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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Vapor or sublimation pressure, kPa (2)
Activity coefficient of 2-Butene, (Z)- (2)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 2-Butene, (Z)- (2) - Liquid |
| 300.00 |
2.91 |
| 309.99 |
2.77 |
| 320.00 |
2.67 |
| 330.00 |
2.59 |
Activity coefficient of 2-Butene, (Z)- (2)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 2-Butene, (Z)- (2) - Liquid |
| 300.00 |
2.91 |
| 309.99 |
2.77 |
| 320.00 |
2.67 |
| 330.00 |
2.59 |
Henry's Law constant (mole fraction scale), kPa of 2-Butene, (Z)- (2)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Butene, (Z)- (2) - Liquid |
| 300.00 |
620.0 |
| 309.99 |
780.0 |
| 320.00 |
990.0 |
| 330.00 |
1230.0 |
Henry's Law constant (mole fraction scale), kPa of 2-Butene, (Z)- (2)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Butene, (Z)- (2) - Liquid |
| 300.00 |
620.0 |
| 309.99 |
780.0 |
| 320.00 |
990.0 |
| 330.00 |
1230.0 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of 2-Butene, (Z)- (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Gas |
| 0.0000 |
364.52 |
143.00 |
| 0.0230 |
364.52 |
190.00 |
| 0.0392 |
364.51 |
221.90 |
| 0.0591 |
364.52 |
259.80 |
| 0.1046 |
364.52 |
341.40 |
| 0.1517 |
364.52 |
418.90 |
| 0.2006 |
364.52 |
493.20 |
| 0.2490 |
364.52 |
560.40 |
| 0.2984 |
364.52 |
623.80 |
| 0.3483 |
364.53 |
682.60 |
| 0.3984 |
364.53 |
737.00 |
| 0.4492 |
364.52 |
787.70 |
| 0.4996 |
364.52 |
833.90 |
| 0.4997 |
364.51 |
834.40 |
| 0.5479 |
364.52 |
875.20 |
| 0.5968 |
364.52 |
914.30 |
| 0.6457 |
364.52 |
951.10 |
| 0.6953 |
364.52 |
986.40 |
| 0.7445 |
364.52 |
1019.90 |
| 0.7945 |
364.52 |
1052.70 |
| 0.8451 |
364.52 |
1085.30 |
| 0.8962 |
364.52 |
1118.40 |
| 0.9480 |
364.52 |
1153.40 |
| 0.9684 |
364.52 |
1167.70 |
| 0.9803 |
364.52 |
1176.20 |
| 0.9892 |
364.52 |
1182.60 |
| 1.0000 |
364.53 |
1190.70 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of 2-Butene, (Z)- (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Gas |
| 0.0000 |
364.52 |
143.00 |
| 0.0230 |
364.52 |
190.00 |
| 0.0392 |
364.51 |
221.90 |
| 0.0591 |
364.52 |
259.80 |
| 0.1046 |
364.52 |
341.40 |
| 0.1517 |
364.52 |
418.90 |
| 0.2006 |
364.52 |
493.20 |
| 0.2490 |
364.52 |
560.40 |
| 0.2984 |
364.52 |
623.80 |
| 0.3483 |
364.53 |
682.60 |
| 0.3984 |
364.53 |
737.00 |
| 0.4492 |
364.52 |
787.70 |
| 0.4996 |
364.52 |
833.90 |
| 0.4997 |
364.51 |
834.40 |
| 0.5479 |
364.52 |
875.20 |
| 0.5968 |
364.52 |
914.30 |
| 0.6457 |
364.52 |
951.10 |
| 0.6953 |
364.52 |
986.40 |
| 0.7445 |
364.52 |
1019.90 |
| 0.7945 |
364.52 |
1052.70 |
| 0.8451 |
364.52 |
1085.30 |
| 0.8962 |
364.52 |
1118.40 |
| 0.9480 |
364.52 |
1153.40 |
| 0.9684 |
364.52 |
1167.70 |
| 0.9803 |
364.52 |
1176.20 |
| 0.9892 |
364.52 |
1182.60 |
| 1.0000 |
364.53 |
1190.70 |
Sources
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Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
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Vapor-Liquid Equilibrium for the cis-2-Butene + Methanol, + 2-Propanol, + 2-Butanol, + 2-Methyl-2-propanol Systems at 364.5 K