Mixture of 2-Butanone, 3-methyl- + Pentane, 2,2,4-trimethyl-

Datasets

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

Mole fraction of 2-Butanone, 3-methyl- (1) [ref]

Fixed		Measured
Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid	Temperature, K - Liquid	Mole fraction of 2-Butanone, 3-methyl- (1) - Gas
0.0000	330.00	0.0000
0.0000	340.00	0.0000
0.0160	330.00	0.0461
0.0168	340.00	0.0461
0.0473	340.00	0.1209
0.0496	330.00	0.1233
0.0975	340.00	0.2088
0.1023	330.00	0.2095
0.1704	330.00	0.2904
0.1747	340.00	0.2920
0.2516	330.00	0.3631
0.2571	340.00	0.3618
0.3484	330.00	0.4264
0.3485	340.00	0.4263
0.4472	340.00	0.4851
0.4476	330.00	0.4825
0.5433	340.00	0.5384
0.5437	330.00	0.5328
0.6337	340.00	0.5895
0.6363	330.00	0.5850
0.7143	340.00	0.6451
0.7187	330.00	0.6379
0.7841	340.00	0.6973
0.7886	330.00	0.6917
0.8786	340.00	0.7902
0.8818	330.00	0.7849
0.9192	340.00	0.8468
0.9227	330.00	0.8445
0.9526	340.00	0.9049
0.9542	330.00	0.8986
0.9758	340.00	0.9500
0.9776	330.00	0.9474
0.9909	340.00	0.9810
0.9914	330.00	0.9802
1.0000	330.00	1.0000
1.0000	340.00	1.0000

Mole fraction of 2-Butanone, 3-methyl- (1) [ref]

Fixed		Measured
Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid	Temperature, K - Liquid	Mole fraction of 2-Butanone, 3-methyl- (1) - Gas
0.0000	330.00	0.0000
0.0000	340.00	0.0000
0.0160	330.00	0.0461
0.0168	340.00	0.0461
0.0473	340.00	0.1209
0.0496	330.00	0.1233
0.0975	340.00	0.2088
0.1023	330.00	0.2095
0.1704	330.00	0.2904
0.1747	340.00	0.2920
0.2516	330.00	0.3631
0.2571	340.00	0.3618
0.3484	330.00	0.4264
0.3485	340.00	0.4263
0.4472	340.00	0.4851
0.4476	330.00	0.4825
0.5433	340.00	0.5384
0.5437	330.00	0.5328
0.6337	340.00	0.5895
0.6363	330.00	0.5850
0.7143	340.00	0.6451
0.7187	330.00	0.6379
0.7841	340.00	0.6973
0.7886	330.00	0.6917
0.8786	340.00	0.7902
0.8818	330.00	0.7849
0.9192	340.00	0.8468
0.9227	330.00	0.8445
0.9526	340.00	0.9049
0.9542	330.00	0.8986
0.9758	340.00	0.9500
0.9776	330.00	0.9474
0.9909	340.00	0.9810
0.9914	330.00	0.9802
1.0000	330.00	1.0000
1.0000	340.00	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	330.00	25.47
0.0000	340.00	36.64
0.0160	330.00	26.28
0.0168	340.00	37.78
0.0473	340.00	39.75
0.0496	330.00	27.68
0.0975	340.00	42.10
0.1023	330.00	29.38
0.1704	330.00	30.98
0.1747	340.00	44.40
0.2516	330.00	32.27
0.2571	340.00	46.15
0.3484	330.00	33.14
0.3485	340.00	47.46
0.4472	340.00	48.22
0.4476	330.00	33.70
0.5433	340.00	48.58
0.5437	330.00	33.91
0.6337	340.00	48.48
0.6363	330.00	33.76
0.7143	340.00	47.98
0.7187	330.00	33.36
0.7841	340.00	47.12
0.7886	330.00	32.71
0.8786	340.00	45.11
0.8818	330.00	31.19
0.9192	340.00	43.93
0.9227	330.00	30.28
0.9526	340.00	42.69
0.9542	330.00	29.34
0.9758	340.00	41.65
0.9776	330.00	28.54
0.9909	340.00	40.94
0.9914	330.00	28.01
1.0000	330.00	27.69
1.0000	340.00	40.45

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	330.00	25.47
0.0000	340.00	36.64
0.0160	330.00	26.28
0.0168	340.00	37.78
0.0473	340.00	39.75
0.0496	330.00	27.68
0.0975	340.00	42.10
0.1023	330.00	29.38
0.1704	330.00	30.98
0.1747	340.00	44.40
0.2516	330.00	32.27
0.2571	340.00	46.15
0.3484	330.00	33.14
0.3485	340.00	47.46
0.4472	340.00	48.22
0.4476	330.00	33.70
0.5433	340.00	48.58
0.5437	330.00	33.91
0.6337	340.00	48.48
0.6363	330.00	33.76
0.7143	340.00	47.98
0.7187	330.00	33.36
0.7841	340.00	47.12
0.7886	330.00	32.71
0.8786	340.00	45.11
0.8818	330.00	31.19
0.9192	340.00	43.93
0.9227	330.00	30.28
0.9526	340.00	42.69
0.9542	330.00	29.34
0.9758	340.00	41.65
0.9776	330.00	28.54
0.9909	340.00	40.94
0.9914	330.00	28.01
1.0000	330.00	27.69
1.0000	340.00	40.45

Sources

• Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, 3-methyl-2-butanone and 2,2,4-trimethylpentane