Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -218.74 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -813.79 | kJ/mol | Joback Calculated Property |
ΔfusH° | 50.10 | kJ/mol | Joback Calculated Property |
ΔvapH° | 89.49 | kJ/mol | Joback Calculated Property |
log10WS | [-7.06; -6.96] |
![]() |
|
log10WS | -7.06 | Aq. Sol... | |
log10WS | -6.96 | Estimat... | |
logPoct/wat | 6.433 | Crippen Calculated Property | |
McVol | 340.140 | ml/mol | McGowan Calculated Property |
Pc | 1070.00 | kPa | Critica... |
Inp | [402.20; 2552.00] |
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|
Inp | 2492.60 | NIST | |
Inp | 2509.00 | NIST | |
Inp | 2507.00 | NIST | |
Inp | 2499.40 | NIST | |
Inp | 2499.00 | NIST | |
Inp | 2499.00 | NIST | |
Inp | 2505.00 | NIST | |
Inp | 2546.00 | NIST | |
Inp | 2488.00 | NIST | |
Inp | 2498.00 | NIST | |
Inp | 2552.00 | NIST | |
Inp | 2539.00 | NIST | |
Inp | 2544.00 | NIST | |
Inp | 2551.00 | NIST | |
Inp | 2509.00 | NIST | |
Inp | 2550.00 | NIST | |
Inp | 2519.00 | NIST | |
Inp | 2504.00 | NIST | |
Inp | 2505.00 | NIST | |
Inp | 2506.00 | NIST | |
Inp | 2480.00 | NIST | |
Inp | 2505.00 | NIST | |
Inp | 2506.00 | NIST | |
Inp | 2509.00 | NIST | |
Inp | 2506.00 | NIST | |
Inp | 2507.00 | NIST | |
Inp | Outlier 418.60 | NIST | |
Inp | Outlier 418.70 | NIST | |
Inp | Outlier 402.20 | NIST | |
Inp | Outlier 406.14 | NIST | |
Inp | Outlier 406.15 | NIST | |
Inp | 2488.00 | NIST | |
Inp | 2505.00 | NIST | |
Inp | 2492.60 | NIST | |
Inp | Outlier 418.60 | NIST | |
Inp | 2499.40 | NIST | |
Inp | 2507.00 | NIST | |
Inp | Outlier 406.14 | NIST | |
Inp | 2539.00 | NIST | |
Inp | 2519.00 | NIST | |
I | [3106.00; 3106.00] |
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|
I | 3106.00 | NIST | |
I | 3106.00 | NIST | |
I | 3106.00 | NIST | |
I | 3106.00 | NIST | |
I | 3106.00 | NIST | |
S°liquid | [755.20; 807.70] | J/mol×K |
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S°liquid | 807.70 | J/mol×K | NIST |
S°liquid | 755.20 | J/mol×K | NIST |
Tboil | 657.20 | K | NIST |
Tc | 1142.43 | K | Joback Calculated Property |
Tfus | 219.82 | K | Aq. Sol... |
Vc | 1.308 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [1120.29; 1202.19] | J/mol×K | [931.88; 1142.43] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 1120 1140 1160 1180 1200 950 1000 1050 1100 | ||||
Cp,gas | 1120.29 | J/mol×K | 931.88 | Joback Calculated Property |
Cp,gas | 1137.32 | J/mol×K | 966.97 | Joback Calculated Property |
Cp,gas | 1152.94 | J/mol×K | 1002.06 | Joback Calculated Property |
Cp,gas | 1167.20 | J/mol×K | 1037.16 | Joback Calculated Property |
Cp,gas | 1180.14 | J/mol×K | 1072.25 | Joback Calculated Property |
Cp,gas | 1191.79 | J/mol×K | 1107.34 | Joback Calculated Property |
Cp,gas | 1202.19 | J/mol×K | 1142.43 | Joback Calculated Property |
Cp,liquid | [669.40; 704.70] | J/mol×K | [298.15; 300.00] | ![]() |
Cp,liquid | 704.70 | J/mol×K | 298.15 | NIST |
Cp,liquid | 669.40 | J/mol×K | 300.00 | NIST |
η | [0.0061990; 0.1107000] | Pa×s | [288.53; 353.68] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 0.02 0.04 0.06 0.08 0.1 0.12 300 320 340 | ||||
η | 0.1107000 | Pa×s | 288.53 | Measure... |
η | 0.0787300 | Pa×s | 293.38 | Measure... |
η | 0.0579400 | Pa×s | 298.29 | Measure... |
η | 0.0432700 | Pa×s | 303.33 | Measure... |
η | 0.0331700 | Pa×s | 308.23 | Measure... |
η | 0.0261300 | Pa×s | 313.18 | Measure... |
η | 0.0210800 | Pa×s | 317.99 | Measure... |
η | 0.0169600 | Pa×s | 323.02 | Measure... |
η | 0.0139100 | Pa×s | 328.12 | Measure... |
η | 0.0116200 | Pa×s | 333.19 | Measure... |
η | 0.0099030 | Pa×s | 337.71 | Measure... |
η | 0.0082680 | Pa×s | 343.53 | Measure... |
η | 0.0071580 | Pa×s | 348.48 | Measure... |
η | 0.0061990 | Pa×s | 353.68 | Measure... |
ΔvapH | [102.50; 116.90] | kJ/mol | [298.00; 516.50] | ![]() |
ΔvapH | 116.90 | kJ/mol | 298.00 | A Compa... |
ΔvapH | 110.70 | kJ/mol | 412.50 | NIST |
ΔvapH | 102.50 | kJ/mol | 516.50 | NIST |
Pvap | [8.00e-03; 0.19] | kPa | [423.15; 473.15] | ![]() |
T(K) Vapor pressure (kPa) 0 0.05 0.1 0.15 0.2 440 460 | ||||
Pvap | 8.00e-03 | kPa | 423.15 | Vapor P... |
Pvap | 0.02 | kPa | 433.15 | Vapor P... |
Pvap | 0.03 | kPa | 443.15 | Vapor P... |
Pvap | 0.04 | kPa | 448.15 | Vapor P... |
Pvap | 0.07 | kPa | 453.15 | Vapor P... |
Pvap | 0.12 | kPa | 463.15 | Vapor P... |
Pvap | 0.19 | kPa | 473.15 | Vapor P... |
ρl | [931.85; 998.82] | kg/m3 | [273.15; 363.15] | ![]() |
T(K) Liquid Density (kg/m3) 930 940 950 960 970 980 990 1000 300 350 | ||||
ρl | 998.82 | kg/m3 | 273.15 | Tempera... |
ρl | 995.01 | kg/m3 | 278.15 | Tempera... |
ρl | 991.26 | kg/m3 | 283.15 | Tempera... |
ρl | 983.87 | kg/m3 | 293.15 | Tempera... |
ρl | 980.15 | kg/m3 | 298.15 | Tempera... |
ρl | 976.42 | kg/m3 | 303.15 | Tempera... |
ρl | 968.98 | kg/m3 | 313.15 | Tempera... |
ρl | 961.53 | kg/m3 | 323.15 | Tempera... |
ρl | 954.11 | kg/m3 | 333.15 | Tempera... |
ρl | 946.68 | kg/m3 | 343.15 | Tempera... |
ρl | 939.27 | kg/m3 | 353.15 | Tempera... |
ρl | 931.85 | kg/m3 | 363.15 | Tempera... |
D*i | [0.00; 0.00] | m2/s | [303.18; 362.75] | ![]() |
T(K) Self diffusion coefficient (m2/s) 5.00e-11 1.00e-10 1.50e-10 320 340 360 | ||||
D*i | 0.00 | m2/s | 303.18 | Viscous... |
D*i | 0.00 | m2/s | 312.89 | Viscous... |
D*i | 0.00 | m2/s | 322.70 | Viscous... |
D*i | 0.00 | m2/s | 322.84 | Viscous... |
D*i | 0.00 | m2/s | 322.88 | Viscous... |
D*i | 0.00 | m2/s | 323.03 | Viscous... |
D*i | 0.00 | m2/s | 323.05 | Viscous... |
D*i | 0.00 | m2/s | 333.16 | Viscous... |
D*i | 0.00 | m2/s | 333.20 | Viscous... |
D*i | 0.00 | m2/s | 343.65 | Viscous... |
D*i | 0.00 | m2/s | 343.70 | Viscous... |
D*i | 0.00 | m2/s | 352.86 | Viscous... |
D*i | 0.00 | m2/s | 352.88 | Viscous... |
D*i | 0.00 | m2/s | 362.72 | Viscous... |
D*i | 0.00 | m2/s | 362.75 | Viscous... |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
293.15 | 100.00 | 703.00 |
293.15 | 10000.00 | 701.50 |
293.15 | 20000.00 | 699.90 |
293.15 | 30000.00 | 699.60 |
313.15 | 100.00 | 726.90 |
313.15 | 10000.00 | 724.90 |
313.15 | 20000.00 | 723.00 |
313.15 | 30000.00 | 722.00 |
333.15 | 100.00 | 751.30 |
333.15 | 10000.00 | 750.00 |
333.15 | 20000.00 | 747.50 |
333.15 | 30000.00 | 746.00 |
353.15 | 100.00 | 774.50 |
353.15 | 10000.00 | 770.50 |
353.15 | 20000.00 | 767.90 |
353.15 | 30000.00 | 763.40 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
373.29 | 3800.00 | 921.0 |
373.29 | 7600.00 | 924.0 |
373.29 | 12200.00 | 928.0 |
373.29 | 15900.00 | 931.0 |
373.29 | 18100.00 | 933.0 |
373.29 | 22300.00 | 936.0 |
373.29 | 28300.00 | 940.0 |
373.29 | 34800.00 | 945.0 |
373.29 | 42200.00 | 950.0 |
373.29 | 48900.00 | 954.0 |
373.29 | 56100.00 | 959.0 |
373.29 | 69500.00 | 967.0 |
373.29 | 83700.00 | 974.0 |
373.29 | 104200.00 | 984.0 |
373.29 | 125400.00 | 994.0 |
373.29 | 138900.00 | 1001.0 |
373.29 | 152900.00 | 1007.0 |
373.29 | 174400.00 | 1015.0 |
373.29 | 208300.00 | 1029.0 |
373.29 | 240000.00 | 1041.0 |
373.29 | 262100.00 | 1046.0 |
423.53 | 4200.00 | 878.0 |
423.53 | 7900.00 | 885.0 |
423.53 | 11100.00 | 890.0 |
423.53 | 14500.00 | 895.0 |
423.53 | 18000.00 | 898.0 |
423.53 | 21200.00 | 901.0 |
423.53 | 27800.00 | 908.0 |
423.53 | 35200.00 | 914.0 |
423.53 | 42100.00 | 918.0 |
423.53 | 49200.00 | 924.0 |
423.53 | 55700.00 | 930.0 |
423.53 | 70700.00 | 939.0 |
423.53 | 83700.00 | 948.0 |
423.53 | 104200.00 | 960.0 |
423.53 | 125400.00 | 970.0 |
423.53 | 139900.00 | 977.0 |
423.53 | 153700.00 | 983.0 |
423.53 | 173400.00 | 992.0 |
423.53 | 207100.00 | 1006.0 |
423.53 | 239400.00 | 1018.0 |
423.53 | 263800.00 | 1028.0 |
476.20 | 5500.00 | 847.0 |
476.20 | 9500.00 | 853.0 |
476.20 | 9400.00 | 853.0 |
476.20 | 15700.00 | 861.0 |
476.20 | 15200.00 | 861.0 |
476.20 | 15200.00 | 861.0 |
476.20 | 27500.00 | 874.0 |
476.20 | 27300.00 | 874.0 |
476.20 | 26800.00 | 874.0 |
476.20 | 46900.00 | 894.0 |
476.20 | 46700.00 | 894.0 |
476.20 | 59800.00 | 905.0 |
476.20 | 71500.00 | 913.0 |
476.20 | 70700.00 | 914.0 |
476.20 | 96400.00 | 931.0 |
476.20 | 95700.00 | 931.0 |
476.20 | 114800.00 | 942.0 |
476.20 | 114200.00 | 942.0 |
476.20 | 140400.00 | 958.0 |
476.20 | 139800.00 | 959.0 |
476.20 | 176200.00 | 975.0 |
476.20 | 206900.00 | 990.0 |
476.20 | 240200.00 | 1002.0 |
476.20 | 269000.00 | 1013.0 |
491.86 | 3900.00 | 830.0 |
491.86 | 4100.00 | 830.0 |
491.86 | 3900.00 | 831.0 |
491.86 | 10500.00 | 839.0 |
491.86 | 9900.00 | 840.0 |
491.86 | 23300.00 | 856.0 |
491.86 | 23300.00 | 856.0 |
491.86 | 22800.00 | 856.0 |
491.86 | 37500.00 | 870.0 |
491.86 | 37200.00 | 870.0 |
491.86 | 51100.00 | 885.0 |
491.86 | 50700.00 | 886.0 |
491.86 | 71500.00 | 902.0 |
491.86 | 71900.00 | 902.0 |
491.86 | 95000.00 | 918.0 |
491.86 | 94800.00 | 918.0 |
491.86 | 121700.00 | 934.0 |
491.86 | 121800.00 | 934.0 |
491.86 | 145400.00 | 948.0 |
491.86 | 145600.00 | 948.0 |
491.86 | 177200.00 | 964.0 |
491.86 | 177400.00 | 964.0 |
491.86 | 204300.00 | 977.0 |
491.86 | 206000.00 | 978.0 |
491.86 | 230800.00 | 988.0 |
491.86 | 229400.00 | 989.0 |
491.86 | 253700.00 | 998.0 |
491.86 | 258100.00 | 1000.0 |
523.60 | 5700.00 | 811.0 |
523.60 | 9200.00 | 817.0 |
523.60 | 9200.00 | 817.0 |
523.60 | 16100.00 | 827.0 |
523.60 | 16100.00 | 827.0 |
523.60 | 21600.00 | 835.0 |
523.60 | 21600.00 | 835.0 |
523.60 | 27500.00 | 842.0 |
523.60 | 27300.00 | 842.0 |
523.60 | 35700.00 | 851.0 |
523.60 | 35500.00 | 851.0 |
523.60 | 44400.00 | 860.0 |
523.60 | 44600.00 | 860.0 |
523.60 | 44300.00 | 860.0 |
523.60 | 44200.00 | 860.0 |
523.60 | 56300.00 | 871.0 |
523.60 | 55800.00 | 871.0 |
523.60 | 68900.00 | 882.0 |
523.60 | 68500.00 | 882.0 |
523.60 | 82500.00 | 892.0 |
523.60 | 82200.00 | 893.0 |
523.60 | 97300.00 | 903.0 |
523.60 | 97000.00 | 903.0 |
523.60 | 117000.00 | 916.0 |
523.60 | 117700.00 | 916.0 |
523.60 | 117400.00 | 916.0 |
523.60 | 155700.00 | 939.0 |
523.60 | 156100.00 | 939.0 |
523.60 | 181500.00 | 952.0 |
523.60 | 181200.00 | 952.0 |
523.60 | 209500.00 | 964.0 |
523.60 | 209900.00 | 964.0 |
523.60 | 233900.00 | 974.0 |
523.60 | 234000.00 | 974.0 |
523.60 | 253600.00 | 983.0 |
523.60 | 253400.00 | 983.0 |
523.60 | 263500.00 | 987.0 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [512.02; 762.10] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.26088e+01 | |||
Coefficient B | -4.47566e+03 | |||
Coefficient C | -1.48765e+02 | |||
Temperature range, min. | 512.02 | |||
Temperature range, max. | 762.10 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 600 700 | ||||
Pvap | 1.33 | kPa | 512.02 | Calculated Property |
Pvap | 3.20 | kPa | 539.81 | Calculated Property |
Pvap | 6.84 | kPa | 567.59 | Calculated Property |
Pvap | 13.30 | kPa | 595.38 | Calculated Property |
Pvap | 23.91 | kPa | 623.17 | Calculated Property |
Pvap | 40.30 | kPa | 650.95 | Calculated Property |
Pvap | 64.31 | kPa | 678.74 | Calculated Property |
Pvap | 97.95 | kPa | 706.53 | Calculated Property |
Pvap | 143.34 | kPa | 734.31 | Calculated Property |
Pvap | 202.65 | kPa | 762.10 | Calculated Property |
Pvap | [9.39e-09; 1155.41] | kPa | [298.00; 806.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.60562e+02 | |||
Coefficient B | -2.04275e+04 | |||
Coefficient C | -1.94419e+01 | |||
Coefficient D | 2.98773e-06 | |||
Temperature range, min. | 298.00 | |||
Temperature range, max. | 806.00 | |||
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 400 600 800 | ||||
Pvap | 9.39e-09 | kPa | 298.00 | Calculated Property |
Pvap | 1.98e-05 | kPa | 354.44 | Calculated Property |
Pvap | 3.50e-03 | kPa | 410.89 | Calculated Property |
Pvap | 0.13 | kPa | 467.33 | Calculated Property |
Pvap | 1.92 | kPa | 523.78 | Calculated Property |
Pvap | 14.08 | kPa | 580.22 | Calculated Property |
Pvap | 64.50 | kPa | 636.67 | Calculated Property |
Pvap | 211.11 | kPa | 693.11 | Calculated Property |
Pvap | 540.72 | kPa | 749.56 | Calculated Property |
Pvap | 1155.41 | kPa | 806.00 | Calculated Property |
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