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https://github.com/CoolProp/CoolProp.git
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478 lines
11 KiB
JSON
478 lines
11 KiB
JSON
{
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"ALIASES": [
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"deuterium",
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"DEUTERIUM",
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"D2"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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142.20573706270545,
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-388.17431247992545,
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50.92150411340013,
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-3.2787190503797596,
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0.1250559473187705,
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-0.002845315927149983,
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3.572982687929778e-05,
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-1.9148918622448812e-07
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],
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"B": [
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1,
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-0.02572149122128609
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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": 2.3816767643807566,
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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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-2547.5249465644265,
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1004.6849731117768,
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0.006720168624233064,
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-8.458382239101899e-05,
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4.54033966232595e-07
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],
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"B": [
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1,
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-0.02569380935774139
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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": 5.1567028571888045,
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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": 38.34,
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"Tmax": 38.33999999999991,
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"Tmin": 18.72400000000001,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.005537849329229072,
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"n": [
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"t": [
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],
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"type": "pL",
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"using_tau_r": true
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},
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"pV": {
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"T_r": 38.34,
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"Tmax": 38.33999999999991,
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"Tmin": 18.72400000000001,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.006717131880518146,
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"n": [
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18.491
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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": 38.34,
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"Tmax": 38.33999999999991,
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"Tmin": 18.72400000000001,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.17429991279744872,
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"n": [
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"t": [
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1.992,
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19.493
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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": 38.34,
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"Tmax": 38.33999999999991,
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"Tmin": 18.72400000000001,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.0174186911302332,
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"n": [
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"t": [
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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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0.0027033285748731435,
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8.04968457370522e-07,
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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": 0.060586293911335076,
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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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254.53855072679576,
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0.7537041537435683,
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7.161833788601245e-05,
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6.79327502468355e-09
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],
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"B": [
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1,
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-0.02569685779284826
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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": 0.13354546382785593,
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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": 38.34,
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"a": [
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0.009376
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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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1.258
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]
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}
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},
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"CAS": "7782-39-0",
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"ENVIRONMENTAL": {
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"ASHRAE34": "UNKNOWN",
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"FH": -1,
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"GWP100": 0.0,
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"GWP20": 0.0,
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"GWP500": 0.0,
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"HH": -1,
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"Name": "Deuterium",
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"ODP": -1.0,
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"PH": -1
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},
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"EOS": [
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{
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"BibTeX_CP0": "",
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"BibTeX_EOS": "Richardson-JPCRD-2013",
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"STATES": {
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"hs_anchor": {
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"T": 42.17400000000001,
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"T_units": "K",
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"hmolar": 1012.7149455649957,
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"hmolar_units": "J/mol",
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"p": 2471528.9989254335,
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"p_units": "Pa",
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"rhomolar": 15507.0,
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"rhomolar_units": "mol/m^3",
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},
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"reducing": {
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"T": 38.34,
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"T_units": "K",
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"p": 1679600,
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},
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}
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},
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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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{
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"type": "IdealGasHelmholtzLead"
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"n": [
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"epsilon": [
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"gamma": [
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"type": "ResidualHelmholtzGaussian"
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"gas_constant": 8.3144621,
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"molar_mass": 0.0040282,
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"molar_mass_units": "kg/mol",
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"p_max": 2000000000,
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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": "Deuterium",
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"REFPROP_NAME": "D2",
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"STATES": {
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"critical": {
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"T": 38.34,
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"T_units": "K",
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"p": 1679600.0,
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"p_units": "Pa",
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"rhomolar": 17230.0,
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"rhomolar_units": "mol/m^3"
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},
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"triple_liquid": {
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"T": 18.724,
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"T_units": "K",
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"p": 17.1891019732537,
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"p_units": "Pa",
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"rhomolar_units": "mol/m^3"
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},
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"triple_vapor": {
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"T": 18.724,
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"T_units": "K",
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"p": 17.1891019732537,
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"p_units": "Pa",
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"rhomolar": 112.95640342174914,
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}
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}
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} |