Mixture of 2-Butanone, 3-methyl- + Butane, 2,3-dimethyl-

Datasets

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

Mole fraction of Butane, 2,3-dimethyl- (2) [ref]

Fixed		Measured
Mole fraction of Butane, 2,3-dimethyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 2,3-dimethyl- (2) - Gas
0.0000	313.15	0.0000
0.0029	313.15	0.0277
0.0088	313.15	0.0750
0.0183	313.15	0.1532
0.0394	313.15	0.2707
0.0754	313.15	0.4210
0.0994	313.15	0.4829
0.1532	313.15	0.5799
0.1874	313.15	0.6330
0.2557	313.15	0.6905
0.3536	313.15	0.7503
0.4424	313.15	0.7883
0.5504	313.15	0.8224
0.6520	313.15	0.8533
0.7417	313.15	0.8812
0.8256	313.15	0.9089
0.8893	313.15	0.9341
1.0000	313.15	1.0000
0.0000	323.15	0.0000
0.0036	323.15	0.0309
0.0096	323.15	0.0778
0.0206	323.15	0.1506
0.0436	323.15	0.2749
0.0756	323.15	0.3926
0.1106	323.15	0.4756
0.1516	323.15	0.5551
0.2033	323.15	0.6222
0.2472	323.15	0.6652
0.3471	323.15	0.7304
0.4395	323.15	0.7726
0.5455	323.15	0.8102
0.6576	323.15	0.8457
0.7431	323.15	0.8728
0.8260	323.15	0.9038
0.8883	323.15	0.9317
1.0000	323.15	1.0000
0.0000	333.15	0.0000
0.0111	333.15	0.0797
0.0224	333.15	0.1504
0.0475	333.15	0.2700
0.0765	333.15	0.3713
0.1114	333.15	0.4588
0.1496	333.15	0.5273
0.2079	333.15	0.6016
0.2544	333.15	0.6451
0.3472	333.15	0.7070
0.4413	333.15	0.7525
0.5484	333.15	0.7988
0.6592	333.15	0.8354
0.7440	333.15	0.8652
0.8256	333.15	0.8974
0.8895	333.15	0.9286
1.0000	333.15	1.0000

Mole fraction of Butane, 2,3-dimethyl- (2) [ref]

Fixed		Measured
Mole fraction of Butane, 2,3-dimethyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 2,3-dimethyl- (2) - Gas
0.0000	313.15	0.0000
0.0029	313.15	0.0277
0.0088	313.15	0.0750
0.0183	313.15	0.1532
0.0394	313.15	0.2707
0.0754	313.15	0.4210
0.0994	313.15	0.4829
0.1532	313.15	0.5799
0.1874	313.15	0.6330
0.2557	313.15	0.6905
0.3536	313.15	0.7503
0.4424	313.15	0.7883
0.5504	313.15	0.8224
0.6520	313.15	0.8533
0.7417	313.15	0.8812
0.8256	313.15	0.9089
0.8893	313.15	0.9341
1.0000	313.15	1.0000
0.0000	323.15	0.0000
0.0036	323.15	0.0309
0.0096	323.15	0.0778
0.0206	323.15	0.1506
0.0436	323.15	0.2749
0.0756	323.15	0.3926
0.1106	323.15	0.4756
0.1516	323.15	0.5551
0.2033	323.15	0.6222
0.2472	323.15	0.6652
0.3471	323.15	0.7304
0.4395	323.15	0.7726
0.5455	323.15	0.8102
0.6576	323.15	0.8457
0.7431	323.15	0.8728
0.8260	323.15	0.9038
0.8883	323.15	0.9317
1.0000	323.15	1.0000
0.0000	333.15	0.0000
0.0111	333.15	0.0797
0.0224	333.15	0.1504
0.0475	333.15	0.2700
0.0765	333.15	0.3713
0.1114	333.15	0.4588
0.1496	333.15	0.5273
0.2079	333.15	0.6016
0.2544	333.15	0.6451
0.3472	333.15	0.7070
0.4413	333.15	0.7525
0.5484	333.15	0.7988
0.6592	333.15	0.8354
0.7440	333.15	0.8652
0.8256	333.15	0.8974
0.8895	333.15	0.9286
1.0000	333.15	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 2,3-dimethyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	313.15	13.73
0.0029	313.15	14.11
0.0088	313.15	14.79
0.0183	313.15	16.07
0.0394	313.15	18.46
0.0754	313.15	22.21
0.0994	313.15	24.56
0.1532	313.15	28.87
0.1874	313.15	31.62
0.2557	313.15	35.44
0.3536	313.15	40.04
0.4424	313.15	43.45
0.5504	313.15	46.61
0.6520	313.15	49.30
0.7417	313.15	51.10
0.8256	313.15	52.67
0.8893	313.15	53.77
1.0000	313.15	55.13
0.0000	323.15	21.09
0.0036	323.15	21.73
0.0096	323.15	22.78
0.0206	323.15	24.59
0.0436	323.15	28.09
0.0756	323.15	32.51
0.1106	323.15	36.56
0.1516	323.15	41.42
0.2033	323.15	46.54
0.2472	323.15	50.40
0.3471	323.15	56.82
0.4395	323.15	61.56
0.5455	323.15	66.15
0.6576	323.15	70.02
0.7431	323.15	72.54
0.8260	323.15	74.73
0.8883	323.15	76.22
1.0000	323.15	78.12
0.0000	333.15	31.43
0.0111	333.15	33.93
0.0224	333.15	36.47
0.0475	333.15	41.44
0.0765	333.15	46.57
0.1114	333.15	52.74
0.1496	333.15	58.13
0.2079	333.15	65.98
0.2544	333.15	70.20
0.3472	333.15	78.83
0.4413	333.15	85.42
0.5484	333.15	91.68
0.6592	333.15	97.08
0.7440	333.15	100.49
0.8256	333.15	103.47
0.8895	333.15	105.46
1.0000	333.15	107.99

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 2,3-dimethyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	313.15	13.73
0.0029	313.15	14.11
0.0088	313.15	14.79
0.0183	313.15	16.07
0.0394	313.15	18.46
0.0754	313.15	22.21
0.0994	313.15	24.56
0.1532	313.15	28.87
0.1874	313.15	31.62
0.2557	313.15	35.44
0.3536	313.15	40.04
0.4424	313.15	43.45
0.5504	313.15	46.61
0.6520	313.15	49.30
0.7417	313.15	51.10
0.8256	313.15	52.67
0.8893	313.15	53.77
1.0000	313.15	55.13
0.0000	323.15	21.09
0.0036	323.15	21.73
0.0096	323.15	22.78
0.0206	323.15	24.59
0.0436	323.15	28.09
0.0756	323.15	32.51
0.1106	323.15	36.56
0.1516	323.15	41.42
0.2033	323.15	46.54
0.2472	323.15	50.40
0.3471	323.15	56.82
0.4395	323.15	61.56
0.5455	323.15	66.15
0.6576	323.15	70.02
0.7431	323.15	72.54
0.8260	323.15	74.73
0.8883	323.15	76.22
1.0000	323.15	78.12
0.0000	333.15	31.43
0.0111	333.15	33.93
0.0224	333.15	36.47
0.0475	333.15	41.44
0.0765	333.15	46.57
0.1114	333.15	52.74
0.1496	333.15	58.13
0.2079	333.15	65.98
0.2544	333.15	70.20
0.3472	333.15	78.83
0.4413	333.15	85.42
0.5484	333.15	91.68
0.6592	333.15	97.08
0.7440	333.15	100.49
0.8256	333.15	103.47
0.8895	333.15	105.46
1.0000	333.15	107.99

Sources

• Vapour-liquid equilibria in binary and ternary systems composed of 2,3-dimethylbutane, diisopropyl ether, and 3-methyl-2-butanone at 313.15, 323.15 and 313.15 K