Datasets
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Activity coefficient (2)
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Henry's Law constant (mole fraction scale), kPa (2)
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Pvap - Vapor or sublimation pressure, kPa (2)
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Vapor or sublimation pressure, kPa (2)
Activity coefficient of Isobutane (2)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Isobutane (2) - Liquid |
300.00 |
3.6 |
310.00 |
3.44 |
320.00 |
3.35 |
330.00 |
3.24 |
Activity coefficient of Isobutane (2)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Isobutane (2) - Liquid |
300.00 |
3.6 |
310.00 |
3.44 |
320.00 |
3.35 |
330.00 |
3.24 |
Henry's Law constant (mole fraction scale), kPa of Isobutane (2)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of Isobutane (2) - Liquid |
300.00 |
1190.0 |
310.00 |
1480.0 |
320.00 |
1820.0 |
330.00 |
2190.0 |
Henry's Law constant (mole fraction scale), kPa of Isobutane (2)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of Isobutane (2) - Liquid |
300.00 |
1190.0 |
310.00 |
1480.0 |
320.00 |
1820.0 |
330.00 |
2190.0 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Isobutane (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
364.50 |
0.0000 |
142.60 |
364.50 |
0.1902 |
673.90 |
364.50 |
0.2384 |
776.00 |
364.50 |
0.2873 |
869.20 |
364.50 |
0.3389 |
957.60 |
364.50 |
0.4964 |
1174.80 |
364.50 |
0.5440 |
1231.40 |
364.50 |
0.7387 |
1430.50 |
364.50 |
0.9885 |
1673.10 |
364.50 |
1.0000 |
1685.60 |
364.51 |
0.0158 |
196.80 |
364.51 |
0.0334 |
254.50 |
364.51 |
0.0503 |
307.70 |
364.51 |
0.0970 |
443.00 |
364.51 |
0.1424 |
562.00 |
364.51 |
0.3907 |
1038.00 |
364.51 |
0.4433 |
1112.30 |
364.51 |
0.4953 |
1178.80 |
364.51 |
0.5917 |
1284.60 |
364.51 |
0.6405 |
1335.70 |
364.51 |
0.6893 |
1383.50 |
364.51 |
0.7896 |
1477.40 |
364.51 |
0.8405 |
1524.10 |
364.51 |
0.8942 |
1574.60 |
364.51 |
0.9677 |
1649.90 |
364.51 |
0.9785 |
1661.80 |
364.52 |
0.9464 |
1627.20 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Isobutane (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
364.50 |
0.0000 |
142.60 |
364.50 |
0.1902 |
673.90 |
364.50 |
0.2384 |
776.00 |
364.50 |
0.2873 |
869.20 |
364.50 |
0.3389 |
957.60 |
364.50 |
0.4964 |
1174.80 |
364.50 |
0.5440 |
1231.40 |
364.50 |
0.7387 |
1430.50 |
364.50 |
0.9885 |
1673.10 |
364.50 |
1.0000 |
1685.60 |
364.51 |
0.0158 |
196.80 |
364.51 |
0.0334 |
254.50 |
364.51 |
0.0503 |
307.70 |
364.51 |
0.0970 |
443.00 |
364.51 |
0.1424 |
562.00 |
364.51 |
0.3907 |
1038.00 |
364.51 |
0.4433 |
1112.30 |
364.51 |
0.4953 |
1178.80 |
364.51 |
0.5917 |
1284.60 |
364.51 |
0.6405 |
1335.70 |
364.51 |
0.6893 |
1383.50 |
364.51 |
0.7896 |
1477.40 |
364.51 |
0.8405 |
1524.10 |
364.51 |
0.8942 |
1574.60 |
364.51 |
0.9677 |
1649.90 |
364.51 |
0.9785 |
1661.80 |
364.52 |
0.9464 |
1627.20 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Isobutane (2) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
313.08 |
0.0000 |
13.77 |
313.08 |
0.0370 |
67.47 |
313.08 |
0.0521 |
87.87 |
313.08 |
0.0981 |
142.67 |
313.08 |
0.1477 |
193.16 |
313.08 |
0.1965 |
235.36 |
313.08 |
0.2955 |
304.26 |
313.08 |
0.3455 |
332.46 |
313.08 |
0.3966 |
357.96 |
313.08 |
0.4476 |
380.45 |
313.08 |
0.7981 |
485.25 |
313.08 |
0.9484 |
516.25 |
313.08 |
0.9718 |
521.35 |
313.08 |
0.9909 |
526.85 |
313.08 |
0.9957 |
527.45 |
313.08 |
1.0000 |
529.95 |
313.09 |
0.2441 |
270.96 |
313.09 |
0.4506 |
381.45 |
313.09 |
0.4997 |
400.65 |
313.09 |
0.5490 |
418.05 |
313.09 |
0.6482 |
448.45 |
313.09 |
0.6975 |
461.55 |
313.09 |
0.7472 |
473.75 |
313.09 |
0.8475 |
495.75 |
313.09 |
0.8980 |
505.95 |
313.10 |
0.5975 |
433.65 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Isobutane (2) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
313.08 |
0.0000 |
13.77 |
313.08 |
0.0370 |
67.47 |
313.08 |
0.0521 |
87.87 |
313.08 |
0.0981 |
142.67 |
313.08 |
0.1477 |
193.16 |
313.08 |
0.1965 |
235.36 |
313.08 |
0.2955 |
304.26 |
313.08 |
0.3455 |
332.46 |
313.08 |
0.3966 |
357.96 |
313.08 |
0.4476 |
380.45 |
313.08 |
0.7981 |
485.25 |
313.08 |
0.9484 |
516.25 |
313.08 |
0.9718 |
521.35 |
313.08 |
0.9909 |
526.85 |
313.08 |
0.9957 |
527.45 |
313.08 |
1.0000 |
529.95 |
313.09 |
0.2441 |
270.96 |
313.09 |
0.4506 |
381.45 |
313.09 |
0.4997 |
400.65 |
313.09 |
0.5490 |
418.05 |
313.09 |
0.6482 |
448.45 |
313.09 |
0.6975 |
461.55 |
313.09 |
0.7472 |
473.75 |
313.09 |
0.8475 |
495.75 |
313.09 |
0.8980 |
505.95 |
313.10 |
0.5975 |
433.65 |
Sources
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Vapour liquid equilibrium for the 2-methylpropane + methanol, +ethanol, +2-propanol, +2-butanol and +2-methyl-2-propanol systems at 313.15K
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Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in isobutanol and tert-butanol
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Vapor Liquid Equilibrium for the Systems 2-Methylpropane + Methanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K