Mixture of 1-Propanol + 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
259.91	4.09
279.95	4.08
299.94	4.04
320.06	4.0
340.16	3.94

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
259.91	4.09
279.95	4.08
299.94	4.04
320.06	4.0
340.16	3.94

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
259.91	308.0
279.95	641.0
299.94	1173.0
320.06	1946.0
340.16	2956.0

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
259.91	308.0
279.95	641.0
299.94	1173.0
320.06	1946.0
340.16	2956.0

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
323.07	0.0000	12.07
323.07	0.7972	560.94
323.07	0.8967	578.74
323.07	0.9479	589.54
323.07	0.9682	595.14
323.07	0.9881	602.24
323.07	1.0000	607.94
323.08	0.0132	38.97
323.08	0.2951	396.25
323.08	0.5984	522.95
323.08	0.6476	533.55
323.08	0.6975	543.25
323.08	0.7473	552.24
323.08	0.8470	569.64
323.09	0.0312	73.57
323.09	0.0497	107.07
323.09	0.0977	185.16
323.09	0.1456	251.26
323.09	0.1947	308.26
323.09	0.2447	356.36
323.09	0.3447	428.55
323.09	0.3956	455.55
323.09	0.4470	477.75
323.09	0.4978	495.75
323.09	0.4999	496.45
323.09	0.5491	510.75

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
364.50	0.8933	1443.40
364.50	0.9470	1489.30
364.51	0.0000	81.30
364.51	0.0129	135.20
364.51	0.0304	205.10
364.51	0.0473	268.80
364.51	0.0930	427.50
364.51	0.1399	568.50
364.51	0.1861	688.70
364.51	0.2354	798.70
364.51	0.2869	896.10
364.51	0.3386	978.80
364.51	0.3907	1049.50
364.51	0.4429	1109.60
364.51	0.4956	1161.90
364.51	0.4974	1163.00
364.51	0.5937	1242.30
364.51	0.6423	1277.10
364.51	0.6920	1310.30
364.51	0.7418	1342.60
364.51	0.7911	1374.00
364.51	0.8424	1407.60
364.51	0.9677	1510.30
364.51	0.9796	1523.50
364.51	0.9888	1533.70
364.51	1.0000	1546.60
364.52	0.5455	1204.70

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
323.07	0.0000	12.07
323.07	0.7972	560.94
323.07	0.8967	578.74
323.07	0.9479	589.54
323.07	0.9682	595.14
323.07	0.9881	602.24
323.07	1.0000	607.94
323.08	0.0132	38.97
323.08	0.2951	396.25
323.08	0.5984	522.95
323.08	0.6476	533.55
323.08	0.6975	543.25
323.08	0.7473	552.24
323.08	0.8470	569.64
323.09	0.0312	73.57
323.09	0.0497	107.07
323.09	0.0977	185.16
323.09	0.1456	251.26
323.09	0.1947	308.26
323.09	0.2447	356.36
323.09	0.3447	428.55
323.09	0.3956	455.55
323.09	0.4470	477.75
323.09	0.4978	495.75
323.09	0.4999	496.45
323.09	0.5491	510.75

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
364.50	0.8933	1443.40
364.50	0.9470	1489.30
364.51	0.0000	81.30
364.51	0.0129	135.20
364.51	0.0304	205.10
364.51	0.0473	268.80
364.51	0.0930	427.50
364.51	0.1399	568.50
364.51	0.1861	688.70
364.51	0.2354	798.70
364.51	0.2869	896.10
364.51	0.3386	978.80
364.51	0.3907	1049.50
364.51	0.4429	1109.60
364.51	0.4956	1161.90
364.51	0.4974	1163.00
364.51	0.5937	1242.30
364.51	0.6423	1277.10
364.51	0.6920	1310.30
364.51	0.7418	1342.60
364.51	0.7911	1374.00
364.51	0.8424	1407.60
364.51	0.9677	1510.30
364.51	0.9796	1523.50
364.51	0.9888	1533.70
364.51	1.0000	1546.60
364.52	0.5455	1204.70

Sources

• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutene, 1-butene, isobutane, trans-2-butene and 1,3-butadiene in 1-propanol at T=(260 to 340) K
• Vapor-Liquid Equilibrium for 1-Propanol + 1-Butene, + cis-2-Butene, + 2-Methyl-propene, + trans-2-Butene, + n-Butane, and + 2-Methyl-propane
• 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