Datasets
-
Mass fraction (4)
-
η - Viscosity, Pa*s (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρl - Mass density, kg/m3 (6)
Mass fraction of Ethane (1)
[ref]
Operational condition: Temperature, K =
294.9 (Liquid mixture 1)
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Ethane (1) - Liquid mixture 1 |
4891.00 |
0.9710 |
6081.00 |
0.9230 |
7087.00 |
0.9070 |
8090.00 |
0.8860 |
9076.00 |
0.8630 |
10093.00 |
0.7910 |
Mass fraction of Ethane (1)
[ref]
Operational condition: Temperature, K =
294.9 (Liquid mixture 1)
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Ethane (1) - Liquid mixture 2 |
4891.00 |
0.4220 |
6081.00 |
0.4680 |
7087.00 |
0.5200 |
8090.00 |
0.5440 |
9076.00 |
0.5630 |
10093.00 |
0.6000 |
Mass fraction of Ethane (1)
[ref]
Operational condition: Temperature, K =
294.9 (Liquid mixture 1)
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Ethane (1) - Liquid mixture 1 |
4891.00 |
0.9710 |
6081.00 |
0.9230 |
7087.00 |
0.9070 |
8090.00 |
0.8860 |
9076.00 |
0.8630 |
10093.00 |
0.7910 |
Mass fraction of Ethane (1)
[ref]
Operational condition: Temperature, K =
294.9 (Liquid mixture 1)
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Ethane (1) - Liquid mixture 2 |
4891.00 |
0.4220 |
6081.00 |
0.4680 |
7087.00 |
0.5200 |
8090.00 |
0.5440 |
9076.00 |
0.5630 |
10093.00 |
0.6000 |
Viscosity, Pa*s
[ref]
Operational condition: Temperature, K =
294.9 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mass fraction of Ethane (1) - Liquid |
Viscosity, Pa*s - Liquid |
1196.00 |
0.0560 |
0.0005 |
2123.00 |
0.1200 |
0.0004 |
3130.00 |
0.2250 |
0.0003 |
Viscosity, Pa*s
[ref]
Operational condition: Temperature, K =
294.9 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mass fraction of Ethane (1) - Liquid |
Viscosity, Pa*s - Liquid |
1196.00 |
0.0560 |
0.0005 |
2123.00 |
0.1200 |
0.0004 |
3130.00 |
0.2250 |
0.0003 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
294.9 (Liquid)
Mass fraction of Ethane (1) - Gas |
Vapor or sublimation pressure, kPa - Liquid |
0.0560 |
1196.00 |
0.1200 |
2123.00 |
0.2250 |
3130.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
294.9 (Liquid)
Mass fraction of Ethane (1) - Gas |
Vapor or sublimation pressure, kPa - Liquid |
0.0560 |
1196.00 |
0.1200 |
2123.00 |
0.2250 |
3130.00 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
294.9 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mass fraction of Ethane (1) - Liquid |
Mass density, kg/m3 - Liquid |
1196.00 |
0.0560 |
750.0 |
2123.00 |
0.1200 |
720.0 |
3130.00 |
0.2250 |
671.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Ethane (1) - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 1 |
4891.00 |
0.9710 |
375.0 |
6081.00 |
0.9230 |
400.0 |
7087.00 |
0.9070 |
437.0 |
8090.00 |
0.8860 |
455.0 |
9076.00 |
0.8630 |
464.0 |
10093.00 |
0.7910 |
469.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Ethane (1) - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 2 |
4891.00 |
0.4220 |
590.0 |
6081.00 |
0.4680 |
564.0 |
7087.00 |
0.5200 |
550.0 |
8090.00 |
0.5440 |
532.0 |
9076.00 |
0.5630 |
528.0 |
10093.00 |
0.6000 |
523.0 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
294.9 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mass fraction of Ethane (1) - Liquid |
Mass density, kg/m3 - Liquid |
1196.00 |
0.0560 |
750.0 |
2123.00 |
0.1200 |
720.0 |
3130.00 |
0.2250 |
671.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Ethane (1) - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 1 |
4891.00 |
0.9710 |
375.0 |
6081.00 |
0.9230 |
400.0 |
7087.00 |
0.9070 |
437.0 |
8090.00 |
0.8860 |
455.0 |
9076.00 |
0.8630 |
464.0 |
10093.00 |
0.7910 |
469.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Ethane (1) - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 2 |
4891.00 |
0.4220 |
590.0 |
6081.00 |
0.4680 |
564.0 |
7087.00 |
0.5200 |
550.0 |
8090.00 |
0.5440 |
532.0 |
9076.00 |
0.5630 |
528.0 |
10093.00 |
0.6000 |
523.0 |
Sources