Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (6)
-
csound,fluid - Speed of Sound, m/s (2)
Mole fraction of Octane (2)
[ref]
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Temperature, K - Gas |
Mole fraction of Octane (2) - Gas |
0.1859 |
323.20 |
0.1278 |
0.3985 |
323.20 |
0.2756 |
0.5966 |
323.20 |
0.4301 |
0.8004 |
323.20 |
0.6588 |
0.2014 |
343.20 |
0.1451 |
0.3987 |
343.20 |
0.2871 |
0.5874 |
343.20 |
0.4397 |
0.7863 |
343.20 |
0.6451 |
0.1963 |
363.20 |
0.1498 |
0.4006 |
363.20 |
0.2971 |
0.5834 |
363.20 |
0.4583 |
0.7968 |
363.20 |
0.6743 |
Mole fraction of Octane (2)
[ref]
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Temperature, K - Gas |
Mole fraction of Octane (2) - Gas |
0.1859 |
323.20 |
0.1278 |
0.3985 |
323.20 |
0.2756 |
0.5966 |
323.20 |
0.4301 |
0.8004 |
323.20 |
0.6588 |
0.2014 |
343.20 |
0.1451 |
0.3987 |
343.20 |
0.2871 |
0.5874 |
343.20 |
0.4397 |
0.7863 |
343.20 |
0.6451 |
0.1963 |
363.20 |
0.1498 |
0.4006 |
363.20 |
0.2971 |
0.5834 |
363.20 |
0.4583 |
0.7968 |
363.20 |
0.6743 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1859 |
323.20 |
11.40 |
0.3985 |
323.20 |
10.50 |
0.5966 |
323.20 |
9.40 |
0.8004 |
323.20 |
8.10 |
0.2014 |
343.20 |
25.60 |
0.3987 |
343.20 |
23.50 |
0.5874 |
343.20 |
21.60 |
0.7863 |
343.20 |
19.00 |
0.1963 |
363.20 |
51.00 |
0.4006 |
363.20 |
47.70 |
0.5834 |
363.20 |
43.90 |
0.7968 |
363.20 |
39.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1859 |
323.20 |
11.40 |
0.3985 |
323.20 |
10.50 |
0.5966 |
323.20 |
9.40 |
0.8004 |
323.20 |
8.10 |
0.2014 |
343.20 |
25.60 |
0.3987 |
343.20 |
23.50 |
0.5874 |
343.20 |
21.60 |
0.7863 |
343.20 |
19.00 |
0.1963 |
363.20 |
51.00 |
0.4006 |
363.20 |
47.70 |
0.5834 |
363.20 |
43.90 |
0.7968 |
363.20 |
39.00 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Octane (2) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0000 |
1.4851 |
0.0542 |
1.4771 |
0.1022 |
1.4698 |
0.2014 |
1.4567 |
0.3037 |
1.4446 |
0.3965 |
1.4336 |
0.4983 |
1.4247 |
0.5986 |
1.4157 |
0.7016 |
1.4075 |
0.8007 |
1.4005 |
0.9020 |
1.3938 |
0.9493 |
1.3908 |
1.0000 |
1.3877 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Octane (2) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0000 |
1.4851 |
0.0542 |
1.4771 |
0.1022 |
1.4698 |
0.2014 |
1.4567 |
0.3037 |
1.4446 |
0.3965 |
1.4336 |
0.4983 |
1.4247 |
0.5986 |
1.4157 |
0.7016 |
1.4075 |
0.8007 |
1.4005 |
0.9020 |
1.3938 |
0.9493 |
1.3908 |
1.0000 |
1.3877 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Octane (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
862.29 |
298.15 |
0.0654 |
845.89 |
298.15 |
0.1283 |
831.23 |
298.15 |
0.1979 |
816.17 |
298.15 |
0.2524 |
805.13 |
298.15 |
0.3120 |
793.74 |
298.15 |
0.3931 |
779.27 |
298.15 |
0.4544 |
769.05 |
298.15 |
0.5409 |
755.59 |
298.15 |
0.6029 |
746.56 |
298.15 |
0.6717 |
737.09 |
298.15 |
0.7202 |
730.75 |
298.15 |
0.8064 |
720.08 |
298.15 |
0.8727 |
712.36 |
298.15 |
0.9312 |
705.88 |
298.15 |
1.0000 |
698.61 |
308.15 |
0.0000 |
852.86 |
308.15 |
0.0654 |
836.6 |
308.15 |
0.1283 |
822.06 |
308.15 |
0.1979 |
807.1 |
308.15 |
0.2524 |
796.14 |
308.15 |
0.3120 |
784.82 |
308.15 |
0.3931 |
770.46 |
308.15 |
0.4544 |
760.31 |
308.15 |
0.5409 |
746.93 |
308.15 |
0.6029 |
737.98 |
308.15 |
0.6717 |
728.58 |
308.15 |
0.7202 |
722.3 |
308.15 |
0.8064 |
711.7 |
308.15 |
0.8727 |
704.05 |
308.15 |
0.9312 |
697.62 |
308.15 |
1.0000 |
690.44 |
318.15 |
0.0000 |
843.6 |
318.15 |
0.0675 |
826.95 |
318.15 |
0.1229 |
814.22 |
318.15 |
0.2052 |
796.69 |
318.15 |
0.2613 |
785.56 |
318.15 |
0.3142 |
775.67 |
318.15 |
0.3980 |
761.0 |
318.15 |
0.4553 |
751.61 |
318.15 |
0.5388 |
738.82 |
318.15 |
0.6078 |
728.94 |
318.15 |
0.6679 |
720.81 |
318.15 |
0.7262 |
713.32 |
318.15 |
0.7985 |
704.51 |
318.15 |
0.8630 |
697.07 |
318.15 |
0.9143 |
691.43 |
318.15 |
1.0000 |
682.49 |
328.15 |
0.0000 |
834.29 |
328.15 |
0.0675 |
817.77 |
328.15 |
0.1229 |
805.12 |
328.15 |
0.2052 |
787.73 |
328.15 |
0.2613 |
776.68 |
328.15 |
0.3142 |
766.87 |
328.15 |
0.3980 |
752.32 |
328.15 |
0.4553 |
743.01 |
328.15 |
0.5388 |
730.32 |
328.15 |
0.6078 |
720.55 |
328.15 |
0.6679 |
712.48 |
328.15 |
0.7262 |
705.06 |
328.15 |
0.7985 |
696.33 |
328.15 |
0.8630 |
688.97 |
328.15 |
0.9143 |
683.39 |
328.15 |
1.0000 |
674.55 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Octane (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
848.0 |
0.0542 |
834.6 |
0.1022 |
823.4 |
0.2014 |
802.0 |
0.3037 |
782.0 |
0.3965 |
765.5 |
0.4983 |
749.1 |
0.5986 |
734.3 |
0.7016 |
720.5 |
0.8007 |
708.4 |
0.9020 |
696.6 |
0.9493 |
691.6 |
1.0000 |
686.3 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of Octane (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
862.17 |
0.0982 |
838.13 |
0.1977 |
816.31 |
0.2975 |
796.62 |
0.3983 |
778.64 |
0.5005 |
761.92 |
0.5988 |
747.35 |
0.6990 |
733.63 |
0.7966 |
721.31 |
0.8955 |
709.92 |
1.0000 |
698.6 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Octane (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
862.29 |
298.15 |
0.0654 |
845.89 |
298.15 |
0.1283 |
831.23 |
298.15 |
0.1979 |
816.17 |
298.15 |
0.2524 |
805.13 |
298.15 |
0.3120 |
793.74 |
298.15 |
0.3931 |
779.27 |
298.15 |
0.4544 |
769.05 |
298.15 |
0.5409 |
755.59 |
298.15 |
0.6029 |
746.56 |
298.15 |
0.6717 |
737.09 |
298.15 |
0.7202 |
730.75 |
298.15 |
0.8064 |
720.08 |
298.15 |
0.8727 |
712.36 |
298.15 |
0.9312 |
705.88 |
298.15 |
1.0000 |
698.61 |
308.15 |
0.0000 |
852.86 |
308.15 |
0.0654 |
836.6 |
308.15 |
0.1283 |
822.06 |
308.15 |
0.1979 |
807.1 |
308.15 |
0.2524 |
796.14 |
308.15 |
0.3120 |
784.82 |
308.15 |
0.3931 |
770.46 |
308.15 |
0.4544 |
760.31 |
308.15 |
0.5409 |
746.93 |
308.15 |
0.6029 |
737.98 |
308.15 |
0.6717 |
728.58 |
308.15 |
0.7202 |
722.3 |
308.15 |
0.8064 |
711.7 |
308.15 |
0.8727 |
704.05 |
308.15 |
0.9312 |
697.62 |
308.15 |
1.0000 |
690.44 |
318.15 |
0.0000 |
843.6 |
318.15 |
0.0675 |
826.95 |
318.15 |
0.1229 |
814.22 |
318.15 |
0.2052 |
796.69 |
318.15 |
0.2613 |
785.56 |
318.15 |
0.3142 |
775.67 |
318.15 |
0.3980 |
761.0 |
318.15 |
0.4553 |
751.61 |
318.15 |
0.5388 |
738.82 |
318.15 |
0.6078 |
728.94 |
318.15 |
0.6679 |
720.81 |
318.15 |
0.7262 |
713.32 |
318.15 |
0.7985 |
704.51 |
318.15 |
0.8630 |
697.07 |
318.15 |
0.9143 |
691.43 |
318.15 |
1.0000 |
682.49 |
328.15 |
0.0000 |
834.29 |
328.15 |
0.0675 |
817.77 |
328.15 |
0.1229 |
805.12 |
328.15 |
0.2052 |
787.73 |
328.15 |
0.2613 |
776.68 |
328.15 |
0.3142 |
766.87 |
328.15 |
0.3980 |
752.32 |
328.15 |
0.4553 |
743.01 |
328.15 |
0.5388 |
730.32 |
328.15 |
0.6078 |
720.55 |
328.15 |
0.6679 |
712.48 |
328.15 |
0.7262 |
705.06 |
328.15 |
0.7985 |
696.33 |
328.15 |
0.8630 |
688.97 |
328.15 |
0.9143 |
683.39 |
328.15 |
1.0000 |
674.55 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Octane (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
848.0 |
0.0542 |
834.6 |
0.1022 |
823.4 |
0.2014 |
802.0 |
0.3037 |
782.0 |
0.3965 |
765.5 |
0.4983 |
749.1 |
0.5986 |
734.3 |
0.7016 |
720.5 |
0.8007 |
708.4 |
0.9020 |
696.6 |
0.9493 |
691.6 |
1.0000 |
686.3 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of Octane (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
862.17 |
0.0982 |
838.13 |
0.1977 |
816.31 |
0.2975 |
796.62 |
0.3983 |
778.64 |
0.5005 |
761.92 |
0.5988 |
747.35 |
0.6990 |
733.63 |
0.7966 |
721.31 |
0.8955 |
709.92 |
1.0000 |
698.6 |
Speed of sound, m/s
[ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Octane (2) - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
1240.7 |
0.0542 |
1226.2 |
0.1022 |
1214.8 |
0.2014 |
1194.1 |
0.3037 |
1176.2 |
0.3965 |
1162.3 |
0.4983 |
1149.7 |
0.5986 |
1139.1 |
0.7016 |
1130.0 |
0.8007 |
1122.5 |
0.9020 |
1116.1 |
0.9493 |
1113.1 |
1.0000 |
1110.6 |
Speed of sound, m/s
[ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Octane (2) - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
1240.7 |
0.0542 |
1226.2 |
0.1022 |
1214.8 |
0.2014 |
1194.1 |
0.3037 |
1176.2 |
0.3965 |
1162.3 |
0.4983 |
1149.7 |
0.5986 |
1139.1 |
0.7016 |
1130.0 |
0.8007 |
1122.5 |
0.9020 |
1116.1 |
0.9493 |
1113.1 |
1.0000 |
1110.6 |
Sources
-
Excess molar volumes of (octane + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures between (298.15 and 328.15) K
-
Experimental densities, refractive indices, and speeds of sound of 12 binary mixtures containing alkanes and aromatic compounds at T = 313.15 K
-
Separation of toluene from alkanes using 1-ethyl-3-methylpyridinium ethylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
-
Vapor Liquid Equilibria for (n-Hexane, n-Octane, Cyclohexane, or 2,3-Dimethylpentane) + Toluene + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} Mixed Ionic Liquids