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

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 Propane, 1-chloro-2-methyl- (2) [ref]

Fixed		Measured
Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Gas
0.0554	288.15	0.1292
0.0632	298.15	0.1424
0.0681	308.15	0.1461
0.1179	288.15	0.2720
0.1245	298.15	0.2676
0.1302	308.15	0.2640
0.2154	288.15	0.4398
0.2263	298.15	0.4257
0.2272	308.15	0.4232
0.2888	288.15	0.5302
0.3299	298.15	0.5507
0.3385	308.15	0.5554
0.3762	288.15	0.6049
0.4082	298.15	0.6337
0.4165	308.15	0.6367
0.4496	288.15	0.6981
0.4871	298.15	0.7032
0.4911	308.15	0.7010
0.5366	288.15	0.7549
0.5609	298.15	0.7640
0.5795	308.15	0.7704
0.6344	288.15	0.8305
0.6531	298.15	0.8285
0.6643	308.15	0.8278
0.7256	288.15	0.8789
0.7292	298.15	0.8716
0.7349	308.15	0.8703
0.8114	288.15	0.9229
0.8155	298.15	0.9177
0.8196	308.15	0.9157
0.8869	288.15	0.9570
0.8935	298.15	0.9551
0.8948	308.15	0.9525

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

Fixed		Measured
Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Gas
0.0554	288.15	0.1292
0.0632	298.15	0.1424
0.0681	308.15	0.1461
0.1179	288.15	0.2720
0.1245	298.15	0.2676
0.1302	308.15	0.2640
0.2154	288.15	0.4398
0.2263	298.15	0.4257
0.2272	308.15	0.4232
0.2888	288.15	0.5302
0.3299	298.15	0.5507
0.3385	308.15	0.5554
0.3762	288.15	0.6049
0.4082	298.15	0.6337
0.4165	308.15	0.6367
0.4496	288.15	0.6981
0.4871	298.15	0.7032
0.4911	308.15	0.7010
0.5366	288.15	0.7549
0.5609	298.15	0.7640
0.5795	308.15	0.7704
0.6344	288.15	0.8305
0.6531	298.15	0.8285
0.6643	308.15	0.8278
0.7256	288.15	0.8789
0.7292	298.15	0.8716
0.7349	308.15	0.8703
0.8114	288.15	0.9229
0.8155	298.15	0.9177
0.8196	308.15	0.9157
0.8869	288.15	0.9570
0.8935	298.15	0.9551
0.8948	308.15	0.9525

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0005
283.15	0.0493	0.0005
283.15	0.1004	0.0005
283.15	0.2001	0.0005
283.15	0.3012	0.0005
283.15	0.4021	0.0005
283.15	0.5025	0.0005
283.15	0.6007	0.0005
283.15	0.6993	0.0005
283.15	0.7994	0.0005
283.15	0.8993	0.0005
283.15	0.9491	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0005
288.15	0.0493	0.0005
288.15	0.1004	0.0005
288.15	0.2001	0.0005
288.15	0.3012	0.0005
288.15	0.4021	0.0005
288.15	0.5025	0.0005
288.15	0.6007	0.0005
288.15	0.6993	0.0005
288.15	0.7994	0.0005
288.15	0.8993	0.0005
288.15	0.9491	0.0005
288.15	1.0000	0.0005
293.15	0.0000	0.0004
293.15	0.0493	0.0004
293.15	0.1004	0.0004
293.15	0.2001	0.0004
293.15	0.3012	0.0004
293.15	0.4021	0.0004
293.15	0.5025	0.0004
293.15	0.6007	0.0004
293.15	0.6993	0.0004
293.15	0.7994	0.0004
293.15	0.8993	0.0004
293.15	0.9491	0.0005
293.15	1.0000	0.0005
298.15	0.0000	0.0004
298.15	0.0493	0.0004
298.15	0.1004	0.0004
298.15	0.2001	0.0004
298.15	0.3012	0.0004
298.15	0.4021	0.0004
298.15	0.5025	0.0004
298.15	0.6007	0.0004
298.15	0.6993	0.0004
298.15	0.7994	0.0004
298.15	0.8993	0.0004
298.15	0.9491	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0004
303.15	0.0493	0.0004
303.15	0.1004	0.0004
303.15	0.2001	0.0004
303.15	0.3012	0.0004
303.15	0.4021	0.0004
303.15	0.5025	0.0004
303.15	0.6007	0.0004
303.15	0.6993	0.0004
303.15	0.7994	0.0004
303.15	0.8993	0.0004
303.15	0.9491	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0004
308.15	0.0493	0.0004
308.15	0.1004	0.0004
308.15	0.2001	0.0004
308.15	0.3012	0.0004
308.15	0.4021	0.0004
308.15	0.5025	0.0004
308.15	0.6007	0.0004
308.15	0.6993	0.0004
308.15	0.7994	0.0004
308.15	0.8993	0.0004
308.15	0.9491	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0493	0.0003
313.15	0.1004	0.0003
313.15	0.2001	0.0003
313.15	0.3012	0.0003
313.15	0.4021	0.0004
313.15	0.5025	0.0004
313.15	0.6007	0.0004
313.15	0.6993	0.0004
313.15	0.7994	0.0004
313.15	0.8993	0.0004
313.15	0.9491	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 Propane, 1-chloro-2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0005
283.15	0.0493	0.0005
283.15	0.1004	0.0005
283.15	0.2001	0.0005
283.15	0.3012	0.0005
283.15	0.4021	0.0005
283.15	0.5025	0.0005
283.15	0.6007	0.0005
283.15	0.6993	0.0005
283.15	0.7994	0.0005
283.15	0.8993	0.0005
283.15	0.9491	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0005
288.15	0.0493	0.0005
288.15	0.1004	0.0005
288.15	0.2001	0.0005
288.15	0.3012	0.0005
288.15	0.4021	0.0005
288.15	0.5025	0.0005
288.15	0.6007	0.0005
288.15	0.6993	0.0005
288.15	0.7994	0.0005
288.15	0.8993	0.0005
288.15	0.9491	0.0005
288.15	1.0000	0.0005
293.15	0.0000	0.0004
293.15	0.0493	0.0004
293.15	0.1004	0.0004
293.15	0.2001	0.0004
293.15	0.3012	0.0004
293.15	0.4021	0.0004
293.15	0.5025	0.0004
293.15	0.6007	0.0004
293.15	0.6993	0.0004
293.15	0.7994	0.0004
293.15	0.8993	0.0004
293.15	0.9491	0.0005
293.15	1.0000	0.0005
298.15	0.0000	0.0004
298.15	0.0493	0.0004
298.15	0.1004	0.0004
298.15	0.2001	0.0004
298.15	0.3012	0.0004
298.15	0.4021	0.0004
298.15	0.5025	0.0004
298.15	0.6007	0.0004
298.15	0.6993	0.0004
298.15	0.7994	0.0004
298.15	0.8993	0.0004
298.15	0.9491	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0004
303.15	0.0493	0.0004
303.15	0.1004	0.0004
303.15	0.2001	0.0004
303.15	0.3012	0.0004
303.15	0.4021	0.0004
303.15	0.5025	0.0004
303.15	0.6007	0.0004
303.15	0.6993	0.0004
303.15	0.7994	0.0004
303.15	0.8993	0.0004
303.15	0.9491	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0004
308.15	0.0493	0.0004
308.15	0.1004	0.0004
308.15	0.2001	0.0004
308.15	0.3012	0.0004
308.15	0.4021	0.0004
308.15	0.5025	0.0004
308.15	0.6007	0.0004
308.15	0.6993	0.0004
308.15	0.7994	0.0004
308.15	0.8993	0.0004
308.15	0.9491	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0493	0.0003
313.15	0.1004	0.0003
313.15	0.2001	0.0003
313.15	0.3012	0.0003
313.15	0.4021	0.0004
313.15	0.5025	0.0004
313.15	0.6007	0.0004
313.15	0.6993	0.0004
313.15	0.7994	0.0004
313.15	0.8993	0.0004
313.15	0.9491	0.0004
313.15	1.0000	0.0004

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0554	288.15	4.95
0.0632	298.15	8.33
0.0681	308.15	13.40
0.1179	288.15	5.32
0.1245	298.15	9.15
0.1302	308.15	14.55
0.2154	288.15	6.17
0.2263	298.15	10.36
0.2272	308.15	16.37
0.2888	288.15	7.08
0.3299	298.15	11.73
0.3385	308.15	18.39
0.3762	288.15	7.70
0.4082	298.15	12.74
0.4165	308.15	19.86
0.4496	288.15	8.35
0.4871	298.15	13.65
0.4911	308.15	21.10
0.5366	288.15	9.01
0.5609	298.15	14.67
0.5795	308.15	22.71
0.6344	288.15	9.74
0.6531	298.15	15.84
0.6643	308.15	24.32
0.7256	288.15	10.51
0.7292	298.15	16.78
0.7349	308.15	25.68
0.8114	288.15	11.26
0.8155	298.15	17.88
0.8196	308.15	27.20
0.8869	288.15	11.89
0.8935	298.15	18.78
0.8948	308.15	28.63

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0554	288.15	4.95
0.0632	298.15	8.33
0.0681	308.15	13.40
0.1179	288.15	5.32
0.1245	298.15	9.15
0.1302	308.15	14.55
0.2154	288.15	6.17
0.2263	298.15	10.36
0.2272	308.15	16.37
0.2888	288.15	7.08
0.3299	298.15	11.73
0.3385	308.15	18.39
0.3762	288.15	7.70
0.4082	298.15	12.74
0.4165	308.15	19.86
0.4496	288.15	8.35
0.4871	298.15	13.65
0.4911	308.15	21.10
0.5366	288.15	9.01
0.5609	298.15	14.67
0.5795	308.15	22.71
0.6344	288.15	9.74
0.6531	298.15	15.84
0.6643	308.15	24.32
0.7256	288.15	10.51
0.7292	298.15	16.78
0.7349	308.15	25.68
0.8114	288.15	11.26
0.8155	298.15	17.88
0.8196	308.15	27.20
0.8869	288.15	11.89
0.8935	298.15	18.78
0.8948	308.15	28.63

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	759.632
283.15	0.0493	764.735
283.15	0.1004	770.137
283.15	0.2001	781.028
283.15	0.3012	792.555
283.15	0.4021	804.548
283.15	0.5025	817.044
283.15	0.6007	829.846
283.15	0.6993	843.3
283.15	0.7994	857.698
283.15	0.8993	872.788
283.15	0.9491	880.632
283.15	1.0000	888.845
288.15	0.0000	754.838
288.15	0.0493	759.907
288.15	0.1004	765.272
288.15	0.2001	776.091
288.15	0.3012	787.532
288.15	0.4021	799.452
288.15	0.5025	811.866
288.15	0.6007	824.578
288.15	0.6993	837.948
288.15	0.7994	852.259
288.15	0.8993	867.257
288.15	0.9491	875.039
288.15	1.0000	883.211
293.15	0.0000	750.018
293.15	0.0493	755.052
293.15	0.1004	760.38
293.15	0.2001	771.122
293.15	0.3012	782.49
293.15	0.4021	794.323
293.15	0.5025	806.657
293.15	0.6007	819.292
293.15	0.6993	832.566
293.15	0.7994	846.776
293.15	0.8993	861.681
293.15	0.9491	869.418
293.15	1.0000	877.539
298.15	0.0000	745.173
298.15	0.0493	750.159
298.15	0.1004	755.442
298.15	0.2001	766.084
298.15	0.3012	777.343
298.15	0.4021	789.076
298.15	0.5025	801.298
298.15	0.6007	813.811
298.15	0.6993	826.968
298.15	0.7994	841.05
298.15	0.8993	855.823
298.15	0.9491	863.487
298.15	1.0000	871.533
303.15	0.0000	740.3
303.15	0.0493	745.258
303.15	0.1004	750.513
303.15	0.2001	761.103
303.15	0.3012	772.31
303.15	0.4021	783.985
303.15	0.5025	796.151
303.15	0.6007	808.609
303.15	0.6993	821.703
303.15	0.7994	835.732
303.15	0.8993	850.449
303.15	0.9491	858.083
303.15	1.0000	866.096
308.15	0.0000	735.393
308.15	0.0493	740.313
308.15	0.1004	745.53
308.15	0.2001	756.045
308.15	0.3012	767.176
308.15	0.4021	778.762
308.15	0.5025	790.846
308.15	0.6007	803.216
308.15	0.6993	816.231
308.15	0.7994	830.162
308.15	0.8993	844.774
308.15	0.9491	852.361
308.15	1.0000	860.319
313.15	0.0000	730.451
313.15	0.0493	735.316
313.15	0.1004	740.473
313.15	0.2001	750.861
313.15	0.3012	761.864
313.15	0.4021	773.319
313.15	0.5025	785.257
313.15	0.6007	797.479
313.15	0.6993	810.348
313.15	0.7994	824.103
313.15	0.8993	838.543
313.15	0.9491	846.035
313.15	1.0000	853.902

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	759.632
283.15	0.0493	764.735
283.15	0.1004	770.137
283.15	0.2001	781.028
283.15	0.3012	792.555
283.15	0.4021	804.548
283.15	0.5025	817.044
283.15	0.6007	829.846
283.15	0.6993	843.3
283.15	0.7994	857.698
283.15	0.8993	872.788
283.15	0.9491	880.632
283.15	1.0000	888.845
288.15	0.0000	754.838
288.15	0.0493	759.907
288.15	0.1004	765.272
288.15	0.2001	776.091
288.15	0.3012	787.532
288.15	0.4021	799.452
288.15	0.5025	811.866
288.15	0.6007	824.578
288.15	0.6993	837.948
288.15	0.7994	852.259
288.15	0.8993	867.257
288.15	0.9491	875.039
288.15	1.0000	883.211
293.15	0.0000	750.018
293.15	0.0493	755.052
293.15	0.1004	760.38
293.15	0.2001	771.122
293.15	0.3012	782.49
293.15	0.4021	794.323
293.15	0.5025	806.657
293.15	0.6007	819.292
293.15	0.6993	832.566
293.15	0.7994	846.776
293.15	0.8993	861.681
293.15	0.9491	869.418
293.15	1.0000	877.539
298.15	0.0000	745.173
298.15	0.0493	750.159
298.15	0.1004	755.442
298.15	0.2001	766.084
298.15	0.3012	777.343
298.15	0.4021	789.076
298.15	0.5025	801.298
298.15	0.6007	813.811
298.15	0.6993	826.968
298.15	0.7994	841.05
298.15	0.8993	855.823
298.15	0.9491	863.487
298.15	1.0000	871.533
303.15	0.0000	740.3
303.15	0.0493	745.258
303.15	0.1004	750.513
303.15	0.2001	761.103
303.15	0.3012	772.31
303.15	0.4021	783.985
303.15	0.5025	796.151
303.15	0.6007	808.609
303.15	0.6993	821.703
303.15	0.7994	835.732
303.15	0.8993	850.449
303.15	0.9491	858.083
303.15	1.0000	866.096
308.15	0.0000	735.393
308.15	0.0493	740.313
308.15	0.1004	745.53
308.15	0.2001	756.045
308.15	0.3012	767.176
308.15	0.4021	778.762
308.15	0.5025	790.846
308.15	0.6007	803.216
308.15	0.6993	816.231
308.15	0.7994	830.162
308.15	0.8993	844.774
308.15	0.9491	852.361
308.15	1.0000	860.319
313.15	0.0000	730.451
313.15	0.0493	735.316
313.15	0.1004	740.473
313.15	0.2001	750.861
313.15	0.3012	761.864
313.15	0.4021	773.319
313.15	0.5025	785.257
313.15	0.6007	797.479
313.15	0.6993	810.348
313.15	0.7994	824.103
313.15	0.8993	838.543
313.15	0.9491	846.035
313.15	1.0000	853.902

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