Property | Value | Unit | Source |
---|---|---|---|
ω | 0.9400 | KDB | |
ΔcH°liquid | -7253.70 ± 0.80 | kJ/mol | NIST |
ΔfG° | -95.08 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -422.60 | kJ/mol | Joback Calculated Property |
ΔfH°liquid | -504.90 ± 0.80 | kJ/mol | NIST |
ΔfusH° | 28.33 | kJ/mol | Joback Calculated Property |
ΔvapH° | [83.50; 86.80] | kJ/mol | |
ΔvapH° | 85.80 ± 2.10 | kJ/mol | NIST |
ΔvapH° | 84.70 | kJ/mol | NIST |
ΔvapH° | 83.50 | kJ/mol | NIST |
ΔvapH° | 86.80 | kJ/mol | NIST |
ΔvapH° | 85.60 | kJ/mol | NIST |
log10WS | -3.69 | Crippen Calculated Property | |
logPoct/wat | 3.509 | Crippen Calculated Property | |
McVol | 171.720 | ml/mol | McGowan Calculated Property |
Pc | [2147.00; 2150.00] | kPa | |
Pc | 2147.00 | kPa | KDB |
Pc | 2150.00 ± 50.00 | kPa | NIST |
Pc | 2147.00 ± 30.00 | kPa | NIST |
Pc | 2147.00 ± 30.00 | kPa | NIST |
ρc | [239.51; 239.51] | kg/m3 | |
ρc | 239.51 ± 8.62 | kg/m3 | NIST |
ρc | 239.51 | kg/m3 | NIST |
ρc | 239.51 ± 5.17 | kg/m3 | NIST |
Inp | [233.42; 1387.00] | ||
Inp | 1355.10 | NIST | |
Inp | 1359.91 | NIST | |
Inp | 1371.50 | NIST | |
Inp | 1370.50 | NIST | |
Inp | 1363.00 | NIST | |
Inp | 1363.30 | NIST | |
Inp | 1364.30 | NIST | |
Inp | 1380.40 | NIST | |
Inp | 1356.40 | NIST | |
Inp | 1349.00 | NIST | |
Inp | 1347.00 | NIST | |
Inp | 1348.00 | NIST | |
Inp | 1349.00 | NIST | |
Inp | 1350.00 | NIST | |
Inp | 1348.00 | NIST | |
Inp | 1348.00 | NIST | |
Inp | 1366.00 | NIST | |
Inp | 1379.00 | NIST | |
Inp | 1360.00 | NIST | |
Inp | 1361.00 | NIST | |
Inp | 1370.00 | NIST | |
Inp | 1370.00 | NIST | |
Inp | 1356.00 | NIST | |
Inp | 1373.70 | NIST | |
Inp | 1355.00 | NIST | |
Inp | 1358.00 | NIST | |
Inp | 1361.00 | NIST | |
Inp | 1370.00 | NIST | |
Inp | 1364.60 | NIST | |
Inp | 1374.00 | NIST | |
Inp | 1387.00 | NIST | |
Inp | 1371.00 | NIST | |
Inp | 1374.40 | NIST | |
Inp | 1377.50 | NIST | |
Inp | 1356.00 | NIST | |
Inp | 1371.00 | NIST | |
Inp | 1371.00 | NIST | |
Inp | 1371.00 | NIST | |
Inp | 1372.00 | NIST | |
Inp | 1372.00 | NIST | |
Inp | 1374.00 | NIST | |
Inp | 1374.00 | NIST | |
Inp | 1375.00 | NIST | |
Inp | 1376.00 | NIST | |
Inp | 1374.00 | NIST | |
Inp | 1364.00 | NIST | |
Inp | 1363.00 | NIST | |
Inp | 1367.00 | NIST | |
Inp | 1363.00 | NIST | |
Inp | 1371.00 | NIST | |
Inp | 1357.00 | NIST | |
Inp | 1356.00 | NIST | |
Inp | 1372.00 | NIST | |
Inp | 1372.00 | NIST | |
Inp | 1374.00 | NIST | |
Inp | 1360.00 | NIST | |
Inp | 1351.00 | NIST | |
Inp | 1367.00 | NIST | |
Inp | 1381.00 | NIST | |
Inp | 1357.00 | NIST | |
Inp | 1349.00 | NIST | |
Inp | 1354.00 | NIST | |
Inp | 1364.00 | NIST | |
Inp | 1357.00 | NIST | |
Inp | 1357.00 | NIST | |
Inp | 1365.00 | NIST | |
Inp | 1355.00 | NIST | |
Inp | 1355.00 | NIST | |
Inp | 1368.00 | NIST | |
Inp | 1367.00 | NIST | |
Inp | 1357.00 | NIST | |
Inp | 1360.00 | NIST | |
Inp | 1382.00 | NIST | |
Inp | 1387.00 | NIST | |
Inp | 1356.00 | NIST | |
Inp | 1357.00 | NIST | |
Inp | 1358.00 | NIST | |
Inp | 1386.00 | NIST | |
Inp | 1370.00 | NIST | |
Inp | 1382.00 | NIST | |
Inp | 1364.00 | NIST | |
Inp | 1362.00 | NIST | |
Inp | 1361.00 | NIST | |
Inp | Outlier 233.42 | NIST | |
Inp | Outlier 234.77 | NIST | |
Inp | Outlier 234.41 | NIST | |
I | [1816.00; 1886.00] | ||
I | 1845.00 | NIST | |
I | 1826.00 | NIST | |
I | 1861.00 | NIST | |
I | 1856.00 | NIST | |
I | 1853.00 | NIST | |
I | 1861.00 | NIST | |
I | 1886.00 | NIST | |
I | 1850.00 | NIST | |
I | 1840.00 | NIST | |
I | 1840.00 | NIST | |
I | 1847.00 | NIST | |
I | 1875.00 | NIST | |
I | 1876.00 | NIST | |
I | 1853.00 | NIST | |
I | 1820.00 | NIST | |
I | 1816.00 | NIST | |
I | 1883.00 | NIST | |
I | 1838.00 | NIST | |
I | 1827.00 | NIST | |
I | 1822.00 | NIST | |
I | 1867.00 | NIST | |
I | 1871.00 | NIST | |
I | 1871.00 | NIST | |
I | 1822.00 | NIST | |
I | 1871.00 | NIST | |
I | 1835.00 | NIST | |
Tboil | [516.20; 518.30] | K | |
Tboil | 516.20 | K | KDB |
Tboil | 518.30 | K | Ternary... |
Tc | 703.60 | K | KDB |
Tfus | [288.45; 292.00] | K | |
Tfus | 292.00 | K | KDB |
Tfus | 289.63 | K | Experim... |
Tfus | 288.45 ± 0.50 | K | NIST |
Tfus | 289.65 ± 0.30 | K | NIST |
Vc | [0.718; 0.718] | m3/kmol | |
Vc | 0.718 | m3/kmol | KDB |
Vc | 0.718 | m3/kmol | NIST |
Zc | 0.2635080 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [428.64; 504.67] | J/mol×K | [543.26; 701.29] | |
T(K) Ideal gas heat capacity (J/mol×K) 440 460 480 500 550 600 650 700 | ||||
Cp,gas | 428.64 | J/mol×K | 543.26 | Joback Calculated Property |
Cp,gas | 442.60 | J/mol×K | 569.60 | Joback Calculated Property |
Cp,gas | 456.02 | J/mol×K | 595.94 | Joback Calculated Property |
Cp,gas | 468.92 | J/mol×K | 622.27 | Joback Calculated Property |
Cp,gas | 481.33 | J/mol×K | 648.61 | Joback Calculated Property |
Cp,gas | 493.24 | J/mol×K | 674.95 | Joback Calculated Property |
Cp,gas | 504.67 | J/mol×K | 701.29 | Joback Calculated Property |
Cp,liquid | [406.34; 419.80] | J/mol×K | [298.15; 303.65] | |
Cp,liquid | 406.34 | J/mol×K | 298.15 | NIST |
Cp,liquid | 419.80 | J/mol×K | 303.00 | NIST |
Cp,liquid | 406.80 | J/mol×K | 303.15 | NIST |
Cp,liquid | 414.80 | J/mol×K | 303.65 | NIST |
η | [0.0078410; 0.0172840] | Pa×s | [293.15; 313.15] | |
T(K) Dynamic viscosity (Pa×s) 8.00e-3 0.01 0.01 0.01 0.02 0.02 295 300 305 310 | ||||
η | 0.0172840 | Pa×s | 293.15 | Measure... |
η | 0.0171820 | Pa×s | 293.15 | Densiti... |
η | 0.0137210 | Pa×s | 298.15 | Measure... |
η | 0.0140250 | Pa×s | 298.15 | Densiti... |
η | 0.0115240 | Pa×s | 303.15 | Measure... |
η | 0.0093500 | Pa×s | 308.15 | Measure... |
η | 0.0078410 | Pa×s | 313.15 | Measure... |
ΔvapH | [68.50; 83.60] | kJ/mol | [317.50; 463.50] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 70 75 80 85 350 400 450 | ||||
ΔvapH | 83.60 | kJ/mol | 317.50 | NIST |
ΔvapH | 79.50 | kJ/mol | 333.50 | NIST |
ΔvapH | 72.30 | kJ/mol | 454.50 | NIST |
ΔvapH | 68.70 | kJ/mol | 458.00 | NIST |
ΔvapH | 68.50 | kJ/mol | 463.50 | NIST |
ρl | [800.20; 829.34] | kg/m3 | [298.15; 338.15] | |
T(K) Liquid Density (kg/m3) 800 805 810 815 820 825 830 300 310 320 330 | ||||
ρl | 828.00 | kg/m3 | 298.15 | Viscosi... |
ρl | 829.34 | kg/m3 | 298.15 | Experim... |
ρl | 821.00 | kg/m3 | 308.15 | Viscosi... |
ρl | 814.20 | kg/m3 | 318.15 | Viscosi... |
ρl | 807.20 | kg/m3 | 328.15 | Viscosi... |
ρl | 800.20 | kg/m3 | 338.15 | Viscosi... |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | [404.20; 419.20] | K | [2.00; 4.00] | |
Tboilr | 404.20 | K | 2.00 | NIST |
Tboilr | 419.20 | K | 4.00 | NIST |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 100.00 | 827.7 |
298.15 | 1000.00 | 828.2 |
298.15 | 5000.00 | 830.7 |
298.15 | 10000.00 | 833.6 |
298.15 | 15000.00 | 836.4 |
298.15 | 20000.00 | 839.2 |
298.15 | 25000.00 | 841.8 |
298.15 | 30000.00 | 844.4 |
298.15 | 35000.00 | 846.9 |
298.15 | 40000.00 | 849.4 |
298.15 | 45000.00 | 851.8 |
298.15 | 50000.00 | 854.2 |
298.15 | 55000.00 | 856.5 |
298.15 | 60000.00 | 858.7 |
308.15 | 100.00 | 820.9 |
308.15 | 1000.00 | 821.5 |
308.15 | 5000.00 | 824.0 |
308.15 | 10000.00 | 827.1 |
308.15 | 15000.00 | 830.0 |
308.15 | 20000.00 | 832.9 |
308.15 | 25000.00 | 835.6 |
308.15 | 30000.00 | 838.3 |
308.15 | 35000.00 | 840.9 |
308.15 | 40000.00 | 843.4 |
308.15 | 45000.00 | 845.9 |
308.15 | 50000.00 | 848.3 |
308.15 | 55000.00 | 850.7 |
308.15 | 60000.00 | 852.9 |
318.15 | 100.00 | 814.1 |
318.15 | 1000.00 | 814.7 |
318.15 | 5000.00 | 817.4 |
318.15 | 10000.00 | 820.6 |
318.15 | 15000.00 | 823.7 |
318.15 | 20000.00 | 826.6 |
318.15 | 25000.00 | 829.5 |
318.15 | 30000.00 | 832.3 |
318.15 | 35000.00 | 834.8 |
318.15 | 40000.00 | 837.6 |
318.15 | 45000.00 | 840.1 |
318.15 | 50000.00 | 842.6 |
318.15 | 55000.00 | 845.1 |
318.15 | 60000.00 | 847.3 |
328.15 | 100.00 | 807.4 |
328.15 | 1000.00 | 808.0 |
328.15 | 5000.00 | 810.8 |
328.15 | 10000.00 | 814.1 |
328.15 | 15000.00 | 817.3 |
328.15 | 20000.00 | 820.4 |
328.15 | 25000.00 | 823.3 |
328.15 | 30000.00 | 826.2 |
328.15 | 35000.00 | 829.0 |
328.15 | 40000.00 | 831.7 |
328.15 | 45000.00 | 834.4 |
328.15 | 50000.00 | 837.0 |
328.15 | 55000.00 | 839.5 |
328.15 | 60000.00 | 841.8 |
338.15 | 100.00 | 800.5 |
338.15 | 1000.00 | 801.1 |
338.15 | 5000.00 | 803.9 |
338.15 | 10000.00 | 807.3 |
338.15 | 15000.00 | 810.6 |
338.15 | 20000.00 | 813.8 |
338.15 | 25000.00 | 816.9 |
338.15 | 30000.00 | 819.9 |
338.15 | 35000.00 | 822.8 |
338.15 | 40000.00 | 825.6 |
338.15 | 45000.00 | 828.4 |
338.15 | 50000.00 | 831.0 |
338.15 | 55000.00 | 833.6 |
338.15 | 60000.00 | 836.0 |
348.15 | 100.00 | 793.3 |
348.15 | 1000.00 | 793.8 |
348.15 | 5000.00 | 797.1 |
348.15 | 10000.00 | 800.8 |
348.15 | 15000.00 | 804.3 |
348.15 | 20000.00 | 807.6 |
348.15 | 25000.00 | 810.8 |
348.15 | 30000.00 | 813.9 |
348.15 | 35000.00 | 816.9 |
348.15 | 40000.00 | 819.9 |
348.15 | 45000.00 | 822.7 |
348.15 | 50000.00 | 825.5 |
348.15 | 55000.00 | 828.1 |
348.15 | 60000.00 | 830.7 |
358.15 | 100.00 | 786.0 |
358.15 | 1000.00 | 786.8 |
358.15 | 5000.00 | 790.0 |
358.15 | 10000.00 | 793.9 |
358.15 | 15000.00 | 797.6 |
358.15 | 20000.00 | 801.1 |
358.15 | 25000.00 | 804.4 |
358.15 | 30000.00 | 807.7 |
358.15 | 35000.00 | 810.8 |
358.15 | 40000.00 | 813.9 |
358.15 | 45000.00 | 816.6 |
358.15 | 50000.00 | 819.6 |
358.15 | 55000.00 | 822.4 |
358.15 | 60000.00 | 824.9 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [401.52; 529.24] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.77538e+01 | |||
Coefficient B | -5.52497e+03 | |||
Coefficient C | -8.51960e+01 | |||
Temperature range, min. | 401.52 | |||
Temperature range, max. | 529.24 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 401.52 | Calculated Property |
Pvap | 2.82 | kPa | 415.71 | Calculated Property |
Pvap | 5.62 | kPa | 429.90 | Calculated Property |
Pvap | 10.59 | kPa | 444.09 | Calculated Property |
Pvap | 19.01 | kPa | 458.28 | Calculated Property |
Pvap | 32.71 | kPa | 472.48 | Calculated Property |
Pvap | 54.16 | kPa | 486.67 | Calculated Property |
Pvap | 86.64 | kPa | 500.86 | Calculated Property |
Pvap | 134.37 | kPa | 515.05 | Calculated Property |
Pvap | 202.63 | kPa | 529.24 | Calculated Property |
Pvap | [1.27e-04; 2061.92] | kPa | [289.05; 704.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.67298e+02 | |||
Coefficient B | -2.08778e+04 | |||
Coefficient C | -3.62321e+01 | |||
Coefficient D | 1.52436e-05 | |||
Temperature range, min. | 289.05 | |||
Temperature range, max. | 704.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 400 600 | ||||
Pvap | 1.27e-04 | kPa | 289.05 | Calculated Property |
Pvap | 0.02 | kPa | 335.16 | Calculated Property |
Pvap | 0.55 | kPa | 381.26 | Calculated Property |
Pvap | 5.75 | kPa | 427.37 | Calculated Property |
Pvap | 30.79 | kPa | 473.47 | Calculated Property |
Pvap | 106.83 | kPa | 519.58 | Calculated Property |
Pvap | 278.28 | kPa | 565.68 | Calculated Property |
Pvap | 601.06 | kPa | 611.79 | Calculated Property |
Pvap | 1152.94 | kPa | 657.89 | Calculated Property |
Pvap | 2061.92 | kPa | 704.00 | Calculated Property |
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