Mixture of Ethane, hexafluoro- + Cyclohexane, methyl-
Datasets
-
Mole fraction (4)
-
Pvap - Vapor or sublimation pressure, kPa (4)
Mole fraction of Ethane, hexafluoro- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane, hexafluoro- (1) - Liquid mixture 1 |
Mole fraction of Ethane, hexafluoro- (1) - Gas |
293.11 |
0.0300 |
0.9740 |
293.10 |
0.0380 |
0.9820 |
293.10 |
0.0460 |
0.9800 |
293.10 |
0.0610 |
0.9850 |
293.10 |
0.0740 |
0.9840 |
293.12 |
0.0880 |
0.9830 |
293.11 |
0.1030 |
0.9870 |
293.11 |
0.1020 |
0.9920 |
303.11 |
0.0280 |
0.9420 |
303.11 |
0.0370 |
0.9710 |
303.11 |
0.0410 |
0.9780 |
303.11 |
0.0520 |
0.9750 |
303.10 |
0.0650 |
0.9810 |
303.11 |
0.0750 |
0.9780 |
303.12 |
0.0860 |
0.9780 |
303.12 |
0.1000 |
0.9820 |
303.12 |
0.1070 |
0.9830 |
303.12 |
0.1180 |
0.9770 |
303.12 |
0.1210 |
0.9710 |
303.12 |
0.1230 |
0.9600 |
313.14 |
0.0290 |
0.9710 |
313.14 |
0.0380 |
0.9750 |
313.15 |
0.0450 |
0.9760 |
313.14 |
0.0640 |
0.9780 |
313.13 |
0.0780 |
0.9820 |
313.14 |
0.0930 |
0.9730 |
313.13 |
0.1020 |
0.9790 |
313.14 |
0.1120 |
0.9760 |
313.13 |
0.1240 |
0.9760 |
313.13 |
0.1280 |
0.9760 |
313.12 |
0.1310 |
0.9770 |
313.12 |
0.1340 |
0.9660 |
Mole fraction of Ethane, hexafluoro- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Mole fraction of Ethane, hexafluoro- (1) - Liquid mixture 2 |
Mole fraction of Ethane, hexafluoro- (1) - Gas |
293.11 |
0.9250 |
0.9920 |
293.11 |
0.9410 |
0.9950 |
293.10 |
0.9820 |
0.9940 |
293.11 |
0.9940 |
0.9980 |
Mole fraction of Ethane, hexafluoro- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane, hexafluoro- (1) - Liquid mixture 1 |
Mole fraction of Ethane, hexafluoro- (1) - Gas |
293.11 |
0.0300 |
0.9740 |
293.10 |
0.0380 |
0.9820 |
293.10 |
0.0460 |
0.9800 |
293.10 |
0.0610 |
0.9850 |
293.10 |
0.0740 |
0.9840 |
293.12 |
0.0880 |
0.9830 |
293.11 |
0.1030 |
0.9870 |
293.11 |
0.1020 |
0.9920 |
303.11 |
0.0280 |
0.9420 |
303.11 |
0.0370 |
0.9710 |
303.11 |
0.0410 |
0.9780 |
303.11 |
0.0520 |
0.9750 |
303.10 |
0.0650 |
0.9810 |
303.11 |
0.0750 |
0.9780 |
303.12 |
0.0860 |
0.9780 |
303.12 |
0.1000 |
0.9820 |
303.12 |
0.1070 |
0.9830 |
303.12 |
0.1180 |
0.9770 |
303.12 |
0.1210 |
0.9710 |
303.12 |
0.1230 |
0.9600 |
313.14 |
0.0290 |
0.9710 |
313.14 |
0.0380 |
0.9750 |
313.15 |
0.0450 |
0.9760 |
313.14 |
0.0640 |
0.9780 |
313.13 |
0.0780 |
0.9820 |
313.14 |
0.0930 |
0.9730 |
313.13 |
0.1020 |
0.9790 |
313.14 |
0.1120 |
0.9760 |
313.13 |
0.1240 |
0.9760 |
313.13 |
0.1280 |
0.9760 |
313.12 |
0.1310 |
0.9770 |
313.12 |
0.1340 |
0.9660 |
Mole fraction of Ethane, hexafluoro- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Mole fraction of Ethane, hexafluoro- (1) - Liquid mixture 2 |
Mole fraction of Ethane, hexafluoro- (1) - Gas |
293.11 |
0.9250 |
0.9920 |
293.11 |
0.9410 |
0.9950 |
293.10 |
0.9820 |
0.9940 |
293.11 |
0.9940 |
0.9980 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane, hexafluoro- (1) - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
293.11 |
0.0300 |
941.00 |
293.10 |
0.0380 |
1240.00 |
293.10 |
0.0460 |
1517.00 |
293.10 |
0.0610 |
1871.00 |
293.10 |
0.0740 |
2164.00 |
293.12 |
0.0880 |
2464.00 |
293.11 |
0.1030 |
2737.00 |
293.11 |
0.1020 |
2778.00 |
303.11 |
0.0280 |
912.00 |
303.11 |
0.0370 |
1129.00 |
303.11 |
0.0410 |
1342.00 |
303.11 |
0.0520 |
1667.00 |
303.10 |
0.0650 |
1990.00 |
303.11 |
0.0750 |
2337.00 |
303.12 |
0.0860 |
2651.00 |
303.12 |
0.1000 |
2966.00 |
303.12 |
0.1070 |
3212.00 |
303.12 |
0.1180 |
3384.00 |
303.12 |
0.1210 |
3451.00 |
303.12 |
0.1230 |
3486.00 |
313.14 |
0.0290 |
962.00 |
313.14 |
0.0380 |
1264.00 |
313.15 |
0.0450 |
1516.00 |
313.14 |
0.0640 |
1994.00 |
313.13 |
0.0780 |
2416.00 |
313.14 |
0.0930 |
2807.00 |
313.13 |
0.1020 |
3057.00 |
313.14 |
0.1120 |
3361.00 |
313.13 |
0.1240 |
3656.00 |
313.13 |
0.1280 |
3819.00 |
313.12 |
0.1310 |
3972.00 |
313.12 |
0.1340 |
4220.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Mole fraction of Ethane, hexafluoro- (1) - Liquid mixture 2 |
Vapor or sublimation pressure, kPa - Liquid mixture 2 |
293.11 |
0.9250 |
2778.00 |
293.11 |
0.9410 |
2830.00 |
293.10 |
0.9820 |
2928.00 |
293.11 |
0.9940 |
3010.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane, hexafluoro- (1) - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
293.11 |
0.0300 |
941.00 |
293.10 |
0.0380 |
1240.00 |
293.10 |
0.0460 |
1517.00 |
293.10 |
0.0610 |
1871.00 |
293.10 |
0.0740 |
2164.00 |
293.12 |
0.0880 |
2464.00 |
293.11 |
0.1030 |
2737.00 |
293.11 |
0.1020 |
2778.00 |
303.11 |
0.0280 |
912.00 |
303.11 |
0.0370 |
1129.00 |
303.11 |
0.0410 |
1342.00 |
303.11 |
0.0520 |
1667.00 |
303.10 |
0.0650 |
1990.00 |
303.11 |
0.0750 |
2337.00 |
303.12 |
0.0860 |
2651.00 |
303.12 |
0.1000 |
2966.00 |
303.12 |
0.1070 |
3212.00 |
303.12 |
0.1180 |
3384.00 |
303.12 |
0.1210 |
3451.00 |
303.12 |
0.1230 |
3486.00 |
313.14 |
0.0290 |
962.00 |
313.14 |
0.0380 |
1264.00 |
313.15 |
0.0450 |
1516.00 |
313.14 |
0.0640 |
1994.00 |
313.13 |
0.0780 |
2416.00 |
313.14 |
0.0930 |
2807.00 |
313.13 |
0.1020 |
3057.00 |
313.14 |
0.1120 |
3361.00 |
313.13 |
0.1240 |
3656.00 |
313.13 |
0.1280 |
3819.00 |
313.12 |
0.1310 |
3972.00 |
313.12 |
0.1340 |
4220.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Mole fraction of Ethane, hexafluoro- (1) - Liquid mixture 2 |
Vapor or sublimation pressure, kPa - Liquid mixture 2 |
293.11 |
0.9250 |
2778.00 |
293.11 |
0.9410 |
2830.00 |
293.10 |
0.9820 |
2928.00 |
293.11 |
0.9940 |
3010.00 |
Sources