Mixture of 1-Propene, 2-methyl- + Propanenitrile

Datasets

1. Mole fraction (2)
2. Vapor or sublimation pressure, kPa (2)

Mole fraction of 1-Propene, 2-methyl- (1) [ref]

Fixed		Measured
Mole fraction of 1-Propene, 2-methyl- (1) - Liquid	Temperature, K - Gas	Mole fraction of 1-Propene, 2-methyl- (1) - Gas
0.0000	312.58	0.0000
0.0080	312.59	0.4785
0.0355	312.59	0.7995
0.0483	312.59	0.8426
0.0975	312.59	0.9113
0.1465	312.59	0.9363
0.1975	312.59	0.9496
0.2456	312.59	0.9573
0.2961	312.59	0.9628
0.3463	312.59	0.9667
0.3976	312.59	0.9698
0.4480	312.59	0.9723
0.4983	312.59	0.9743
0.5002	312.59	0.9743
0.5496	312.58	0.9760
0.5990	312.59	0.9774
0.6496	312.59	0.9787
0.6992	312.59	0.9799
0.7486	312.59	0.9811
0.7988	312.59	0.9825
0.8490	312.58	0.9842
0.9011	312.59	0.9870
0.9490	312.59	0.9914
0.9711	312.59	0.9945
0.9932	312.59	0.9985
1.0000	312.59	1.0000

Mole fraction of 1-Propene, 2-methyl- (1) [ref]

Fixed		Measured
Mole fraction of 1-Propene, 2-methyl- (1) - Liquid	Temperature, K - Gas	Mole fraction of 1-Propene, 2-methyl- (1) - Gas
0.0000	312.58	0.0000
0.0080	312.59	0.4785
0.0355	312.59	0.7995
0.0483	312.59	0.8426
0.0975	312.59	0.9113
0.1465	312.59	0.9363
0.1975	312.59	0.9496
0.2456	312.59	0.9573
0.2961	312.59	0.9628
0.3463	312.59	0.9667
0.3976	312.59	0.9698
0.4480	312.59	0.9723
0.4983	312.59	0.9743
0.5002	312.59	0.9743
0.5496	312.58	0.9760
0.5990	312.59	0.9774
0.6496	312.59	0.9787
0.6992	312.59	0.9799
0.7486	312.59	0.9811
0.7988	312.59	0.9825
0.8490	312.58	0.9842
0.9011	312.59	0.9870
0.9490	312.59	0.9914
0.9711	312.59	0.9945
0.9932	312.59	0.9985
1.0000	312.59	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 1-Propene, 2-methyl- (1) - Liquid	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.0000	312.58	11.90
0.0080	312.59	22.70
0.0355	312.59	58.70
0.0483	312.59	74.30
0.0975	312.59	128.80
0.1465	312.59	175.50
0.1975	312.59	216.70
0.2456	312.59	249.60
0.2961	312.59	279.10
0.3463	312.59	303.90
0.3976	312.59	325.50
0.4480	312.59	343.90
0.4983	312.59	360.50
0.5002	312.59	361.90
0.5496	312.58	373.10
0.5990	312.59	383.30
0.6496	312.59	392.90
0.6992	312.59	401.60
0.7486	312.59	410.00
0.7988	312.59	418.50
0.8490	312.58	427.50
0.9011	312.59	438.10
0.9490	312.59	449.90
0.9711	312.59	456.50
0.9932	312.59	464.20
1.0000	312.59	467.10

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 1-Propene, 2-methyl- (1) - Liquid	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.0000	312.58	11.90
0.0080	312.59	22.70
0.0355	312.59	58.70
0.0483	312.59	74.30
0.0975	312.59	128.80
0.1465	312.59	175.50
0.1975	312.59	216.70
0.2456	312.59	249.60
0.2961	312.59	279.10
0.3463	312.59	303.90
0.3976	312.59	325.50
0.4480	312.59	343.90
0.4983	312.59	360.50
0.5002	312.59	361.90
0.5496	312.58	373.10
0.5990	312.59	383.30
0.6496	312.59	392.90
0.6992	312.59	401.60
0.7486	312.59	410.00
0.7988	312.59	418.50
0.8490	312.58	427.50
0.9011	312.59	438.10
0.9490	312.59	449.90
0.9711	312.59	456.50
0.9932	312.59	464.20
1.0000	312.59	467.10

Sources

• Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons