Mixture of Ethane + Octadecane
Datasets
-
η - Viscosity, Pa*s (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρl - Mass density, kg/m3 (2)
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane (1) - Liquid |
Viscosity, Pa*s - Liquid |
323.10 |
0.2700 |
0.0016 |
323.10 |
0.4150 |
0.0011 |
323.10 |
0.7890 |
0.0003 |
323.10 |
0.8440 |
0.0002 |
323.30 |
0.5460 |
0.0008 |
323.30 |
0.6540 |
0.0006 |
372.80 |
0.1270 |
0.0009 |
372.80 |
0.2980 |
0.0007 |
372.80 |
0.3720 |
0.0006 |
372.80 |
0.4740 |
0.0005 |
372.80 |
0.5360 |
0.0005 |
372.80 |
0.5990 |
0.0004 |
372.80 |
0.6660 |
0.0003 |
372.80 |
0.7010 |
0.0003 |
422.50 |
0.5470 |
0.0003 |
422.50 |
0.5880 |
0.0003 |
422.60 |
0.0960 |
0.0006 |
422.60 |
0.1940 |
0.0005 |
422.60 |
0.2960 |
0.0004 |
422.60 |
0.3650 |
0.0004 |
422.60 |
0.4270 |
0.0004 |
422.60 |
0.4770 |
0.0003 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane (1) - Liquid |
Viscosity, Pa*s - Liquid |
323.10 |
0.2700 |
0.0016 |
323.10 |
0.4150 |
0.0011 |
323.10 |
0.7890 |
0.0003 |
323.10 |
0.8440 |
0.0002 |
323.30 |
0.5460 |
0.0008 |
323.30 |
0.6540 |
0.0006 |
372.80 |
0.1270 |
0.0009 |
372.80 |
0.2980 |
0.0007 |
372.80 |
0.3720 |
0.0006 |
372.80 |
0.4740 |
0.0005 |
372.80 |
0.5360 |
0.0005 |
372.80 |
0.5990 |
0.0004 |
372.80 |
0.6660 |
0.0003 |
372.80 |
0.7010 |
0.0003 |
422.50 |
0.5470 |
0.0003 |
422.50 |
0.5880 |
0.0003 |
422.60 |
0.0960 |
0.0006 |
422.60 |
0.1940 |
0.0005 |
422.60 |
0.2960 |
0.0004 |
422.60 |
0.3650 |
0.0004 |
422.60 |
0.4270 |
0.0004 |
422.60 |
0.4770 |
0.0003 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
323.10 |
0.2700 |
1150.00 |
323.10 |
0.4150 |
1950.00 |
323.10 |
0.7890 |
5230.00 |
323.10 |
0.8440 |
5890.00 |
323.30 |
0.5460 |
3010.00 |
323.30 |
0.6540 |
3970.00 |
372.80 |
0.1270 |
940.00 |
372.80 |
0.2980 |
2180.00 |
372.80 |
0.3720 |
2920.00 |
372.80 |
0.4740 |
4080.00 |
372.80 |
0.5360 |
4940.00 |
372.80 |
0.5990 |
5980.00 |
372.80 |
0.6660 |
7120.00 |
372.80 |
0.7010 |
7980.00 |
422.50 |
0.5470 |
7160.00 |
422.50 |
0.5880 |
8170.00 |
422.60 |
0.0960 |
950.00 |
422.60 |
0.1940 |
1930.00 |
422.60 |
0.2960 |
3060.00 |
422.60 |
0.3650 |
3970.00 |
422.60 |
0.4270 |
5000.00 |
422.60 |
0.4770 |
5940.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
323.10 |
0.2700 |
1150.00 |
323.10 |
0.4150 |
1950.00 |
323.10 |
0.7890 |
5230.00 |
323.10 |
0.8440 |
5890.00 |
323.30 |
0.5460 |
3010.00 |
323.30 |
0.6540 |
3970.00 |
372.80 |
0.1270 |
940.00 |
372.80 |
0.2980 |
2180.00 |
372.80 |
0.3720 |
2920.00 |
372.80 |
0.4740 |
4080.00 |
372.80 |
0.5360 |
4940.00 |
372.80 |
0.5990 |
5980.00 |
372.80 |
0.6660 |
7120.00 |
372.80 |
0.7010 |
7980.00 |
422.50 |
0.5470 |
7160.00 |
422.50 |
0.5880 |
8170.00 |
422.60 |
0.0960 |
950.00 |
422.60 |
0.1940 |
1930.00 |
422.60 |
0.2960 |
3060.00 |
422.60 |
0.3650 |
3970.00 |
422.60 |
0.4270 |
5000.00 |
422.60 |
0.4770 |
5940.00 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane (1) - Liquid |
Mass density, kg/m3 - Liquid |
323.10 |
0.2700 |
732.0 |
323.10 |
0.4150 |
715.0 |
323.10 |
0.7890 |
606.0 |
323.10 |
0.8440 |
572.0 |
323.30 |
0.5460 |
691.0 |
323.30 |
0.6540 |
662.0 |
372.80 |
0.1270 |
719.0 |
372.80 |
0.2980 |
703.0 |
372.80 |
0.3720 |
692.0 |
372.80 |
0.4740 |
676.0 |
372.80 |
0.5360 |
664.0 |
372.80 |
0.5990 |
648.0 |
372.80 |
0.6660 |
628.0 |
372.80 |
0.7010 |
614.0 |
422.50 |
0.5470 |
624.0 |
422.50 |
0.5880 |
613.0 |
422.60 |
0.0960 |
688.0 |
422.60 |
0.1940 |
679.0 |
422.60 |
0.2960 |
667.0 |
422.60 |
0.3650 |
659.0 |
422.60 |
0.4270 |
648.0 |
422.60 |
0.4770 |
640.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane (1) - Liquid |
Mass density, kg/m3 - Liquid |
323.10 |
0.2700 |
732.0 |
323.10 |
0.4150 |
715.0 |
323.10 |
0.7890 |
606.0 |
323.10 |
0.8440 |
572.0 |
323.30 |
0.5460 |
691.0 |
323.30 |
0.6540 |
662.0 |
372.80 |
0.1270 |
719.0 |
372.80 |
0.2980 |
703.0 |
372.80 |
0.3720 |
692.0 |
372.80 |
0.4740 |
676.0 |
372.80 |
0.5360 |
664.0 |
372.80 |
0.5990 |
648.0 |
372.80 |
0.6660 |
628.0 |
372.80 |
0.7010 |
614.0 |
422.50 |
0.5470 |
624.0 |
422.50 |
0.5880 |
613.0 |
422.60 |
0.0960 |
688.0 |
422.60 |
0.1940 |
679.0 |
422.60 |
0.2960 |
667.0 |
422.60 |
0.3650 |
659.0 |
422.60 |
0.4270 |
648.0 |
422.60 |
0.4770 |
640.0 |
Sources