Mixture of n-Hexane + Butane, 2-chloro-

Datasets

1. Mole fraction (2)
2. ν - Kinematic viscosity, m2/s (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. ρ_l - Mass density, kg/m3 (2)
5. c_sound,fluid - Speed of Sound, m/s (2)

Mole fraction of n-Hexane (1) [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Liquid	Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Gas
0.0000	288.15	0.0000
0.0574	288.15	0.0747
0.1476	288.15	0.1868
0.2386	288.15	0.2737
0.3098	288.15	0.3353
0.3804	288.15	0.4007
0.4244	288.15	0.4345
0.4853	288.15	0.4843
0.5277	288.15	0.5162
0.5583	288.15	0.5413
0.6269	288.15	0.5953
0.7126	288.15	0.6642
0.8235	288.15	0.7547
0.9377	288.15	0.9115
1.0000	288.15	1.0000
0.0000	298.15	0.0000
0.0566	298.15	0.0770
0.1532	298.15	0.1901
0.2390	298.15	0.2771
0.3101	298.15	0.3357
0.3912	298.15	0.4057
0.4253	298.15	0.4363
0.4853	298.15	0.4843
0.5253	298.15	0.5162
0.5559	298.15	0.5408
0.6219	298.15	0.5948
0.7042	298.15	0.6636
0.8064	298.15	0.7504
0.9377	298.15	0.9109
1.0000	298.15	1.0000
0.0000	308.15	0.0000
0.0555	308.15	0.0747
0.1431	308.15	0.1885
0.2377	308.15	0.2719
0.3105	308.15	0.3351
0.3813	308.15	0.3989
0.4253	308.15	0.4349
0.4853	308.15	0.4843
0.5258	308.15	0.5148
0.5544	308.15	0.5403
0.6163	308.15	0.5943
0.7121	308.15	0.6662
0.8080	308.15	0.7676
0.9383	308.15	0.9121
1.0000	308.15	1.0000

Mole fraction of n-Hexane (1) [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Liquid	Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Gas
0.0000	288.15	0.0000
0.0574	288.15	0.0747
0.1476	288.15	0.1868
0.2386	288.15	0.2737
0.3098	288.15	0.3353
0.3804	288.15	0.4007
0.4244	288.15	0.4345
0.4853	288.15	0.4843
0.5277	288.15	0.5162
0.5583	288.15	0.5413
0.6269	288.15	0.5953
0.7126	288.15	0.6642
0.8235	288.15	0.7547
0.9377	288.15	0.9115
1.0000	288.15	1.0000
0.0000	298.15	0.0000
0.0566	298.15	0.0770
0.1532	298.15	0.1901
0.2390	298.15	0.2771
0.3101	298.15	0.3357
0.3912	298.15	0.4057
0.4253	298.15	0.4363
0.4853	298.15	0.4843
0.5253	298.15	0.5162
0.5559	298.15	0.5408
0.6219	298.15	0.5948
0.7042	298.15	0.6636
0.8064	298.15	0.7504
0.9377	298.15	0.9109
1.0000	298.15	1.0000
0.0000	308.15	0.0000
0.0555	308.15	0.0747
0.1431	308.15	0.1885
0.2377	308.15	0.2719
0.3105	308.15	0.3351
0.3813	308.15	0.3989
0.4253	308.15	0.4349
0.4853	308.15	0.4843
0.5258	308.15	0.5148
0.5544	308.15	0.5403
0.6163	308.15	0.5943
0.7121	308.15	0.6662
0.8080	308.15	0.7676
0.9383	308.15	0.9121
1.0000	308.15	1.0000

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0509	5.1860e-07
283.15	0.1002	5.1470e-07
283.15	0.1802	5.0900e-07
283.15	0.3029	5.0250e-07
283.15	0.4045	4.9890e-07
283.15	0.4991	4.9750e-07
283.15	0.5974	4.9680e-07
283.15	0.6992	4.9820e-07
283.15	0.7996	5.0070e-07
283.15	0.8981	5.0550e-07
283.15	0.9477	5.0860e-07
298.15	0.0509	4.5790e-07
298.15	0.1002	4.5480e-07
298.15	0.1802	4.5010e-07
298.15	0.3029	4.4480e-07
298.15	0.4045	4.4200e-07
298.15	0.4991	4.4080e-07
298.15	0.5974	4.4010e-07
298.15	0.6992	4.4060e-07
298.15	0.7996	4.4190e-07
298.15	0.8981	4.4470e-07
298.15	0.9477	4.4650e-07
313.15	0.0509	4.0340e-07
313.15	0.1002	4.0120e-07
313.15	0.1802	3.9800e-07
313.15	0.3029	3.9480e-07
313.15	0.4045	3.9320e-07
313.15	0.4991	3.9260e-07
313.15	0.5974	3.9260e-07
313.15	0.6992	3.9390e-07
313.15	0.7996	3.9610e-07
313.15	0.8981	3.9930e-07
313.15	0.9477	4.0150e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0509	5.1860e-07
283.15	0.1002	5.1470e-07
283.15	0.1802	5.0900e-07
283.15	0.3029	5.0250e-07
283.15	0.4045	4.9890e-07
283.15	0.4991	4.9750e-07
283.15	0.5974	4.9680e-07
283.15	0.6992	4.9820e-07
283.15	0.7996	5.0070e-07
283.15	0.8981	5.0550e-07
283.15	0.9477	5.0860e-07
298.15	0.0509	4.5790e-07
298.15	0.1002	4.5480e-07
298.15	0.1802	4.5010e-07
298.15	0.3029	4.4480e-07
298.15	0.4045	4.4200e-07
298.15	0.4991	4.4080e-07
298.15	0.5974	4.4010e-07
298.15	0.6992	4.4060e-07
298.15	0.7996	4.4190e-07
298.15	0.8981	4.4470e-07
298.15	0.9477	4.4650e-07
313.15	0.0509	4.0340e-07
313.15	0.1002	4.0120e-07
313.15	0.1802	3.9800e-07
313.15	0.3029	3.9480e-07
313.15	0.4045	3.9320e-07
313.15	0.4991	3.9260e-07
313.15	0.5974	3.9260e-07
313.15	0.6992	3.9390e-07
313.15	0.7996	3.9610e-07
313.15	0.8981	3.9930e-07
313.15	0.9477	4.0150e-07

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	288.15	13.36
0.0574	288.15	13.56
0.1476	288.15	13.97
0.2386	288.15	14.27
0.3098	288.15	14.41
0.3804	288.15	14.53
0.4244	288.15	14.56
0.4853	288.15	14.56
0.5277	288.15	14.59
0.5583	288.15	14.54
0.6269	288.15	14.44
0.7126	288.15	14.29
0.8235	288.15	13.97
0.9377	288.15	13.29
1.0000	288.15	12.89
0.0000	298.15	20.91
0.0566	298.15	21.21
0.1532	298.15	21.88
0.2390	298.15	22.29
0.3101	298.15	22.52
0.3912	298.15	22.67
0.4253	298.15	22.68
0.4853	298.15	22.75
0.5253	298.15	22.71
0.5559	298.15	22.68
0.6219	298.15	22.57
0.7042	298.15	22.34
0.8064	298.15	21.86
0.9377	298.15	20.88
1.0000	298.15	20.22
0.0000	308.15	31.55
0.0555	308.15	32.15
0.1431	308.15	33.10
0.2377	308.15	33.69
0.3105	308.15	34.00
0.3813	308.15	34.25
0.4253	308.15	34.33
0.4853	308.15	34.33
0.5258	308.15	34.31
0.5544	308.15	34.23
0.6163	308.15	34.06
0.7121	308.15	33.76
0.8080	308.15	33.11
0.9383	308.15	31.71
1.0000	308.15	30.70

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	288.15	13.36
0.0574	288.15	13.56
0.1476	288.15	13.97
0.2386	288.15	14.27
0.3098	288.15	14.41
0.3804	288.15	14.53
0.4244	288.15	14.56
0.4853	288.15	14.56
0.5277	288.15	14.59
0.5583	288.15	14.54
0.6269	288.15	14.44
0.7126	288.15	14.29
0.8235	288.15	13.97
0.9377	288.15	13.29
1.0000	288.15	12.89
0.0000	298.15	20.91
0.0566	298.15	21.21
0.1532	298.15	21.88
0.2390	298.15	22.29
0.3101	298.15	22.52
0.3912	298.15	22.67
0.4253	298.15	22.68
0.4853	298.15	22.75
0.5253	298.15	22.71
0.5559	298.15	22.68
0.6219	298.15	22.57
0.7042	298.15	22.34
0.8064	298.15	21.86
0.9377	298.15	20.88
1.0000	298.15	20.22
0.0000	308.15	31.55
0.0555	308.15	32.15
0.1431	308.15	33.10
0.2377	308.15	33.69
0.3105	308.15	34.00
0.3813	308.15	34.25
0.4253	308.15	34.33
0.4853	308.15	34.33
0.5258	308.15	34.31
0.5544	308.15	34.23
0.6163	308.15	34.06
0.7121	308.15	33.76
0.8080	308.15	33.11
0.9383	308.15	31.71
1.0000	308.15	30.70

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	884.34
283.15	0.0509	870.642
283.15	0.1002	857.772
283.15	0.1802	837.449
283.15	0.3029	807.817
283.15	0.4045	784.524
283.15	0.4991	763.875
283.15	0.5974	743.353
283.15	0.6992	723.059
283.15	0.7996	704.031
283.15	0.8981	686.218
283.15	0.9477	677.555
283.15	1.0000	668.609
298.15	0.0000	867.474
298.15	0.0509	853.976
298.15	0.1002	841.229
298.15	0.1802	821.198
298.15	0.3029	791.981
298.15	0.4045	769.021
298.15	0.4991	748.682
298.15	0.5974	728.495
298.15	0.6992	708.519
298.15	0.7996	689.807
298.15	0.8981	672.305
298.15	0.9477	663.793
298.15	1.0000	654.96
313.15	0.0000	850.266
313.15	0.0509	836.967
313.15	0.1002	824.438
313.15	0.1802	804.693
313.15	0.3029	775.929
313.15	0.4045	753.339
313.15	0.4991	733.339
313.15	0.5974	713.496
313.15	0.6992	693.898
313.15	0.7996	675.523
313.15	0.8981	658.349
313.15	0.9477	650.005
313.15	1.0000	641.39

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	884.34
283.15	0.0509	870.642
283.15	0.1002	857.772
283.15	0.1802	837.449
283.15	0.3029	807.817
283.15	0.4045	784.524
283.15	0.4991	763.875
283.15	0.5974	743.353
283.15	0.6992	723.059
283.15	0.7996	704.031
283.15	0.8981	686.218
283.15	0.9477	677.555
283.15	1.0000	668.609
298.15	0.0000	867.474
298.15	0.0509	853.976
298.15	0.1002	841.229
298.15	0.1802	821.198
298.15	0.3029	791.981
298.15	0.4045	769.021
298.15	0.4991	748.682
298.15	0.5974	728.495
298.15	0.6992	708.519
298.15	0.7996	689.807
298.15	0.8981	672.305
298.15	0.9477	663.793
298.15	1.0000	654.96
313.15	0.0000	850.266
313.15	0.0509	836.967
313.15	0.1002	824.438
313.15	0.1802	804.693
313.15	0.3029	775.929
313.15	0.4045	753.339
313.15	0.4991	733.339
313.15	0.5974	713.496
313.15	0.6992	693.898
313.15	0.7996	675.523
313.15	0.8981	658.349
313.15	0.9477	650.005
313.15	1.0000	641.39

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0000	1127.71
283.15	0.0509	1126.4
283.15	0.1002	1125.21
283.15	0.1802	1124.04
283.15	0.3029	1123.11
283.15	0.4045	1123.38
283.15	0.4991	1124.48
283.15	0.5974	1126.49
283.15	0.6992	1129.46
283.15	0.7996	1133.35
283.15	0.8981	1138.31
283.15	0.9477	1141.38
283.15	1.0000	1145.13
298.15	0.0000	1066.24
298.15	0.0509	1064.52
298.15	0.1002	1063.14
298.15	0.1802	1061.38
298.15	0.3029	1059.69
298.15	0.4045	1059.27
298.15	0.4991	1059.75
298.15	0.5974	1061.1
298.15	0.6992	1063.44
298.15	0.7996	1066.75
298.15	0.8981	1071.08
298.15	0.9477	1073.72
298.15	1.0000	1077.0
313.15	0.0000	1005.32
313.15	0.0509	1003.32
313.15	0.1002	1001.59
313.15	0.1802	999.26
313.15	0.3029	996.75
313.15	0.4045	995.71
313.15	0.4991	995.56
313.15	0.5974	996.3
313.15	0.6992	998.0
313.15	0.7996	1000.76
313.15	0.8981	1004.46
313.15	0.9477	1006.85
313.15	1.0000	1009.88

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0000	1127.71
283.15	0.0509	1126.4
283.15	0.1002	1125.21
283.15	0.1802	1124.04
283.15	0.3029	1123.11
283.15	0.4045	1123.38
283.15	0.4991	1124.48
283.15	0.5974	1126.49
283.15	0.6992	1129.46
283.15	0.7996	1133.35
283.15	0.8981	1138.31
283.15	0.9477	1141.38
283.15	1.0000	1145.13
298.15	0.0000	1066.24
298.15	0.0509	1064.52
298.15	0.1002	1063.14
298.15	0.1802	1061.38
298.15	0.3029	1059.69
298.15	0.4045	1059.27
298.15	0.4991	1059.75
298.15	0.5974	1061.1
298.15	0.6992	1063.44
298.15	0.7996	1066.75
298.15	0.8981	1071.08
298.15	0.9477	1073.72
298.15	1.0000	1077.0
313.15	0.0000	1005.32
313.15	0.0509	1003.32
313.15	0.1002	1001.59
313.15	0.1802	999.26
313.15	0.3029	996.75
313.15	0.4045	995.71
313.15	0.4991	995.56
313.15	0.5974	996.3
313.15	0.6992	998.0
313.15	0.7996	1000.76
313.15	0.8981	1004.46
313.15	0.9477	1006.85
313.15	1.0000	1009.88

Sources

• Volumetric and acoustic behaviour of systems containing n-hexane, or n-heptane and isomeric chlorobutanes
• Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
• Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions