Property | Value | Unit | Source |
---|---|---|---|
PAff | 923.20 | kJ/mol | NIST |
BasG | [879.50; 889.30] | kJ/mol |
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BasG | 889.30 | kJ/mol | NIST |
BasG | 879.50 ± 9.20 | kJ/mol | NIST |
ΔcH°liquid | -4949.70 | kJ/mol | NIST |
ΔfG° | 74.51 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -216.00 | kJ/mol | NIST |
ΔfH°liquid | -266.00 | kJ/mol | NIST |
ΔfusH° | 19.08 | kJ/mol | Joback Calculated Property |
ΔvapH° | [49.90; 50.00] | kJ/mol |
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ΔvapH° | 49.98 | kJ/mol | NIST |
ΔvapH° | 49.90 | kJ/mol | NIST |
ΔvapH° | 50.00 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 49.96 ± 0.08 | kJ/mol | NIST |
log10WS | -1.85 | Aq. Sol... | |
logPoct/wat | 1.915 | Crippen Calculated Property | |
McVol | 119.470 | ml/mol | McGowan Calculated Property |
Pc | 2976.29 | kPa | Joback Calculated Property |
Inp | [912.00; 943.20] |
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|
Inp | 928.00 | NIST | |
Inp | 943.20 | NIST | |
Inp | Outlier 918.00 | NIST | |
Inp | 932.00 | NIST | |
Inp | 932.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 934.00 | NIST | |
Inp | 934.00 | NIST | |
Inp | 935.00 | NIST | |
Inp | 930.00 | NIST | |
Inp | 931.00 | NIST | |
Inp | 932.00 | NIST | |
Inp | 932.00 | NIST | |
Inp | 932.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 931.00 | NIST | |
Inp | 932.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 934.00 | NIST | |
Inp | 935.00 | NIST | |
Inp | 939.00 | NIST | |
Inp | 931.00 | NIST | |
Inp | 931.00 | NIST | |
Inp | 930.00 | NIST | |
Inp | 942.00 | NIST | |
Inp | Outlier 912.00 | NIST | |
Inp | 930.00 | NIST | |
Inp | 937.00 | NIST | |
Inp | 941.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 934.00 | NIST | |
Inp | 935.00 | NIST | |
Inp | 932.00 | NIST | |
Inp | 942.00 | NIST | |
I | [1213.00; 1223.00] |
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|
I | 1220.00 | NIST | |
I | 1219.00 | NIST | |
I | 1223.00 | NIST | |
I | 1215.00 | NIST | |
I | 1217.00 | NIST | |
I | 1215.00 | NIST | |
I | 1218.00 | NIST | |
I | 1213.00 | NIST | |
Tboil | 432.09 | K | Joback Calculated Property |
Tc | 610.78 | K | Joback Calculated Property |
Tfus | [250.15; 253.48] | K |
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Tfus | 253.48 | K | Aq. Sol... |
Tfus | 250.15 ± 0.60 | K | NIST |
Vc | 0.457 | m3/kmol | Joback Calculated Property |
Vm | 1.50e-04 | m3/mol | Thermod... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [250.70; 318.89] | J/mol×K | [432.09; 610.78] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 250 260 270 280 290 300 310 320 450 500 550 600 | ||||
Cp,gas | 250.70 | J/mol×K | 432.09 | Joback Calculated Property |
Cp,gas | 263.29 | J/mol×K | 461.87 | Joback Calculated Property |
Cp,gas | 275.37 | J/mol×K | 491.65 | Joback Calculated Property |
Cp,gas | 286.95 | J/mol×K | 521.43 | Joback Calculated Property |
Cp,gas | 298.06 | J/mol×K | 551.21 | Joback Calculated Property |
Cp,gas | 308.70 | J/mol×K | 581.00 | Joback Calculated Property |
Cp,gas | 318.89 | J/mol×K | 610.78 | Joback Calculated Property |
ΔvapH | 46.50 | kJ/mol | 378.00 | NIST |
Pvap | [0.08; 0.50] | kPa | [280.20; 306.20] | ![]() |
T(K) Vapor pressure (kPa) 0.1 0.2 0.3 0.4 0.5 280 290 300 | ||||
Pvap | 0.08 | kPa | 280.20 | The Vap... |
Pvap | 0.09 | kPa | 282.20 | The Vap... |
Pvap | 0.11 | kPa | 284.20 | The Vap... |
Pvap | 0.12 | kPa | 286.20 | The Vap... |
Pvap | 0.14 | kPa | 288.20 | The Vap... |
Pvap | 0.16 | kPa | 290.20 | The Vap... |
Pvap | 0.19 | kPa | 292.20 | The Vap... |
Pvap | 0.22 | kPa | 294.20 | The Vap... |
Pvap | 0.25 | kPa | 296.20 | The Vap... |
Pvap | 0.29 | kPa | 298.30 | The Vap... |
Pvap | 0.33 | kPa | 300.30 | The Vap... |
Pvap | 0.38 | kPa | 302.20 | The Vap... |
Pvap | 0.41 | kPa | 303.20 | The Vap... |
Pvap | 0.50 | kPa | 306.20 | The Vap... |
Fixed | Measured | |
---|---|---|
Pressure, kPa - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
100.00 | 293.15 | 0.0011 |
100.00 | 313.15 | 0.0008 |
100.00 | 333.15 | 0.0006 |
100.00 | 353.15 | 0.0005 |
20000.00 | 293.15 | 0.0013 |
20000.00 | 313.15 | 0.0009 |
20000.00 | 333.15 | 0.0007 |
20000.00 | 353.15 | 0.0006 |
40000.00 | 293.15 | 0.0015 |
40000.00 | 313.15 | 0.0011 |
40000.00 | 333.15 | 0.0008 |
40000.00 | 353.15 | 0.0007 |
60000.00 | 293.15 | 0.0018 |
60000.00 | 313.15 | 0.0013 |
60000.00 | 333.15 | 0.0010 |
60000.00 | 353.15 | 0.0008 |
80000.00 | 293.15 | 0.0021 |
80000.00 | 313.15 | 0.0015 |
80000.00 | 333.15 | 0.0011 |
80000.00 | 353.15 | 0.0009 |
100000.00 | 293.15 | 0.0024 |
100000.00 | 313.15 | 0.0017 |
100000.00 | 333.15 | 0.0012 |
100000.00 | 353.15 | 0.0010 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 100.00 | 774.9 |
293.15 | 10000.00 | 781.1 |
293.15 | 20000.00 | 787.1 |
293.15 | 30000.00 | 792.6 |
293.15 | 40000.00 | 797.8 |
293.15 | 50000.00 | 802.7 |
293.15 | 60000.00 | 807.4 |
293.15 | 70000.00 | 811.8 |
293.15 | 80000.00 | 816.1 |
293.15 | 90000.00 | 820.2 |
293.15 | 100000.00 | 824.0 |
293.15 | 110000.00 | 827.8 |
293.15 | 120000.00 | 831.5 |
293.15 | 130000.00 | 835.0 |
293.15 | 140000.00 | 838.3 |
303.15 | 100.00 | 766.5 |
303.15 | 10000.00 | 773.6 |
303.15 | 20000.00 | 780.0 |
303.15 | 30000.00 | 785.8 |
303.15 | 40000.00 | 791.3 |
303.15 | 50000.00 | 796.5 |
303.15 | 60000.00 | 801.3 |
303.15 | 70000.00 | 806.0 |
303.15 | 80000.00 | 810.4 |
303.15 | 90000.00 | 814.6 |
303.15 | 100000.00 | 818.7 |
303.15 | 110000.00 | 822.5 |
303.15 | 120000.00 | 826.2 |
303.15 | 130000.00 | 829.9 |
303.15 | 140000.00 | 833.3 |
313.15 | 100.00 | 758.2 |
313.15 | 10000.00 | 765.4 |
313.15 | 20000.00 | 772.0 |
313.15 | 30000.00 | 778.2 |
313.15 | 40000.00 | 784.0 |
313.15 | 50000.00 | 789.3 |
313.15 | 60000.00 | 794.5 |
313.15 | 70000.00 | 799.2 |
313.15 | 80000.00 | 803.7 |
313.15 | 90000.00 | 808.0 |
313.15 | 100000.00 | 812.2 |
313.15 | 110000.00 | 816.2 |
313.15 | 120000.00 | 820.1 |
313.15 | 130000.00 | 823.8 |
313.15 | 140000.00 | 827.4 |
323.15 | 100.00 | 749.8 |
323.15 | 10000.00 | 757.6 |
323.15 | 20000.00 | 764.5 |
323.15 | 30000.00 | 771.0 |
323.15 | 40000.00 | 777.0 |
323.15 | 50000.00 | 782.6 |
323.15 | 60000.00 | 787.8 |
323.15 | 70000.00 | 792.7 |
323.15 | 80000.00 | 797.5 |
323.15 | 90000.00 | 802.0 |
323.15 | 100000.00 | 806.3 |
323.15 | 110000.00 | 810.6 |
323.15 | 120000.00 | 814.5 |
323.15 | 130000.00 | 818.4 |
323.15 | 140000.00 | 822.1 |
333.15 | 100.00 | 741.4 |
333.15 | 10000.00 | 749.5 |
333.15 | 20000.00 | 756.8 |
333.15 | 30000.00 | 763.4 |
333.15 | 40000.00 | 769.6 |
333.15 | 50000.00 | 775.5 |
333.15 | 60000.00 | 780.9 |
333.15 | 70000.00 | 786.2 |
333.15 | 80000.00 | 791.1 |
333.15 | 90000.00 | 795.6 |
333.15 | 100000.00 | 800.0 |
333.15 | 110000.00 | 804.3 |
333.15 | 120000.00 | 808.4 |
333.15 | 130000.00 | 812.4 |
333.15 | 140000.00 | 816.2 |
343.15 | 100.00 | 732.6 |
343.15 | 10000.00 | 741.7 |
343.15 | 20000.00 | 749.6 |
343.15 | 30000.00 | 756.7 |
343.15 | 40000.00 | 763.3 |
343.15 | 50000.00 | 769.4 |
343.15 | 60000.00 | 775.1 |
343.15 | 70000.00 | 780.4 |
343.15 | 80000.00 | 785.5 |
343.15 | 90000.00 | 790.3 |
343.15 | 100000.00 | 794.9 |
343.15 | 110000.00 | 799.2 |
343.15 | 120000.00 | 803.3 |
343.15 | 130000.00 | 807.4 |
343.15 | 140000.00 | 811.3 |
353.15 | 100.00 | 724.4 |
353.15 | 10000.00 | 733.7 |
353.15 | 20000.00 | 741.9 |
353.15 | 30000.00 | 749.3 |
353.15 | 40000.00 | 756.2 |
353.15 | 50000.00 | 762.6 |
353.15 | 60000.00 | 768.7 |
353.15 | 70000.00 | 774.2 |
353.15 | 80000.00 | 779.5 |
353.15 | 90000.00 | 784.3 |
353.15 | 100000.00 | 789.2 |
353.15 | 110000.00 | 793.7 |
353.15 | 120000.00 | 797.9 |
353.15 | 130000.00 | 802.1 |
353.15 | 140000.00 | 806.1 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [326.04; 453.39] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.57790e+01 | |||
Coefficient B | -4.11042e+03 | |||
Coefficient C | -6.07040e+01 | |||
Temperature range, min. | 326.04 | |||
Temperature range, max. | 453.39 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 326.04 | Calculated Property |
Pvap | 2.92 | kPa | 340.19 | Calculated Property |
Pvap | 5.93 | kPa | 354.34 | Calculated Property |
Pvap | 11.29 | kPa | 368.49 | Calculated Property |
Pvap | 20.31 | kPa | 382.64 | Calculated Property |
Pvap | 34.77 | kPa | 396.79 | Calculated Property |
Pvap | 56.99 | kPa | 410.94 | Calculated Property |
Pvap | 89.89 | kPa | 425.09 | Calculated Property |
Pvap | 137.04 | kPa | 439.24 | Calculated Property |
Pvap | 202.66 | kPa | 453.39 | Calculated Property |
Pvap | [9.62e-03; 2866.79] | kPa | [254.15; 607.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.39695e+02 | |||
Coefficient B | -1.08451e+04 | |||
Coefficient C | -1.85086e+01 | |||
Coefficient D | 1.28802e-05 | |||
Temperature range, min. | 254.15 | |||
Temperature range, max. | 607.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 300 400 500 600 | ||||
Pvap | 9.62e-03 | kPa | 254.15 | Calculated Property |
Pvap | 0.27 | kPa | 293.36 | Calculated Property |
Pvap | 2.81 | kPa | 332.56 | Calculated Property |
Pvap | 15.87 | kPa | 371.77 | Calculated Property |
Pvap | 59.56 | kPa | 410.97 | Calculated Property |
Pvap | 169.62 | kPa | 450.18 | Calculated Property |
Pvap | 400.39 | kPa | 489.38 | Calculated Property |
Pvap | 831.96 | kPa | 528.59 | Calculated Property |
Pvap | 1587.38 | kPa | 567.79 | Calculated Property |
Pvap | 2866.79 | kPa | 607.00 | Calculated Property |
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