Files
CoolProp/dev/fluids/R245fa.json
2014-11-07 16:25:42 -05:00

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{
"ALIASES": [
"R245FA"
],
"ANCILLARIES": {
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2.4544895629954687e-10,
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],
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1,
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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",
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"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
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6.237303367666788e-07,
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3.6686975741803814e-13
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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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},
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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2.1517255420533435e-13,
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1,
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],
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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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},
"surface_tension": {
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"Tc": 427.16,
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}
},
"CAS": "460-73-1",
"ENVIRONMENTAL": {
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"FH": 0,
"GWP100": 1030.0,
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"GWP500": 314.0,
"HH": 2,
"Name": "R245fa",
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},
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{
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"accentric": 0.3776,
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{
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{
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{
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10.385,
12.554
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2.364453600524394,
5.735555763648281
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1,
2,
3,
1,
3,
2,
2,
7
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0,
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2,
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0.57971151,
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{
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1,
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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": [
0.0,
0.0,
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427.02048895043913
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0.0,
0.0,
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426.9980413529563
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{
"BibTeX_CP0": "",
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},
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},
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},
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{
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{
"a": 3,
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1,
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}
],
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}
],
"NAME": "R245fa",
"REFPROP_NAME": "R245FA",
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},
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},
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"p": 13.757432845489019,
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}
},
"TRANSPORT": {
"conductivity": {
"BibTeX": "Huber-IECR-2003",
"f_int": {
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"a": [
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],
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0,
1
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},
"psi": {
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],
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},
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"reference_fluid": "R134a",
"type": "ECS"
},
"viscosity": {
"BibTeX": "Huber-IECR-2003",
"epsilon_over_k": 329.72,
"epsilon_over_k_units": "K",
"psi": {
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0.0
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},
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"sigma_eta": 5.529e-10,
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}
}
}