Mixture of Diisopropyl ether + 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
0.1350	313.15	0.1989
0.2075	313.15	0.2918
0.3131	313.15	0.4130
0.4443	313.15	0.5412
0.5888	313.15	0.6759
0.6669	313.15	0.7412
0.7336	313.15	0.7965
0.7880	313.15	0.8397
0.8447	313.15	0.8837
0.9017	313.15	0.9270
0.9486	313.15	0.9622
0.9862	313.15	0.9900
1.0000	313.15	1.0000
0.0000	323.15	0.0000
0.1355	323.15	0.1938
0.2095	323.15	0.2866
0.3163	323.15	0.4077
0.4506	323.15	0.5410
0.5882	323.15	0.6701
0.6689	323.15	0.7379
0.7336	323.15	0.7915
0.7900	323.15	0.8369
0.8450	323.15	0.8807
0.9017	323.15	0.9252
0.9486	323.15	0.9611
0.9863	323.15	0.9897
1.0000	323.15	1.0000
0.0000	333.15	0.0000
0.2116	333.15	0.2823
0.3174	333.15	0.4020
0.4518	333.15	0.5346
0.5898	333.15	0.6648
0.6702	333.15	0.7340
0.7343	333.15	0.7876
0.7893	333.15	0.8340
0.8455	333.15	0.8778
0.9027	333.15	0.9238
0.9484	333.15	0.9601
0.9863	333.15	0.9894
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
0.1350	313.15	0.1989
0.2075	313.15	0.2918
0.3131	313.15	0.4130
0.4443	313.15	0.5412
0.5888	313.15	0.6759
0.6669	313.15	0.7412
0.7336	313.15	0.7965
0.7880	313.15	0.8397
0.8447	313.15	0.8837
0.9017	313.15	0.9270
0.9486	313.15	0.9622
0.9862	313.15	0.9900
1.0000	313.15	1.0000
0.0000	323.15	0.0000
0.1355	323.15	0.1938
0.2095	323.15	0.2866
0.3163	323.15	0.4077
0.4506	323.15	0.5410
0.5882	323.15	0.6701
0.6689	323.15	0.7379
0.7336	323.15	0.7915
0.7900	323.15	0.8369
0.8450	323.15	0.8807
0.9017	323.15	0.9252
0.9486	323.15	0.9611
0.9863	323.15	0.9897
1.0000	323.15	1.0000
0.0000	333.15	0.0000
0.2116	333.15	0.2823
0.3174	333.15	0.4020
0.4518	333.15	0.5346
0.5898	333.15	0.6648
0.6702	333.15	0.7340
0.7343	333.15	0.7876
0.7893	333.15	0.8340
0.8455	333.15	0.8778
0.9027	333.15	0.9238
0.9484	333.15	0.9601
0.9863	333.15	0.9894
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	37.09
0.1350	313.15	39.99
0.2075	313.15	41.46
0.3131	313.15	43.65
0.4443	313.15	46.14
0.5888	313.15	48.73
0.6669	313.15	50.05
0.7336	313.15	51.14
0.7880	313.15	51.98
0.8447	313.15	52.85
0.9017	313.15	53.69
0.9486	313.15	54.37
0.9862	313.15	54.91
1.0000	313.15	55.13
0.0000	323.15	54.14
0.1355	323.15	58.06
0.2095	323.15	60.03
0.3163	323.15	62.89
0.4506	323.15	66.23
0.5882	323.15	69.54
0.6689	323.15	71.36
0.7336	323.15	72.76
0.7900	323.15	73.92
0.8450	323.15	75.04
0.9017	323.15	76.17
0.9486	323.15	77.04
0.9863	323.15	77.80
1.0000	323.15	78.12
0.0000	333.15	76.90
0.2116	333.15	84.58
0.3174	333.15	88.30
0.4518	333.15	92.59
0.5898	333.15	96.92
0.6702	333.15	99.25
0.7343	333.15	101.04
0.7893	333.15	102.57
0.8455	333.15	103.98
0.9027	333.15	105.47
0.9484	333.15	106.61
0.9863	333.15	107.57
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	37.09
0.1350	313.15	39.99
0.2075	313.15	41.46
0.3131	313.15	43.65
0.4443	313.15	46.14
0.5888	313.15	48.73
0.6669	313.15	50.05
0.7336	313.15	51.14
0.7880	313.15	51.98
0.8447	313.15	52.85
0.9017	313.15	53.69
0.9486	313.15	54.37
0.9862	313.15	54.91
1.0000	313.15	55.13
0.0000	323.15	54.14
0.1355	323.15	58.06
0.2095	323.15	60.03
0.3163	323.15	62.89
0.4506	323.15	66.23
0.5882	323.15	69.54
0.6689	323.15	71.36
0.7336	323.15	72.76
0.7900	323.15	73.92
0.8450	323.15	75.04
0.9017	323.15	76.17
0.9486	323.15	77.04
0.9863	323.15	77.80
1.0000	323.15	78.12
0.0000	333.15	76.90
0.2116	333.15	84.58
0.3174	333.15	88.30
0.4518	333.15	92.59
0.5898	333.15	96.92
0.6702	333.15	99.25
0.7343	333.15	101.04
0.7893	333.15	102.57
0.8455	333.15	103.98
0.9027	333.15	105.47
0.9484	333.15	106.61
0.9863	333.15	107.57
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