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CoolProp/dev/fluids/R113.json

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{
"ANCILLARIES": {
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2.0092965982548803e-10,
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],
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"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
"max_abs_error": 409.858498633359,
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"type": "rational_polynomial"
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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1.4585128338720422e-13,
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"_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
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"type": "rational_polynomial"
},
"surface_tension": {
"BibTeX": "Mulero-JPCRD-2012",
"Tc": 487.21,
"a": [
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"description": "sigma = sum(a_i*(1-T/Tc)^n_i)",
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},
"EOS": [
{
"BibTeX_CP0": "",
"BibTeX_EOS": "Marx-BOOK-1992",
"STATES": {
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"acentric": 0.252535,
"acentric_units": "-",
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{
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"type": "IdealGasHelmholtzLead"
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{
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8.62650812,
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{
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"type": "ResidualHelmholtzPower"
}
],
"critical_region_splines": {
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"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
"cL": [
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0.0,
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487.19193982414185
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"gas_constant": 8.314471,
"gas_constant_units": "J/mol/K",
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"molar_mass_units": "kg/mol",
"p_max": 200000000,
"p_max_units": "Pa",
"pseudo_pure": false
}
],
"INFO": {
"2DPNG_URL": "http://www.chemspider.com/ImagesHandler.ashx?id=6188",
"ALIASES": [],
"CAS": "76-13-1",
"CHEMSPIDER_ID": 6188,
"ENVIRONMENTAL": {
"ASHRAE34": "A1",
"FH": 0,
"GWP100": 6130.0,
"GWP20": 6540.0,
"GWP500": 2700.0,
"HH": 1,
"Name": "R113",
"ODP": 1.0,
"PH": 0
},
"FORMULA": "C_{2}Cl_{3}F_{3}",
"INCHI_KEY": "AJDIZQLSFPQPEY-UHFFFAOYSA-N",
"INCHI_STRING": "InChI=1S/C2Cl3F3/c3-1(4,6)2(5,7)8",
"NAME": "R113",
"REFPROP_NAME": "R113",
"SMILES": "C(C(F)(Cl)Cl)(F)(F)Cl"
},
"STATES": {
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},
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"rhomolar_units": "mol/m^3",
"smolar": 297.90329244375033,
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}
}
}
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