n-Hexane + Heptane

Datasets

P_c - Critical pressure, kPa (2)
ρ_l - Mass density, kg/m3 (2)
T_c - Critical temperature, K (2)

Critical pressure, kPa [ref]

Mole fraction of n-Hexane (1) - Liquid	Critical pressure, kPa - Liquid
0.1000	2796.00
0.2000	2831.00
0.3000	2866.00
0.4000	2903.00
0.5000	2937.00
0.6000	2967.00
0.7000	2996.00
0.8000	3021.00
0.9000	3030.00

Critical pressure, kPa [ref]

Mole fraction of n-Hexane (1) - Liquid	Critical pressure, kPa - Liquid
0.1000	2796.00
0.2000	2831.00
0.3000	2866.00
0.4000	2903.00
0.5000	2937.00
0.6000	2967.00
0.7000	2996.00
0.8000	3021.00
0.9000	3030.00

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of n-Hexane (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.1019	273.15	698.37
0.1019	278.15	694.22
0.1019	283.15	690.04
0.1019	288.15	685.84
0.1019	293.15	681.62
0.1019	298.15	677.38
0.1019	303.15	673.11
0.1019	308.15	668.81
0.1019	313.15	664.47
0.1019	318.15	660.11
0.1019	323.15	655.71
0.1019	328.15	651.27
0.1019	333.15	646.79
0.1019	338.15	642.28
0.1019	343.15	637.71
0.1019	348.15	633.1
0.1019	353.15	628.43
0.1019	358.15	623.71
0.1019	363.15	618.94
0.2003	273.15	696.77
0.2003	278.15	692.61
0.2003	283.15	688.42
0.2003	288.15	684.21
0.2003	293.15	679.97
0.2003	298.15	675.7
0.2003	303.15	671.42
0.2003	308.15	667.09
0.2003	313.15	662.74
0.2003	318.15	658.36
0.2003	323.15	653.93
0.2003	328.15	649.47
0.2003	333.15	644.97
0.2003	338.15	640.43
0.2003	343.15	635.84
0.2003	348.15	631.2
0.2003	353.15	626.5
0.2003	358.15	621.75
0.2003	363.15	616.94
0.3005	273.15	694.27
0.3005	278.15	690.08
0.3005	283.15	685.86
0.3005	288.15	681.62
0.3005	293.15	677.36
0.3005	298.15	673.06
0.3005	303.15	668.74
0.3005	308.15	664.39
0.3005	313.15	660.0
0.3005	318.15	655.58
0.3005	323.15	651.12
0.3005	328.15	646.62
0.3005	333.15	642.07
0.3005	338.15	637.49
0.3005	343.15	632.85
0.3005	348.15	628.16
0.3005	353.15	623.42
0.3005	358.15	618.61
0.3005	363.15	613.75
0.4007	273.15	692.25
0.4007	278.15	688.04
0.4007	283.15	683.8
0.4007	288.15	679.53
0.4007	293.15	675.24
0.4007	298.15	670.93
0.4007	303.15	666.58
0.4007	308.15	662.2
0.4007	313.15	657.78
0.4007	318.15	653.33
0.4007	323.15	648.84
0.4007	328.15	644.31
0.4007	333.15	639.73
0.4007	338.15	635.11
0.4007	343.15	630.44
0.4007	348.15	625.71
0.4007	353.15	620.92
0.4007	358.15	616.08
0.4007	363.15	611.16
0.5001	273.15	689.57
0.5001	278.15	685.35
0.5001	283.15	681.08
0.5001	288.15	676.79
0.5001	293.15	672.47
0.5001	298.15	668.12
0.5001	303.15	663.74
0.5001	308.15	659.32
0.5001	313.15	654.86
0.5001	318.15	650.35
0.5001	323.15	645.81
0.5001	328.15	641.22
0.5001	333.15	636.58
0.5001	338.15	631.89
0.5001	343.15	627.14
0.5001	348.15	622.33
0.5984	273.15	687.14
0.5984	278.15	682.88
0.5984	283.15	678.58
0.5984	288.15	674.26
0.5984	293.15	669.91
0.5984	298.15	665.53
0.5984	303.15	661.12
0.5984	308.15	656.67
0.5984	313.15	652.19
0.5984	318.15	647.66
0.5984	323.15	643.1
0.5984	328.15	638.48
0.5984	333.15	633.82
0.7002	273.15	684.81
0.7002	278.15	680.52
0.7002	283.15	676.2
0.7002	288.15	671.85
0.7002	293.15	667.47
0.7002	298.15	663.06
0.7002	303.15	658.62
0.7002	308.15	654.14
0.7002	313.15	649.62
0.7002	318.15	645.06
0.7002	323.15	640.45
0.7002	328.15	635.8
0.7002	333.15	631.24
0.7002	338.15	626.48
0.7002	343.15	621.67
0.7002	348.15	616.8
0.7995	273.15	682.14
0.7995	278.15	677.82
0.7995	283.15	673.47
0.7995	288.15	669.1
0.7995	293.15	664.69
0.7995	298.15	660.24
0.7995	303.15	655.77
0.7995	308.15	651.25
0.7995	313.15	646.69
0.7995	318.15	642.1
0.7995	323.15	637.45
0.7995	328.15	632.76
0.7995	333.15	628.01
0.7995	338.15	623.2
0.8974	273.15	679.66
0.8974	278.15	675.32
0.8974	283.15	670.94
0.8974	288.15	666.54
0.8974	293.15	662.1
0.8974	298.15	657.62
0.8974	303.15	653.12
0.8974	308.15	648.57
0.8974	313.15	643.98
0.8974	318.15	639.34
0.8974	323.15	634.65
0.8974	328.15	629.92
0.8974	333.15	625.13
0.8974	338.15	620.28

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of n-Hexane (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.1019	273.15	698.37
0.1019	278.15	694.22
0.1019	283.15	690.04
0.1019	288.15	685.84
0.1019	293.15	681.62
0.1019	298.15	677.38
0.1019	303.15	673.11
0.1019	308.15	668.81
0.1019	313.15	664.47
0.1019	318.15	660.11
0.1019	323.15	655.71
0.1019	328.15	651.27
0.1019	333.15	646.79
0.1019	338.15	642.28
0.1019	343.15	637.71
0.1019	348.15	633.1
0.1019	353.15	628.43
0.1019	358.15	623.71
0.1019	363.15	618.94
0.2003	273.15	696.77
0.2003	278.15	692.61
0.2003	283.15	688.42
0.2003	288.15	684.21
0.2003	293.15	679.97
0.2003	298.15	675.7
0.2003	303.15	671.42
0.2003	308.15	667.09
0.2003	313.15	662.74
0.2003	318.15	658.36
0.2003	323.15	653.93
0.2003	328.15	649.47
0.2003	333.15	644.97
0.2003	338.15	640.43
0.2003	343.15	635.84
0.2003	348.15	631.2
0.2003	353.15	626.5
0.2003	358.15	621.75
0.2003	363.15	616.94
0.3005	273.15	694.27
0.3005	278.15	690.08
0.3005	283.15	685.86
0.3005	288.15	681.62
0.3005	293.15	677.36
0.3005	298.15	673.06
0.3005	303.15	668.74
0.3005	308.15	664.39
0.3005	313.15	660.0
0.3005	318.15	655.58
0.3005	323.15	651.12
0.3005	328.15	646.62
0.3005	333.15	642.07
0.3005	338.15	637.49
0.3005	343.15	632.85
0.3005	348.15	628.16
0.3005	353.15	623.42
0.3005	358.15	618.61
0.3005	363.15	613.75
0.4007	273.15	692.25
0.4007	278.15	688.04
0.4007	283.15	683.8
0.4007	288.15	679.53
0.4007	293.15	675.24
0.4007	298.15	670.93
0.4007	303.15	666.58
0.4007	308.15	662.2
0.4007	313.15	657.78
0.4007	318.15	653.33
0.4007	323.15	648.84
0.4007	328.15	644.31
0.4007	333.15	639.73
0.4007	338.15	635.11
0.4007	343.15	630.44
0.4007	348.15	625.71
0.4007	353.15	620.92
0.4007	358.15	616.08
0.4007	363.15	611.16
0.5001	273.15	689.57
0.5001	278.15	685.35
0.5001	283.15	681.08
0.5001	288.15	676.79
0.5001	293.15	672.47
0.5001	298.15	668.12
0.5001	303.15	663.74
0.5001	308.15	659.32
0.5001	313.15	654.86
0.5001	318.15	650.35
0.5001	323.15	645.81
0.5001	328.15	641.22
0.5001	333.15	636.58
0.5001	338.15	631.89
0.5001	343.15	627.14
0.5001	348.15	622.33
0.5984	273.15	687.14
0.5984	278.15	682.88
0.5984	283.15	678.58
0.5984	288.15	674.26
0.5984	293.15	669.91
0.5984	298.15	665.53
0.5984	303.15	661.12
0.5984	308.15	656.67
0.5984	313.15	652.19
0.5984	318.15	647.66
0.5984	323.15	643.1
0.5984	328.15	638.48
0.5984	333.15	633.82
0.7002	273.15	684.81
0.7002	278.15	680.52
0.7002	283.15	676.2
0.7002	288.15	671.85
0.7002	293.15	667.47
0.7002	298.15	663.06
0.7002	303.15	658.62
0.7002	308.15	654.14
0.7002	313.15	649.62
0.7002	318.15	645.06
0.7002	323.15	640.45
0.7002	328.15	635.8
0.7002	333.15	631.24
0.7002	338.15	626.48
0.7002	343.15	621.67
0.7002	348.15	616.8
0.7995	273.15	682.14
0.7995	278.15	677.82
0.7995	283.15	673.47
0.7995	288.15	669.1
0.7995	293.15	664.69
0.7995	298.15	660.24
0.7995	303.15	655.77
0.7995	308.15	651.25
0.7995	313.15	646.69
0.7995	318.15	642.1
0.7995	323.15	637.45
0.7995	328.15	632.76
0.7995	333.15	628.01
0.7995	338.15	623.2
0.8974	273.15	679.66
0.8974	278.15	675.32
0.8974	283.15	670.94
0.8974	288.15	666.54
0.8974	293.15	662.1
0.8974	298.15	657.62
0.8974	303.15	653.12
0.8974	308.15	648.57
0.8974	313.15	643.98
0.8974	318.15	639.34
0.8974	323.15	634.65
0.8974	328.15	629.92
0.8974	333.15	625.13
0.8974	338.15	620.28

Critical temperature, K [ref]

Mole fraction of n-Hexane (1) - Liquid	Critical temperature, K - Liquid
0.1000	537.41
0.2000	534.58
0.3000	531.71
0.4000	528.64
0.5000	525.61
0.6000	522.15
0.7000	518.62
0.8000	515.02
0.9000	511.43

Critical temperature, K [ref]

Mole fraction of n-Hexane (1) - Liquid	Critical temperature, K - Liquid
0.1000	537.41
0.2000	534.58
0.3000	531.71
0.4000	528.64
0.5000	525.61
0.6000	522.15
0.7000	518.62
0.8000	515.02
0.9000	511.43

Sources

Experimental measurements and prediction of liquid densities for n-alkane mixtures
Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus

Mixture of n-Hexane + Heptane

Datasets

Critical pressure, kPa [ref]

Critical pressure, kPa [ref]

Mass density, kg/m3 [ref]

Mass density, kg/m3 [ref]

Critical temperature, K [ref]

Critical temperature, K [ref]

Sources