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https://github.com/CoolProp/CoolProp.git
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476 lines
11 KiB
JSON
476 lines
11 KiB
JSON
{
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"ALIASES": [
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"toluene",
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"TOLUENE"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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-127816.60934245441,
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446.0102277664863,
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-1.026134239964676,
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0.0027814810910275246,
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-4.25324565453859e-06,
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1.7635980914094698e-09,
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2.0764196231802587e-12,
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-1.924517644518835e-15
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],
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"B": [
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1,
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-0.0016732414940376819
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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": 533.0430122778798,
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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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58306.378118599954,
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-120.75285948710511,
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-0.767894598936851,
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0.006122946178697713,
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-2.080754466354321e-05,
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3.8277021134686824e-08,
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-3.7202650791366816e-11,
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1.51416107873666e-14
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],
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"B": [
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1,
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-0.001668265490735538
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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": 1171.643610263692,
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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": 591.75,
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"Tmax": 591.7499999999987,
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"Tmin": 178.0,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.013628695855705253,
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"n": [
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-11.639922828598088,
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5.650211353764286,
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-2.6974053250328165,
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-3.164119945892499,
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1.8859792463505036,
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-5.2234698853395525
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],
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"reducing_value": 4126000.0,
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"t": [
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1.041,
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1.184,
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3.013,
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5.82,
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8.325,
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15.907
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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": 591.75,
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"Tmax": 591.7499999999987,
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"Tmin": 178.0,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.009539128608204717,
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"n": [
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-41.682551388800405,
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35.681619568443324,
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1.6090346729113876,
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-6.971566618092907
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],
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"reducing_value": 4126000.0,
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"t": [
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1.081,
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1.11,
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2.974,
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5.067,
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13.97,
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17.253
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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": 591.75,
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"Tmax": 591.7499999999987,
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"Tmin": 178.0,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.8197967086870594,
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"n": [
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2.731439741297877,
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-1.4311921172736468,
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1.7220225715861872,
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-1.3959592517619432,
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25.019574322670564,
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-106.28098773992355
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],
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"reducing_value": 3169.0,
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"t": [
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0.413,
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1.151,
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1.592,
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6.141,
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12.914,
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18.579
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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": 591.75,
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"Tmax": 591.7499999999987,
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"Tmin": 178.0,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.610452170273057,
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"n": [
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-2.079525851134041,
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2945.506923819063
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],
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"reducing_value": 3169.0,
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"t": [
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0.4,
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0.697,
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3.764,
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8.691,
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19.351,
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19.782
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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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-531.4163066284109,
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4.156850911423105,
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-0.02100500083113781,
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7.425415705230403e-05,
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2.2768612133924225e-10,
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-1.7213031766029153e-13,
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5.545557860969033e-17
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],
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"B": [
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1,
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-0.0016631904668857418
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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": 1.1354396470978294,
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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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1334.5167341532049,
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-16.246141546661086,
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0.098043332108851,
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-0.00035415392917483685,
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7.947463423920035e-07,
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-1.0872778128637114e-09,
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8.312251428464904e-13,
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-2.721887982430085e-16
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],
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"B": [
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1,
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-0.0016412193464999411
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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": 2.7780355815007107,
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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": 591.75,
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"a": [
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0.06897
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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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1.291
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]
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}
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},
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"CAS": "108-88-3",
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"ENVIRONMENTAL": {
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"ASHRAE34": "UNKNOWN",
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"FH": 3,
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"GWP100": 3.3,
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"GWP20": -1.0,
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"GWP500": -1.0,
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"HH": 2,
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"Name": "Toluene",
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"ODP": -1.0,
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"PH": 0
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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": "Lemmon-JCED-2006",
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"STATES": {
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"hs_anchor": {
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"T": 650.9250000000001,
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"T_units": "K",
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"hmolar": 66706.5573260888,
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"hmolar_units": "J/mol",
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"p": 6835695.766761503,
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"p_units": "Pa",
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"rhomolar": 2852.1,
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"rhomolar_units": "mol/m^3",
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"smolar": 126.11884906567118,
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"smolar_units": "J/mol/K"
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},
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"reducing": {
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"T": 591.75,
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"T_units": "K",
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"p": 4126000,
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"p_units": "Pa",
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"rhomolar": 3169,
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"rhomolar_units": "mol/m^3"
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},
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"sat_min_liquid": {
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"T": 178.0,
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"T_units": "K",
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"p": 3.9393478817276356e-05,
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"p_units": "Pa",
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"rhomolar": 10580.06048163071,
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"rhomolar_units": "mol/m^3"
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},
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"sat_min_vapor": {
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"T": 178.0,
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"T_units": "K",
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"p": 3.9393478817276356e-05,
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"p_units": "Pa",
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"rhomolar": 2.661765525110245e-05,
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"rhomolar_units": "mol/m^3"
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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": 178,
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"Ttriple_units": "K",
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"accentric": 0.2657,
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"accentric_units": "-",
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"alpha0": [
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{
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"a1": 3.5241174832,
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"a2": 1.1360823464,
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"type": "IdealGasHelmholtzLead"
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},
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{
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"a": 3,
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"type": "IdealGasHelmholtzLogTau"
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},
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{
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"n": [
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"t": [
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],
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"type": "IdealGasHelmholtzPlanckEinstein"
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}
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],
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"alphar": [
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"d": [
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"l": [
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"n": [
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],
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"t": [
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],
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"type": "ResidualHelmholtzPower"
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}
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],
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"gas_constant": 8.314472,
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"gas_constant_units": "J/mol/K",
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"molar_mass": 0.09213842,
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"molar_mass_units": "kg/mol",
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"p_max": 500000000,
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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": "Toluene",
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"REFPROP_NAME": "TOLUENE",
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"STATES": {
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"critical": {
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"T": 591.75,
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"T_units": "K",
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"p": 4126000.0,
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"p_units": "Pa",
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"rhomolar": 3169.0,
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"rhomolar_units": "mol/m^3"
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},
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"triple_liquid": {
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"T": 178.0,
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"T_units": "K",
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"p": 3.9393478817276356e-05,
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"p_units": "Pa",
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"rhomolar": 10580.06048163071,
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"rhomolar_units": "mol/m^3"
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},
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"triple_vapor": {
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"T": 178.0,
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"T_units": "K",
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"p": 3.9393478817276356e-05,
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"p_units": "Pa",
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"rhomolar": 2.661765525110245e-05,
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"rhomolar_units": "mol/m^3"
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}
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},
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"TRANSPORT": {
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"conductivity": {
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"BibTeX": "Assael-JPCRD-2012-Toluene",
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"critical": {
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"GAMMA": 0.05,
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"qD": 1613000000.0,
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"type": "simplified_Olchowy_Sengers",
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"zeta0": 2.2e-10
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},
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"dilute": {
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"A": [
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],
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"B": [
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],
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"T_reducing": 1,
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"m": [
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"n": [
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"type": "ratio_of_polynomials"
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},
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"residual": {
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"B": [
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],
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"T_reducing": 591.75,
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"T_reducing_units": "K",
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"d": [
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],
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"rhomass_reducing": 291.992,
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"rhomass_reducing_units": "kg/m^3",
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"t": [
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"type": "polynomial"
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}
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}
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}
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} |