Mixture of Ethylene + Hexafluoropropylene oxide
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of Ethylene (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethylene (1) - Liquid |
Mole fraction of Ethylene (1) - Gas |
258.38 |
0.1110 |
0.6790 |
258.38 |
0.2280 |
0.8100 |
258.38 |
0.3890 |
0.8740 |
258.38 |
0.5570 |
0.9080 |
258.38 |
0.6510 |
0.9250 |
258.38 |
0.7380 |
0.9400 |
258.38 |
0.7900 |
0.9490 |
258.38 |
0.8890 |
0.9650 |
268.21 |
0.1390 |
0.7020 |
268.21 |
0.2910 |
0.8180 |
268.21 |
0.4000 |
0.8580 |
268.21 |
0.4910 |
0.8780 |
268.21 |
0.5650 |
0.8940 |
268.21 |
0.6510 |
0.9090 |
268.21 |
0.7670 |
0.9290 |
268.21 |
0.8540 |
0.9490 |
268.21 |
0.8940 |
0.9610 |
278.07 |
0.0720 |
0.4840 |
278.07 |
0.1550 |
0.6580 |
278.07 |
0.2470 |
0.7450 |
278.07 |
0.3300 |
0.7930 |
278.07 |
0.4230 |
0.8270 |
278.07 |
0.5210 |
0.8560 |
278.07 |
0.6510 |
0.8840 |
278.07 |
0.7840 |
0.9190 |
278.07 |
0.8900 |
0.9500 |
287.85 |
0.0910 |
0.4690 |
287.85 |
0.1800 |
0.6360 |
287.85 |
0.2880 |
0.7250 |
287.85 |
0.4000 |
0.7720 |
287.85 |
0.5210 |
0.8170 |
287.85 |
0.6230 |
0.8430 |
287.85 |
0.7010 |
0.8650 |
287.85 |
0.8210 |
0.9020 |
297.63 |
0.0770 |
0.3780 |
297.63 |
0.1420 |
0.5250 |
297.63 |
0.2470 |
0.6410 |
297.63 |
0.3330 |
0.7040 |
297.63 |
0.4220 |
0.7450 |
297.63 |
0.5210 |
0.7750 |
297.63 |
0.6230 |
0.8130 |
297.63 |
0.7200 |
0.8380 |
307.38 |
0.0950 |
0.3870 |
307.38 |
0.1660 |
0.4980 |
307.38 |
0.2550 |
0.5960 |
307.38 |
0.3380 |
0.6490 |
307.38 |
0.4800 |
0.7100 |
307.38 |
0.5380 |
0.7290 |
307.38 |
0.6170 |
0.7430 |
Mole fraction of Ethylene (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethylene (1) - Liquid |
Mole fraction of Ethylene (1) - Gas |
258.38 |
0.1110 |
0.6790 |
258.38 |
0.2280 |
0.8100 |
258.38 |
0.3890 |
0.8740 |
258.38 |
0.5570 |
0.9080 |
258.38 |
0.6510 |
0.9250 |
258.38 |
0.7380 |
0.9400 |
258.38 |
0.7900 |
0.9490 |
258.38 |
0.8890 |
0.9650 |
268.21 |
0.1390 |
0.7020 |
268.21 |
0.2910 |
0.8180 |
268.21 |
0.4000 |
0.8580 |
268.21 |
0.4910 |
0.8780 |
268.21 |
0.5650 |
0.8940 |
268.21 |
0.6510 |
0.9090 |
268.21 |
0.7670 |
0.9290 |
268.21 |
0.8540 |
0.9490 |
268.21 |
0.8940 |
0.9610 |
278.07 |
0.0720 |
0.4840 |
278.07 |
0.1550 |
0.6580 |
278.07 |
0.2470 |
0.7450 |
278.07 |
0.3300 |
0.7930 |
278.07 |
0.4230 |
0.8270 |
278.07 |
0.5210 |
0.8560 |
278.07 |
0.6510 |
0.8840 |
278.07 |
0.7840 |
0.9190 |
278.07 |
0.8900 |
0.9500 |
287.85 |
0.0910 |
0.4690 |
287.85 |
0.1800 |
0.6360 |
287.85 |
0.2880 |
0.7250 |
287.85 |
0.4000 |
0.7720 |
287.85 |
0.5210 |
0.8170 |
287.85 |
0.6230 |
0.8430 |
287.85 |
0.7010 |
0.8650 |
287.85 |
0.8210 |
0.9020 |
297.63 |
0.0770 |
0.3780 |
297.63 |
0.1420 |
0.5250 |
297.63 |
0.2470 |
0.6410 |
297.63 |
0.3330 |
0.7040 |
297.63 |
0.4220 |
0.7450 |
297.63 |
0.5210 |
0.7750 |
297.63 |
0.6230 |
0.8130 |
297.63 |
0.7200 |
0.8380 |
307.38 |
0.0950 |
0.3870 |
307.38 |
0.1660 |
0.4980 |
307.38 |
0.2550 |
0.5960 |
307.38 |
0.3380 |
0.6490 |
307.38 |
0.4800 |
0.7100 |
307.38 |
0.5380 |
0.7290 |
307.38 |
0.6170 |
0.7430 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethylene (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
258.38 |
0.1110 |
589.00 |
258.38 |
0.2280 |
957.00 |
258.38 |
0.3890 |
1389.00 |
258.38 |
0.5570 |
1790.00 |
258.38 |
0.6510 |
1992.00 |
258.38 |
0.7380 |
2203.00 |
258.38 |
0.7900 |
2325.00 |
258.38 |
0.8890 |
2551.00 |
268.21 |
0.1390 |
871.00 |
268.21 |
0.2910 |
1440.00 |
268.21 |
0.4000 |
1803.00 |
268.21 |
0.4910 |
2064.00 |
268.21 |
0.5650 |
2281.00 |
268.21 |
0.6510 |
2474.00 |
268.21 |
0.7670 |
2826.00 |
268.21 |
0.8540 |
3091.00 |
268.21 |
0.8940 |
3225.00 |
278.07 |
0.0720 |
724.00 |
278.07 |
0.1550 |
1129.00 |
278.07 |
0.2470 |
1551.00 |
278.07 |
0.3300 |
1877.00 |
278.07 |
0.4230 |
2228.00 |
278.07 |
0.5210 |
2554.00 |
278.07 |
0.6510 |
3003.00 |
278.07 |
0.7840 |
3493.00 |
278.07 |
0.8900 |
4004.00 |
287.85 |
0.0910 |
1047.00 |
287.85 |
0.1800 |
1489.00 |
287.85 |
0.2880 |
1991.00 |
287.85 |
0.4000 |
2496.00 |
287.85 |
0.5210 |
3006.00 |
287.85 |
0.6230 |
3414.00 |
287.85 |
0.7010 |
3816.00 |
287.85 |
0.8210 |
4412.00 |
297.63 |
0.0770 |
1133.00 |
297.63 |
0.1420 |
1501.00 |
297.63 |
0.2470 |
2104.00 |
297.63 |
0.3330 |
2544.00 |
297.63 |
0.4220 |
2991.00 |
297.63 |
0.5210 |
3486.00 |
297.63 |
0.6230 |
4038.00 |
297.63 |
0.7200 |
4541.00 |
307.38 |
0.0950 |
1534.00 |
307.38 |
0.1660 |
1983.00 |
307.38 |
0.2550 |
2526.00 |
307.38 |
0.3380 |
3002.00 |
307.38 |
0.4800 |
3815.00 |
307.38 |
0.5380 |
4123.00 |
307.38 |
0.6170 |
4544.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethylene (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
258.38 |
0.1110 |
589.00 |
258.38 |
0.2280 |
957.00 |
258.38 |
0.3890 |
1389.00 |
258.38 |
0.5570 |
1790.00 |
258.38 |
0.6510 |
1992.00 |
258.38 |
0.7380 |
2203.00 |
258.38 |
0.7900 |
2325.00 |
258.38 |
0.8890 |
2551.00 |
268.21 |
0.1390 |
871.00 |
268.21 |
0.2910 |
1440.00 |
268.21 |
0.4000 |
1803.00 |
268.21 |
0.4910 |
2064.00 |
268.21 |
0.5650 |
2281.00 |
268.21 |
0.6510 |
2474.00 |
268.21 |
0.7670 |
2826.00 |
268.21 |
0.8540 |
3091.00 |
268.21 |
0.8940 |
3225.00 |
278.07 |
0.0720 |
724.00 |
278.07 |
0.1550 |
1129.00 |
278.07 |
0.2470 |
1551.00 |
278.07 |
0.3300 |
1877.00 |
278.07 |
0.4230 |
2228.00 |
278.07 |
0.5210 |
2554.00 |
278.07 |
0.6510 |
3003.00 |
278.07 |
0.7840 |
3493.00 |
278.07 |
0.8900 |
4004.00 |
287.85 |
0.0910 |
1047.00 |
287.85 |
0.1800 |
1489.00 |
287.85 |
0.2880 |
1991.00 |
287.85 |
0.4000 |
2496.00 |
287.85 |
0.5210 |
3006.00 |
287.85 |
0.6230 |
3414.00 |
287.85 |
0.7010 |
3816.00 |
287.85 |
0.8210 |
4412.00 |
297.63 |
0.0770 |
1133.00 |
297.63 |
0.1420 |
1501.00 |
297.63 |
0.2470 |
2104.00 |
297.63 |
0.3330 |
2544.00 |
297.63 |
0.4220 |
2991.00 |
297.63 |
0.5210 |
3486.00 |
297.63 |
0.6230 |
4038.00 |
297.63 |
0.7200 |
4541.00 |
307.38 |
0.0950 |
1534.00 |
307.38 |
0.1660 |
1983.00 |
307.38 |
0.2550 |
2526.00 |
307.38 |
0.3380 |
3002.00 |
307.38 |
0.4800 |
3815.00 |
307.38 |
0.5380 |
4123.00 |
307.38 |
0.6170 |
4544.00 |
Sources