Mixture of Butane, 1-ethoxy- + Butane, 1-chloro-

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. ρ_l - Mass density, kg/m3 (2)

Mole fraction of Butane, 1-chloro- (2) [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Gas
0.0695	308.15	0.1150
0.0698	298.15	0.1200
0.0701	288.15	0.1260
0.1273	288.15	0.2093
0.1317	308.15	0.2058
0.1335	298.15	0.2101
0.2170	288.15	0.3262
0.2263	298.15	0.3359
0.2331	308.15	0.3440
0.3123	288.15	0.4548
0.3172	298.15	0.4525
0.3262	308.15	0.4564
0.3808	288.15	0.5263
0.3982	298.15	0.5388
0.4021	308.15	0.5344
0.4449	288.15	0.6018
0.4587	298.15	0.6039
0.4602	308.15	0.6004
0.5085	288.15	0.6704
0.5234	308.15	0.6538
0.5248	298.15	0.6621
0.5789	288.15	0.7227
0.5961	298.15	0.7220
0.6032	308.15	0.7146
0.6427	288.15	0.7789
0.6510	298.15	0.7684
0.6601	308.15	0.7678
0.7119	288.15	0.8176
0.7207	298.15	0.8195
0.7267	308.15	0.8163
0.8060	288.15	0.8841
0.8131	308.15	0.8804
0.8137	298.15	0.8835
0.8841	288.15	0.9334
0.8878	298.15	0.9316
0.8884	308.15	0.9298
0.9346	308.15	0.9597
0.9352	288.15	0.9626
0.9358	298.15	0.9608

Mole fraction of Butane, 1-chloro- (2) [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Gas
0.0695	308.15	0.1150
0.0698	298.15	0.1200
0.0701	288.15	0.1260
0.1273	288.15	0.2093
0.1317	308.15	0.2058
0.1335	298.15	0.2101
0.2170	288.15	0.3262
0.2263	298.15	0.3359
0.2331	308.15	0.3440
0.3123	288.15	0.4548
0.3172	298.15	0.4525
0.3262	308.15	0.4564
0.3808	288.15	0.5263
0.3982	298.15	0.5388
0.4021	308.15	0.5344
0.4449	288.15	0.6018
0.4587	298.15	0.6039
0.4602	308.15	0.6004
0.5085	288.15	0.6704
0.5234	308.15	0.6538
0.5248	298.15	0.6621
0.5789	288.15	0.7227
0.5961	298.15	0.7220
0.6032	308.15	0.7146
0.6427	288.15	0.7789
0.6510	298.15	0.7684
0.6601	308.15	0.7678
0.7119	288.15	0.8176
0.7207	298.15	0.8195
0.7267	308.15	0.8163
0.8060	288.15	0.8841
0.8131	308.15	0.8804
0.8137	298.15	0.8835
0.8841	288.15	0.9334
0.8878	298.15	0.9316
0.8884	308.15	0.9298
0.9346	308.15	0.9597
0.9352	288.15	0.9626
0.9358	298.15	0.9608

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0005
283.15	0.0515	0.0005
283.15	0.1016	0.0005
283.15	0.2008	0.0005
283.15	0.3003	0.0005
283.15	0.4002	0.0005
283.15	0.5014	0.0005
283.15	0.6023	0.0005
283.15	0.7003	0.0005
283.15	0.8004	0.0005
283.15	0.9006	0.0005
283.15	0.9502	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0005
288.15	0.0515	0.0005
288.15	0.1016	0.0005
288.15	0.2008	0.0005
288.15	0.3003	0.0005
288.15	0.4002	0.0005
288.15	0.5014	0.0005
288.15	0.6023	0.0005
288.15	0.7003	0.0005
288.15	0.8004	0.0005
288.15	0.9006	0.0005
288.15	0.9502	0.0005
288.15	1.0000	0.0005
293.15	0.0000	0.0004
293.15	0.0515	0.0004
293.15	0.1016	0.0004
293.15	0.2008	0.0004
293.15	0.3003	0.0004
293.15	0.4002	0.0004
293.15	0.5014	0.0004
293.15	0.6023	0.0004
293.15	0.7003	0.0004
293.15	0.8004	0.0004
293.15	0.9006	0.0004
293.15	0.9502	0.0004
293.15	1.0000	0.0004
298.15	0.0000	0.0004
298.15	0.0515	0.0004
298.15	0.1016	0.0004
298.15	0.2008	0.0004
298.15	0.3003	0.0004
298.15	0.4002	0.0004
298.15	0.5014	0.0004
298.15	0.6023	0.0004
298.15	0.7003	0.0004
298.15	0.8004	0.0004
298.15	0.9006	0.0004
298.15	0.9502	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0004
303.15	0.0515	0.0004
303.15	0.1016	0.0004
303.15	0.2008	0.0004
303.15	0.3003	0.0004
303.15	0.4002	0.0004
303.15	0.5014	0.0004
303.15	0.6023	0.0004
303.15	0.7003	0.0004
303.15	0.8004	0.0004
303.15	0.9006	0.0004
303.15	0.9502	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0004
308.15	0.0515	0.0004
308.15	0.1016	0.0004
308.15	0.2008	0.0004
308.15	0.3003	0.0004
308.15	0.4002	0.0004
308.15	0.5014	0.0004
308.15	0.6023	0.0004
308.15	0.7003	0.0004
308.15	0.8004	0.0004
308.15	0.9006	0.0004
308.15	0.9502	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0515	0.0003
313.15	0.1016	0.0003
313.15	0.2008	0.0003
313.15	0.3003	0.0003
313.15	0.4002	0.0003
313.15	0.5014	0.0004
313.15	0.6023	0.0004
313.15	0.7003	0.0004
313.15	0.8004	0.0004
313.15	0.9006	0.0004
313.15	0.9502	0.0004
313.15	1.0000	0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0005
283.15	0.0515	0.0005
283.15	0.1016	0.0005
283.15	0.2008	0.0005
283.15	0.3003	0.0005
283.15	0.4002	0.0005
283.15	0.5014	0.0005
283.15	0.6023	0.0005
283.15	0.7003	0.0005
283.15	0.8004	0.0005
283.15	0.9006	0.0005
283.15	0.9502	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0005
288.15	0.0515	0.0005
288.15	0.1016	0.0005
288.15	0.2008	0.0005
288.15	0.3003	0.0005
288.15	0.4002	0.0005
288.15	0.5014	0.0005
288.15	0.6023	0.0005
288.15	0.7003	0.0005
288.15	0.8004	0.0005
288.15	0.9006	0.0005
288.15	0.9502	0.0005
288.15	1.0000	0.0005
293.15	0.0000	0.0004
293.15	0.0515	0.0004
293.15	0.1016	0.0004
293.15	0.2008	0.0004
293.15	0.3003	0.0004
293.15	0.4002	0.0004
293.15	0.5014	0.0004
293.15	0.6023	0.0004
293.15	0.7003	0.0004
293.15	0.8004	0.0004
293.15	0.9006	0.0004
293.15	0.9502	0.0004
293.15	1.0000	0.0004
298.15	0.0000	0.0004
298.15	0.0515	0.0004
298.15	0.1016	0.0004
298.15	0.2008	0.0004
298.15	0.3003	0.0004
298.15	0.4002	0.0004
298.15	0.5014	0.0004
298.15	0.6023	0.0004
298.15	0.7003	0.0004
298.15	0.8004	0.0004
298.15	0.9006	0.0004
298.15	0.9502	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0004
303.15	0.0515	0.0004
303.15	0.1016	0.0004
303.15	0.2008	0.0004
303.15	0.3003	0.0004
303.15	0.4002	0.0004
303.15	0.5014	0.0004
303.15	0.6023	0.0004
303.15	0.7003	0.0004
303.15	0.8004	0.0004
303.15	0.9006	0.0004
303.15	0.9502	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0004
308.15	0.0515	0.0004
308.15	0.1016	0.0004
308.15	0.2008	0.0004
308.15	0.3003	0.0004
308.15	0.4002	0.0004
308.15	0.5014	0.0004
308.15	0.6023	0.0004
308.15	0.7003	0.0004
308.15	0.8004	0.0004
308.15	0.9006	0.0004
308.15	0.9502	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0515	0.0003
313.15	0.1016	0.0003
313.15	0.2008	0.0003
313.15	0.3003	0.0003
313.15	0.4002	0.0003
313.15	0.5014	0.0004
313.15	0.6023	0.0004
313.15	0.7003	0.0004
313.15	0.8004	0.0004
313.15	0.9006	0.0004
313.15	0.9502	0.0004
313.15	1.0000	0.0004

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0695	308.15	12.86
0.0698	298.15	7.96
0.0701	288.15	4.75
0.1273	288.15	5.01
0.1317	308.15	13.30
0.1335	298.15	8.31
0.2170	288.15	5.33
0.2263	298.15	8.86
0.2331	308.15	14.29
0.3123	288.15	5.72
0.3172	298.15	9.45
0.3262	308.15	15.16
0.3808	288.15	5.99
0.3982	298.15	9.90
0.4021	308.15	15.86
0.4449	288.15	6.25
0.4587	298.15	10.27
0.4602	308.15	16.34
0.5085	288.15	6.46
0.5234	308.15	16.83
0.5248	298.15	10.55
0.5789	288.15	6.75
0.5961	298.15	11.04
0.6032	308.15	17.43
0.6427	288.15	6.97
0.6510	298.15	11.38
0.6601	308.15	18.08
0.7119	288.15	7.18
0.7207	298.15	11.76
0.7267	308.15	18.67
0.8060	288.15	7.52
0.8131	308.15	19.51
0.8137	298.15	12.32
0.8841	288.15	7.84
0.8878	298.15	12.73
0.8884	308.15	20.14
0.9346	308.15	20.50
0.9352	288.15	8.09
0.9358	298.15	12.97

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0695	308.15	12.86
0.0698	298.15	7.96
0.0701	288.15	4.75
0.1273	288.15	5.01
0.1317	308.15	13.30
0.1335	298.15	8.31
0.2170	288.15	5.33
0.2263	298.15	8.86
0.2331	308.15	14.29
0.3123	288.15	5.72
0.3172	298.15	9.45
0.3262	308.15	15.16
0.3808	288.15	5.99
0.3982	298.15	9.90
0.4021	308.15	15.86
0.4449	288.15	6.25
0.4587	298.15	10.27
0.4602	308.15	16.34
0.5085	288.15	6.46
0.5234	308.15	16.83
0.5248	298.15	10.55
0.5789	288.15	6.75
0.5961	298.15	11.04
0.6032	308.15	17.43
0.6427	288.15	6.97
0.6510	298.15	11.38
0.6601	308.15	18.08
0.7119	288.15	7.18
0.7207	298.15	11.76
0.7267	308.15	18.67
0.8060	288.15	7.52
0.8131	308.15	19.51
0.8137	298.15	12.32
0.8841	288.15	7.84
0.8878	298.15	12.73
0.8884	308.15	20.14
0.9346	308.15	20.50
0.9352	288.15	8.09
0.9358	298.15	12.97

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	759.632
283.15	0.0515	765.327
283.15	0.1016	770.975
283.15	0.2008	782.481
283.15	0.3003	794.487
283.15	0.4002	807.103
283.15	0.5014	820.515
283.15	0.6023	834.564
283.15	0.7003	848.874
283.15	0.8004	864.228
283.15	0.9006	880.441
283.15	0.9502	888.751
283.15	1.0000	897.339
288.15	0.0000	754.838
288.15	0.0515	760.502
288.15	0.1016	766.116
288.15	0.2008	777.558
288.15	0.3003	789.495
288.15	0.4002	802.048
288.15	0.5014	815.388
288.15	0.6023	829.367
288.15	0.7003	843.608
288.15	0.8004	858.892
288.15	0.9006	875.027
288.15	0.9502	883.298
288.15	1.0000	891.855
293.15	0.0000	750.018
293.15	0.0515	755.65
293.15	0.1016	761.228
293.15	0.2008	772.608
293.15	0.3003	784.476
293.15	0.4002	796.966
293.15	0.5014	810.236
293.15	0.6023	824.135
293.15	0.7003	838.316
293.15	0.8004	853.521
293.15	0.9006	869.579
293.15	0.9502	877.811
293.15	1.0000	886.335
298.15	0.0000	745.173
298.15	0.0515	750.771
298.15	0.1016	756.31
298.15	0.2008	767.618
298.15	0.3003	779.408
298.15	0.4002	791.831
298.15	0.5014	805.027
298.15	0.6023	818.844
298.15	0.7003	832.944
298.15	0.8004	848.064
298.15	0.9006	864.029
298.15	0.9502	872.223
298.15	1.0000	880.705
303.15	0.0000	740.3
303.15	0.0515	745.868
303.15	0.1016	751.377
303.15	0.2008	762.625
303.15	0.3003	774.357
303.15	0.4002	786.72
303.15	0.5014	799.854
303.15	0.6023	813.609
303.15	0.7003	827.644
303.15	0.8004	842.691
303.15	0.9006	858.59
303.15	0.9502	866.755
303.15	1.0000	875.204
308.15	0.0000	735.393
308.15	0.0515	740.929
308.15	0.1016	746.404
308.15	0.2008	757.59
308.15	0.3003	769.254
308.15	0.4002	781.55
308.15	0.5014	794.607
308.15	0.6023	808.295
308.15	0.7003	822.252
308.15	0.8004	837.226
308.15	0.9006	853.042
308.15	0.9502	861.177
308.15	1.0000	869.585
313.15	0.0000	730.451
313.15	0.0515	735.953
313.15	0.1016	741.393
313.15	0.2008	752.51
313.15	0.3003	764.108
313.15	0.4002	776.324
313.15	0.5014	789.31
313.15	0.6023	802.917
313.15	0.7003	816.794
313.15	0.8004	831.687
313.15	0.9006	847.412
313.15	0.9502	855.518
313.15	1.0000	863.882

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	759.632
283.15	0.0515	765.327
283.15	0.1016	770.975
283.15	0.2008	782.481
283.15	0.3003	794.487
283.15	0.4002	807.103
283.15	0.5014	820.515
283.15	0.6023	834.564
283.15	0.7003	848.874
283.15	0.8004	864.228
283.15	0.9006	880.441
283.15	0.9502	888.751
283.15	1.0000	897.339
288.15	0.0000	754.838
288.15	0.0515	760.502
288.15	0.1016	766.116
288.15	0.2008	777.558
288.15	0.3003	789.495
288.15	0.4002	802.048
288.15	0.5014	815.388
288.15	0.6023	829.367
288.15	0.7003	843.608
288.15	0.8004	858.892
288.15	0.9006	875.027
288.15	0.9502	883.298
288.15	1.0000	891.855
293.15	0.0000	750.018
293.15	0.0515	755.65
293.15	0.1016	761.228
293.15	0.2008	772.608
293.15	0.3003	784.476
293.15	0.4002	796.966
293.15	0.5014	810.236
293.15	0.6023	824.135
293.15	0.7003	838.316
293.15	0.8004	853.521
293.15	0.9006	869.579
293.15	0.9502	877.811
293.15	1.0000	886.335
298.15	0.0000	745.173
298.15	0.0515	750.771
298.15	0.1016	756.31
298.15	0.2008	767.618
298.15	0.3003	779.408
298.15	0.4002	791.831
298.15	0.5014	805.027
298.15	0.6023	818.844
298.15	0.7003	832.944
298.15	0.8004	848.064
298.15	0.9006	864.029
298.15	0.9502	872.223
298.15	1.0000	880.705
303.15	0.0000	740.3
303.15	0.0515	745.868
303.15	0.1016	751.377
303.15	0.2008	762.625
303.15	0.3003	774.357
303.15	0.4002	786.72
303.15	0.5014	799.854
303.15	0.6023	813.609
303.15	0.7003	827.644
303.15	0.8004	842.691
303.15	0.9006	858.59
303.15	0.9502	866.755
303.15	1.0000	875.204
308.15	0.0000	735.393
308.15	0.0515	740.929
308.15	0.1016	746.404
308.15	0.2008	757.59
308.15	0.3003	769.254
308.15	0.4002	781.55
308.15	0.5014	794.607
308.15	0.6023	808.295
308.15	0.7003	822.252
308.15	0.8004	837.226
308.15	0.9006	853.042
308.15	0.9502	861.177
308.15	1.0000	869.585
313.15	0.0000	730.451
313.15	0.0515	735.953
313.15	0.1016	741.393
313.15	0.2008	752.51
313.15	0.3003	764.108
313.15	0.4002	776.324
313.15	0.5014	789.31
313.15	0.6023	802.917
313.15	0.7003	816.794
313.15	0.8004	831.687
313.15	0.9006	847.412
313.15	0.9502	855.518
313.15	1.0000	863.882

Sources

• Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
• Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether