mirror of
https://github.com/CoolProp/CoolProp.git
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422 lines
9.8 KiB
JSON
422 lines
9.8 KiB
JSON
{
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"ALIASES": [
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"pXylene",
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"p-xylene",
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"P-XYLENE"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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-107546.35780329119,
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-292.3625818681443,
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4.537588818872309,
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-0.01879507357283591,
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4.524746505534091e-05,
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-6.554776575854516e-08,
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5.2211258465919434e-11,
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-1.7679361960577362e-14
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],
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"B": [
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1,
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-0.0016047019504799305
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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": 387.82029030051854,
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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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0.06082423372270578,
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2.1934428398818863e-07,
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-1.7556227983837822e-10,
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5.964205565488495e-14
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],
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"B": [
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1,
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-0.001602334844094644
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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": 891.9150056397721,
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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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"pL": {
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"T_r": 616.168,
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"Tmax": 616.1679999999988,
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"Tmin": 286.4,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.018225495845447526,
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"n": [
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"t": [
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],
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"type": "pL",
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},
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"pV": {
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"T_r": 616.168,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"n": [
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2.955,
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4.359,
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5.234
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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": 616.168,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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0.617,
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6.974,
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11.02,
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11.7
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],
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"type": "rhoLnoexp",
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"using_tau_r": false
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},
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"rhoV": {
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"T_r": 616.168,
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"Tmin": 286.4,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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"n": [
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3.948
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],
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"type": "rhoV",
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"using_tau_r": true
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},
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"sL": {
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"A": [
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5.2981001270844324e-14,
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],
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"B": [
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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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"max_abs_error": 0.6264274726032184,
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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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0.0315140904929448,
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2.6074644173387687e-17
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],
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"B": [
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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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"max_abs_error": 1.4539401112910189,
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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-2014",
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"Tc": 616.168,
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"a": [
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0.0619
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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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1.21
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]
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}
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},
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"CAS": "106-42-3",
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"EOS": [
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{
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"BibTeX_CP0": "",
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"BibTeX_EOS": "Zhou-JPCRD-2012",
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"STATES": {
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"hs_anchor": {
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"T": 677.7848,
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"T_units": "K",
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"hmolar": 79390.53700947785,
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"p": 6002755.904468263,
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},
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"reducing": {
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"p": 3531500,
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},
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"sat_min_liquid": {
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"T": 286.4,
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"p": 0.5800850024867812,
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},
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"sat_min_vapor": {
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"T": 286.4,
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}
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},
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"T_max": 700,
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"T_max_units": "K",
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"Ttriple": 286.4,
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"accentric": 0.324,
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"accentric_units": "-",
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"alpha0": [
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{
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"type": "IdealGasHelmholtzLead"
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},
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{
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"a": 4.2430504,
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{
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"n": [
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"type": "ResidualHelmholtzPower"
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{
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"epsilon": [
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],
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"eta": [
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"gamma": [
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"type": "ResidualHelmholtzGaussian"
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"gas_constant": 8.314472,
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"molar_mass": 0.106165,
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"p_max": 200000000,
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"p_max_units": "Pa",
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"pseudo_pure": false
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}
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],
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"NAME": "p-Xylene",
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"REFPROP_NAME": "PXYLENE",
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"STATES": {
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"critical": {
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"T": 616.168,
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"T_units": "K",
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"p": 3531500.0,
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"p_units": "Pa",
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"rhomolar": 2693.92,
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},
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"triple_liquid": {
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"T": 286.4,
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"T_units": "K",
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"p": 0.5800850024867812,
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"p_units": "Pa",
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"rhomolar": 8165.004739624582,
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"rhomolar_units": "mol/m^3"
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},
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"triple_vapor": {
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"T": 286.4,
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"T_units": "K",
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"p": 0.5800850024867812,
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"p_units": "Pa",
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"rhomolar_units": "mol/m^3"
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}
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}
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} |