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)
Activity coefficient of 2-Butene, (Z)- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of 2-Butene, (Z)- (1) - Liquid |
249.98 |
10.1 |
269.98 |
9.7 |
289.99 |
9.44 |
300.00 |
9.33 |
310.00 |
9.15 |
320.00 |
8.96 |
330.00 |
8.73 |
Activity coefficient of 2-Butene, (Z)- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of 2-Butene, (Z)- (1) - Liquid |
249.98 |
10.1 |
269.98 |
9.7 |
289.99 |
9.44 |
300.00 |
9.33 |
310.00 |
9.15 |
320.00 |
8.96 |
330.00 |
8.73 |
Henry's Law constant (mole fraction scale), kPa of 2-Butene, (Z)- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Butene, (Z)- (1) - Liquid |
249.98 |
319.0 |
269.98 |
730.0 |
289.99 |
1460.0 |
300.00 |
1980.0 |
310.00 |
2590.0 |
320.00 |
3310.0 |
330.00 |
4130.0 |
Henry's Law constant (mole fraction scale), kPa of 2-Butene, (Z)- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Butene, (Z)- (1) - Liquid |
249.98 |
319.0 |
269.98 |
730.0 |
289.99 |
1460.0 |
300.00 |
1980.0 |
310.00 |
2590.0 |
320.00 |
3310.0 |
330.00 |
4130.0 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of 2-Butene, (Z)- (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
364.52 |
267.30 |
0.0157 |
364.52 |
379.60 |
0.0307 |
364.51 |
475.60 |
0.0474 |
364.52 |
568.40 |
0.0902 |
364.52 |
758.80 |
0.1348 |
364.52 |
899.90 |
0.1834 |
364.52 |
1007.60 |
0.2343 |
364.52 |
1085.40 |
0.2864 |
364.53 |
1140.50 |
0.3391 |
364.53 |
1179.80 |
0.3918 |
364.52 |
1208.10 |
0.4443 |
364.53 |
1229.40 |
0.4965 |
364.52 |
1245.90 |
0.4990 |
364.52 |
1246.20 |
0.5479 |
364.52 |
1258.20 |
0.5981 |
364.52 |
1268.80 |
0.6473 |
364.53 |
1277.60 |
0.6976 |
364.53 |
1285.50 |
0.7475 |
364.52 |
1292.20 |
0.7980 |
364.51 |
1297.50 |
0.8484 |
364.51 |
1300.30 |
0.9005 |
364.51 |
1297.40 |
0.9501 |
364.52 |
1275.40 |
0.9701 |
364.52 |
1251.90 |
0.9827 |
364.52 |
1229.70 |
0.9896 |
364.52 |
1215.50 |
1.0000 |
364.52 |
1190.50 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of 2-Butene, (Z)- (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
364.52 |
267.30 |
0.0157 |
364.52 |
379.60 |
0.0307 |
364.51 |
475.60 |
0.0474 |
364.52 |
568.40 |
0.0902 |
364.52 |
758.80 |
0.1348 |
364.52 |
899.90 |
0.1834 |
364.52 |
1007.60 |
0.2343 |
364.52 |
1085.40 |
0.2864 |
364.53 |
1140.50 |
0.3391 |
364.53 |
1179.80 |
0.3918 |
364.52 |
1208.10 |
0.4443 |
364.53 |
1229.40 |
0.4965 |
364.52 |
1245.90 |
0.4990 |
364.52 |
1246.20 |
0.5479 |
364.52 |
1258.20 |
0.5981 |
364.52 |
1268.80 |
0.6473 |
364.53 |
1277.60 |
0.6976 |
364.53 |
1285.50 |
0.7475 |
364.52 |
1292.20 |
0.7980 |
364.51 |
1297.50 |
0.8484 |
364.51 |
1300.30 |
0.9005 |
364.51 |
1297.40 |
0.9501 |
364.52 |
1275.40 |
0.9701 |
364.52 |
1251.90 |
0.9827 |
364.52 |
1229.70 |
0.9896 |
364.52 |
1215.50 |
1.0000 |
364.52 |
1190.50 |
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