Mixture of Isopropyl Alcohol + 2-Butene, (E)-

Datasets

1. Activity coefficient (2)
2. Mole fraction (4)
3. P_vap - Vapor or sublimation pressure, kPa (4)

Activity coefficient of 2-Butene, (E)- (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 2-Butene, (E)- (2) - Liquid
249.96	4.3
270.04	4.3
290.00	4.2
310.00	4.1
330.00	3.9

Activity coefficient of 2-Butene, (E)- (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of 2-Butene, (E)- (2) - Liquid
249.96	4.3
270.04	4.3
290.00	4.2
310.00	4.1
330.00	3.9

Mole fraction of 2-Butene, (E)- (2) [ref]

Fixed		Measured
Mole fraction of 2-Butene, (E)- (2) - Liquid	Temperature, K - Liquid	Mole fraction of 2-Butene, (E)- (2) - Gas
0.0000	332.03	0.0000
0.0420	332.03	0.6849
0.0850	332.03	0.8047
0.1030	332.03	0.8306
0.1540	332.03	0.8730
0.1980	332.02	0.8934
0.2460	332.02	0.9081
0.2900	332.02	0.9173
0.3410	332.01	0.9254
0.3970	332.01	0.9320
0.4400	332.01	0.9360
0.4510	332.08	0.9368
0.4880	332.01	0.9399
0.5000	332.08	0.9407
0.5150	332.00	0.9420
0.5490	332.08	0.9442
0.5990	332.08	0.9475
0.6490	332.08	0.9505
0.6980	332.08	0.9535
0.7490	332.08	0.9565
0.7990	332.09	0.9596
0.8500	332.08	0.9633
0.9010	332.08	0.9686
0.9510	332.08	0.9784
0.9920	332.08	0.9948
1.0000	332.08	1.0000

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

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (mole fraction scale), kPa of 2-Butene, (E)- (2) - Liquid
249.96	155.0
270.04	358.0
290.00	720.0
310.00	1250.0
330.00	1950.0

Mole fraction of 2-Butene, (E)- (2) [ref]

Fixed		Measured
Mole fraction of 2-Butene, (E)- (2) - Liquid	Temperature, K - Liquid	Mole fraction of 2-Butene, (E)- (2) - Gas
0.0000	332.03	0.0000
0.0420	332.03	0.6849
0.0850	332.03	0.8047
0.1030	332.03	0.8306
0.1540	332.03	0.8730
0.1980	332.02	0.8934
0.2460	332.02	0.9081
0.2900	332.02	0.9173
0.3410	332.01	0.9254
0.3970	332.01	0.9320
0.4400	332.01	0.9360
0.4510	332.08	0.9368
0.4880	332.01	0.9399
0.5000	332.08	0.9407
0.5150	332.00	0.9420
0.5490	332.08	0.9442
0.5990	332.08	0.9475
0.6490	332.08	0.9505
0.6980	332.08	0.9535
0.7490	332.08	0.9565
0.7990	332.09	0.9596
0.8500	332.08	0.9633
0.9010	332.08	0.9686
0.9510	332.08	0.9784
0.9920	332.08	0.9948
1.0000	332.08	1.0000

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

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (mole fraction scale), kPa of 2-Butene, (E)- (2) - Liquid
249.96	155.0
270.04	358.0
290.00	720.0
310.00	1250.0
330.00	1950.0

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 2-Butene, (E)- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	332.03	36.47
0.0420	332.03	114.07
0.0850	332.03	181.16
0.1030	332.03	207.06
0.1540	332.03	270.46
0.1980	332.02	315.76
0.2460	332.02	357.96
0.2900	332.02	389.35
0.3410	332.01	420.75
0.3970	332.01	449.25
0.4400	332.01	467.15
0.4510	332.08	473.15
0.4880	332.01	484.95
0.5000	332.08	490.55
0.5150	332.00	494.05
0.5490	332.08	505.75
0.5990	332.08	519.65
0.6490	332.08	532.05
0.6980	332.08	543.54
0.7490	332.08	554.54
0.7990	332.09	564.84
0.8500	332.08	574.94
0.9010	332.08	584.94
0.9510	332.08	595.24
0.9920	332.08	604.54
1.0000	332.08	606.44

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butene, (E)- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
364.51	0.0000	144.10
364.52	0.0208	212.70
364.52	0.0357	258.30
364.52	0.0558	317.60
364.52	0.1014	437.00
364.52	0.1474	540.70
364.52	0.1950	632.90
364.52	0.2440	714.10
364.52	0.2944	785.90
364.52	0.3444	847.00
364.52	0.3954	901.00
364.52	0.4455	947.50
364.52	0.4970	989.60
364.52	0.4989	990.50
364.52	0.5472	1025.80
364.52	0.5961	1058.50
364.52	0.6451	1088.40
364.52	0.6943	1116.40
364.52	0.7438	1143.00
364.52	0.8441	1194.50
364.52	0.8947	1219.30
364.52	0.9484	1246.00
364.52	0.9678	1255.30
364.52	0.9780	1259.90
364.52	1.0000	1268.70
364.53	0.7942	1169.40
364.53	0.9885	1264.50

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 2-Butene, (E)- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	332.03	36.47
0.0420	332.03	114.07
0.0850	332.03	181.16
0.1030	332.03	207.06
0.1540	332.03	270.46
0.1980	332.02	315.76
0.2460	332.02	357.96
0.2900	332.02	389.35
0.3410	332.01	420.75
0.3970	332.01	449.25
0.4400	332.01	467.15
0.4510	332.08	473.15
0.4880	332.01	484.95
0.5000	332.08	490.55
0.5150	332.00	494.05
0.5490	332.08	505.75
0.5990	332.08	519.65
0.6490	332.08	532.05
0.6980	332.08	543.54
0.7490	332.08	554.54
0.7990	332.09	564.84
0.8500	332.08	574.94
0.9010	332.08	584.94
0.9510	332.08	595.24
0.9920	332.08	604.54
1.0000	332.08	606.44

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butene, (E)- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
364.51	0.0000	144.10
364.52	0.0208	212.70
364.52	0.0357	258.30
364.52	0.0558	317.60
364.52	0.1014	437.00
364.52	0.1474	540.70
364.52	0.1950	632.90
364.52	0.2440	714.10
364.52	0.2944	785.90
364.52	0.3444	847.00
364.52	0.3954	901.00
364.52	0.4455	947.50
364.52	0.4970	989.60
364.52	0.4989	990.50
364.52	0.5472	1025.80
364.52	0.5961	1058.50
364.52	0.6451	1088.40
364.52	0.6943	1116.40
364.52	0.7438	1143.00
364.52	0.8441	1194.50
364.52	0.8947	1219.30
364.52	0.9484	1246.00
364.52	0.9678	1255.30
364.52	0.9780	1259.90
364.52	1.0000	1268.70
364.53	0.7942	1169.40
364.53	0.9885	1264.50

Sources

• Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
• 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
• Vapor Liquid Equilibrium for the Systems trans-2-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K