Mixture of Isopropyl Alcohol + 1-Propene, 2-methyl-

Datasets

1. Activity coefficient (2)
2. Henry's Law constant (mole fraction scale), kPa (2)
3. P_vap - Vapor or sublimation pressure, kPa (4)

Activity coefficient of 1-Propene, 2-methyl- (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Propene, 2-methyl- (2) - Liquid
249.97	4.4
270.03	4.3
290.00	4.2
310.00	4.0
330.00	3.8

Activity coefficient of 1-Propene, 2-methyl- (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 1-Propene, 2-methyl- (2) - Liquid
249.97	4.4
270.03	4.3
290.00	4.2
310.00	4.0
330.00	3.8

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

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (mole fraction scale), kPa of 1-Propene, 2-methyl- (2) - Liquid
249.97	215.0
270.03	474.0
290.00	920.0
310.00	1530.0
330.00	2320.0

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

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (mole fraction scale), kPa of 1-Propene, 2-methyl- (2) - Liquid
249.97	215.0
270.03	474.0
290.00	920.0
310.00	1530.0
330.00	2320.0

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Propene, 2-methyl- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
323.13	0.4493	469.95
323.13	0.4983	487.15
323.13	0.5964	515.95
323.13	0.6458	528.35
323.13	0.6954	539.95
323.13	0.7461	551.04
323.14	0.7943	561.24
323.14	0.8441	571.64
323.14	0.8945	582.04
323.14	0.9447	593.04
323.14	1.0000	609.14
323.15	0.0414	101.27
323.15	0.1531	260.96
323.15	0.9862	604.44
323.16	0.0000	23.47
323.16	0.0653	141.17
323.16	0.1065	202.26
323.16	0.2015	311.96
323.16	0.2500	354.46
323.16	0.2993	390.45
323.16	0.3490	420.65
323.16	0.3983	445.85
323.16	0.4491	467.65
323.16	0.5092	489.45
323.16	0.5502	501.15

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Propene, 2-methyl- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
364.48	0.2918	895.90
364.49	0.0216	225.10
364.49	0.0377	282.10
364.49	0.5464	1201.80
364.49	0.5949	1243.60
364.49	0.9678	1520.10
364.50	0.0000	144.50
364.50	0.6932	1320.60
364.50	0.9763	1527.40
364.50	0.9884	1537.10
364.51	0.1453	600.20
364.51	0.1932	711.20
364.51	0.2421	809.70
364.51	0.3430	973.90
364.51	0.4968	1154.50
364.51	0.6434	1283.40
364.51	0.7425	1356.50
364.51	0.7929	1391.50
364.51	0.8429	1426.50
364.51	0.8951	1464.90
364.51	0.9475	1504.50
364.51	1.0000	1546.50
364.52	0.0549	340.60
364.52	0.3942	1041.70
364.52	0.4981	1157.40
364.54	0.1001	479.40
364.54	0.4460	1102.70

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Propene, 2-methyl- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
323.13	0.4493	469.95
323.13	0.4983	487.15
323.13	0.5964	515.95
323.13	0.6458	528.35
323.13	0.6954	539.95
323.13	0.7461	551.04
323.14	0.7943	561.24
323.14	0.8441	571.64
323.14	0.8945	582.04
323.14	0.9447	593.04
323.14	1.0000	609.14
323.15	0.0414	101.27
323.15	0.1531	260.96
323.15	0.9862	604.44
323.16	0.0000	23.47
323.16	0.0653	141.17
323.16	0.1065	202.26
323.16	0.2015	311.96
323.16	0.2500	354.46
323.16	0.2993	390.45
323.16	0.3490	420.65
323.16	0.3983	445.85
323.16	0.4491	467.65
323.16	0.5092	489.45
323.16	0.5502	501.15

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Propene, 2-methyl- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
364.48	0.2918	895.90
364.49	0.0216	225.10
364.49	0.0377	282.10
364.49	0.5464	1201.80
364.49	0.5949	1243.60
364.49	0.9678	1520.10
364.50	0.0000	144.50
364.50	0.6932	1320.60
364.50	0.9763	1527.40
364.50	0.9884	1537.10
364.51	0.1453	600.20
364.51	0.1932	711.20
364.51	0.2421	809.70
364.51	0.3430	973.90
364.51	0.4968	1154.50
364.51	0.6434	1283.40
364.51	0.7425	1356.50
364.51	0.7929	1391.50
364.51	0.8429	1426.50
364.51	0.8951	1464.90
364.51	0.9475	1504.50
364.51	1.0000	1546.50
364.52	0.0549	340.60
364.52	0.3942	1041.70
364.52	0.4981	1157.40
364.54	0.1001	479.40
364.54	0.4460	1102.70

Sources

• Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
• Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene, and 1,3-butadiene in 2-propanol at 250-330 K
• Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K