Files
CoolProp/dev/fluids/R1234ze(Z).json
Ian Bell 183868dee2 Implement acentric factor through AbstractState and Props1SI; closes #448
Fix all instances of accentric->acentric in fluid files and codebase.

Signed-off-by: Ian Bell <ian.h.bell@gmail.com>
2015-02-03 17:37:53 -05:00

434 lines
11 KiB
JSON

{
"ALIASES": [
"R1234ZE(Z)",
"R1234ZE"
],
"ANCILLARIES": {
"hL": {
"A": [
661341.6719107341,
-15127.133650206008,
138.91087893469512,
-0.6980587134971441,
0.002098499633604347,
-3.7793519929234075e-06,
3.774511596585241e-09,
-1.6130483991223831e-12
],
"B": [
1,
-0.0023491427415732965
],
"Tmax": 423.16999999999996,
"Tmin": 273.0,
"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
"max_abs_error": 179.97713685777762,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"hLV": {
"A": [
-1828209.8209888446,
39416.47687723154,
-358.30636912688453,
1.8003457633178375,
-0.0054136167749014065,
9.744568144367385e-06,
-9.723381288946163e-09,
4.150647373162431e-12
],
"B": [
1,
-0.002348564097658635
],
"Tmax": 423.16999999999996,
"Tmin": 273.0,
"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
"max_abs_error": 437.77812959121843,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"pL": {
"T_r": 423.27,
"Tmax": 423.2699999999993,
"Tmin": 273.0,
"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.015877796614871542,
"n": [
0.0117990424214877,
-6.803022339042438,
5.362164910742748,
-12.094491173809551,
-254.2811081944286,
171.34274686639145
],
"reducing_value": 3533000.0,
"t": [
0.631,
0.974,
3.244,
3.59,
7.592,
6.934
],
"type": "pL",
"using_tau_r": true
},
"pV": {
"T_r": 423.27,
"Tmax": 423.2699999999993,
"Tmin": 273.0,
"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.013861437588635894,
"n": [
-8.177106613433029,
1.5142657359326417,
-2.790441012266599,
0.00919594460120844,
-8.214525035988535,
-5309.748045808004
],
"reducing_value": 3533000.0,
"t": [
0.993,
1.127,
3.259,
4.649,
8.29,
18.573
],
"type": "pV",
"using_tau_r": true
},
"rhoL": {
"T_r": 423.27,
"Tmax": 423.2699999999993,
"Tmin": 273.0,
"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.36780472644506457,
"n": [
2.8054215733649555,
-0.5782847268115662,
6.657750631664868,
-28488.415580838606,
68499.04449007797,
-85980.39928084945
],
"reducing_value": 4121.303363626818,
"t": [
0.414,
0.901,
2.913,
8.026,
8.631,
10.213
],
"type": "rhoLnoexp",
"using_tau_r": false
},
"rhoV": {
"T_r": 423.27,
"Tmax": 423.2699999999993,
"Tmin": 273.0,
"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 1.0860081017443401,
"n": [
-3.8008160798898456,
-1.14790031265839,
-281.54354036613495,
6472.299051044157,
-1985193.1508489654,
2037392.973112241
],
"reducing_value": 4121.303363626818,
"t": [
0.43,
0.95,
4.5,
6.507,
8.994,
9.048
],
"type": "rhoV",
"using_tau_r": true
},
"sL": {
"A": [
1303.8187095473975,
-31.93845588433953,
0.3004627114725399,
-0.0015238403825847317,
4.598136568105457e-06,
-8.296900897960336e-09,
8.296774715164654e-12,
-3.5487904739583724e-15
],
"B": [
1,
-0.0023493955432933368
],
"Tmax": 423.16999999999996,
"Tmin": 273.0,
"_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
"max_abs_error": 0.41975135410767805,
"max_abs_error_units": "J/mol/K",
"type": "rational_polynomial"
},
"sLV": {
"A": [
-3372.3450064808153,
78.44275112099125,
-0.7390101155794137,
0.003785229753629718,
-1.1515953877343451e-05,
2.089341655885634e-08,
-2.0967591691283893e-11,
8.988690381042343e-15
],
"B": [
1,
-0.0023487962484419356
],
"Tmax": 423.16999999999996,
"Tmin": 273.0,
"_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
"max_abs_error": 1.0220801074081636,
"max_abs_error_units": "J/mol/K",
"type": "rational_polynomial"
}
},
"CAS": "29118-25-0",
"EOS": [
{
"BibTeX_CP0": "",
"BibTeX_EOS": "Akasaka-DELFT-2013",
"STATES": {
"hs_anchor": {
"T": 465.59700000000004,
"T_units": "K",
"hmolar": 8356.216717020856,
"hmolar_units": "J/mol",
"p": 6082696.015266482,
"p_units": "Pa",
"rhomolar": 3714.0265196296004,
"rhomolar_units": "mol/m^3",
"smolar": 30.226552329410275,
"smolar_units": "J/mol/K"
},
"reducing": {
"T": 423.27,
"T_units": "K",
"hmolar": 1000.6072356724737,
"hmolar_units": "J/mol",
"p": 3533000,
"p_units": "Pa",
"rhomolar": 4126.696132921778,
"rhomolar_units": "mol/m^3",
"smolar": 15.115785966250435,
"smolar_units": "J/mol/K"
},
"sat_min_liquid": {
"T": 273.0,
"T_units": "K",
"hmolar": -27727.96883868131,
"hmolar_units": "J/mol",
"p": 67802.93935916605,
"p_units": "Pa",
"rhomolar": 11250.756301033874,
"rhomolar_units": "mol/m^3",
"smolar": -64.58713826359764,
"smolar_units": "J/mol/K"
},
"sat_min_vapor": {
"T": 273.0,
"T_units": "K",
"hmolar": -2603.769449881924,
"hmolar_units": "J/mol",
"p": 67802.93965438179,
"p_units": "Pa",
"rhomolar": 31.076296674814373,
"rhomolar_units": "mol/m^3",
"smolar": 27.44289609285729,
"smolar_units": "J/mol/K"
}
},
"T_max": 430,
"T_max_units": "K",
"Ttriple": 273,
"Ttriple_units": "K",
"acentric": 0.3274,
"acentric_units": "-",
"alpha0": [
{
"a1": 0,
"a2": 0,
"type": "IdealGasHelmholtzLead"
},
{
"a": -1,
"type": "IdealGasHelmholtzLogTau"
},
{
"T0": 298,
"Tc": 423.27,
"c": [
-1.6994,
0.05794646443168663,
-5.539762719017151e-05,
1.998892498570471e-08
],
"t": [
0,
1,
2,
3
],
"type": "IdealGasHelmholtzCP0PolyT"
}
],
"alphar": [
{
"d": [
1,
1,
1,
2,
5,
1,
3,
5,
7,
1,
2,
2,
3,
4,
2,
3,
5
],
"l": [
0,
0,
0,
0,
0,
1,
1,
1,
1,
2,
2,
2,
2,
2,
3,
3,
3
],
"n": [
7.7652368,
-8.7025756,
-0.28352251,
0.14534501,
0.0092092105,
-0.24997382,
0.09667436,
0.024685924,
-0.013255083,
-0.06423133,
0.36638206,
-0.25548847,
-0.095592361,
0.086271444,
0.015997412,
-0.013127234,
0.004229399
],
"t": [
0.685,
0.8494,
1.87,
2,
0.142,
4.2,
0.08,
0,
1.1,
5.5,
6.6,
8.4,
7.2,
7.6,
8.5,
23,
18
],
"type": "ResidualHelmholtzPower"
}
],
"critical_region_splines": {
"T_max": 423.27,
"T_min": 423.26310506132734,
"_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": [
-1.0661006391670194e-09,
1.2653370461499062e-05,
-0.04997314613163001,
488.933234607043
],
"cV": [
-8.160851613585538e-10,
9.267609720003654e-06,
-0.03480529660648677,
466.4282367596696
],
"rhomolar_max": 4225.213370352157,
"rhomolar_min": 4025.0245673273625
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",
"molar_mass": 0.1140415928,
"molar_mass_units": "kg/mol",
"p_max": 6000000,
"p_max_units": "Pa",
"pseudo_pure": false
}
],
"NAME": "R1234ze(Z)",
"REFPROP_NAME": "N/A",
"STATES": {
"critical": {
"T": 423.27,
"T_units": "K",
"p": 3533000.0,
"p_units": "Pa",
"rhomolar": 4121.303363626818,
"rhomolar_units": "mol/m^3"
},
"triple_liquid": {
"T": 273.0,
"T_units": "K",
"hmolar": -27727.96883868131,
"hmolar_units": "J/mol",
"p": 67802.93935916605,
"p_units": "Pa",
"rhomolar": 11250.756301033874,
"rhomolar_units": "mol/m^3",
"smolar": -64.58713826359764,
"smolar_units": "J/mol/K"
},
"triple_vapor": {
"T": 273.0,
"T_units": "K",
"hmolar": -2603.769449881924,
"hmolar_units": "J/mol",
"p": 67802.93965438179,
"p_units": "Pa",
"rhomolar": 31.076296674814373,
"rhomolar_units": "mol/m^3",
"smolar": 27.44289609285729,
"smolar_units": "J/mol/K"
}
}
}