Mixture of Butane, 1-ethoxy- + Propane, 2-chloro-2-methyl-

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. ρ_l - Mass density, kg/m3 (2)

Mole fraction of Propane, 2-chloro-2-methyl- (2) [ref]

Fixed		Measured
Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Gas
0.0214	288.15	0.1229
0.0638	298.15	0.2774
0.0651	308.15	0.2596
0.1007	288.15	0.4085
0.1459	298.15	0.4755
0.1596	308.15	0.4801
0.1991	288.15	0.5998
0.2670	298.15	0.6488
0.2706	308.15	0.6377
0.2813	288.15	0.6850
0.3228	298.15	0.7054
0.3275	308.15	0.6895
0.4119	298.15	0.7501
0.4187	308.15	0.7651
0.4447	288.15	0.8161
0.4927	288.15	0.8324
0.5026	298.15	0.8347
0.5037	308.15	0.8240
0.5223	288.15	0.8527
0.5484	298.15	0.8568
0.5678	308.15	0.8568
0.6585	288.15	0.9189
0.6782	298.15	0.9024
0.6884	308.15	0.9105
0.7452	288.15	0.9364
0.7681	298.15	0.9354
0.7701	308.15	0.9392
0.8327	288.15	0.9656
0.8404	298.15	0.9611
0.8462	308.15	0.9611
0.9161	288.15	0.9827
0.9198	298.15	0.9818
0.9245	308.15	0.9800

Mole fraction of Propane, 2-chloro-2-methyl- (2) [ref]

Fixed		Measured
Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Gas
0.0214	288.15	0.1229
0.0638	298.15	0.2774
0.0651	308.15	0.2596
0.1007	288.15	0.4085
0.1459	298.15	0.4755
0.1596	308.15	0.4801
0.1991	288.15	0.5998
0.2670	298.15	0.6488
0.2706	308.15	0.6377
0.2813	288.15	0.6850
0.3228	298.15	0.7054
0.3275	308.15	0.6895
0.4119	298.15	0.7501
0.4187	308.15	0.7651
0.4447	288.15	0.8161
0.4927	288.15	0.8324
0.5026	298.15	0.8347
0.5037	308.15	0.8240
0.5223	288.15	0.8527
0.5484	298.15	0.8568
0.5678	308.15	0.8568
0.6585	288.15	0.9189
0.6782	298.15	0.9024
0.6884	308.15	0.9105
0.7452	288.15	0.9364
0.7681	298.15	0.9354
0.7701	308.15	0.9392
0.8327	288.15	0.9656
0.8404	298.15	0.9611
0.8462	308.15	0.9611
0.9161	288.15	0.9827
0.9198	298.15	0.9818
0.9245	308.15	0.9800

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0214	288.15	5.04
0.0638	298.15	9.80
0.0651	308.15	15.61
0.1007	288.15	6.82
0.1459	298.15	12.71
0.1596	308.15	20.42
0.1991	288.15	9.09
0.2670	298.15	16.62
0.2706	308.15	25.45
0.2813	288.15	10.70
0.3228	298.15	18.22
0.3275	308.15	28.25
0.4119	298.15	21.03
0.4187	308.15	32.47
0.4447	288.15	14.36
0.4927	288.15	15.25
0.5026	298.15	24.14
0.5037	308.15	36.33
0.5223	288.15	16.05
0.5484	298.15	25.59
0.5678	308.15	39.10
0.6585	288.15	18.88
0.6782	298.15	29.57
0.6884	308.15	44.70
0.7452	288.15	20.86
0.7681	298.15	32.45
0.7701	308.15	48.52
0.8327	288.15	22.70
0.8404	298.15	34.81
0.8462	308.15	52.10
0.9161	288.15	24.62
0.9198	298.15	37.42
0.9245	308.15	56.12

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0214	288.15	5.04
0.0638	298.15	9.80
0.0651	308.15	15.61
0.1007	288.15	6.82
0.1459	298.15	12.71
0.1596	308.15	20.42
0.1991	288.15	9.09
0.2670	298.15	16.62
0.2706	308.15	25.45
0.2813	288.15	10.70
0.3228	298.15	18.22
0.3275	308.15	28.25
0.4119	298.15	21.03
0.4187	308.15	32.47
0.4447	288.15	14.36
0.4927	288.15	15.25
0.5026	298.15	24.14
0.5037	308.15	36.33
0.5223	288.15	16.05
0.5484	298.15	25.59
0.5678	308.15	39.10
0.6585	288.15	18.88
0.6782	298.15	29.57
0.6884	308.15	44.70
0.7452	288.15	20.86
0.7681	298.15	32.45
0.7701	308.15	48.52
0.8327	288.15	22.70
0.8404	298.15	34.81
0.8462	308.15	52.10
0.9161	288.15	24.62
0.9198	298.15	37.42
0.9245	308.15	56.12

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	759.632
283.15	0.0513	763.717
283.15	0.1036	767.95
283.15	0.2014	776.093
283.15	0.2999	784.57
283.15	0.4014	793.617
283.15	0.4981	802.566
283.15	0.5997	812.333
283.15	0.6993	822.302
283.15	0.7999	832.784
283.15	0.8997	843.668
283.15	0.9492	849.296
283.15	1.0000	855.249
288.15	0.0000	754.838
288.15	0.0513	758.88
288.15	0.1036	763.077
288.15	0.2014	771.117
288.15	0.2999	779.5
288.15	0.4014	788.445
288.15	0.4981	797.281
288.15	0.5997	806.924
288.15	0.6993	816.764
288.15	0.7999	827.106
288.15	0.8997	837.83
288.15	0.9492	843.371
288.15	1.0000	849.243
293.15	0.0000	750.018
293.15	0.0513	754.015
293.15	0.1036	758.169
293.15	0.2014	766.112
293.15	0.2999	774.394
293.15	0.4014	783.227
293.15	0.4981	791.954
293.15	0.5997	801.472
293.15	0.6993	811.175
293.15	0.7999	821.38
293.15	0.8997	831.949
293.15	0.9492	837.407
293.15	1.0000	843.191
298.15	0.0000	745.173
298.15	0.0513	749.127
298.15	0.1036	753.235
298.15	0.2014	761.079
298.15	0.2999	769.258
298.15	0.4014	777.984
298.15	0.4981	786.598
298.15	0.5997	795.991
298.15	0.6993	805.576
298.15	0.7999	815.625
298.15	0.8997	826.038
298.15	0.9492	831.404
298.15	1.0000	837.096
303.15	0.0000	740.3
303.15	0.0513	744.21
303.15	0.1036	748.267
303.15	0.2014	756.014
303.15	0.2999	764.087
303.15	0.4014	772.7
303.15	0.4981	781.202
303.15	0.5997	790.468
303.15	0.6993	799.919
303.15	0.7999	809.827
303.15	0.8997	820.071
303.15	0.9492	825.359
303.15	1.0000	830.958
308.15	0.0000	735.393
308.15	0.0513	739.257
308.15	0.1036	743.265
308.15	0.2014	750.913
308.15	0.2999	758.885
308.15	0.4014	767.383
308.15	0.4981	775.775
308.15	0.5997	784.917
308.15	0.6993	794.231
308.15	0.7999	803.986
308.15	0.8997	814.067
308.15	0.9492	819.262
308.15	1.0000	824.772
313.15	0.0000	730.451
313.15	0.0513	734.27
313.15	0.1036	738.231
313.15	0.2014	745.779
313.15	0.2999	753.639
313.15	0.4014	762.025
313.15	0.4981	770.298
313.15	0.5997	779.314
313.15	0.6993	788.493
313.15	0.7999	798.098
313.15	0.8997	808.015
313.15	0.9492	813.117
313.15	1.0000	818.536

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	759.632
283.15	0.0513	763.717
283.15	0.1036	767.95
283.15	0.2014	776.093
283.15	0.2999	784.57
283.15	0.4014	793.617
283.15	0.4981	802.566
283.15	0.5997	812.333
283.15	0.6993	822.302
283.15	0.7999	832.784
283.15	0.8997	843.668
283.15	0.9492	849.296
283.15	1.0000	855.249
288.15	0.0000	754.838
288.15	0.0513	758.88
288.15	0.1036	763.077
288.15	0.2014	771.117
288.15	0.2999	779.5
288.15	0.4014	788.445
288.15	0.4981	797.281
288.15	0.5997	806.924
288.15	0.6993	816.764
288.15	0.7999	827.106
288.15	0.8997	837.83
288.15	0.9492	843.371
288.15	1.0000	849.243
293.15	0.0000	750.018
293.15	0.0513	754.015
293.15	0.1036	758.169
293.15	0.2014	766.112
293.15	0.2999	774.394
293.15	0.4014	783.227
293.15	0.4981	791.954
293.15	0.5997	801.472
293.15	0.6993	811.175
293.15	0.7999	821.38
293.15	0.8997	831.949
293.15	0.9492	837.407
293.15	1.0000	843.191
298.15	0.0000	745.173
298.15	0.0513	749.127
298.15	0.1036	753.235
298.15	0.2014	761.079
298.15	0.2999	769.258
298.15	0.4014	777.984
298.15	0.4981	786.598
298.15	0.5997	795.991
298.15	0.6993	805.576
298.15	0.7999	815.625
298.15	0.8997	826.038
298.15	0.9492	831.404
298.15	1.0000	837.096
303.15	0.0000	740.3
303.15	0.0513	744.21
303.15	0.1036	748.267
303.15	0.2014	756.014
303.15	0.2999	764.087
303.15	0.4014	772.7
303.15	0.4981	781.202
303.15	0.5997	790.468
303.15	0.6993	799.919
303.15	0.7999	809.827
303.15	0.8997	820.071
303.15	0.9492	825.359
303.15	1.0000	830.958
308.15	0.0000	735.393
308.15	0.0513	739.257
308.15	0.1036	743.265
308.15	0.2014	750.913
308.15	0.2999	758.885
308.15	0.4014	767.383
308.15	0.4981	775.775
308.15	0.5997	784.917
308.15	0.6993	794.231
308.15	0.7999	803.986
308.15	0.8997	814.067
308.15	0.9492	819.262
308.15	1.0000	824.772
313.15	0.0000	730.451
313.15	0.0513	734.27
313.15	0.1036	738.231
313.15	0.2014	745.779
313.15	0.2999	753.639
313.15	0.4014	762.025
313.15	0.4981	770.298
313.15	0.5997	779.314
313.15	0.6993	788.493
313.15	0.7999	798.098
313.15	0.8997	808.015
313.15	0.9492	813.117
313.15	1.0000	818.536

Sources

• Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether