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CoolProp/dev/fluids/OrthoDeuterium.json

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{
"ALIASES": [
"orthodeuterium",
"ORTHODEUTERIUM"
],
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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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"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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0.7537041861041885,
0.016472625168686524,
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6.793274915681606e-09
],
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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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"type": "rational_polynomial"
}
},
"CAS": "7782-39-0o",
"EOS": [
{
"BibTeX_CP0": "",
"BibTeX_EOS": "Richardson-JPCRD-2013",
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},
"T_max": 600,
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"Ttriple": 18.724,
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"accentric": -0.136290274128,
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"alpha0": [
{
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"type": "IdealGasHelmholtzLead"
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{
"a": 1.5,
"type": "IdealGasHelmholtzLogTau"
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{
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4.32447
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12.56129368805425,
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25.08346374543558,
6.604068857589984
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}
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{
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4,
1,
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2,
3,
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3,
2,
2,
2,
1,
1,
3,
2
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2,
2,
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},
{
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0.57,
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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,
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38.37745911877317
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},
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"pseudo_pure": false
}
],
"NAME": "OrthoDeuterium",
"REFPROP_NAME": "N/A",
"STATES": {
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"p": 1679600.0,
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}
}
}