Files
CoolProp/dev/fluids/IsoButane.json
2014-11-07 16:25:42 -05:00

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{
"ALIASES": [
"isobutane",
"Isobutane",
"ISOBUTANE",
"R600A",
"R600a",
"ISOBUTAN"
],
"ANCILLARIES": {
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6.675734904499258e-11,
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],
"B": [
1,
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],
"Tmax": 407.717,
"Tmin": 113.73,
"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
"max_abs_error": 312.66228021911775,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"hLV": {
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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": 725.5919123687981,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"melting_line": {
"BibTeX": "Buecker-JPCRD-2006B",
"T_m": 113.55,
"parts": [
{
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"T_max": 127,
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"a": [
1953637130.9
],
"p_0": 0.0219,
"t": [
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}
],
"type": "polynomial_in_Tr"
},
"pL": {
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"t": [
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2.407,
3.825,
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"type": "pL",
"using_tau_r": true
},
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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4.045,
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14.042
],
"type": "pV",
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},
"rhoL": {
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"type": "rhoLnoexp",
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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"type": "rhoV",
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1.354840234432422e-16
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1,
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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"
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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": {
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"Tc": 407.81,
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0.06121
],
"description": "sigma = sum(a_i*(1-T/Tc)^n_i)",
"n": [
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1.304
]
}
},
"CAS": "75-28-5",
"ENVIRONMENTAL": {
"ASHRAE34": "UNKNOWN",
"FH": 4,
"GWP100": -1.0,
"GWP20": -1.0,
"GWP500": -1.0,
"HH": 1,
"Name": "IsoButane",
"ODP": -1.0,
"PH": 0
},
"EOS": [
{
"BibTeX_CP0": "",
"BibTeX_EOS": "Buecker-JPCRD-2006B",
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},
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}
},
"T_max": 575,
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"Ttriple": 113.73,
"Ttriple_units": "K",
"accentric": 0.183531783208,
"accentric_units": "-",
"alpha0": [
{
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"type": "IdealGasHelmholtzLead"
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{
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{
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{
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{
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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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}
],
"NAME": "IsoButane",
"REFPROP_NAME": "ISOBUTAN",
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}
},
"TRANSPORT": {
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"gamma": 1.239,
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"type": "simplified_Olchowy_Sengers",
"zeta0": 1.94e-10
},
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"type": "polynomial"
}
},
"viscosity": {
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"dilute": {
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"type": "modified_Batschinski_Hildebrand"
},
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"type": "Rainwater-Friend"
},
"sigma_eta": 4.6445e-10,
"sigma_eta_units": "m"
}
}
}