mirror of
https://github.com/CoolProp/CoolProp.git
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423 lines
9.7 KiB
JSON
423 lines
9.7 KiB
JSON
{
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"ALIASES": [
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"R1233zdE",
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"R1233ZDE",
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"R1233ZD(E)"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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-71240.16240436904,
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-52.28428814528902,
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4.353924212663744,
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-0.02904954974384171,
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0.00010343521939827723,
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-2.1508865651262542e-07,
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2.4420925451029555e-10,
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-1.1773776340977882e-13
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],
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"B": [
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1,
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-0.0022591095350531047
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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": 328.8190658937674,
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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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9711.524274702817,
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868.5716099956185,
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-11.950503169491826,
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0.07453440075323205,
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-0.00026566999078229926,
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5.540692918902807e-07,
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-6.315785387642259e-10,
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3.0556010842488237e-13
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],
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"B": [
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1,
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-0.00225764683205724
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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": 734.1268745730167,
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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": 438.75,
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"Tmax": 438.74999999999915,
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"Tmin": 195.15,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.04812397751767783,
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"n": [
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0.029762994134254272,
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-6.47060943833758,
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-4.614592689331627,
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-9.236029232181323,
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659.8939410067252
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],
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"reducing_value": 3570900.0,
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"t": [
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0.408,
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0.959,
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1.67,
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3.873,
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10.203,
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19.884
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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": 438.75,
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"Tmax": 438.74999999999915,
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"Tmin": 195.15,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.04812235123814457,
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"n": [
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0.021088508639502585,
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121247.44743084916
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],
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"reducing_value": 3570900.0,
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"t": [
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0.967,
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3.777,
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10.577,
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19.909,
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19.956
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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": 438.75,
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"Tmax": 438.74999999999915,
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"Tmin": 195.15,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.49366683042657566,
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"n": [
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3.3871208714378995,
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-1.54887974718069,
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7.422063780601333,
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90.2369693095755,
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],
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"reducing_value": 3670.0,
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"t": [
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0.414,
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0.659,
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1.968,
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2.399,
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7.587,
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8.501
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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": 438.75,
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"Tmax": 438.74999999999915,
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"Tmin": 195.15,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.4192570094541437,
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"n": [
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1.4537714001445163,
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4775.150913792323
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"reducing_value": 3670.0,
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"t": [
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0.258,
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0.32,
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0.93,
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4.132,
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17.885,
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19.89
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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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-514.6834417545941,
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4.648567313245329,
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-0.02089134136229189,
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5.621105033746908e-05,
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1.2281857875247076e-11,
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9.740736047982299e-14,
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-8.508047230648248e-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": 0.7533170166193806,
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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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1158.7404093102787,
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0.10143696597999319,
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8.883769623997838e-07,
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-1.207789993711683e-09,
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8.65163332368902e-13,
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-2.346106390791771e-16
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],
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"B": [
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1,
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-0.0022565761391423566
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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": 1.724469868885146,
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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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},
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"CAS": "102687-65-0",
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"EOS": [
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{
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"BibTeX_CP0": "",
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"BibTeX_EOS": "",
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"STATES": {
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"hs_anchor": {
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"T": 482.62500000000006,
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"T_units": "K",
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"hmolar": 67574.558560245,
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"hmolar_units": "J/mol",
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"p": 5982345.633645476,
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"p_units": "Pa",
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"rhomolar": 3303.0,
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"rhomolar_units": "mol/m^3",
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"smolar": 237.87159003957794,
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"smolar_units": "J/mol/K"
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},
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"reducing": {
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"T": 438.75,
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"T_units": "K",
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"p": 3570900,
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"p_units": "Pa",
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"rhomolar": 3670,
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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": 195.15,
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"T_units": "K",
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"p": 250.26557780679073,
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"p_units": "Pa",
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"rhomolar": 11408.679640912957,
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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": 195.15,
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"T_units": "K",
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"p": 250.2655780810378,
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"p_units": "Pa",
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"rhomolar": 0.15430391943019858,
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"rhomolar_units": "mol/m^3"
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}
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},
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"T_max": 550,
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"T_max_units": "K",
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"Ttriple": 195.15,
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"Ttriple_units": "K",
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"accentric": 0.305,
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"accentric_units": "-",
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"alpha0": [
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{
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"a1": 0,
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"a2": 0,
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"type": "IdealGasHelmholtzLead"
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},
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{
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"a": -1,
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"type": "IdealGasHelmholtzLogTau"
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},
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{
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"T0": 298.15,
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"Tc": 438.75,
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"c": [
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4
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],
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"t": [
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0
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],
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"type": "IdealGasHelmholtzCP0PolyT"
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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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"reference": "IIR",
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"type": "IdealGasHelmholtzEnthalpyEntropyOffset"
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}
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],
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"alphar": [
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{
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"d": [
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1,
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"l": [
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"n": [
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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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"beta": [
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1.27,
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"d": [
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],
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"epsilon": [
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0.77,
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0.62,
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],
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"eta": [
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1.215,
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1.5,
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1.1,
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2.52,
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4.55
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],
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"gamma": [
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1.32,
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],
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"n": [
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"t": [
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"type": "ResidualHelmholtzGaussian"
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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": 0.1304961896,
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"molar_mass_units": "kg/mol",
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"p_max": 100000000,
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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": "R1233zd(E)",
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"REFPROP_NAME": "R1233ZD",
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"STATES": {
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"critical": {
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"T": 438.75,
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"T_units": "K",
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"p": 3570900.0,
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"p_units": "Pa",
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"rhomolar": 3670.0,
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"rhomolar_units": "mol/m^3"
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},
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"triple_liquid": {
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"T": 195.15,
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"T_units": "K",
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"p": 250.26557780679073,
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"p_units": "Pa",
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"rhomolar": 11408.679640912957,
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"rhomolar_units": "mol/m^3"
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},
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"triple_vapor": {
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"T": 195.15,
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"T_units": "K",
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"p": 250.2655780810378,
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"p_units": "Pa",
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"rhomolar": 0.15430391943019858,
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"rhomolar_units": "mol/m^3"
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}
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}
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} |