Mixture of n-Hexane + n-Propyl chloride

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. n₀ - Refractive index (Na D-line) (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]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mole fraction of n-Hexane (1) - Gas
0.0705	0.0422
0.1205	0.0783
0.1791	0.1104
0.2658	0.1657
0.3496	0.2108
0.4421	0.2695
0.4970	0.3070
0.5492	0.3520
0.6456	0.4233
0.7223	0.4932
0.7902	0.5593
0.8481	0.6536
0.9353	0.7943

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

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mole fraction of n-Hexane (1) - Gas
0.0705	0.0422
0.1205	0.0783
0.1791	0.1104
0.2658	0.1657
0.3496	0.2108
0.4421	0.2695
0.4970	0.3070
0.5492	0.3520
0.6456	0.4233
0.7223	0.4932
0.7902	0.5593
0.8481	0.6536
0.9353	0.7943

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0705	44.55
0.1205	44.00
0.1791	42.98
0.2658	41.45
0.3496	40.08
0.4421	38.24
0.4970	37.02
0.5492	35.38
0.6456	33.39
0.7223	31.00
0.7902	29.07
0.8481	27.07
0.9353	23.49

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0705	44.55
0.1205	44.00
0.1791	42.98
0.2658	41.45
0.3496	40.08
0.4421	38.24
0.4970	37.02
0.5492	35.38
0.6456	33.39
0.7223	31.00
0.7902	29.07
0.8481	27.07
0.9353	23.49

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0516	1.393
283.15	0.1008	1.3919
283.15	0.1992	1.3897
283.15	0.2976	1.3878
283.15	0.3852	1.3864
283.15	0.4999	1.3847
283.15	0.5996	1.3835
283.15	0.7017	1.3825
283.15	0.7929	1.3817
283.15	0.9005	1.381
283.15	0.9504	1.3807
288.15	0.0516	1.3901
288.15	0.1008	1.389
288.15	0.1992	1.3868
288.15	0.2976	1.385
288.15	0.3852	1.3835
288.15	0.4999	1.3819
288.15	0.5996	1.3807
288.15	0.7017	1.3797
288.15	0.7929	1.379
288.15	0.9005	1.3783
288.15	0.9504	1.378
293.15	0.0516	1.3872
293.15	0.1008	1.3861
293.15	0.1992	1.3839
293.15	0.2976	1.3821
293.15	0.3852	1.3807
293.15	0.4999	1.3791
293.15	0.5996	1.3779
293.15	0.7017	1.3769
293.15	0.7929	1.3762
293.15	0.9005	1.3755
293.15	0.9504	1.3753
298.15	0.0516	1.3843
298.15	0.1008	1.3831
298.15	0.1992	1.381
298.15	0.2976	1.3792
298.15	0.3852	1.3778
298.15	0.4999	1.3762
298.15	0.5996	1.375
298.15	0.7017	1.3741
298.15	0.7929	1.3734
298.15	0.9005	1.3727
298.15	0.9504	1.3725
303.15	0.0516	1.3813
303.15	0.1008	1.3801
303.15	0.1992	1.3781
303.15	0.2976	1.3762
303.15	0.3852	1.3748
303.15	0.4999	1.3733
303.15	0.5996	1.3721
303.15	0.7017	1.3712
303.15	0.7929	1.3705
303.15	0.9005	1.3699
303.15	0.9504	1.3697
308.15	0.0516	1.3783
308.15	0.1008	1.3772
308.15	0.1992	1.3751
308.15	0.2976	1.3733
308.15	0.3852	1.3719
308.15	0.4999	1.3703
308.15	0.5996	1.3692
308.15	0.7017	1.3683
308.15	0.7929	1.3677
308.15	0.9005	1.3671
308.15	0.9504	1.3669
313.15	0.0516	1.3752
313.15	0.1008	1.3741
313.15	0.1992	1.3721
313.15	0.2976	1.3705
313.15	0.3852	1.3687
313.15	0.4999	1.3673
313.15	0.5996	1.3662
313.15	0.7017	1.3653
313.15	0.7929	1.3647
313.15	0.9005	1.3642
313.15	0.9504	1.3641

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0516	1.393
283.15	0.1008	1.3919
283.15	0.1992	1.3897
283.15	0.2976	1.3878
283.15	0.3852	1.3864
283.15	0.4999	1.3847
283.15	0.5996	1.3835
283.15	0.7017	1.3825
283.15	0.7929	1.3817
283.15	0.9005	1.381
283.15	0.9504	1.3807
288.15	0.0516	1.3901
288.15	0.1008	1.389
288.15	0.1992	1.3868
288.15	0.2976	1.385
288.15	0.3852	1.3835
288.15	0.4999	1.3819
288.15	0.5996	1.3807
288.15	0.7017	1.3797
288.15	0.7929	1.379
288.15	0.9005	1.3783
288.15	0.9504	1.378
293.15	0.0516	1.3872
293.15	0.1008	1.3861
293.15	0.1992	1.3839
293.15	0.2976	1.3821
293.15	0.3852	1.3807
293.15	0.4999	1.3791
293.15	0.5996	1.3779
293.15	0.7017	1.3769
293.15	0.7929	1.3762
293.15	0.9005	1.3755
293.15	0.9504	1.3753
298.15	0.0516	1.3843
298.15	0.1008	1.3831
298.15	0.1992	1.381
298.15	0.2976	1.3792
298.15	0.3852	1.3778
298.15	0.4999	1.3762
298.15	0.5996	1.375
298.15	0.7017	1.3741
298.15	0.7929	1.3734
298.15	0.9005	1.3727
298.15	0.9504	1.3725
303.15	0.0516	1.3813
303.15	0.1008	1.3801
303.15	0.1992	1.3781
303.15	0.2976	1.3762
303.15	0.3852	1.3748
303.15	0.4999	1.3733
303.15	0.5996	1.3721
303.15	0.7017	1.3712
303.15	0.7929	1.3705
303.15	0.9005	1.3699
303.15	0.9504	1.3697
308.15	0.0516	1.3783
308.15	0.1008	1.3772
308.15	0.1992	1.3751
308.15	0.2976	1.3733
308.15	0.3852	1.3719
308.15	0.4999	1.3703
308.15	0.5996	1.3692
308.15	0.7017	1.3683
308.15	0.7929	1.3677
308.15	0.9005	1.3671
308.15	0.9504	1.3669
313.15	0.0516	1.3752
313.15	0.1008	1.3741
313.15	0.1992	1.3721
313.15	0.2976	1.3705
313.15	0.3852	1.3687
313.15	0.4999	1.3673
313.15	0.5996	1.3662
313.15	0.7017	1.3653
313.15	0.7929	1.3647
313.15	0.9005	1.3642
313.15	0.9504	1.3641

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	0.0516	884.79
283.15	0.1008	868.63
283.15	0.1992	838.29
283.15	0.2976	810.48
283.15	0.3852	787.75
283.15	0.4999	760.62
283.15	0.5996	739.12
283.15	0.7017	718.9
283.15	0.7929	702.22
283.15	0.9005	684.04
283.15	0.9504	676.12
288.15	0.0516	878.37
288.15	0.1008	862.33
288.15	0.1992	832.23
288.15	0.2976	804.73
288.15	0.3852	782.15
288.15	0.4999	755.29
288.15	0.5996	734.0
288.15	0.7017	713.96
288.15	0.7929	697.43
288.15	0.9005	679.39
288.15	0.9504	671.54
293.15	0.0516	872.24
293.15	0.1008	856.3
293.15	0.1992	826.43
293.15	0.2976	799.11
293.15	0.3852	776.76
293.15	0.4999	750.09
293.15	0.5996	728.96
293.15	0.7017	709.06
293.15	0.7929	692.68
293.15	0.9005	674.8
293.15	0.9504	667.0
298.15	0.0516	865.98
298.15	0.1008	850.13
298.15	0.1992	820.47
298.15	0.2976	793.42
298.15	0.3852	771.26
298.15	0.4999	744.73
298.15	0.5996	723.8
298.15	0.7017	704.08
298.15	0.7929	687.82
298.15	0.9005	670.08
298.15	0.9504	662.34
303.15	0.0516	859.75
303.15	0.1008	844.01
303.15	0.1992	814.62
303.15	0.2976	787.75
303.15	0.3852	765.76
303.15	0.4999	739.45
303.15	0.5996	718.66
303.15	0.7017	699.15
303.15	0.7929	683.04
303.15	0.9005	665.45
303.15	0.9504	657.78
308.15	0.0516	853.37
308.15	0.1008	837.77
308.15	0.1992	808.59
308.15	0.2976	781.96
308.15	0.3852	760.14
308.15	0.4999	734.06
308.15	0.5996	713.46
308.15	0.7017	694.09
308.15	0.7929	678.11
308.15	0.9005	660.68
308.15	0.9504	653.06
313.15	0.0516	847.65
313.15	0.1008	832.1
313.15	0.1992	803.1
313.15	0.2976	776.65
313.15	0.3852	754.99
313.15	0.4999	729.12
313.15	0.5996	708.62
313.15	0.7017	689.41
313.15	0.7929	673.58
313.15	0.9005	656.23
313.15	0.9504	648.68

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	0.0516	884.79
283.15	0.1008	868.63
283.15	0.1992	838.29
283.15	0.2976	810.48
283.15	0.3852	787.75
283.15	0.4999	760.62
283.15	0.5996	739.12
283.15	0.7017	718.9
283.15	0.7929	702.22
283.15	0.9005	684.04
283.15	0.9504	676.12
288.15	0.0516	878.37
288.15	0.1008	862.33
288.15	0.1992	832.23
288.15	0.2976	804.73
288.15	0.3852	782.15
288.15	0.4999	755.29
288.15	0.5996	734.0
288.15	0.7017	713.96
288.15	0.7929	697.43
288.15	0.9005	679.39
288.15	0.9504	671.54
293.15	0.0516	872.24
293.15	0.1008	856.3
293.15	0.1992	826.43
293.15	0.2976	799.11
293.15	0.3852	776.76
293.15	0.4999	750.09
293.15	0.5996	728.96
293.15	0.7017	709.06
293.15	0.7929	692.68
293.15	0.9005	674.8
293.15	0.9504	667.0
298.15	0.0516	865.98
298.15	0.1008	850.13
298.15	0.1992	820.47
298.15	0.2976	793.42
298.15	0.3852	771.26
298.15	0.4999	744.73
298.15	0.5996	723.8
298.15	0.7017	704.08
298.15	0.7929	687.82
298.15	0.9005	670.08
298.15	0.9504	662.34
303.15	0.0516	859.75
303.15	0.1008	844.01
303.15	0.1992	814.62
303.15	0.2976	787.75
303.15	0.3852	765.76
303.15	0.4999	739.45
303.15	0.5996	718.66
303.15	0.7017	699.15
303.15	0.7929	683.04
303.15	0.9005	665.45
303.15	0.9504	657.78
308.15	0.0516	853.37
308.15	0.1008	837.77
308.15	0.1992	808.59
308.15	0.2976	781.96
308.15	0.3852	760.14
308.15	0.4999	734.06
308.15	0.5996	713.46
308.15	0.7017	694.09
308.15	0.7929	678.11
308.15	0.9005	660.68
308.15	0.9504	653.06
313.15	0.0516	847.65
313.15	0.1008	832.1
313.15	0.1992	803.1
313.15	0.2976	776.65
313.15	0.3852	754.99
313.15	0.4999	729.12
313.15	0.5996	708.62
313.15	0.7017	689.41
313.15	0.7929	673.58
313.15	0.9005	656.23
313.15	0.9504	648.68

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	0.0516	1127.7
283.15	0.1008	1125.9
283.15	0.1992	1122.9
283.15	0.2976	1121.7
283.15	0.3852	1121.6
283.15	0.4999	1122.8
283.15	0.5996	1125.1
283.15	0.7017	1128.3
283.15	0.7929	1132.0
283.15	0.9005	1137.6
283.15	0.9504	1140.6
288.15	0.0516	1106.4
288.15	0.1008	1104.4
288.15	0.1992	1101.2
288.15	0.2976	1099.9
288.15	0.3852	1099.6
288.15	0.4999	1100.9
288.15	0.5996	1103.0
288.15	0.7017	1106.2
288.15	0.7929	1109.8
288.15	0.9005	1115.3
288.15	0.9504	1118.3
293.15	0.0516	1084.5
293.15	0.1008	1082.5
293.15	0.1992	1079.2
293.15	0.2976	1077.8
293.15	0.3852	1077.5
293.15	0.4999	1078.7
293.15	0.5996	1080.7
293.15	0.7017	1083.8
293.15	0.7929	1087.6
293.15	0.9005	1093.0
293.15	0.9504	1095.9
298.15	0.0516	1062.4
298.15	0.1008	1060.3
298.15	0.1992	1057.0
298.15	0.2976	1055.5
298.15	0.3852	1055.1
298.15	0.4999	1056.3
298.15	0.5996	1058.2
298.15	0.7017	1061.2
298.15	0.7929	1064.8
298.15	0.9005	1070.2
298.15	0.9504	1073.1
303.15	0.0516	1040.9
303.15	0.1008	1038.6
303.15	0.1992	1035.2
303.15	0.2976	1033.5
303.15	0.3852	1033.0
303.15	0.4999	1034.1
303.15	0.5996	1036.0
303.15	0.7017	1039.1
303.15	0.7929	1042.6
303.15	0.9005	1047.9
303.15	0.9504	1050.7
308.15	0.0516	1019.2
308.15	0.1008	1016.7
308.15	0.1992	1013.3
308.15	0.2976	1011.7
308.15	0.3852	1011.2
308.15	0.4999	1012.1
308.15	0.5996	1014.0
308.15	0.7017	1016.9
308.15	0.7929	1020.5
308.15	0.9005	1025.5
308.15	0.9504	1028.4
313.15	0.0516	997.2
313.15	0.1008	994.8
313.15	0.1992	991.5
313.15	0.2976	989.7
313.15	0.3852	989.3
313.15	0.4999	990.1
313.15	0.5996	992.0
313.15	0.7017	994.9
313.15	0.7929	998.4
313.15	0.9005	1003.7
313.15	0.9504	1006.4

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	0.0516	1127.7
283.15	0.1008	1125.9
283.15	0.1992	1122.9
283.15	0.2976	1121.7
283.15	0.3852	1121.6
283.15	0.4999	1122.8
283.15	0.5996	1125.1
283.15	0.7017	1128.3
283.15	0.7929	1132.0
283.15	0.9005	1137.6
283.15	0.9504	1140.6
288.15	0.0516	1106.4
288.15	0.1008	1104.4
288.15	0.1992	1101.2
288.15	0.2976	1099.9
288.15	0.3852	1099.6
288.15	0.4999	1100.9
288.15	0.5996	1103.0
288.15	0.7017	1106.2
288.15	0.7929	1109.8
288.15	0.9005	1115.3
288.15	0.9504	1118.3
293.15	0.0516	1084.5
293.15	0.1008	1082.5
293.15	0.1992	1079.2
293.15	0.2976	1077.8
293.15	0.3852	1077.5
293.15	0.4999	1078.7
293.15	0.5996	1080.7
293.15	0.7017	1083.8
293.15	0.7929	1087.6
293.15	0.9005	1093.0
293.15	0.9504	1095.9
298.15	0.0516	1062.4
298.15	0.1008	1060.3
298.15	0.1992	1057.0
298.15	0.2976	1055.5
298.15	0.3852	1055.1
298.15	0.4999	1056.3
298.15	0.5996	1058.2
298.15	0.7017	1061.2
298.15	0.7929	1064.8
298.15	0.9005	1070.2
298.15	0.9504	1073.1
303.15	0.0516	1040.9
303.15	0.1008	1038.6
303.15	0.1992	1035.2
303.15	0.2976	1033.5
303.15	0.3852	1033.0
303.15	0.4999	1034.1
303.15	0.5996	1036.0
303.15	0.7017	1039.1
303.15	0.7929	1042.6
303.15	0.9005	1047.9
303.15	0.9504	1050.7
308.15	0.0516	1019.2
308.15	0.1008	1016.7
308.15	0.1992	1013.3
308.15	0.2976	1011.7
308.15	0.3852	1011.2
308.15	0.4999	1012.1
308.15	0.5996	1014.0
308.15	0.7017	1016.9
308.15	0.7929	1020.5
308.15	0.9005	1025.5
308.15	0.9504	1028.4
313.15	0.0516	997.2
313.15	0.1008	994.8
313.15	0.1992	991.5
313.15	0.2976	989.7
313.15	0.3852	989.3
313.15	0.4999	990.1
313.15	0.5996	992.0
313.15	0.7017	994.9
313.15	0.7929	998.4
313.15	0.9005	1003.7
313.15	0.9504	1006.4

Sources

• Thermophysical Study of the n-Hexane or n-Heptane with 1- Chloropropane Systems