|
"hmolar": 3522.347496266107,
|
|
"hmolar_units": "J/mol",
|
|
"p": 517964.34344772575,
|
|
"p_units": "Pa",
|
|
"rhomolar": 26777.277860217495,
|
|
"rhomolar_units": "mol/m^3",
|
|
"smolar": 22.943179480180966,
|
|
"smolar_units": "J/mol/K"
|
|
},
|
|
"triple_vapor": {
|
|
"T": 216.592,
|
|
"T_units": "K",
|
|
"hmolar": 18942.529431708266,
|
|
"hmolar_units": "J/mol",
|
|
"p": 517964.36480694986,
|
|
"p_units": "Pa",
|
|
"rhomolar": 312.6777588871105,
|
|
"rhomolar_units": "mol/m^3",
|
|
"smolar": 94.13778439068052,
|
|
"smolar_units": "J/mol/K"
|
|
}
|
|
},
|
|
"TRANSPORT": {
|
|
"conductivity": {
|
|
"BibTeX": "Scalabrin-JPCRD-2006-CO2",
|
|
"critical": {
|
|
"hardcoded": "CarbonDioxideScalabrinJPCRD2006"
|
|
},
|
|
"dilute": {
|
|
"hardcoded": "none"
|
|
},
|
|
"residual": {
|
|
"A": [
|
|
0.0370597124660408,
|
|
0.0007696647124242399,
|
|
0.0075538113451464,
|
|
-0.032416436589336,
|
|
0.078894098855904,
|
|
0.0177830586854928,
|
|
0.10744756315137599,
|
|
0.31839746259479995,
|
|
-0.00082691726160072,
|
|
2.0846013855224798e-05
|
|
],
|
|
"T_reducing": 304.1282,
|
|
"T_reducing_units": "K",
|
|
"d": [
|
|
1.0,
|
|
5.0,
|
|
1.0,
|
|
1.0,
|
|
2.0,
|
|
0.0,
|
|
5.0,
|
|
9.0,
|
|
0.0,
|
|
0.0
|
|
],
|
|
"gamma": [
|
|
0,
|
|
0,
|
|
0,
|
|
5,
|
|
5,
|
|
5,
|
|
5,
|
|
5,
|
|
5,
|
|
5
|
|
],
|
|
"l": [
|
|
0,
|
|
0,
|
|
0,
|
|
2,
|
|
2,
|
|
2,
|
|
2,
|
|
2,
|
|
2,
|
|
2
|
|
],
|
|
"rhomass_reducing": 467.6,
|
|
"rhomass_reducing_units": "kg/m^3",
|
|
"t": [
|
|
0.0,
|
|
0.0,
|
|
-1.5,
|
|
0.0,
|
|
-1.0,
|
|
-1.5,
|
|
-1.5,
|
|
-1.5,
|
|
-3.5,
|
|
-5.5
|
|
],
|
|
"type": "polynomial_and_exponential"
|
|
}
|
|
},
|
|
"viscosity": {
|
|
"BibTeX": "Fenghour-JPCRD-1998",
|
|
"_note": "sigma set to 1 nm in since sigma wrapped into constant in equation in Fenghour",
|
|
"dilute": {
|
|
"C": 1.5178953643112785e-07,
|
|
"_note": "Leading coefficient was back calculated from 1.00697e-6/(44.0098)**0.5 (using sigma = 1 nm)",
|
|
"a": [
|
|
0.235156,
|
|
-0.491266,
|
|
0.05211155,
|
|
0.05347906,
|
|
-0.01537102
|
|
],
|
|
"molar_mass": 0.0440098,
|
|
"molar_mass_units": "kg/mol",
|
|
"t": [
|
|
0,
|
|
1,
|
|
2,
|
|
3,
|
|
4
|
|
],
|
|
"type": "collision_integral"
|
|
},
|
|
"epsilon_over_k": 251.196,
|
|
"epsilon_over_k_units": "K",
|
|
"higher_order": {
|
|
"T_reduce": 304.1282,
|
|
"T_reduce_units": "K",
|
|
"_note": "All of the coefficients for higher order viscosity contribution were converted to be in terms of delta and tau",
|
|
"a": [
|
|
1.9036541208525784e-06,
|
|
1.57384720473354e-05,
|
|
1.4207809578440784e-07,
|
|
6.79058431241662e-08,
|
|
-3.0732988514867565e-08
|
|
],
|
|
"d1": [
|
|
1,
|
|
2,
|
|
6,
|
|
8,
|
|
8
|
|
],
|
|
"d2": [
|
|
1
|
|
],
|
|
"f": [
|
|
0
|
|
],
|
|
"g": [
|
|
1
|
|
],
|
|
"gamma": [
|
|
0,
|
|
0,
|
|
0,
|
|
0,
|
|
0
|
|
],
|
|
"h": [
|
|
0
|
|
],
|
|
"l": [
|
|
1,
|
|
1,
|
|
1,
|
|
1,
|
|
0
|
|
],
|
|
"p": [
|
|
1
|
|
],
|
|
"q": [
|
|
0
|
|
],
|
|
"rhomolar_reduce": 10624.9,
|
|
"rhomolar_reduce_units": "mol/m^3",
|
|
"t1": [
|
|
0,
|
|
0,
|
|
3,
|
|
0,
|
|
1
|
|
],
|
|
"t2": [
|
|
0
|
|
],
|
|
"type": "modified_Batschinski_Hildebrand"
|
|
},
|
|
"sigma_eta": 1e-09,
|
|
"sigma_eta_units": "m"
|
|
}
|
|
}
|
|
} |