Datasets
-
Mole fraction (6)
-
Pvap - Vapor or sublimation pressure, kPa (4)
-
ρl - Mass density, kg/m3 (2)
Mole fraction of Methane (2)
[ref]
Operational condition: Temperature, K =
310.9 (Liquid)
Pressure, kPa - Liquid |
Mole fraction of Methane (2) - Liquid |
2150.00 |
0.0985 |
4500.00 |
0.1921 |
6000.00 |
0.2540 |
Mole fraction of n-Hexane (1)
[ref]
Fixed |
Measured |
Mole fraction of Methane (2) - Liquid |
Temperature, K - Gas |
Mole fraction of n-Hexane (1) - Gas |
0.1120 |
303.15 |
0.0168 |
0.1220 |
318.15 |
0.0283 |
0.1230 |
333.15 |
0.0350 |
0.1360 |
288.15 |
0.0097 |
0.1420 |
273.15 |
0.0037 |
0.1520 |
253.15 |
0.0033 |
0.1820 |
233.15 |
0.0009 |
0.1960 |
333.15 |
0.0289 |
0.2140 |
203.15 |
0.0006 |
0.2210 |
288.15 |
0.0126 |
0.2280 |
318.15 |
0.0228 |
0.2330 |
273.15 |
0.0039 |
0.2520 |
213.15 |
0.0004 |
0.2590 |
253.15 |
0.0020 |
0.2670 |
303.15 |
0.0199 |
0.2950 |
333.15 |
0.0377 |
0.2990 |
288.15 |
0.0137 |
0.3060 |
273.15 |
0.0048 |
0.3140 |
233.15 |
0.0011 |
0.3150 |
273.15 |
0.0042 |
0.3230 |
318.15 |
0.0244 |
0.3520 |
193.15 |
0.0002 |
0.3530 |
303.15 |
0.0182 |
0.3610 |
253.15 |
0.0028 |
0.3820 |
203.15 |
0.0005 |
0.3860 |
333.15 |
0.0375 |
0.4000 |
288.15 |
0.0130 |
0.4010 |
273.15 |
0.0056 |
0.4130 |
183.15 |
0.0002 |
0.4150 |
213.15 |
0.0007 |
0.4150 |
233.15 |
0.0018 |
0.4290 |
318.15 |
0.0321 |
0.4450 |
303.15 |
0.0229 |
0.4770 |
253.15 |
0.0056 |
0.4980 |
273.15 |
0.0109 |
0.5020 |
333.15 |
0.0390 |
0.5160 |
288.15 |
0.0222 |
0.5170 |
233.15 |
0.0037 |
0.5190 |
193.15 |
0.0003 |
0.5290 |
318.15 |
0.0217 |
0.5350 |
193.15 |
0.0004 |
0.5460 |
203.15 |
0.0005 |
0.5460 |
303.15 |
0.0170 |
0.5520 |
183.15 |
0.0003 |
0.5750 |
253.15 |
0.0057 |
0.5920 |
213.15 |
0.0017 |
0.6110 |
273.15 |
0.0270 |
0.6470 |
233.15 |
0.0105 |
0.6770 |
203.15 |
0.0015 |
0.6930 |
183.15 |
0.0002 |
0.6980 |
183.15 |
0.0009 |
0.7070 |
193.15 |
0.0021 |
0.7140 |
193.15 |
0.0009 |
0.9550 |
183.15 |
0.0002 |
0.9590 |
233.15 |
0.0250 |
Mole fraction of Methane (2)
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Pressure, kPa - Liquid |
Mole fraction of Methane (2) - Liquid |
2050.00 |
0.0982 |
5050.00 |
0.2283 |
8100.00 |
0.3451 |
Mole fraction of Methane (2)
[ref]
Operational condition: Temperature, K =
310.9 (Liquid)
Pressure, kPa - Liquid |
Mole fraction of Methane (2) - Liquid |
2150.00 |
0.0985 |
4500.00 |
0.1921 |
6000.00 |
0.2540 |
Mole fraction of n-Hexane (1)
[ref]
Fixed |
Measured |
Mole fraction of Methane (2) - Liquid |
Temperature, K - Gas |
Mole fraction of n-Hexane (1) - Gas |
0.1120 |
303.15 |
0.0168 |
0.1220 |
318.15 |
0.0283 |
0.1230 |
333.15 |
0.0350 |
0.1360 |
288.15 |
0.0097 |
0.1420 |
273.15 |
0.0037 |
0.1520 |
253.15 |
0.0033 |
0.1820 |
233.15 |
0.0009 |
0.1960 |
333.15 |
0.0289 |
0.2140 |
203.15 |
0.0006 |
0.2210 |
288.15 |
0.0126 |
0.2280 |
318.15 |
0.0228 |
0.2330 |
273.15 |
0.0039 |
0.2520 |
213.15 |
0.0004 |
0.2590 |
253.15 |
0.0020 |
0.2670 |
303.15 |
0.0199 |
0.2950 |
333.15 |
0.0377 |
0.2990 |
288.15 |
0.0137 |
0.3060 |
273.15 |
0.0048 |
0.3140 |
233.15 |
0.0011 |
0.3150 |
273.15 |
0.0042 |
0.3230 |
318.15 |
0.0244 |
0.3520 |
193.15 |
0.0002 |
0.3530 |
303.15 |
0.0182 |
0.3610 |
253.15 |
0.0028 |
0.3820 |
203.15 |
0.0005 |
0.3860 |
333.15 |
0.0375 |
0.4000 |
288.15 |
0.0130 |
0.4010 |
273.15 |
0.0056 |
0.4130 |
183.15 |
0.0002 |
0.4150 |
213.15 |
0.0007 |
0.4150 |
233.15 |
0.0018 |
0.4290 |
318.15 |
0.0321 |
0.4450 |
303.15 |
0.0229 |
0.4770 |
253.15 |
0.0056 |
0.4980 |
273.15 |
0.0109 |
0.5020 |
333.15 |
0.0390 |
0.5160 |
288.15 |
0.0222 |
0.5170 |
233.15 |
0.0037 |
0.5190 |
193.15 |
0.0003 |
0.5290 |
318.15 |
0.0217 |
0.5350 |
193.15 |
0.0004 |
0.5460 |
203.15 |
0.0005 |
0.5460 |
303.15 |
0.0170 |
0.5520 |
183.15 |
0.0003 |
0.5750 |
253.15 |
0.0057 |
0.5920 |
213.15 |
0.0017 |
0.6110 |
273.15 |
0.0270 |
0.6470 |
233.15 |
0.0105 |
0.6770 |
203.15 |
0.0015 |
0.6930 |
183.15 |
0.0002 |
0.6980 |
183.15 |
0.0009 |
0.7070 |
193.15 |
0.0021 |
0.7140 |
193.15 |
0.0009 |
0.9550 |
183.15 |
0.0002 |
0.9590 |
233.15 |
0.0250 |
Mole fraction of Methane (2)
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Pressure, kPa - Liquid |
Mole fraction of Methane (2) - Liquid |
2050.00 |
0.0982 |
5050.00 |
0.2283 |
8100.00 |
0.3451 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Molality, mol/kg of Methane (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
2.157 |
273.10 |
2850.00 |
2.812 |
273.10 |
3620.00 |
3.805 |
273.10 |
4700.00 |
4.686 |
273.10 |
5670.00 |
6.031 |
273.10 |
6920.00 |
7.195 |
273.10 |
7900.00 |
8.724 |
273.10 |
9190.00 |
1.717 |
283.15 |
2500.00 |
2.568 |
283.15 |
3570.00 |
3.533 |
283.15 |
4740.00 |
4.499 |
283.15 |
5840.00 |
5.615 |
283.15 |
7010.00 |
7.345 |
283.15 |
8560.00 |
1.513 |
293.15 |
2360.00 |
2.229 |
293.15 |
3340.00 |
3.042 |
293.15 |
4410.00 |
4.008 |
293.15 |
5620.00 |
5.098 |
293.15 |
6860.00 |
6.638 |
293.15 |
8400.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Methane (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1120 |
303.15 |
2070.00 |
0.1220 |
318.15 |
2430.00 |
0.1230 |
333.15 |
2630.00 |
0.1360 |
288.15 |
2350.00 |
0.1420 |
273.15 |
2290.00 |
0.1520 |
253.15 |
2040.00 |
0.1820 |
233.15 |
1980.00 |
0.1960 |
333.15 |
4570.00 |
0.2140 |
203.15 |
1430.00 |
0.2210 |
288.15 |
4200.00 |
0.2280 |
318.15 |
5110.00 |
0.2330 |
273.15 |
4190.00 |
0.2520 |
213.15 |
2160.00 |
0.2590 |
253.15 |
3970.00 |
0.2670 |
303.15 |
5870.00 |
0.2950 |
333.15 |
7370.00 |
0.2990 |
288.15 |
6220.00 |
0.3060 |
273.15 |
6030.00 |
0.3140 |
233.15 |
4060.00 |
0.3150 |
273.15 |
6110.00 |
0.3230 |
318.15 |
7750.00 |
0.3520 |
193.15 |
2060.00 |
0.3530 |
303.15 |
8390.00 |
0.3610 |
253.15 |
6150.00 |
0.3820 |
203.15 |
3030.00 |
0.3860 |
333.15 |
10150.00 |
0.4000 |
288.15 |
8930.00 |
0.4010 |
273.15 |
8130.00 |
0.4130 |
183.15 |
1860.00 |
0.4150 |
213.15 |
4080.00 |
0.4150 |
233.15 |
5910.00 |
0.4290 |
318.15 |
11180.00 |
0.4450 |
303.15 |
11070.00 |
0.4770 |
253.15 |
9130.00 |
0.4980 |
273.15 |
10850.00 |
0.5020 |
333.15 |
13770.00 |
0.5160 |
288.15 |
12320.00 |
0.5170 |
233.15 |
7990.00 |
0.5190 |
193.15 |
3260.00 |
0.5290 |
318.15 |
14210.00 |
0.5350 |
193.15 |
3390.00 |
0.5460 |
203.15 |
4590.00 |
0.5460 |
303.15 |
14190.00 |
0.5520 |
183.15 |
2510.00 |
0.5750 |
253.15 |
11870.00 |
0.5920 |
213.15 |
6400.00 |
0.6110 |
273.15 |
14230.00 |
0.6470 |
233.15 |
10360.00 |
0.6770 |
203.15 |
6130.00 |
0.6930 |
183.15 |
3030.00 |
0.6980 |
183.15 |
3040.00 |
0.7070 |
193.15 |
4940.00 |
0.7140 |
193.15 |
4880.00 |
0.9550 |
183.15 |
3310.00 |
0.9590 |
233.15 |
12870.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Molality, mol/kg of Methane (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
2.157 |
273.10 |
2850.00 |
2.812 |
273.10 |
3620.00 |
3.805 |
273.10 |
4700.00 |
4.686 |
273.10 |
5670.00 |
6.031 |
273.10 |
6920.00 |
7.195 |
273.10 |
7900.00 |
8.724 |
273.10 |
9190.00 |
1.717 |
283.15 |
2500.00 |
2.568 |
283.15 |
3570.00 |
3.533 |
283.15 |
4740.00 |
4.499 |
283.15 |
5840.00 |
5.615 |
283.15 |
7010.00 |
7.345 |
283.15 |
8560.00 |
1.513 |
293.15 |
2360.00 |
2.229 |
293.15 |
3340.00 |
3.042 |
293.15 |
4410.00 |
4.008 |
293.15 |
5620.00 |
5.098 |
293.15 |
6860.00 |
6.638 |
293.15 |
8400.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Methane (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1120 |
303.15 |
2070.00 |
0.1220 |
318.15 |
2430.00 |
0.1230 |
333.15 |
2630.00 |
0.1360 |
288.15 |
2350.00 |
0.1420 |
273.15 |
2290.00 |
0.1520 |
253.15 |
2040.00 |
0.1820 |
233.15 |
1980.00 |
0.1960 |
333.15 |
4570.00 |
0.2140 |
203.15 |
1430.00 |
0.2210 |
288.15 |
4200.00 |
0.2280 |
318.15 |
5110.00 |
0.2330 |
273.15 |
4190.00 |
0.2520 |
213.15 |
2160.00 |
0.2590 |
253.15 |
3970.00 |
0.2670 |
303.15 |
5870.00 |
0.2950 |
333.15 |
7370.00 |
0.2990 |
288.15 |
6220.00 |
0.3060 |
273.15 |
6030.00 |
0.3140 |
233.15 |
4060.00 |
0.3150 |
273.15 |
6110.00 |
0.3230 |
318.15 |
7750.00 |
0.3520 |
193.15 |
2060.00 |
0.3530 |
303.15 |
8390.00 |
0.3610 |
253.15 |
6150.00 |
0.3820 |
203.15 |
3030.00 |
0.3860 |
333.15 |
10150.00 |
0.4000 |
288.15 |
8930.00 |
0.4010 |
273.15 |
8130.00 |
0.4130 |
183.15 |
1860.00 |
0.4150 |
213.15 |
4080.00 |
0.4150 |
233.15 |
5910.00 |
0.4290 |
318.15 |
11180.00 |
0.4450 |
303.15 |
11070.00 |
0.4770 |
253.15 |
9130.00 |
0.4980 |
273.15 |
10850.00 |
0.5020 |
333.15 |
13770.00 |
0.5160 |
288.15 |
12320.00 |
0.5170 |
233.15 |
7990.00 |
0.5190 |
193.15 |
3260.00 |
0.5290 |
318.15 |
14210.00 |
0.5350 |
193.15 |
3390.00 |
0.5460 |
203.15 |
4590.00 |
0.5460 |
303.15 |
14190.00 |
0.5520 |
183.15 |
2510.00 |
0.5750 |
253.15 |
11870.00 |
0.5920 |
213.15 |
6400.00 |
0.6110 |
273.15 |
14230.00 |
0.6470 |
233.15 |
10360.00 |
0.6770 |
203.15 |
6130.00 |
0.6930 |
183.15 |
3030.00 |
0.6980 |
183.15 |
3040.00 |
0.7070 |
193.15 |
4940.00 |
0.7140 |
193.15 |
4880.00 |
0.9550 |
183.15 |
3310.00 |
0.9590 |
233.15 |
12870.00 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Molality, mol/kg of Methane (2) - Liquid |
Mass density, kg/m3 - Liquid |
273.10 |
2850.00 |
2.157 |
655.0 |
273.10 |
3620.00 |
2.812 |
648.0 |
273.10 |
4700.00 |
3.805 |
638.0 |
273.10 |
5670.00 |
4.686 |
628.0 |
273.10 |
6920.00 |
6.031 |
616.0 |
273.10 |
7900.00 |
7.195 |
604.0 |
273.10 |
9190.00 |
8.724 |
596.0 |
283.15 |
2500.00 |
1.717 |
650.0 |
283.15 |
3570.00 |
2.568 |
640.0 |
283.15 |
4740.00 |
3.533 |
632.0 |
283.15 |
5840.00 |
4.499 |
620.0 |
283.15 |
7010.00 |
5.615 |
610.0 |
283.15 |
8560.00 |
7.345 |
594.0 |
293.15 |
2360.00 |
1.513 |
643.0 |
293.15 |
3340.00 |
2.229 |
635.0 |
293.15 |
4410.00 |
3.042 |
627.0 |
293.15 |
5620.00 |
4.008 |
615.0 |
293.15 |
6860.00 |
5.098 |
604.0 |
293.15 |
8400.00 |
6.638 |
590.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Molality, mol/kg of Methane (2) - Liquid |
Mass density, kg/m3 - Liquid |
273.10 |
2850.00 |
2.157 |
655.0 |
273.10 |
3620.00 |
2.812 |
648.0 |
273.10 |
4700.00 |
3.805 |
638.0 |
273.10 |
5670.00 |
4.686 |
628.0 |
273.10 |
6920.00 |
6.031 |
616.0 |
273.10 |
7900.00 |
7.195 |
604.0 |
273.10 |
9190.00 |
8.724 |
596.0 |
283.15 |
2500.00 |
1.717 |
650.0 |
283.15 |
3570.00 |
2.568 |
640.0 |
283.15 |
4740.00 |
3.533 |
632.0 |
283.15 |
5840.00 |
4.499 |
620.0 |
283.15 |
7010.00 |
5.615 |
610.0 |
283.15 |
8560.00 |
7.345 |
594.0 |
293.15 |
2360.00 |
1.513 |
643.0 |
293.15 |
3340.00 |
2.229 |
635.0 |
293.15 |
4410.00 |
3.042 |
627.0 |
293.15 |
5620.00 |
4.008 |
615.0 |
293.15 |
6860.00 |
5.098 |
604.0 |
293.15 |
8400.00 |
6.638 |
590.0 |
Sources