Property | Value | Unit | Source |
---|---|---|---|
PAff | 768.80 | kJ/mol | NIST |
BasG | 729.80 | kJ/mol | NIST |
ΔcH°liquid | -1880.00 | kJ/mol | NIST |
η | 0.0015119 | Pa×s | Volumet... |
ΔfG° | -267.44 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-395.90; -376.90] | kJ/mol |
![]() |
ΔfH°gas | -376.90 ± 8.10 | kJ/mol | NIST |
ΔfH°gas | -395.90 | kJ/mol | NIST |
ΔfH°liquid | [-441.00; -422.00] | kJ/mol |
![]() |
ΔfH°liquid | -422.00 ± 7.60 | kJ/mol | NIST |
ΔfH°liquid | -441.00 | kJ/mol | NIST |
ΔfusH° | 8.80 | kJ/mol | Joback Calculated Property |
ΔvapH° | [45.10; 45.20] | kJ/mol |
![]() |
ΔvapH° | 45.20 | kJ/mol | NIST |
ΔvapH° | 45.10 | kJ/mol | NIST |
ΔvapH° | 45.20 ± 0.20 | kJ/mol | NIST |
IE | 10.13 | eV | NIST |
log10WS | 0.57 | Crippen Calculated Property | |
logPoct/wat | -0.375 | Crippen Calculated Property | |
McVol | 64.870 | ml/mol | McGowan Calculated Property |
Pc | [3600.00; 5285.00] | kPa |
![]() |
Pc | 5285.00 ± 20.00 | kPa | NIST |
Pc | 3600.00 ± 5.00 | kPa | NIST |
ρc | [289.16; 306.66] | kg/m3 |
![]() |
ρc | 289.16 ± 6.85 | kg/m3 | NIST |
ρc | 306.66 ± 3.04 | kg/m3 | NIST |
Inp | [588.00; 646.00] |
![]() |
|
Inp | 630.00 | NIST | |
Inp | Outlier 588.00 | NIST | |
Inp | 591.00 | NIST | |
Inp | 595.00 | NIST | |
Inp | 617.00 | NIST | |
Inp | 624.00 | NIST | |
Inp | 635.00 | NIST | |
Inp | 629.00 | NIST | |
Inp | 629.00 | NIST | |
Inp | 618.00 | NIST | |
Inp | 646.00 | NIST | |
Inp | 626.00 | NIST | |
Inp | 623.00 | NIST | |
Inp | 616.00 | NIST | |
Inp | 635.30 | NIST | |
Inp | 617.00 | NIST | |
Inp | 617.00 | NIST | |
Inp | 616.00 | NIST | |
Inp | 616.00 | NIST | |
Inp | 617.00 | NIST | |
I | [1172.00; 1225.00] |
![]() |
|
I | 1184.00 | NIST | |
I | Outlier 1225.00 | NIST | |
I | 1180.00 | NIST | |
I | 1202.00 | NIST | |
I | 1199.00 | NIST | |
I | 1199.00 | NIST | |
I | 1172.00 | NIST | |
I | 1180.00 | NIST | |
Tboil | [397.30; 397.70] | K |
![]() |
Tboil | 397.63 | K | Isobari... |
Tboil | 397.67 | K | Isobari... |
Tboil | 397.67 | K | Isobari... |
Tboil | 397.58 | K | Evaluat... |
Tboil | 397.60 ± 0.40 | K | NIST |
Tboil | 397.50 ± 0.50 | K | NIST |
Tboil | 397.70 | K | NIST |
Tboil | Outlier 397.30 | K | NIST |
Tboil | 397.65 ± 0.40 | K | NIST |
Tboil | 397.36 ± 0.20 | K | NIST |
Tboil | 397.65 | K | NIST |
Tboil | 397.70 ± 0.50 | K | NIST |
Tboil | 397.60 ± 1.00 | K | NIST |
Tc | [571.00; 597.60] | K |
![]() |
Tc | 597.60 ± 0.20 | K | NIST |
Tc | 571.00 ± 2.00 | K | NIST |
Tfus | 188.05 | K | NIST |
Vc | 0.240 | m3/kmol | Joback Calculated Property |
Vm | 7.93e-05 | m3/mol | Excess ... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [120.54; 151.76] | J/mol×K | [382.64; 545.53] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 120 125 130 135 140 145 150 400 450 500 | ||||
Cp,gas | 120.54 | J/mol×K | 382.64 | Joback Calculated Property |
Cp,gas | 126.06 | J/mol×K | 409.79 | Joback Calculated Property |
Cp,gas | 131.45 | J/mol×K | 436.94 | Joback Calculated Property |
Cp,gas | 136.72 | J/mol×K | 464.08 | Joback Calculated Property |
Cp,gas | 141.87 | J/mol×K | 491.23 | Joback Calculated Property |
Cp,gas | 146.88 | J/mol×K | 518.38 | Joback Calculated Property |
Cp,gas | 151.76 | J/mol×K | 545.53 | Joback Calculated Property |
Cp,liquid | [174.90; 176.60] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 175.38 | J/mol×K | 298.15 | NIST |
Cp,liquid | 176.60 | J/mol×K | 298.15 | NIST |
Cp,liquid | 174.90 | J/mol×K | 298.15 | NIST |
η | [0.0010470; 0.0017080] | Pa×s | [293.15; 318.15] | ![]() |
T(K) Dynamic viscosity (Pa×s) 1.00e-3 1.10e-3 1.20e-3 1.30e-3 1.40e-3 1.50e-3 1.60e-3 1.70e-3 300 310 | ||||
η | 0.0017080 | Pa×s | 293.15 | Relativ... |
η | 0.0015440 | Pa×s | 298.15 | Relativ... |
η | 0.0015430 | Pa×s | 298.15 | Viscosi... |
η | 0.0015920 | Pa×s | 298.15 | Densiti... |
η | 0.0015430 | Pa×s | 298.15 | Density... |
η | 0.0014040 | Pa×s | 303.15 | Relativ... |
η | 0.0012420 | Pa×s | 308.15 | Densiti... |
η | 0.0012560 | Pa×s | 308.15 | Density... |
η | 0.0012570 | Pa×s | 308.15 | Viscosi... |
η | 0.0010470 | Pa×s | 318.15 | Density... |
η | 0.0010510 | Pa×s | 318.15 | Viscosi... |
ΔvapH | [37.54; 43.00] | kJ/mol | [273.00; 397.30] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 37 38 39 40 41 42 43 300 350 400 | ||||
ΔvapH | 41.30 | kJ/mol | 273.00 | NIST |
ΔvapH | 42.90 | kJ/mol | 362.50 | NIST |
ΔvapH | 43.00 | kJ/mol | 371.50 | NIST |
ΔvapH | 42.80 | kJ/mol | 378.00 | NIST |
ΔvapH | 37.54 | kJ/mol | 397.30 | NIST |
Pvap | [15.00; 176.50] | kPa | [346.40; 416.60] | ![]() |
T(K) Vapor pressure (kPa) 0 50 100 150 360 380 400 | ||||
Pvap | 15.00 | kPa | 346.40 | Supplem... |
Pvap | 23.50 | kPa | 356.90 | Supplem... |
Pvap | 28.10 | kPa | 364.15 | Vapor-l... |
Pvap | 32.00 | kPa | 364.70 | Supplem... |
Pvap | 34.20 | kPa | 368.84 | Vapor-l... |
Pvap | 41.30 | kPa | 373.48 | Vapor-l... |
Pvap | 49.00 | kPa | 376.00 | Supplem... |
Pvap | 47.90 | kPa | 377.22 | Vapor-l... |
Pvap | 53.70 | kPa | 380.17 | Vapor-l... |
Pvap | 57.50 | kPa | 380.60 | Supplem... |
Pvap | 60.50 | kPa | 383.30 | Vapor-l... |
Pvap | 66.00 | kPa | 384.50 | Supplem... |
Pvap | 68.60 | kPa | 386.66 | Vapor-l... |
Pvap | 74.50 | kPa | 388.10 | Supplem... |
Pvap | 76.40 | kPa | 389.59 | Vapor-l... |
Pvap | 81.20 | kPa | 391.28 | Vapor-l... |
Pvap | 83.00 | kPa | 391.30 | Supplem... |
Pvap | 88.70 | kPa | 393.75 | Vapor-l... |
Pvap | 91.50 | kPa | 394.40 | Supplem... |
Pvap | 95.30 | kPa | 395.78 | Vapor-l... |
Pvap | 100.00 | kPa | 397.20 | Supplem... |
Pvap | 101.30 | kPa | 397.58 | Evaluat... |
Pvap | 101.30 | kPa | 397.67 | Isobari... |
Pvap | 108.50 | kPa | 400.10 | Supplem... |
Pvap | 117.00 | kPa | 402.60 | Supplem... |
Pvap | 125.50 | kPa | 404.90 | Supplem... |
Pvap | 134.00 | kPa | 407.00 | Supplem... |
Pvap | 142.50 | kPa | 409.10 | Supplem... |
Pvap | 151.00 | kPa | 411.10 | Supplem... |
Pvap | 159.50 | kPa | 412.90 | Supplem... |
Pvap | 168.00 | kPa | 414.70 | Supplem... |
Pvap | 176.50 | kPa | 416.60 | Supplem... |
n0 | [1.39830; 1.40060] | [298.15; 303.15] | ![]() |
|
T(K) Refractive Index 1.4 1.4 1.4 1.4 1.4 300 302 | ||||
n0 | 1.40060 | 298.15 | Isobari... | |
n0 | 1.40020 | 298.15 | Effect ... | |
n0 | 1.40040 | 298.15 | Non-ide... | |
n0 | 1.40040 | 298.15 | Physica... | |
n0 | 1.40020 | 298.15 | Thermod... | |
n0 | 1.40030 | 298.15 | Volumet... | |
n0 | 1.39830 | 303.15 | Densiti... | |
ρl | [898.55; 974.70] | kg/m3 | [283.15; 363.15] | ![]() |
T(K) Liquid Density (kg/m3) 900 920 940 960 980 300 320 340 360 | ||||
ρl | 974.70 | kg/m3 | 283.15 | Solubil... |
ρl | 969.90 | kg/m3 | 288.15 | Solubil... |
ρl | 966.52 | kg/m3 | 291.15 | Density... |
ρl | 964.70 | kg/m3 | 293.15 | Density... |
ρl | 964.86 | kg/m3 | 293.15 | Densiti... |
ρl | 964.88 | kg/m3 | 293.15 | Volumet... |
ρl | 965.20 | kg/m3 | 293.15 | Viscosi... |
ρl | 964.88 | kg/m3 | 293.15 | Density... |
ρl | 964.70 | kg/m3 | 293.15 | Solubil... |
ρl | 964.70 | kg/m3 | 293.15 | Monoeth... |
ρl | 960.32 | kg/m3 | 298.15 | Speeds ... |
ρl | 960.10 | kg/m3 | 298.15 | Monoeth... |
ρl | 960.90 | kg/m3 | 298.15 | Study o... |
ρl | 960.31 | kg/m3 | 298.15 | Density... |
ρl | 960.89 | kg/m3 | 298.15 | Modifie... |
ρl | 960.29 | kg/m3 | 298.15 | Density... |
ρl | 960.10 | kg/m3 | 298.15 | Solubil... |
ρl | 960.29 | kg/m3 | 298.15 | Volumet... |
ρl | 960.10 | kg/m3 | 298.15 | Isobari... |
ρl | 960.32 | kg/m3 | 298.15 | Study o... |
ρl | 960.29 | kg/m3 | 298.15 | FT-IR s... |
ρl | 960.01 | kg/m3 | 298.15 | Excess ... |
ρl | 959.73 | kg/m3 | 298.15 | Liquid ... |
ρl | 960.20 | kg/m3 | 298.15 | Isobari... |
ρl | 960.20 | kg/m3 | 298.15 | Density... |
ρl | 955.76 | kg/m3 | 303.15 | Volumet... |
ρl | 956.73 | kg/m3 | 303.15 | Surface... |
ρl | 955.76 | kg/m3 | 303.15 | Density... |
ρl | 955.50 | kg/m3 | 303.15 | Monoeth... |
ρl | 955.84 | kg/m3 | 303.15 | FT-IR s... |
ρl | 955.68 | kg/m3 | 303.15 | Densiti... |
ρl | 955.50 | kg/m3 | 303.15 | Density... |
ρl | 955.71 | kg/m3 | 303.15 | Density... |
ρl | 955.50 | kg/m3 | 303.15 | Solubil... |
ρl | 955.71 | kg/m3 | 303.15 | Study o... |
ρl | 955.72 | kg/m3 | 303.15 | Intermo... |
ρl | 951.11 | kg/m3 | 308.15 | Intermo... |
ρl | 951.08 | kg/m3 | 308.15 | Study o... |
ρl | 951.10 | kg/m3 | 308.15 | Volumet... |
ρl | 952.09 | kg/m3 | 308.15 | Surface... |
ρl | 951.16 | kg/m3 | 308.15 | FT-IR s... |
ρl | 950.90 | kg/m3 | 308.15 | Solubil... |
ρl | 950.90 | kg/m3 | 308.15 | Monoeth... |
ρl | 951.10 | kg/m3 | 308.15 | Density... |
ρl | 951.70 | kg/m3 | 308.15 | Study o... |
ρl | 951.08 | kg/m3 | 308.15 | Density... |
ρl | 950.90 | kg/m3 | 308.15 | Density... |
ρl | 946.27 | kg/m3 | 313.15 | Intermo... |
ρl | 946.20 | kg/m3 | 313.15 | Density... |
ρl | 946.20 | kg/m3 | 313.15 | Monoeth... |
ρl | 946.20 | kg/m3 | 313.15 | Solubil... |
ρl | 946.54 | kg/m3 | 313.15 | Volumet... |
ρl | 947.42 | kg/m3 | 313.15 | Surface... |
ρl | 946.49 | kg/m3 | 313.15 | FT-IR s... |
ρl | 946.41 | kg/m3 | 313.15 | Density... |
ρl | 946.42 | kg/m3 | 313.15 | Study o... |
ρl | 946.38 | kg/m3 | 313.15 | Densiti... |
ρl | 941.50 | kg/m3 | 318.15 | Density... |
ρl | 942.72 | kg/m3 | 318.15 | Surface... |
ρl | 941.50 | kg/m3 | 318.15 | Solubil... |
ρl | 942.70 | kg/m3 | 318.15 | Study o... |
ρl | 941.50 | kg/m3 | 318.15 | Monoeth... |
ρl | 941.72 | kg/m3 | 318.15 | Density... |
ρl | 941.64 | kg/m3 | 318.15 | Intermo... |
ρl | 941.89 | kg/m3 | 318.15 | FT-IR s... |
ρl | 941.72 | kg/m3 | 318.15 | Study o... |
ρl | 936.95 | kg/m3 | 323.15 | Densiti... |
ρl | 936.88 | kg/m3 | 323.15 | Intermo... |
ρl | 936.70 | kg/m3 | 323.15 | Monoeth... |
ρl | 937.98 | kg/m3 | 323.15 | Surface... |
ρl | 936.70 | kg/m3 | 323.15 | Solubil... |
ρl | 936.89 | kg/m3 | 323.15 | Study o... |
ρl | 936.80 | kg/m3 | 323.15 | Density... |
ρl | 936.99 | kg/m3 | 323.15 | Density... |
ρl | 933.40 | kg/m3 | 328.15 | Study o... |
ρl | 932.00 | kg/m3 | 328.15 | Monoeth... |
ρl | 932.00 | kg/m3 | 328.15 | Solubil... |
ρl | 933.21 | kg/m3 | 328.15 | Surface... |
ρl | 932.00 | kg/m3 | 328.15 | Density... |
ρl | 927.20 | kg/m3 | 333.15 | Density... |
ρl | 928.39 | kg/m3 | 333.15 | Surface... |
ρl | 927.20 | kg/m3 | 333.15 | Monoeth... |
ρl | 927.38 | kg/m3 | 333.15 | Densiti... |
ρl | 927.20 | kg/m3 | 333.15 | Solubil... |
ρl | 923.54 | kg/m3 | 338.15 | Surface... |
ρl | 922.30 | kg/m3 | 338.15 | Monoeth... |
ρl | 922.40 | kg/m3 | 338.15 | Density... |
ρl | 917.40 | kg/m3 | 343.15 | Monoeth... |
ρl | 918.64 | kg/m3 | 343.15 | Surface... |
ρl | 917.64 | kg/m3 | 343.15 | Densiti... |
ρl | 917.50 | kg/m3 | 343.15 | Density... |
ρl | 912.40 | kg/m3 | 348.15 | Monoeth... |
ρl | 912.50 | kg/m3 | 348.15 | Density... |
ρl | 913.69 | kg/m3 | 348.15 | Surface... |
ρl | 908.70 | kg/m3 | 353.15 | Surface... |
ρl | 907.50 | kg/m3 | 353.15 | Density... |
ρl | 907.40 | kg/m3 | 353.15 | Monoeth... |
ρl | 903.65 | kg/m3 | 358.15 | Surface... |
ρl | 898.55 | kg/m3 | 363.15 | Surface... |
csound,fluid | [1260.70; 1380.00] | m/s | [288.15; 323.15] | ![]() |
T(K) Speed of sound in fluid (m/s) 1260 1280 1300 1320 1340 1360 1380 290 300 310 320 | ||||
csound,fluid | 1376.47 | m/s | 288.15 | Densiti... |
csound,fluid | 1380.00 | m/s | 288.15 | Volumet... |
csound,fluid | 1359.04 | m/s | 293.15 | Densiti... |
csound,fluid | 1367.00 | m/s | 293.15 | Volumet... |
csound,fluid | 1351.00 | m/s | 298.15 | Volumet... |
csound,fluid | 1341.72 | m/s | 298.15 | Densiti... |
csound,fluid | 1324.47 | m/s | 303.15 | Densiti... |
csound,fluid | 1337.00 | m/s | 303.15 | Volumet... |
csound,fluid | 1324.20 | m/s | 303.15 | Acousti... |
csound,fluid | 1324.50 | m/s | 303.15 | Densiti... |
csound,fluid | 1312.60 | m/s | 308.15 | Densiti... |
csound,fluid | 1321.00 | m/s | 308.15 | Volumet... |
csound,fluid | 1307.14 | m/s | 308.15 | Densiti... |
csound,fluid | 1289.95 | m/s | 313.15 | Densiti... |
csound,fluid | 1304.00 | m/s | 313.15 | Volumet... |
csound,fluid | 1293.90 | m/s | 313.15 | Acousti... |
csound,fluid | 1299.60 | m/s | 313.15 | Densiti... |
csound,fluid | 1272.81 | m/s | 318.15 | Densiti... |
csound,fluid | 1287.20 | m/s | 318.15 | Densiti... |
csound,fluid | 1287.00 | m/s | 318.15 | Volumet... |
csound,fluid | 1260.70 | m/s | 323.15 | Acousti... |
γ | [0.03; 0.03] | N/m | [298.15; 318.15] | ![]() |
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.03 300 305 310 315 | ||||
γ | 0.03 | N/m | 298.15 | Experim... |
γ | 0.03 | N/m | 298.15 | Excess ... |
γ | 0.03 | N/m | 308.15 | Experim... |
γ | 0.03 | N/m | 313.15 | Excess ... |
γ | 0.03 | N/m | 318.15 | Experim... |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 20000.00 | 0.0019 |
293.15 | 40000.00 | 0.0022 |
293.15 | 60000.00 | 0.0024 |
293.15 | 80000.00 | 0.0027 |
293.15 | 100000.00 | 0.0029 |
303.15 | 20000.00 | 0.0016 |
303.15 | 40000.00 | 0.0018 |
303.15 | 60000.00 | 0.0020 |
303.15 | 80000.00 | 0.0022 |
303.15 | 100000.00 | 0.0024 |
313.15 | 20000.00 | 0.0013 |
313.15 | 40000.00 | 0.0015 |
313.15 | 60000.00 | 0.0016 |
313.15 | 80000.00 | 0.0018 |
313.15 | 100000.00 | 0.0020 |
323.15 | 20000.00 | 0.0011 |
323.15 | 40000.00 | 0.0013 |
323.15 | 60000.00 | 0.0014 |
323.15 | 80000.00 | 0.0015 |
323.15 | 100000.00 | 0.0017 |
333.15 | 20000.00 | 0.0010 |
333.15 | 40000.00 | 0.0011 |
333.15 | 60000.00 | 0.0012 |
333.15 | 80000.00 | 0.0013 |
333.15 | 100000.00 | 0.0015 |
343.15 | 20000.00 | 0.0009 |
343.15 | 40000.00 | 0.0010 |
343.15 | 60000.00 | 0.0011 |
343.15 | 80000.00 | 0.0011 |
343.15 | 100000.00 | 0.0012 |
353.15 | 20000.00 | 0.0007 |
353.15 | 40000.00 | 0.0008 |
353.15 | 60000.00 | 0.0009 |
353.15 | 80000.00 | 0.0010 |
353.15 | 100000.00 | 0.0011 |
Reference |
Fixed | Measured | |
---|---|---|
Pressure, kPa - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
101.00 | 303.15 | 0.0014 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 100.00 | 964.5 |
293.15 | 5000.00 | 967.5 |
293.15 | 10000.00 | 970.7 |
293.15 | 15000.00 | 973.8 |
293.15 | 20000.00 | 976.6 |
293.15 | 25000.00 | 979.5 |
293.15 | 30000.00 | 982.3 |
293.15 | 35000.00 | 985.1 |
293.15 | 40000.00 | 987.7 |
293.15 | 45000.00 | 990.3 |
293.15 | 50000.00 | 992.9 |
293.15 | 55000.00 | 995.3 |
293.15 | 60000.00 | 997.7 |
303.15 | 100.00 | 955.4 |
303.15 | 5000.00 | 958.4 |
303.15 | 10000.00 | 961.8 |
303.15 | 15000.00 | 965.1 |
303.15 | 20000.00 | 968.0 |
303.15 | 25000.00 | 971.1 |
303.15 | 30000.00 | 974.0 |
303.15 | 35000.00 | 976.9 |
303.15 | 40000.00 | 979.6 |
303.15 | 45000.00 | 982.3 |
303.15 | 50000.00 | 984.8 |
303.15 | 55000.00 | 987.5 |
303.15 | 60000.00 | 989.9 |
313.15 | 100.00 | 945.9 |
313.15 | 5000.00 | 949.3 |
313.15 | 10000.00 | 952.7 |
313.15 | 15000.00 | 956.3 |
313.15 | 20000.00 | 959.5 |
313.15 | 25000.00 | 962.5 |
313.15 | 30000.00 | 965.6 |
313.15 | 35000.00 | 968.5 |
313.15 | 40000.00 | 971.5 |
313.15 | 45000.00 | 974.4 |
313.15 | 50000.00 | 977.0 |
313.15 | 55000.00 | 979.5 |
313.15 | 60000.00 | 982.2 |
323.15 | 100.00 | 936.3 |
323.15 | 5000.00 | 940.2 |
323.15 | 10000.00 | 943.9 |
323.15 | 15000.00 | 947.4 |
323.15 | 20000.00 | 950.8 |
323.15 | 25000.00 | 954.0 |
323.15 | 30000.00 | 957.2 |
323.15 | 35000.00 | 960.5 |
323.15 | 40000.00 | 963.3 |
323.15 | 45000.00 | 966.3 |
323.15 | 50000.00 | 969.1 |
323.15 | 55000.00 | 971.9 |
323.15 | 60000.00 | 974.6 |
333.15 | 100.00 | 926.7 |
333.15 | 5000.00 | 930.9 |
333.15 | 10000.00 | 934.6 |
333.15 | 15000.00 | 938.4 |
333.15 | 20000.00 | 941.9 |
333.15 | 25000.00 | 945.3 |
333.15 | 30000.00 | 948.8 |
333.15 | 35000.00 | 952.0 |
333.15 | 40000.00 | 955.0 |
333.15 | 45000.00 | 958.0 |
333.15 | 50000.00 | 961.0 |
333.15 | 55000.00 | 963.9 |
333.15 | 60000.00 | 966.8 |
343.15 | 100.00 | 917.1 |
343.15 | 5000.00 | 921.2 |
343.15 | 10000.00 | 925.3 |
343.15 | 15000.00 | 929.3 |
343.15 | 20000.00 | 932.9 |
343.15 | 25000.00 | 936.9 |
343.15 | 30000.00 | 940.2 |
343.15 | 35000.00 | 943.6 |
343.15 | 40000.00 | 946.8 |
343.15 | 45000.00 | 950.0 |
343.15 | 50000.00 | 953.1 |
343.15 | 55000.00 | 956.2 |
343.15 | 60000.00 | 959.0 |
353.15 | 100.00 | 907.1 |
353.15 | 5000.00 | 911.7 |
353.15 | 10000.00 | 916.1 |
353.15 | 15000.00 | 920.1 |
353.15 | 20000.00 | 924.0 |
353.15 | 25000.00 | 927.9 |
353.15 | 30000.00 | 931.5 |
353.15 | 35000.00 | 934.9 |
353.15 | 40000.00 | 938.7 |
353.15 | 45000.00 | 941.8 |
353.15 | 50000.00 | 945.1 |
353.15 | 55000.00 | 948.2 |
353.15 | 60000.00 | 951.2 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [300.92; 419.45] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.75122e+01 | |||
Coefficient B | -4.95806e+03 | |||
Coefficient C | -1.30710e+01 | |||
Temperature range, min. | 300.92 | |||
Temperature range, max. | 419.45 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 300.92 | Calculated Property |
Pvap | 2.83 | kPa | 314.09 | Calculated Property |
Pvap | 5.65 | kPa | 327.26 | Calculated Property |
Pvap | 10.66 | kPa | 340.43 | Calculated Property |
Pvap | 19.15 | kPa | 353.60 | Calculated Property |
Pvap | 32.93 | kPa | 366.77 | Calculated Property |
Pvap | 54.47 | kPa | 379.94 | Calculated Property |
Pvap | 87.01 | kPa | 393.11 | Calculated Property |
Pvap | 134.69 | kPa | 406.28 | Calculated Property |
Pvap | 202.67 | kPa | 419.45 | Calculated Property |
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