Mixture of 2-Propanol, 2-methyl- + 1-Butene

Datasets

1. Activity coefficient
2. Henry's Law constant (mole fraction scale), kPa
3. P_vap - Vapor or sublimation pressure, kPa

Activity coefficient of 1-Butene (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Butene (2) - Liquid
300.03	3.09
310.00	2.98
320.00	2.82
330.00	2.66

Henry's Law constant (mole fraction scale), kPa of 1-Butene (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (mole fraction scale), kPa of 1-Butene (2) - Liquid
300.03	892.0
310.00	1130.0
320.00	1370.0
330.00	1620.0

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 1-Butene (2) - Gas	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	364.51	142.70
0.1991	364.51	177.80
0.3723	364.51	226.30
0.4790	364.51	271.20
0.6320	364.50	379.40
0.7135	364.50	480.40
0.7647	364.50	575.30
0.8001	364.51	664.20
0.8263	364.51	747.90
0.8461	364.52	823.70
0.8622	364.52	895.20
0.8756	364.51	960.90
0.8871	364.51	1022.60
0.8875	364.51	1020.60
0.8969	364.51	1074.10
0.9055	364.51	1124.80
0.9136	364.52	1172.40
0.9217	364.51	1218.60
0.9301	364.51	1264.00
0.9390	364.51	1308.50
0.9490	364.51	1352.80
0.9613	364.51	1400.00
0.9769	364.51	1449.90
0.9855	364.50	1474.30
0.9911	364.51	1489.20
0.9946	364.50	1497.30
1.0000	364.50	1509.80

Sources

• 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
• Vapor-Liquid Equilibrium for 1-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and 2-Methyl-2-propanol (TBA) at 364.5 K

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