Mixture of Isobutyl acetate + 1-Propanol, 2-methyl-

Datasets

1. Mole fraction (4)
2. T_boil - Boiling temperature at pressure P, K (4)

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

Fixed		Measured
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Pressure, kPa - Gas	Mole fraction of 1-Propanol, 2-methyl- (2) - Gas
0.0000	20.00	0.0000
0.0000	100.00	0.0000
0.0480	20.00	0.0790
0.0540	100.00	0.0940
0.0740	20.00	0.1190
0.1030	100.00	0.1720
0.1150	20.00	0.1660
0.1670	100.00	0.2520
0.1850	20.00	0.2470
0.2400	100.00	0.3220
0.2530	20.00	0.3140
0.2790	100.00	0.3760
0.3200	20.00	0.3680
0.3290	100.00	0.4160
0.3840	20.00	0.4190
0.3880	100.00	0.4740
0.4370	100.00	0.5160
0.4490	20.00	0.4660
0.4800	100.00	0.5530
0.5090	20.00	0.5080
0.5440	100.00	0.6020
0.5640	20.00	0.5450
0.5830	100.00	0.6400
0.6150	20.00	0.5830
0.6310	100.00	0.6790
0.6630	20.00	0.6130
0.6760	100.00	0.7130
0.6970	20.00	0.6420
0.7230	100.00	0.7490
0.7390	20.00	0.6770
0.7630	100.00	0.7790
0.7790	20.00	0.7130
0.8110	100.00	0.8180
0.8140	20.00	0.7490
0.8530	20.00	0.7860
0.8540	100.00	0.8570
0.8910	100.00	0.8900
0.8960	20.00	0.8410
0.9230	100.00	0.9210
0.9240	20.00	0.8800
0.9560	100.00	0.9520
0.9570	20.00	0.9260
1.0000	20.00	1.0000
1.0000	100.00	1.0000

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

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Mole fraction of 1-Propanol, 2-methyl- (2) - Gas
0.0000	0.0000
0.0490	0.0850
0.0770	0.1270
0.0920	0.1520
0.1800	0.2700
0.2300	0.3340
0.3210	0.4190
0.3620	0.4600
0.3930	0.4830
0.4310	0.5130
0.4990	0.5760
0.5330	0.6070
0.6200	0.6700
0.6480	0.6850
0.7280	0.7490
0.7550	0.7720
0.8350	0.8440
0.8560	0.8580
0.9090	0.9020
1.0000	1.0000

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

Fixed		Measured
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Pressure, kPa - Gas	Mole fraction of 1-Propanol, 2-methyl- (2) - Gas
0.0000	20.00	0.0000
0.0000	100.00	0.0000
0.0480	20.00	0.0790
0.0540	100.00	0.0940
0.0740	20.00	0.1190
0.1030	100.00	0.1720
0.1150	20.00	0.1660
0.1670	100.00	0.2520
0.1850	20.00	0.2470
0.2400	100.00	0.3220
0.2530	20.00	0.3140
0.2790	100.00	0.3760
0.3200	20.00	0.3680
0.3290	100.00	0.4160
0.3840	20.00	0.4190
0.3880	100.00	0.4740
0.4370	100.00	0.5160
0.4490	20.00	0.4660
0.4800	100.00	0.5530
0.5090	20.00	0.5080
0.5440	100.00	0.6020
0.5640	20.00	0.5450
0.5830	100.00	0.6400
0.6150	20.00	0.5830
0.6310	100.00	0.6790
0.6630	20.00	0.6130
0.6760	100.00	0.7130
0.6970	20.00	0.6420
0.7230	100.00	0.7490
0.7390	20.00	0.6770
0.7630	100.00	0.7790
0.7790	20.00	0.7130
0.8110	100.00	0.8180
0.8140	20.00	0.7490
0.8530	20.00	0.7860
0.8540	100.00	0.8570
0.8910	100.00	0.8900
0.8960	20.00	0.8410
0.9230	100.00	0.9210
0.9240	20.00	0.8800
0.9560	100.00	0.9520
0.9570	20.00	0.9260
1.0000	20.00	1.0000
1.0000	100.00	1.0000

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

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Mole fraction of 1-Propanol, 2-methyl- (2) - Gas
0.0000	0.0000
0.0490	0.0850
0.0770	0.1270
0.0920	0.1520
0.1800	0.2700
0.2300	0.3340
0.3210	0.4190
0.3620	0.4600
0.3930	0.4830
0.4310	0.5130
0.4990	0.5760
0.5330	0.6070
0.6200	0.6700
0.6480	0.6850
0.7280	0.7490
0.7550	0.7720
0.8350	0.8440
0.8560	0.8580
0.9090	0.9020
1.0000	1.0000

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	20.00	342.95
0.0000	100.00	389.90
0.0480	20.00	341.96
0.0540	100.00	388.48
0.0740	20.00	341.53
0.1030	100.00	387.28
0.1150	20.00	341.02
0.1670	100.00	386.10
0.1850	20.00	340.25
0.2400	100.00	385.07
0.2530	20.00	339.76
0.2790	100.00	384.38
0.3200	20.00	339.45
0.3290	100.00	383.75
0.3840	20.00	339.22
0.3880	100.00	383.10
0.4370	100.00	382.68
0.4490	20.00	339.14
0.4800	100.00	382.26
0.5090	20.00	339.13
0.5440	100.00	381.93
0.5640	20.00	339.18
0.5830	100.00	381.64
0.6150	20.00	339.28
0.6310	100.00	381.36
0.6630	20.00	339.42
0.6760	100.00	381.16
0.6970	20.00	339.56
0.7230	100.00	381.00
0.7390	20.00	339.75
0.7630	100.00	380.88
0.7790	20.00	340.02
0.8110	100.00	380.80
0.8140	20.00	340.27
0.8530	20.00	340.58
0.8540	100.00	380.76
0.8910	100.00	380.76
0.8960	20.00	340.98
0.9230	100.00	380.80
0.9240	20.00	341.35
0.9560	100.00	380.86
0.9570	20.00	341.77
1.0000	20.00	342.52
1.0000	100.00	381.09

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	389.90
0.0490	388.55
0.0770	387.79
0.0920	387.17
0.1800	385.73
0.2300	384.88
0.3210	383.56
0.3620	382.97
0.3930	382.83
0.4310	382.37
0.4990	381.95
0.5330	381.88
0.6200	381.34
0.6480	380.96
0.7280	380.74
0.7550	380.82
0.8350	380.56
0.8560	380.32
0.9090	380.51
1.0000	380.98

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	20.00	342.95
0.0000	100.00	389.90
0.0480	20.00	341.96
0.0540	100.00	388.48
0.0740	20.00	341.53
0.1030	100.00	387.28
0.1150	20.00	341.02
0.1670	100.00	386.10
0.1850	20.00	340.25
0.2400	100.00	385.07
0.2530	20.00	339.76
0.2790	100.00	384.38
0.3200	20.00	339.45
0.3290	100.00	383.75
0.3840	20.00	339.22
0.3880	100.00	383.10
0.4370	100.00	382.68
0.4490	20.00	339.14
0.4800	100.00	382.26
0.5090	20.00	339.13
0.5440	100.00	381.93
0.5640	20.00	339.18
0.5830	100.00	381.64
0.6150	20.00	339.28
0.6310	100.00	381.36
0.6630	20.00	339.42
0.6760	100.00	381.16
0.6970	20.00	339.56
0.7230	100.00	381.00
0.7390	20.00	339.75
0.7630	100.00	380.88
0.7790	20.00	340.02
0.8110	100.00	380.80
0.8140	20.00	340.27
0.8530	20.00	340.58
0.8540	100.00	380.76
0.8910	100.00	380.76
0.8960	20.00	340.98
0.9230	100.00	380.80
0.9240	20.00	341.35
0.9560	100.00	380.86
0.9570	20.00	341.77
1.0000	20.00	342.52
1.0000	100.00	381.09

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	389.90
0.0490	388.55
0.0770	387.79
0.0920	387.17
0.1800	385.73
0.2300	384.88
0.3210	383.56
0.3620	382.97
0.3930	382.83
0.4310	382.37
0.4990	381.95
0.5330	381.88
0.6200	381.34
0.6480	380.96
0.7280	380.74
0.7550	380.82
0.8350	380.56
0.8560	380.32
0.9090	380.51
1.0000	380.98

Sources

• Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa
• Isobaric Vapor Liquid Equilibrium for the Binary and Ternary System with Isobutyl Alcohol, Isobutyl Acetate and Dimethyl Sulfoxide at 101.3 kPa