Mixture of Butane, 1-ethoxy- + Butane, 2-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, 2-chloro- (2) [ref]

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Gas
0.0669	288.15	0.1728
0.0749	298.15	0.1776
0.0799	308.15	0.1823
0.1331	288.15	0.3017
0.1603	298.15	0.3377
0.1651	308.15	0.3386
0.2259	288.15	0.4689
0.2733	298.15	0.4773
0.2798	308.15	0.4923
0.3315	288.15	0.5894
0.3732	298.15	0.6060
0.3750	308.15	0.6037
0.3943	288.15	0.6791
0.4211	298.15	0.6630
0.4315	308.15	0.6560
0.4823	288.15	0.7319
0.5254	298.15	0.7371
0.5263	308.15	0.7393
0.5645	288.15	0.7958
0.5933	298.15	0.8015
0.6116	308.15	0.7994
0.6529	288.15	0.8500
0.6753	298.15	0.8437
0.6829	308.15	0.8444
0.7430	288.15	0.8884
0.7622	298.15	0.8933
0.7666	308.15	0.8919
0.8209	288.15	0.9330
0.8422	298.15	0.9316
0.8422	308.15	0.9296
0.9084	288.15	0.9666
0.9125	298.15	0.9646
0.9139	308.15	0.9632

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

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Gas
0.0669	288.15	0.1728
0.0749	298.15	0.1776
0.0799	308.15	0.1823
0.1331	288.15	0.3017
0.1603	298.15	0.3377
0.1651	308.15	0.3386
0.2259	288.15	0.4689
0.2733	298.15	0.4773
0.2798	308.15	0.4923
0.3315	288.15	0.5894
0.3732	298.15	0.6060
0.3750	308.15	0.6037
0.3943	288.15	0.6791
0.4211	298.15	0.6630
0.4315	308.15	0.6560
0.4823	288.15	0.7319
0.5254	298.15	0.7371
0.5263	308.15	0.7393
0.5645	288.15	0.7958
0.5933	298.15	0.8015
0.6116	308.15	0.7994
0.6529	288.15	0.8500
0.6753	298.15	0.8437
0.6829	308.15	0.8444
0.7430	288.15	0.8884
0.7622	298.15	0.8933
0.7666	308.15	0.8919
0.8209	288.15	0.9330
0.8422	298.15	0.9316
0.8422	308.15	0.9296
0.9084	288.15	0.9666
0.9125	298.15	0.9646
0.9139	308.15	0.9632

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0005
283.15	0.0525	0.0005
283.15	0.0974	0.0005
283.15	0.2001	0.0005
283.15	0.3027	0.0005
283.15	0.4000	0.0005
283.15	0.5248	0.0005
283.15	0.6016	0.0005
283.15	0.7006	0.0005
283.15	0.7993	0.0005
283.15	0.8997	0.0005
283.15	0.9502	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0005
288.15	0.0525	0.0004
288.15	0.0974	0.0004
288.15	0.2001	0.0004
288.15	0.3027	0.0004
288.15	0.4000	0.0004
288.15	0.5248	0.0004
288.15	0.6016	0.0004
288.15	0.7006	0.0004
288.15	0.7993	0.0004
288.15	0.8997	0.0004
288.15	0.9502	0.0004
288.15	1.0000	0.0004
293.15	0.0000	0.0004
293.15	0.0525	0.0004
293.15	0.0974	0.0004
293.15	0.2001	0.0004
293.15	0.3027	0.0004
293.15	0.4000	0.0004
293.15	0.5248	0.0004
293.15	0.6016	0.0004
293.15	0.7006	0.0004
293.15	0.7993	0.0004
293.15	0.8997	0.0004
293.15	0.9502	0.0004
293.15	1.0000	0.0004
298.15	0.0000	0.0004
298.15	0.0525	0.0004
298.15	0.0974	0.0004
298.15	0.2001	0.0004
298.15	0.3027	0.0004
298.15	0.4000	0.0004
298.15	0.5248	0.0004
298.15	0.6016	0.0004
298.15	0.7006	0.0004
298.15	0.7993	0.0004
298.15	0.8997	0.0004
298.15	0.9502	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0004
303.15	0.0525	0.0004
303.15	0.0974	0.0004
303.15	0.2001	0.0004
303.15	0.3027	0.0004
303.15	0.4000	0.0004
303.15	0.5248	0.0004
303.15	0.6016	0.0004
303.15	0.7006	0.0004
303.15	0.7993	0.0004
303.15	0.8997	0.0004
303.15	0.9502	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0004
308.15	0.0525	0.0004
308.15	0.0974	0.0004
308.15	0.2001	0.0004
308.15	0.3027	0.0004
308.15	0.4000	0.0004
308.15	0.5248	0.0004
308.15	0.6016	0.0004
308.15	0.7006	0.0004
308.15	0.7993	0.0004
308.15	0.8997	0.0004
308.15	0.9502	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0525	0.0003
313.15	0.0974	0.0003
313.15	0.2001	0.0003
313.15	0.3027	0.0003
313.15	0.4000	0.0003
313.15	0.5248	0.0003
313.15	0.6016	0.0003
313.15	0.7006	0.0003
313.15	0.7993	0.0003
313.15	0.8997	0.0003
313.15	0.9502	0.0003
313.15	1.0000	0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0005
283.15	0.0525	0.0005
283.15	0.0974	0.0005
283.15	0.2001	0.0005
283.15	0.3027	0.0005
283.15	0.4000	0.0005
283.15	0.5248	0.0005
283.15	0.6016	0.0005
283.15	0.7006	0.0005
283.15	0.7993	0.0005
283.15	0.8997	0.0005
283.15	0.9502	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0005
288.15	0.0525	0.0004
288.15	0.0974	0.0004
288.15	0.2001	0.0004
288.15	0.3027	0.0004
288.15	0.4000	0.0004
288.15	0.5248	0.0004
288.15	0.6016	0.0004
288.15	0.7006	0.0004
288.15	0.7993	0.0004
288.15	0.8997	0.0004
288.15	0.9502	0.0004
288.15	1.0000	0.0004
293.15	0.0000	0.0004
293.15	0.0525	0.0004
293.15	0.0974	0.0004
293.15	0.2001	0.0004
293.15	0.3027	0.0004
293.15	0.4000	0.0004
293.15	0.5248	0.0004
293.15	0.6016	0.0004
293.15	0.7006	0.0004
293.15	0.7993	0.0004
293.15	0.8997	0.0004
293.15	0.9502	0.0004
293.15	1.0000	0.0004
298.15	0.0000	0.0004
298.15	0.0525	0.0004
298.15	0.0974	0.0004
298.15	0.2001	0.0004
298.15	0.3027	0.0004
298.15	0.4000	0.0004
298.15	0.5248	0.0004
298.15	0.6016	0.0004
298.15	0.7006	0.0004
298.15	0.7993	0.0004
298.15	0.8997	0.0004
298.15	0.9502	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0004
303.15	0.0525	0.0004
303.15	0.0974	0.0004
303.15	0.2001	0.0004
303.15	0.3027	0.0004
303.15	0.4000	0.0004
303.15	0.5248	0.0004
303.15	0.6016	0.0004
303.15	0.7006	0.0004
303.15	0.7993	0.0004
303.15	0.8997	0.0004
303.15	0.9502	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0004
308.15	0.0525	0.0004
308.15	0.0974	0.0004
308.15	0.2001	0.0004
308.15	0.3027	0.0004
308.15	0.4000	0.0004
308.15	0.5248	0.0004
308.15	0.6016	0.0004
308.15	0.7006	0.0004
308.15	0.7993	0.0004
308.15	0.8997	0.0004
308.15	0.9502	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0525	0.0003
313.15	0.0974	0.0003
313.15	0.2001	0.0003
313.15	0.3027	0.0003
313.15	0.4000	0.0003
313.15	0.5248	0.0003
313.15	0.6016	0.0003
313.15	0.7006	0.0003
313.15	0.7993	0.0003
313.15	0.8997	0.0003
313.15	0.9502	0.0003
313.15	1.0000	0.0003

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0669	288.15	5.11
0.0749	298.15	8.61
0.0799	308.15	13.86
0.1331	288.15	5.79
0.1603	298.15	9.79
0.1651	308.15	15.78
0.2259	288.15	6.59
0.2733	298.15	11.20
0.2798	308.15	17.69
0.3315	288.15	7.60
0.3732	298.15	12.51
0.3750	308.15	19.55
0.3943	288.15	8.21
0.4211	298.15	13.21
0.4315	308.15	20.45
0.4823	288.15	9.05
0.5254	298.15	14.63
0.5263	308.15	22.49
0.5645	288.15	9.84
0.5933	298.15	15.74
0.6116	308.15	24.15
0.6529	288.15	10.50
0.6753	298.15	16.66
0.6829	308.15	25.50
0.7430	288.15	11.21
0.7622	298.15	17.75
0.7666	308.15	27.12
0.8209	288.15	11.79
0.8422	298.15	18.66
0.8422	308.15	28.50
0.9084	288.15	12.59
0.9125	298.15	19.73
0.9139	308.15	29.93

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0669	288.15	5.11
0.0749	298.15	8.61
0.0799	308.15	13.86
0.1331	288.15	5.79
0.1603	298.15	9.79
0.1651	308.15	15.78
0.2259	288.15	6.59
0.2733	298.15	11.20
0.2798	308.15	17.69
0.3315	288.15	7.60
0.3732	298.15	12.51
0.3750	308.15	19.55
0.3943	288.15	8.21
0.4211	298.15	13.21
0.4315	308.15	20.45
0.4823	288.15	9.05
0.5254	298.15	14.63
0.5263	308.15	22.49
0.5645	288.15	9.84
0.5933	298.15	15.74
0.6116	308.15	24.15
0.6529	288.15	10.50
0.6753	298.15	16.66
0.6829	308.15	25.50
0.7430	288.15	11.21
0.7622	298.15	17.75
0.7666	308.15	27.12
0.8209	288.15	11.79
0.8422	298.15	18.66
0.8422	308.15	28.50
0.9084	288.15	12.59
0.9125	298.15	19.73
0.9139	308.15	29.93

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	759.632
283.15	0.0525	765.075
283.15	0.0974	769.762
283.15	0.2001	780.678
283.15	0.3027	791.975
283.15	0.4000	803.128
283.15	0.5248	818.168
283.15	0.6016	827.85
283.15	0.7006	840.875
283.15	0.7993	854.496
283.15	0.8997	869.038
283.15	0.9502	876.678
283.15	1.0000	884.34
288.15	0.0000	754.838
288.15	0.0525	760.242
288.15	0.0974	764.897
288.15	0.2001	775.744
288.15	0.3027	786.952
288.15	0.4000	798.037
288.15	0.5248	812.98
288.15	0.6016	822.613
288.15	0.7006	835.554
288.15	0.7993	849.096
288.15	0.8997	863.543
288.15	0.9502	871.137
288.15	1.0000	878.756
293.15	0.0000	750.018
293.15	0.0525	755.382
293.15	0.0974	760.006
293.15	0.2001	770.778
293.15	0.3027	781.909
293.15	0.4000	792.91
293.15	0.5248	807.76
293.15	0.6016	817.343
293.15	0.7006	830.202
293.15	0.7993	843.651
293.15	0.8997	858.003
293.15	0.9502	865.523
293.15	1.0000	873.13
298.15	0.0000	745.173
298.15	0.0525	750.495
298.15	0.0974	755.081
298.15	0.2001	765.789
298.15	0.3027	776.837
298.15	0.4000	787.763
298.15	0.5248	802.529
298.15	0.6016	812.044
298.15	0.7006	824.819
298.15	0.7993	838.178
298.15	0.8997	852.437
298.15	0.9502	859.908
298.15	1.0000	867.474
303.15	0.0000	740.3
303.15	0.0525	745.579
303.15	0.0974	750.131
303.15	0.2001	760.765
303.15	0.3027	771.741
303.15	0.4000	782.594
303.15	0.5248	797.247
303.15	0.6016	806.71
303.15	0.7006	819.404
303.15	0.7993	832.663
303.15	0.8997	846.826
303.15	0.9502	854.248
303.15	1.0000	861.779
308.15	0.0000	735.393
308.15	0.0525	740.632
308.15	0.0974	745.146
308.15	0.2001	755.706
308.15	0.3027	766.603
308.15	0.4000	777.385
308.15	0.5248	791.941
308.15	0.6016	801.337
308.15	0.7006	813.943
308.15	0.7993	827.116
308.15	0.8997	841.188
308.15	0.9502	848.552
308.15	1.0000	856.044
313.15	0.0000	730.451
313.15	0.0525	735.646
313.15	0.0974	740.124
313.15	0.2001	750.603
313.15	0.3027	761.432
313.15	0.4000	772.132
313.15	0.5248	786.597
313.15	0.6016	795.924
313.15	0.7006	808.443
313.15	0.7993	821.529
313.15	0.8997	835.498
313.15	0.9502	842.814
313.15	1.0000	850.266

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	759.632
283.15	0.0525	765.075
283.15	0.0974	769.762
283.15	0.2001	780.678
283.15	0.3027	791.975
283.15	0.4000	803.128
283.15	0.5248	818.168
283.15	0.6016	827.85
283.15	0.7006	840.875
283.15	0.7993	854.496
283.15	0.8997	869.038
283.15	0.9502	876.678
283.15	1.0000	884.34
288.15	0.0000	754.838
288.15	0.0525	760.242
288.15	0.0974	764.897
288.15	0.2001	775.744
288.15	0.3027	786.952
288.15	0.4000	798.037
288.15	0.5248	812.98
288.15	0.6016	822.613
288.15	0.7006	835.554
288.15	0.7993	849.096
288.15	0.8997	863.543
288.15	0.9502	871.137
288.15	1.0000	878.756
293.15	0.0000	750.018
293.15	0.0525	755.382
293.15	0.0974	760.006
293.15	0.2001	770.778
293.15	0.3027	781.909
293.15	0.4000	792.91
293.15	0.5248	807.76
293.15	0.6016	817.343
293.15	0.7006	830.202
293.15	0.7993	843.651
293.15	0.8997	858.003
293.15	0.9502	865.523
293.15	1.0000	873.13
298.15	0.0000	745.173
298.15	0.0525	750.495
298.15	0.0974	755.081
298.15	0.2001	765.789
298.15	0.3027	776.837
298.15	0.4000	787.763
298.15	0.5248	802.529
298.15	0.6016	812.044
298.15	0.7006	824.819
298.15	0.7993	838.178
298.15	0.8997	852.437
298.15	0.9502	859.908
298.15	1.0000	867.474
303.15	0.0000	740.3
303.15	0.0525	745.579
303.15	0.0974	750.131
303.15	0.2001	760.765
303.15	0.3027	771.741
303.15	0.4000	782.594
303.15	0.5248	797.247
303.15	0.6016	806.71
303.15	0.7006	819.404
303.15	0.7993	832.663
303.15	0.8997	846.826
303.15	0.9502	854.248
303.15	1.0000	861.779
308.15	0.0000	735.393
308.15	0.0525	740.632
308.15	0.0974	745.146
308.15	0.2001	755.706
308.15	0.3027	766.603
308.15	0.4000	777.385
308.15	0.5248	791.941
308.15	0.6016	801.337
308.15	0.7006	813.943
308.15	0.7993	827.116
308.15	0.8997	841.188
308.15	0.9502	848.552
308.15	1.0000	856.044
313.15	0.0000	730.451
313.15	0.0525	735.646
313.15	0.0974	740.124
313.15	0.2001	750.603
313.15	0.3027	761.432
313.15	0.4000	772.132
313.15	0.5248	786.597
313.15	0.6016	795.924
313.15	0.7006	808.443
313.15	0.7993	821.529
313.15	0.8997	835.498
313.15	0.9502	842.814
313.15	1.0000	850.266

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