Mixture of Ethane + Perfluoropropane
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of Ethane (1)
[ref]
| Fixed |
Measured |
| Mole fraction of Ethane (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethane (1) - Gas |
| 0.0000 |
264.05 |
0.0000 |
| 0.0640 |
264.05 |
0.3860 |
| 0.1580 |
264.05 |
0.5990 |
| 0.2500 |
264.05 |
0.7210 |
| 0.3560 |
264.05 |
0.7750 |
| 0.4430 |
264.05 |
0.8140 |
| 0.5410 |
264.05 |
0.8420 |
| 0.6590 |
264.05 |
0.8730 |
| 0.7810 |
264.05 |
0.9010 |
| 1.0000 |
264.05 |
1.0000 |
| 0.0000 |
271.05 |
0.0000 |
| 0.0550 |
271.05 |
0.3500 |
| 0.1410 |
271.05 |
0.5370 |
| 0.2460 |
271.05 |
0.6620 |
| 0.3310 |
271.05 |
0.7200 |
| 0.4370 |
271.05 |
0.7700 |
| 0.5690 |
271.05 |
0.8240 |
| 0.8660 |
271.05 |
0.9280 |
| 1.0000 |
271.05 |
1.0000 |
| 0.0000 |
278.05 |
0.0000 |
| 0.0860 |
278.05 |
0.3890 |
| 0.1380 |
278.05 |
0.4990 |
| 0.2380 |
278.05 |
0.6230 |
| 0.3190 |
278.05 |
0.6890 |
| 0.4180 |
278.05 |
0.7380 |
| 0.5190 |
278.05 |
0.7840 |
| 0.6220 |
278.05 |
0.8250 |
| 0.7660 |
278.05 |
0.8780 |
| 0.8660 |
278.05 |
0.9210 |
| 1.0000 |
278.05 |
1.0000 |
| 0.0000 |
303.04 |
0.0000 |
| 0.1430 |
303.04 |
0.3670 |
| 0.2210 |
303.04 |
0.4940 |
| 0.2900 |
303.04 |
0.5560 |
| 0.3710 |
303.04 |
0.6150 |
| 0.4840 |
303.04 |
0.6750 |
| 0.5780 |
303.04 |
0.7190 |
| 0.6870 |
303.04 |
0.7700 |
| 0.8360 |
303.04 |
0.8410 |
| 0.8770 |
303.04 |
0.8830 |
| 0.9200 |
303.04 |
0.9240 |
| 1.0000 |
303.04 |
1.0000 |
| 0.0000 |
308.04 |
0.0000 |
| 0.0810 |
308.04 |
0.2300 |
| 0.1530 |
308.04 |
0.3560 |
| 0.2350 |
308.04 |
0.4570 |
| 0.3310 |
308.04 |
0.5470 |
| 0.4310 |
308.04 |
0.6190 |
| 0.5240 |
308.04 |
0.6620 |
| 0.5990 |
308.04 |
0.6940 |
Mole fraction of Ethane (1)
[ref]
| Fixed |
Measured |
| Mole fraction of Ethane (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethane (1) - Gas |
| 0.0000 |
264.05 |
0.0000 |
| 0.0640 |
264.05 |
0.3860 |
| 0.1580 |
264.05 |
0.5990 |
| 0.2500 |
264.05 |
0.7210 |
| 0.3560 |
264.05 |
0.7750 |
| 0.4430 |
264.05 |
0.8140 |
| 0.5410 |
264.05 |
0.8420 |
| 0.6590 |
264.05 |
0.8730 |
| 0.7810 |
264.05 |
0.9010 |
| 1.0000 |
264.05 |
1.0000 |
| 0.0000 |
271.05 |
0.0000 |
| 0.0550 |
271.05 |
0.3500 |
| 0.1410 |
271.05 |
0.5370 |
| 0.2460 |
271.05 |
0.6620 |
| 0.3310 |
271.05 |
0.7200 |
| 0.4370 |
271.05 |
0.7700 |
| 0.5690 |
271.05 |
0.8240 |
| 0.8660 |
271.05 |
0.9280 |
| 1.0000 |
271.05 |
1.0000 |
| 0.0000 |
278.05 |
0.0000 |
| 0.0860 |
278.05 |
0.3890 |
| 0.1380 |
278.05 |
0.4990 |
| 0.2380 |
278.05 |
0.6230 |
| 0.3190 |
278.05 |
0.6890 |
| 0.4180 |
278.05 |
0.7380 |
| 0.5190 |
278.05 |
0.7840 |
| 0.6220 |
278.05 |
0.8250 |
| 0.7660 |
278.05 |
0.8780 |
| 0.8660 |
278.05 |
0.9210 |
| 1.0000 |
278.05 |
1.0000 |
| 0.0000 |
303.04 |
0.0000 |
| 0.1430 |
303.04 |
0.3670 |
| 0.2210 |
303.04 |
0.4940 |
| 0.2900 |
303.04 |
0.5560 |
| 0.3710 |
303.04 |
0.6150 |
| 0.4840 |
303.04 |
0.6750 |
| 0.5780 |
303.04 |
0.7190 |
| 0.6870 |
303.04 |
0.7700 |
| 0.8360 |
303.04 |
0.8410 |
| 0.8770 |
303.04 |
0.8830 |
| 0.9200 |
303.04 |
0.9240 |
| 1.0000 |
303.04 |
1.0000 |
| 0.0000 |
308.04 |
0.0000 |
| 0.0810 |
308.04 |
0.2300 |
| 0.1530 |
308.04 |
0.3560 |
| 0.2350 |
308.04 |
0.4570 |
| 0.3310 |
308.04 |
0.5470 |
| 0.4310 |
308.04 |
0.6190 |
| 0.5240 |
308.04 |
0.6620 |
| 0.5990 |
308.04 |
0.6940 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Ethane (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0000 |
264.05 |
298.00 |
| 0.0640 |
264.05 |
473.00 |
| 0.1580 |
264.05 |
713.00 |
| 0.2500 |
264.05 |
938.00 |
| 0.3560 |
264.05 |
1117.00 |
| 0.4430 |
264.05 |
1266.00 |
| 0.5410 |
264.05 |
1402.00 |
| 0.6590 |
264.05 |
1550.00 |
| 0.7810 |
264.05 |
1693.00 |
| 1.0000 |
264.05 |
1862.00 |
| 0.0000 |
271.05 |
383.00 |
| 0.0550 |
271.05 |
569.00 |
| 0.1410 |
271.05 |
791.00 |
| 0.2460 |
271.05 |
1069.00 |
| 0.3310 |
271.05 |
1256.00 |
| 0.4370 |
271.05 |
1461.00 |
| 0.5690 |
271.05 |
1693.00 |
| 0.8660 |
271.05 |
2112.00 |
| 1.0000 |
271.05 |
2275.00 |
| 0.0000 |
278.05 |
483.00 |
| 0.0860 |
278.05 |
772.00 |
| 0.1380 |
278.05 |
930.00 |
| 0.2380 |
278.05 |
1231.00 |
| 0.3190 |
278.05 |
1451.00 |
| 0.4180 |
278.05 |
1675.00 |
| 0.5190 |
278.05 |
1865.00 |
| 0.6220 |
278.05 |
2068.00 |
| 0.7660 |
278.05 |
2331.00 |
| 0.8660 |
278.05 |
2498.00 |
| 1.0000 |
278.05 |
2700.00 |
| 0.0000 |
303.04 |
995.00 |
| 0.1430 |
303.04 |
1656.00 |
| 0.2210 |
303.04 |
1981.00 |
| 0.2900 |
303.04 |
2255.00 |
| 0.3710 |
303.04 |
2556.00 |
| 0.4840 |
303.04 |
2973.00 |
| 0.5780 |
303.04 |
3295.00 |
| 0.6870 |
303.04 |
3690.00 |
| 0.8360 |
303.04 |
4149.00 |
| 0.8770 |
303.04 |
4334.00 |
| 0.9200 |
303.04 |
4467.00 |
| 1.0000 |
303.04 |
4600.00 |
| 0.0000 |
308.04 |
1124.00 |
| 0.0810 |
308.04 |
1534.00 |
| 0.1530 |
308.04 |
1858.00 |
| 0.2350 |
308.04 |
2221.00 |
| 0.3310 |
308.04 |
2630.00 |
| 0.4310 |
308.04 |
3028.00 |
| 0.5240 |
308.04 |
3416.00 |
| 0.5990 |
308.04 |
3685.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Ethane (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0000 |
264.05 |
298.00 |
| 0.0640 |
264.05 |
473.00 |
| 0.1580 |
264.05 |
713.00 |
| 0.2500 |
264.05 |
938.00 |
| 0.3560 |
264.05 |
1117.00 |
| 0.4430 |
264.05 |
1266.00 |
| 0.5410 |
264.05 |
1402.00 |
| 0.6590 |
264.05 |
1550.00 |
| 0.7810 |
264.05 |
1693.00 |
| 1.0000 |
264.05 |
1862.00 |
| 0.0000 |
271.05 |
383.00 |
| 0.0550 |
271.05 |
569.00 |
| 0.1410 |
271.05 |
791.00 |
| 0.2460 |
271.05 |
1069.00 |
| 0.3310 |
271.05 |
1256.00 |
| 0.4370 |
271.05 |
1461.00 |
| 0.5690 |
271.05 |
1693.00 |
| 0.8660 |
271.05 |
2112.00 |
| 1.0000 |
271.05 |
2275.00 |
| 0.0000 |
278.05 |
483.00 |
| 0.0860 |
278.05 |
772.00 |
| 0.1380 |
278.05 |
930.00 |
| 0.2380 |
278.05 |
1231.00 |
| 0.3190 |
278.05 |
1451.00 |
| 0.4180 |
278.05 |
1675.00 |
| 0.5190 |
278.05 |
1865.00 |
| 0.6220 |
278.05 |
2068.00 |
| 0.7660 |
278.05 |
2331.00 |
| 0.8660 |
278.05 |
2498.00 |
| 1.0000 |
278.05 |
2700.00 |
| 0.0000 |
303.04 |
995.00 |
| 0.1430 |
303.04 |
1656.00 |
| 0.2210 |
303.04 |
1981.00 |
| 0.2900 |
303.04 |
2255.00 |
| 0.3710 |
303.04 |
2556.00 |
| 0.4840 |
303.04 |
2973.00 |
| 0.5780 |
303.04 |
3295.00 |
| 0.6870 |
303.04 |
3690.00 |
| 0.8360 |
303.04 |
4149.00 |
| 0.8770 |
303.04 |
4334.00 |
| 0.9200 |
303.04 |
4467.00 |
| 1.0000 |
303.04 |
4600.00 |
| 0.0000 |
308.04 |
1124.00 |
| 0.0810 |
308.04 |
1534.00 |
| 0.1530 |
308.04 |
1858.00 |
| 0.2350 |
308.04 |
2221.00 |
| 0.3310 |
308.04 |
2630.00 |
| 0.4310 |
308.04 |
3028.00 |
| 0.5240 |
308.04 |
3416.00 |
| 0.5990 |
308.04 |
3685.00 |
Sources