Mixture of n-Hexane + Propane, 1-chloro-2-methyl-

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
0.0426	288.15	0.0653
0.1396	288.15	0.1700
0.2547	288.15	0.3010
0.3035	288.15	0.3470
0.3893	288.15	0.4200
0.4361	288.15	0.4570
0.5223	288.15	0.5256
0.5956	288.15	0.5839
0.6251	288.15	0.6049
0.6530	288.15	0.6301
0.6942	288.15	0.6656
0.7487	288.15	0.7091
0.8002	288.15	0.7600
0.9011	288.15	0.8680
0.9228	288.15	0.8944
1.0000	288.15	1.0000
0.0000	298.15	0.0000
0.0448	298.15	0.0664
0.1401	298.15	0.1715
0.2489	298.15	0.3001
0.3081	298.15	0.3457
0.3937	298.15	0.4191
0.4411	298.15	0.4597
0.5227	298.15	0.5251
0.5941	298.15	0.5829
0.6226	298.15	0.6049
0.6505	298.15	0.6291
0.6921	298.15	0.6656
0.7451	298.15	0.7091
0.8006	298.15	0.7620
0.8989	298.15	0.8674
0.9222	298.15	0.8966
1.0000	298.15	1.0000
0.0000	308.15	0.0000
0.0485	308.15	0.0656
0.1403	308.15	0.1725
0.2559	308.15	0.2972
0.3064	308.15	0.3414
0.3929	308.15	0.4177
0.4415	308.15	0.4579
0.5227	308.15	0.5246
0.5927	308.15	0.5844
0.6231	308.15	0.6069
0.6485	308.15	0.6311
0.6936	308.15	0.6687
0.7503	308.15	0.7189
0.7645	308.15	0.7345
0.8887	308.15	0.8658
0.9251	308.15	0.8989
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
0.0426	288.15	0.0653
0.1396	288.15	0.1700
0.2547	288.15	0.3010
0.3035	288.15	0.3470
0.3893	288.15	0.4200
0.4361	288.15	0.4570
0.5223	288.15	0.5256
0.5956	288.15	0.5839
0.6251	288.15	0.6049
0.6530	288.15	0.6301
0.6942	288.15	0.6656
0.7487	288.15	0.7091
0.8002	288.15	0.7600
0.9011	288.15	0.8680
0.9228	288.15	0.8944
1.0000	288.15	1.0000
0.0000	298.15	0.0000
0.0448	298.15	0.0664
0.1401	298.15	0.1715
0.2489	298.15	0.3001
0.3081	298.15	0.3457
0.3937	298.15	0.4191
0.4411	298.15	0.4597
0.5227	298.15	0.5251
0.5941	298.15	0.5829
0.6226	298.15	0.6049
0.6505	298.15	0.6291
0.6921	298.15	0.6656
0.7451	298.15	0.7091
0.8006	298.15	0.7620
0.8989	298.15	0.8674
0.9222	298.15	0.8966
1.0000	298.15	1.0000
0.0000	308.15	0.0000
0.0485	308.15	0.0656
0.1403	308.15	0.1725
0.2559	308.15	0.2972
0.3064	308.15	0.3414
0.3929	308.15	0.4177
0.4415	308.15	0.4579
0.5227	308.15	0.5246
0.5927	308.15	0.5844
0.6231	308.15	0.6069
0.6485	308.15	0.6311
0.6936	308.15	0.6687
0.7503	308.15	0.7189
0.7645	308.15	0.7345
0.8887	308.15	0.8658
0.9251	308.15	0.8989
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 n-Hexane (1) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0512	5.7120e-07
283.15	0.0999	5.6310e-07
283.15	0.2003	5.4680e-07
283.15	0.2993	5.3390e-07
283.15	0.4005	5.2390e-07
283.15	0.4977	5.1710e-07
283.15	0.5980	5.1200e-07
283.15	0.6993	5.0890e-07
283.15	0.7990	5.0770e-07
283.15	0.8967	5.0920e-07
283.15	0.9472	5.1030e-07
298.15	0.0512	4.8630e-07
298.15	0.0999	4.8170e-07
298.15	0.2003	4.7110e-07
298.15	0.2993	4.6330e-07
298.15	0.4005	4.5660e-07
298.15	0.4977	4.5170e-07
298.15	0.5980	4.4780e-07
298.15	0.6993	4.4620e-07
298.15	0.7990	4.4550e-07
298.15	0.8967	4.4570e-07
298.15	0.9472	4.4740e-07
313.15	0.0512	4.3200e-07
313.15	0.0999	4.2820e-07
313.15	0.2003	4.1960e-07
313.15	0.2993	4.1280e-07
313.15	0.4005	4.0770e-07
313.15	0.4977	4.0410e-07
313.15	0.5980	4.0170e-07
313.15	0.6993	4.0100e-07
313.15	0.7990	4.0020e-07
313.15	0.8967	4.0060e-07
313.15	0.9472	4.0230e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0512	5.7120e-07
283.15	0.0999	5.6310e-07
283.15	0.2003	5.4680e-07
283.15	0.2993	5.3390e-07
283.15	0.4005	5.2390e-07
283.15	0.4977	5.1710e-07
283.15	0.5980	5.1200e-07
283.15	0.6993	5.0890e-07
283.15	0.7990	5.0770e-07
283.15	0.8967	5.0920e-07
283.15	0.9472	5.1030e-07
298.15	0.0512	4.8630e-07
298.15	0.0999	4.8170e-07
298.15	0.2003	4.7110e-07
298.15	0.2993	4.6330e-07
298.15	0.4005	4.5660e-07
298.15	0.4977	4.5170e-07
298.15	0.5980	4.4780e-07
298.15	0.6993	4.4620e-07
298.15	0.7990	4.4550e-07
298.15	0.8967	4.4570e-07
298.15	0.9472	4.4740e-07
313.15	0.0512	4.3200e-07
313.15	0.0999	4.2820e-07
313.15	0.2003	4.1960e-07
313.15	0.2993	4.1280e-07
313.15	0.4005	4.0770e-07
313.15	0.4977	4.0410e-07
313.15	0.5980	4.0170e-07
313.15	0.6993	4.0100e-07
313.15	0.7990	4.0020e-07
313.15	0.8967	4.0060e-07
313.15	0.9472	4.0230e-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	13.00
0.0426	288.15	13.11
0.1396	288.15	13.57
0.2547	288.15	13.90
0.3035	288.15	13.96
0.3893	288.15	14.12
0.4361	288.15	14.15
0.5223	288.15	14.17
0.5956	288.15	14.16
0.6251	288.15	14.20
0.6530	288.15	14.11
0.6942	288.15	14.06
0.7487	288.15	13.85
0.8002	288.15	13.82
0.9011	288.15	13.44
0.9228	288.15	13.34
1.0000	288.15	12.89
0.0000	298.15	20.35
0.0448	298.15	20.55
0.1401	298.15	21.25
0.2489	298.15	21.77
0.3081	298.15	21.94
0.3937	298.15	22.12
0.4411	298.15	22.16
0.5227	298.15	22.20
0.5941	298.15	22.16
0.6226	298.15	22.16
0.6505	298.15	22.08
0.6921	298.15	21.99
0.7451	298.15	21.84
0.8006	298.15	21.64
0.8989	298.15	21.07
0.9222	298.15	20.88
1.0000	298.15	20.22
0.0000	308.15	30.45
0.0485	308.15	31.10
0.1403	308.15	31.87
0.2559	308.15	32.73
0.3064	308.15	33.02
0.3929	308.15	33.35
0.4415	308.15	33.48
0.5227	308.15	33.55
0.5927	308.15	33.50
0.6231	308.15	33.45
0.6485	308.15	33.41
0.6936	308.15	33.23
0.7503	308.15	33.03
0.7645	308.15	32.76
0.8887	308.15	31.95
0.9251	308.15	31.65
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	13.00
0.0426	288.15	13.11
0.1396	288.15	13.57
0.2547	288.15	13.90
0.3035	288.15	13.96
0.3893	288.15	14.12
0.4361	288.15	14.15
0.5223	288.15	14.17
0.5956	288.15	14.16
0.6251	288.15	14.20
0.6530	288.15	14.11
0.6942	288.15	14.06
0.7487	288.15	13.85
0.8002	288.15	13.82
0.9011	288.15	13.44
0.9228	288.15	13.34
1.0000	288.15	12.89
0.0000	298.15	20.35
0.0448	298.15	20.55
0.1401	298.15	21.25
0.2489	298.15	21.77
0.3081	298.15	21.94
0.3937	298.15	22.12
0.4411	298.15	22.16
0.5227	298.15	22.20
0.5941	298.15	22.16
0.6226	298.15	22.16
0.6505	298.15	22.08
0.6921	298.15	21.99
0.7451	298.15	21.84
0.8006	298.15	21.64
0.8989	298.15	21.07
0.9222	298.15	20.88
1.0000	298.15	20.22
0.0000	308.15	30.45
0.0485	308.15	31.10
0.1403	308.15	31.87
0.2559	308.15	32.73
0.3064	308.15	33.02
0.3929	308.15	33.35
0.4415	308.15	33.48
0.5227	308.15	33.55
0.5927	308.15	33.50
0.6231	308.15	33.45
0.6485	308.15	33.41
0.6936	308.15	33.23
0.7503	308.15	33.03
0.7645	308.15	32.76
0.8887	308.15	31.95
0.9251	308.15	31.65
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	888.845
283.15	0.0512	874.715
283.15	0.0999	861.62
283.15	0.2003	835.641
283.15	0.2993	811.259
283.15	0.4005	787.516
283.15	0.4977	765.822
283.15	0.5980	744.502
283.15	0.6993	723.963
283.15	0.7990	704.731
283.15	0.8967	686.793
283.15	0.9472	677.811
283.15	1.0000	668.609
298.15	0.0000	871.533
298.15	0.0512	857.627
298.15	0.0999	844.732
298.15	0.2003	819.166
298.15	0.2993	795.172
298.15	0.4005	771.817
298.15	0.4977	750.487
298.15	0.5980	729.51
298.15	0.6993	709.35
298.15	0.7990	690.452
298.15	0.8967	672.832
298.15	0.9472	664.036
298.15	1.0000	654.96
313.15	0.0000	853.902
313.15	0.0512	840.236
313.15	0.0999	827.564
313.15	0.2003	802.454
313.15	0.2993	778.889
313.15	0.4005	755.943
313.15	0.4977	735.001
313.15	0.5980	714.446
313.15	0.6993	694.648
313.15	0.7990	676.142
313.15	0.8967	658.858
313.15	0.9472	650.244
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	888.845
283.15	0.0512	874.715
283.15	0.0999	861.62
283.15	0.2003	835.641
283.15	0.2993	811.259
283.15	0.4005	787.516
283.15	0.4977	765.822
283.15	0.5980	744.502
283.15	0.6993	723.963
283.15	0.7990	704.731
283.15	0.8967	686.793
283.15	0.9472	677.811
283.15	1.0000	668.609
298.15	0.0000	871.533
298.15	0.0512	857.627
298.15	0.0999	844.732
298.15	0.2003	819.166
298.15	0.2993	795.172
298.15	0.4005	771.817
298.15	0.4977	750.487
298.15	0.5980	729.51
298.15	0.6993	709.35
298.15	0.7990	690.452
298.15	0.8967	672.832
298.15	0.9472	664.036
298.15	1.0000	654.96
313.15	0.0000	853.902
313.15	0.0512	840.236
313.15	0.0999	827.564
313.15	0.2003	802.454
313.15	0.2993	778.889
313.15	0.4005	755.943
313.15	0.4977	735.001
313.15	0.5980	714.446
313.15	0.6993	694.648
313.15	0.7990	676.142
313.15	0.8967	658.858
313.15	0.9472	650.244
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	1141.74
283.15	0.0512	1139.34
283.15	0.0999	1137.29
283.15	0.2003	1134.05
283.15	0.2993	1131.89
283.15	0.4005	1130.62
283.15	0.4977	1130.53
283.15	0.5980	1131.27
283.15	0.6993	1133.04
283.15	0.7990	1135.76
283.15	0.8967	1139.56
283.15	0.9472	1142.02
283.15	1.0000	1145.13
298.15	0.0000	1078.58
298.15	0.0512	1075.92
298.15	0.0999	1073.68
298.15	0.2003	1070.05
298.15	0.2993	1067.5
298.15	0.4005	1065.79
298.15	0.4977	1065.18
298.15	0.5980	1065.5
298.15	0.6993	1066.74
298.15	0.7990	1068.97
298.15	0.8967	1072.25
298.15	0.9472	1074.34
298.15	1.0000	1077.0
313.15	0.0000	1016.27
313.15	0.0512	1013.39
313.15	0.0999	1010.96
313.15	0.2003	1006.92
313.15	0.2993	1003.89
313.15	0.4005	1001.79
313.15	0.4977	1000.62
313.15	0.5980	1000.4
313.15	0.6993	1001.12
313.15	0.7990	1002.8
313.15	0.8967	1005.59
313.15	0.9472	1007.45
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	1141.74
283.15	0.0512	1139.34
283.15	0.0999	1137.29
283.15	0.2003	1134.05
283.15	0.2993	1131.89
283.15	0.4005	1130.62
283.15	0.4977	1130.53
283.15	0.5980	1131.27
283.15	0.6993	1133.04
283.15	0.7990	1135.76
283.15	0.8967	1139.56
283.15	0.9472	1142.02
283.15	1.0000	1145.13
298.15	0.0000	1078.58
298.15	0.0512	1075.92
298.15	0.0999	1073.68
298.15	0.2003	1070.05
298.15	0.2993	1067.5
298.15	0.4005	1065.79
298.15	0.4977	1065.18
298.15	0.5980	1065.5
298.15	0.6993	1066.74
298.15	0.7990	1068.97
298.15	0.8967	1072.25
298.15	0.9472	1074.34
298.15	1.0000	1077.0
313.15	0.0000	1016.27
313.15	0.0512	1013.39
313.15	0.0999	1010.96
313.15	0.2003	1006.92
313.15	0.2993	1003.89
313.15	0.4005	1001.79
313.15	0.4977	1000.62
313.15	0.5980	1000.4
313.15	0.6993	1001.12
313.15	0.7990	1002.8
313.15	0.8967	1005.59
313.15	0.9472	1007.45
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