Mixture of Ethanol + Butane, 1-chloro-

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. n₀ - Refractive index (Na D-line) (2)
5. ρ_l - Mass density, kg/m3 (2)

Mole fraction of Ethanol (1) [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0567	0.2292
0.0767	0.2649
0.0941	0.2822
0.1071	0.2967
0.1877	0.3462
0.2421	0.3680
0.2686	0.3769
0.2924	0.3829
0.3433	0.3966
0.3702	0.4022
0.4006	0.4111
0.4223	0.4175
0.4615	0.4256
0.4754	0.4283
0.4788	0.4305
0.4822	0.4314
0.5141	0.4388
0.5248	0.4439
0.5500	0.4495
0.5631	0.4521
0.5900	0.4645
0.6171	0.4711
0.6433	0.4794
0.6771	0.4930
0.7038	0.5053
0.7321	0.5196
0.7579	0.5362
0.7835	0.5534
0.8073	0.5717
0.8356	0.6003
0.8564	0.6224
0.8863	0.6645
0.9033	0.6890
0.9161	0.7139
0.9348	0.7577
0.9511	0.8015
0.9638	0.8415
0.9724	0.8721

Mole fraction of Ethanol (1) [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0567	0.2292
0.0767	0.2649
0.0941	0.2822
0.1071	0.2967
0.1877	0.3462
0.2421	0.3680
0.2686	0.3769
0.2924	0.3829
0.3433	0.3966
0.3702	0.4022
0.4006	0.4111
0.4223	0.4175
0.4615	0.4256
0.4754	0.4283
0.4788	0.4305
0.4822	0.4314
0.5141	0.4388
0.5248	0.4439
0.5500	0.4495
0.5631	0.4521
0.5900	0.4645
0.6171	0.4711
0.6433	0.4794
0.6771	0.4930
0.7038	0.5053
0.7321	0.5196
0.7579	0.5362
0.7835	0.5534
0.8073	0.5717
0.8356	0.6003
0.8564	0.6224
0.8863	0.6645
0.9033	0.6890
0.9161	0.7139
0.9348	0.7577
0.9511	0.8015
0.9638	0.8415
0.9724	0.8721

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0005
288.15	0.0500	0.0005
288.15	0.1000	0.0005
288.15	0.2000	0.0005
288.15	0.3000	0.0005
288.15	0.4000	0.0006
288.15	0.5000	0.0006
288.15	0.6000	0.0007
288.15	0.7000	0.0008
288.15	0.8000	0.0009
288.15	0.9000	0.0011
288.15	0.9500	0.0012
288.15	1.0000	0.0013
298.15	0.0000	0.0004
298.15	0.0500	0.0004
298.15	0.1000	0.0004
298.15	0.2000	0.0004
298.15	0.3000	0.0005
298.15	0.4000	0.0005
298.15	0.5000	0.0005
298.15	0.6000	0.0006
298.15	0.7000	0.0007
298.15	0.8000	0.0008
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0004
308.15	0.0500	0.0004
308.15	0.1000	0.0004
308.15	0.2000	0.0004
308.15	0.3000	0.0004
308.15	0.4000	0.0004
308.15	0.5000	0.0005
308.15	0.6000	0.0005
308.15	0.7000	0.0006
308.15	0.8000	0.0007
308.15	0.9000	0.0008
308.15	0.9500	0.0008
308.15	1.0000	0.0009

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0005
288.15	0.0500	0.0005
288.15	0.1000	0.0005
288.15	0.2000	0.0005
288.15	0.3000	0.0005
288.15	0.4000	0.0006
288.15	0.5000	0.0006
288.15	0.6000	0.0007
288.15	0.7000	0.0008
288.15	0.8000	0.0009
288.15	0.9000	0.0011
288.15	0.9500	0.0012
288.15	1.0000	0.0013
298.15	0.0000	0.0004
298.15	0.0500	0.0004
298.15	0.1000	0.0004
298.15	0.2000	0.0004
298.15	0.3000	0.0005
298.15	0.4000	0.0005
298.15	0.5000	0.0005
298.15	0.6000	0.0006
298.15	0.7000	0.0007
298.15	0.8000	0.0008
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0004
308.15	0.0500	0.0004
308.15	0.1000	0.0004
308.15	0.2000	0.0004
308.15	0.3000	0.0004
308.15	0.4000	0.0004
308.15	0.5000	0.0005
308.15	0.6000	0.0005
308.15	0.7000	0.0006
308.15	0.8000	0.0007
308.15	0.9000	0.0008
308.15	0.9500	0.0008
308.15	1.0000	0.0009

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Ethanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0567	68.69
0.0767	71.19
0.0941	72.33
0.1071	73.45
0.1877	76.58
0.2421	77.60
0.2686	77.92
0.2924	77.15
0.3433	78.51
0.3702	78.57
0.4006	78.60
0.4223	78.60
0.4615	78.57
0.4754	78.51
0.4788	78.49
0.4822	78.42
0.5141	78.31
0.5248	78.24
0.5500	78.07
0.5631	77.86
0.5900	77.61
0.6171	77.16
0.6433	76.72
0.6771	76.00
0.7038	75.24
0.7321	74.24
0.7579	73.28
0.7835	72.13
0.8073	70.75
0.8356	68.83
0.8564	67.22
0.8863	64.37
0.9033	62.66
0.9161	60.99
0.9348	58.48
0.9511	55.98
0.9638	53.94
0.9724	52.46

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Ethanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0567	68.69
0.0767	71.19
0.0941	72.33
0.1071	73.45
0.1877	76.58
0.2421	77.60
0.2686	77.92
0.2924	77.15
0.3433	78.51
0.3702	78.57
0.4006	78.60
0.4223	78.60
0.4615	78.57
0.4754	78.51
0.4788	78.49
0.4822	78.42
0.5141	78.31
0.5248	78.24
0.5500	78.07
0.5631	77.86
0.5900	77.61
0.6171	77.16
0.6433	76.72
0.6771	76.00
0.7038	75.24
0.7321	74.24
0.7579	73.28
0.7835	72.13
0.8073	70.75
0.8356	68.83
0.8564	67.22
0.8863	64.37
0.9033	62.66
0.9161	60.99
0.9348	58.48
0.9511	55.98
0.9638	53.94
0.9724	52.46

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.4045
288.15	0.0500	1.403
288.15	0.1000	1.4016
288.15	0.2000	1.3988
288.15	0.3000	1.3958
288.15	0.4000	1.3925
288.15	0.5000	1.389
288.15	0.6000	1.3851
288.15	0.7000	1.3807
288.15	0.8000	1.3756
288.15	0.9000	1.3697
288.15	0.9500	1.3665
288.15	1.0000	1.363
298.15	0.0000	1.3993
298.15	0.0500	1.3978
298.15	0.1000	1.3964
298.15	0.2000	1.3937
298.15	0.3000	1.3907
298.15	0.4000	1.3875
298.15	0.5000	1.384
298.15	0.6000	1.3802
298.15	0.7000	1.3759
298.15	0.8000	1.3711
298.15	0.9000	1.3653
298.15	0.9500	1.3624
298.15	1.0000	1.3591
308.15	0.0000	1.3941
308.15	0.0500	1.3925
308.15	0.1000	1.3912
308.15	0.2000	1.3885
308.15	0.3000	1.3855
308.15	0.4000	1.3823
308.15	0.5000	1.3788
308.15	0.6000	1.375
308.15	0.7000	1.3708
308.15	0.8000	1.3661
308.15	0.9000	1.3609
308.15	0.9500	1.3581
308.15	1.0000	1.355

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.4045
288.15	0.0500	1.403
288.15	0.1000	1.4016
288.15	0.2000	1.3988
288.15	0.3000	1.3958
288.15	0.4000	1.3925
288.15	0.5000	1.389
288.15	0.6000	1.3851
288.15	0.7000	1.3807
288.15	0.8000	1.3756
288.15	0.9000	1.3697
288.15	0.9500	1.3665
288.15	1.0000	1.363
298.15	0.0000	1.3993
298.15	0.0500	1.3978
298.15	0.1000	1.3964
298.15	0.2000	1.3937
298.15	0.3000	1.3907
298.15	0.4000	1.3875
298.15	0.5000	1.384
298.15	0.6000	1.3802
298.15	0.7000	1.3759
298.15	0.8000	1.3711
298.15	0.9000	1.3653
298.15	0.9500	1.3624
298.15	1.0000	1.3591
308.15	0.0000	1.3941
308.15	0.0500	1.3925
308.15	0.1000	1.3912
308.15	0.2000	1.3885
308.15	0.3000	1.3855
308.15	0.4000	1.3823
308.15	0.5000	1.3788
308.15	0.6000	1.375
308.15	0.7000	1.3708
308.15	0.8000	1.3661
308.15	0.9000	1.3609
308.15	0.9500	1.3581
308.15	1.0000	1.355

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	892.2
288.15	0.0500	888.5
288.15	0.1000	885.3
288.15	0.2000	878.7
288.15	0.3000	871.7
288.15	0.4000	864.1
288.15	0.5000	855.7
288.15	0.6000	846.4
288.15	0.7000	835.8
288.15	0.8000	823.9
288.15	0.9000	810.0
288.15	0.9500	802.2
288.15	1.0000	793.8
298.15	0.0000	881.0
298.15	0.0500	877.3
298.15	0.1000	874.2
298.15	0.2000	867.7
298.15	0.3000	860.8
298.15	0.4000	853.4
298.15	0.5000	845.2
298.15	0.6000	836.1
298.15	0.7000	825.9
298.15	0.8000	814.4
298.15	0.9000	800.9
298.15	0.9500	793.4
298.15	1.0000	785.2
308.15	0.0000	869.7
308.15	0.0500	866.0
308.15	0.1000	862.8
308.15	0.2000	856.4
308.15	0.3000	849.7
308.15	0.4000	842.4
308.15	0.5000	834.5
308.15	0.6000	825.7
308.15	0.7000	815.8
308.15	0.8000	804.7
308.15	0.9000	791.7
308.15	0.9500	784.5
308.15	1.0000	776.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	892.2
288.15	0.0500	888.5
288.15	0.1000	885.3
288.15	0.2000	878.7
288.15	0.3000	871.7
288.15	0.4000	864.1
288.15	0.5000	855.7
288.15	0.6000	846.4
288.15	0.7000	835.8
288.15	0.8000	823.9
288.15	0.9000	810.0
288.15	0.9500	802.2
288.15	1.0000	793.8
298.15	0.0000	881.0
298.15	0.0500	877.3
298.15	0.1000	874.2
298.15	0.2000	867.7
298.15	0.3000	860.8
298.15	0.4000	853.4
298.15	0.5000	845.2
298.15	0.6000	836.1
298.15	0.7000	825.9
298.15	0.8000	814.4
298.15	0.9000	800.9
298.15	0.9500	793.4
298.15	1.0000	785.2
308.15	0.0000	869.7
308.15	0.0500	866.0
308.15	0.1000	862.8
308.15	0.2000	856.4
308.15	0.3000	849.7
308.15	0.4000	842.4
308.15	0.5000	834.5
308.15	0.6000	825.7
308.15	0.7000	815.8
308.15	0.8000	804.7
308.15	0.9000	791.7
308.15	0.9500	784.5
308.15	1.0000	776.6

Sources

• Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols at T = (288.15, 298.15 and 308.15) K
• Isothermal Vapor-Liquid Equilibrium of Binary Mixtures Containing 1-Chlorobutane, Ethanol, or Acetonitrile