mirror of
https://github.com/CoolProp/CoolProp.git
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640 lines
14 KiB
JSON
640 lines
14 KiB
JSON
{
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"ALIASES": [
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"R245FA"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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420.8281309300612,
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2.1949355018480847e-05,
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9.436153792908897e-11,
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-5.4843377441499966e-14
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],
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"B": [
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1,
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-0.002320817216912323
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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": 374.96359217885765,
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"max_abs_error_units": "J/mol",
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"type": "rational_polynomial"
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},
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"hLV": {
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"A": [
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38964.50415858328,
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3.6495991177580706e-07,
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2.3902287662235015e-13
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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": 807.8257736525482,
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"type": "rational_polynomial"
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},
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"pL": {
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"T_r": 427.01,
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"Tmax": 427.0,
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"Tmin": 171.05,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"type": "pL",
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},
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"pV": {
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"T_r": 427.01,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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11.456
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],
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"type": "pV",
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"using_tau_r": true
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},
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"rhoL": {
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"T_r": 427.01,
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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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"sL": {
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],
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"B": [
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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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"max_abs_error": 0.9296767865090985,
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"max_abs_error_units": "J/mol/K",
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"type": "rational_polynomial"
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},
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"sLV": {
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"A": [
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0.15010341589090437,
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"B": [
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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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"max_abs_error": 2.0663358632074718,
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"max_abs_error_units": "J/mol/K",
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"type": "rational_polynomial"
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},
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"surface_tension": {
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"BibTeX": "Mulero-JPCRD-2012",
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"Tc": 427.16,
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"a": [
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0.073586,
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0.0103,
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],
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"description": "sigma = sum(a_i*(1-T/Tc)^n_i)",
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"n": [
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1.0983,
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0.60033,
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0.72765
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]
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}
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},
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"CAS": "460-73-1",
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"ENVIRONMENTAL": {
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"ASHRAE34": "B1",
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"FH": 0,
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"HH": 2,
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"Name": "R245fa",
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"PH": 1
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},
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"EOS": [
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{
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"T": 469.711,
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}
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"gamma": [
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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",
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"cL": [
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{
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"STATES": {
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"T": 469.8760000000001,
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},
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"p_max_units": "Pa",
|
|
"pseudo_pure": false
|
|
}
|
|
],
|
|
"NAME": "R245fa",
|
|
"REFPROP_NAME": "R245FA",
|
|
"STATES": {
|
|
"critical": {
|
|
"T": 427.01,
|
|
"T_units": "K",
|
|
"p": 3651000.0,
|
|
"p_units": "Pa",
|
|
"rhomolar": 3875,
|
|
"rhomolar_units": "mol/m^3"
|
|
},
|
|
"triple_liquid": {
|
|
"T": 171.05,
|
|
"T_units": "K",
|
|
"p": 13.757432423113592,
|
|
"p_units": "Pa",
|
|
"rhomolar": 12260.148813937387,
|
|
"rhomolar_units": "mol/m^3"
|
|
},
|
|
"triple_vapor": {
|
|
"T": 171.05,
|
|
"T_units": "K",
|
|
"p": 13.757432845245189,
|
|
"p_units": "Pa",
|
|
"rhomolar": 0.009673802590130228,
|
|
"rhomolar_units": "mol/m^3"
|
|
}
|
|
},
|
|
"TRANSPORT": {
|
|
"conductivity": {
|
|
"BibTeX": "Huber-IECR-2003",
|
|
"f_int": {
|
|
"T_reducing": 1.0,
|
|
"T_reducing_units": "K",
|
|
"a": [
|
|
0.00164999,
|
|
-3.28868e-07
|
|
],
|
|
"t": [
|
|
0,
|
|
1
|
|
]
|
|
},
|
|
"psi": {
|
|
"a": [
|
|
1.1627,
|
|
-0.0473491
|
|
],
|
|
"rhomolar_reducing": 3857.0,
|
|
"rhomolar_reducing_units": "mol/m^3",
|
|
"t": [
|
|
0,
|
|
1
|
|
]
|
|
},
|
|
"q_D": 1999999999.9999998,
|
|
"q_D_units": "m",
|
|
"reference_fluid": "R134a",
|
|
"type": "ECS"
|
|
},
|
|
"viscosity": {
|
|
"BibTeX": "Huber-IECR-2003",
|
|
"epsilon_over_k": 329.72,
|
|
"epsilon_over_k_units": "K",
|
|
"psi": {
|
|
"a": [
|
|
1.1529,
|
|
-0.044154,
|
|
0.0
|
|
],
|
|
"rhomolar_reducing": 3857.0,
|
|
"rhomolar_reducing_units": "mol/m^3",
|
|
"t": [
|
|
0,
|
|
1,
|
|
2
|
|
]
|
|
},
|
|
"reference_fluid": "R134a",
|
|
"sigma_eta": 5.529e-10,
|
|
"sigma_eta_units": "m",
|
|
"type": "ECS"
|
|
}
|
|
}
|
|
} |