Mixture of Fluoroform + Norflurane
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
| Fixed |
Measured |
| Mole fraction of Fluoroform (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Fluoroform (1) - Gas |
| 0.0621 |
293.15 |
0.2194 |
| 0.0691 |
283.15 |
0.2772 |
| 0.0692 |
275.15 |
0.2782 |
| 0.0712 |
268.15 |
0.3399 |
| 0.0731 |
263.15 |
0.4090 |
| 0.0741 |
258.15 |
0.3452 |
| 0.1148 |
293.15 |
0.3608 |
| 0.1179 |
258.15 |
0.5637 |
| 0.1196 |
263.15 |
0.4981 |
| 0.1208 |
275.15 |
0.4086 |
| 0.1223 |
268.15 |
0.4790 |
| 0.1239 |
283.15 |
0.4100 |
| 0.1640 |
258.15 |
0.6513 |
| 0.1851 |
275.15 |
0.5193 |
| 0.1929 |
293.15 |
0.4829 |
| 0.1941 |
263.15 |
0.6263 |
| 0.1957 |
268.15 |
0.5980 |
| 0.1994 |
283.15 |
0.5213 |
| 0.2792 |
293.15 |
0.5830 |
| 0.2901 |
258.15 |
0.7510 |
| 0.2932 |
263.15 |
0.7028 |
| 0.2939 |
283.15 |
0.6000 |
| 0.2954 |
268.15 |
0.6866 |
| 0.2985 |
275.15 |
0.6211 |
| 0.4296 |
258.15 |
0.8338 |
| 0.4669 |
263.15 |
0.8251 |
| 0.4942 |
275.15 |
0.7864 |
| 0.4957 |
268.15 |
0.7998 |
| 0.5012 |
293.15 |
0.7635 |
| 0.5147 |
283.15 |
0.7854 |
| 0.6524 |
258.15 |
0.9109 |
| 0.6682 |
275.15 |
0.8705 |
| 0.6766 |
263.15 |
0.9201 |
| 0.6793 |
283.15 |
0.8725 |
| 0.6874 |
293.15 |
0.8581 |
| 0.6928 |
268.15 |
0.8900 |
| 0.7711 |
293.15 |
0.9055 |
| 0.7892 |
283.15 |
0.9164 |
| 0.7982 |
275.15 |
0.9264 |
| 0.8016 |
258.15 |
0.9540 |
| 0.8039 |
268.15 |
0.9428 |
| 0.8084 |
263.15 |
0.9510 |
| 0.8333 |
258.15 |
0.9653 |
| 0.8533 |
263.15 |
0.9674 |
| 0.8688 |
268.15 |
0.9636 |
| 0.8736 |
283.15 |
0.9467 |
| 0.8741 |
293.15 |
0.9465 |
| 0.8752 |
275.15 |
0.9567 |
| 0.8938 |
258.15 |
0.9830 |
| 0.8979 |
283.15 |
0.9633 |
| 0.8985 |
263.15 |
0.9793 |
| 0.9028 |
268.15 |
0.9778 |
| 0.9053 |
275.15 |
0.9733 |
| Fixed |
Measured |
| Mole fraction of Fluoroform (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Fluoroform (1) - Gas |
| 0.0621 |
293.15 |
0.2194 |
| 0.0691 |
283.15 |
0.2772 |
| 0.0692 |
275.15 |
0.2782 |
| 0.0712 |
268.15 |
0.3399 |
| 0.0731 |
263.15 |
0.4090 |
| 0.0741 |
258.15 |
0.3452 |
| 0.1148 |
293.15 |
0.3608 |
| 0.1179 |
258.15 |
0.5637 |
| 0.1196 |
263.15 |
0.4981 |
| 0.1208 |
275.15 |
0.4086 |
| 0.1223 |
268.15 |
0.4790 |
| 0.1239 |
283.15 |
0.4100 |
| 0.1640 |
258.15 |
0.6513 |
| 0.1851 |
275.15 |
0.5193 |
| 0.1929 |
293.15 |
0.4829 |
| 0.1941 |
263.15 |
0.6263 |
| 0.1957 |
268.15 |
0.5980 |
| 0.1994 |
283.15 |
0.5213 |
| 0.2792 |
293.15 |
0.5830 |
| 0.2901 |
258.15 |
0.7510 |
| 0.2932 |
263.15 |
0.7028 |
| 0.2939 |
283.15 |
0.6000 |
| 0.2954 |
268.15 |
0.6866 |
| 0.2985 |
275.15 |
0.6211 |
| 0.4296 |
258.15 |
0.8338 |
| 0.4669 |
263.15 |
0.8251 |
| 0.4942 |
275.15 |
0.7864 |
| 0.4957 |
268.15 |
0.7998 |
| 0.5012 |
293.15 |
0.7635 |
| 0.5147 |
283.15 |
0.7854 |
| 0.6524 |
258.15 |
0.9109 |
| 0.6682 |
275.15 |
0.8705 |
| 0.6766 |
263.15 |
0.9201 |
| 0.6793 |
283.15 |
0.8725 |
| 0.6874 |
293.15 |
0.8581 |
| 0.6928 |
268.15 |
0.8900 |
| 0.7711 |
293.15 |
0.9055 |
| 0.7892 |
283.15 |
0.9164 |
| 0.7982 |
275.15 |
0.9264 |
| 0.8016 |
258.15 |
0.9540 |
| 0.8039 |
268.15 |
0.9428 |
| 0.8084 |
263.15 |
0.9510 |
| 0.8333 |
258.15 |
0.9653 |
| 0.8533 |
263.15 |
0.9674 |
| 0.8688 |
268.15 |
0.9636 |
| 0.8736 |
283.15 |
0.9467 |
| 0.8741 |
293.15 |
0.9465 |
| 0.8752 |
275.15 |
0.9567 |
| 0.8938 |
258.15 |
0.9830 |
| 0.8979 |
283.15 |
0.9633 |
| 0.8985 |
263.15 |
0.9793 |
| 0.9028 |
268.15 |
0.9778 |
| 0.9053 |
275.15 |
0.9733 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Fluoroform (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0621 |
293.15 |
735.90 |
| 0.0691 |
283.15 |
564.70 |
| 0.0692 |
275.15 |
444.90 |
| 0.0712 |
268.15 |
356.10 |
| 0.0731 |
263.15 |
301.70 |
| 0.0741 |
258.15 |
283.30 |
| 0.1148 |
293.15 |
842.30 |
| 0.1179 |
258.15 |
327.50 |
| 0.1196 |
263.15 |
363.90 |
| 0.1208 |
275.15 |
525.30 |
| 0.1223 |
268.15 |
424.80 |
| 0.1239 |
283.15 |
661.00 |
| 0.1640 |
258.15 |
392.80 |
| 0.1851 |
275.15 |
664.40 |
| 0.1929 |
293.15 |
988.00 |
| 0.1941 |
263.15 |
482.70 |
| 0.1957 |
268.15 |
541.30 |
| 0.1994 |
283.15 |
811.40 |
| 0.2792 |
293.15 |
1212.70 |
| 0.2901 |
258.15 |
515.40 |
| 0.2932 |
263.15 |
619.20 |
| 0.2939 |
283.15 |
953.90 |
| 0.2954 |
268.15 |
692.50 |
| 0.2985 |
275.15 |
838.00 |
| 0.4296 |
258.15 |
715.00 |
| 0.4669 |
263.15 |
907.40 |
| 0.4942 |
275.15 |
1258.80 |
| 0.4957 |
268.15 |
1043.90 |
| 0.5012 |
293.15 |
1873.40 |
| 0.5147 |
283.15 |
1537.40 |
| 0.6524 |
258.15 |
1024.50 |
| 0.6682 |
275.15 |
1626.10 |
| 0.6766 |
263.15 |
1281.80 |
| 0.6793 |
283.15 |
1980.30 |
| 0.6874 |
293.15 |
2512.50 |
| 0.6928 |
268.15 |
1443.50 |
| 0.7711 |
293.15 |
2915.40 |
| 0.7892 |
283.15 |
2387.40 |
| 0.7982 |
275.15 |
1988.00 |
| 0.8016 |
258.15 |
1299.30 |
| 0.8039 |
268.15 |
1710.30 |
| 0.8084 |
263.15 |
1536.00 |
| 0.8333 |
258.15 |
1351.70 |
| 0.8533 |
263.15 |
1631.90 |
| 0.8688 |
268.15 |
1834.10 |
| 0.8736 |
283.15 |
2691.20 |
| 0.8741 |
293.15 |
3421.90 |
| 0.8752 |
275.15 |
2206.80 |
| 0.8938 |
258.15 |
1471.30 |
| 0.8979 |
283.15 |
2823.20 |
| 0.8985 |
263.15 |
1701.40 |
| 0.9028 |
268.15 |
1936.50 |
| 0.9053 |
275.15 |
2328.40 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Fluoroform (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0621 |
293.15 |
735.90 |
| 0.0691 |
283.15 |
564.70 |
| 0.0692 |
275.15 |
444.90 |
| 0.0712 |
268.15 |
356.10 |
| 0.0731 |
263.15 |
301.70 |
| 0.0741 |
258.15 |
283.30 |
| 0.1148 |
293.15 |
842.30 |
| 0.1179 |
258.15 |
327.50 |
| 0.1196 |
263.15 |
363.90 |
| 0.1208 |
275.15 |
525.30 |
| 0.1223 |
268.15 |
424.80 |
| 0.1239 |
283.15 |
661.00 |
| 0.1640 |
258.15 |
392.80 |
| 0.1851 |
275.15 |
664.40 |
| 0.1929 |
293.15 |
988.00 |
| 0.1941 |
263.15 |
482.70 |
| 0.1957 |
268.15 |
541.30 |
| 0.1994 |
283.15 |
811.40 |
| 0.2792 |
293.15 |
1212.70 |
| 0.2901 |
258.15 |
515.40 |
| 0.2932 |
263.15 |
619.20 |
| 0.2939 |
283.15 |
953.90 |
| 0.2954 |
268.15 |
692.50 |
| 0.2985 |
275.15 |
838.00 |
| 0.4296 |
258.15 |
715.00 |
| 0.4669 |
263.15 |
907.40 |
| 0.4942 |
275.15 |
1258.80 |
| 0.4957 |
268.15 |
1043.90 |
| 0.5012 |
293.15 |
1873.40 |
| 0.5147 |
283.15 |
1537.40 |
| 0.6524 |
258.15 |
1024.50 |
| 0.6682 |
275.15 |
1626.10 |
| 0.6766 |
263.15 |
1281.80 |
| 0.6793 |
283.15 |
1980.30 |
| 0.6874 |
293.15 |
2512.50 |
| 0.6928 |
268.15 |
1443.50 |
| 0.7711 |
293.15 |
2915.40 |
| 0.7892 |
283.15 |
2387.40 |
| 0.7982 |
275.15 |
1988.00 |
| 0.8016 |
258.15 |
1299.30 |
| 0.8039 |
268.15 |
1710.30 |
| 0.8084 |
263.15 |
1536.00 |
| 0.8333 |
258.15 |
1351.70 |
| 0.8533 |
263.15 |
1631.90 |
| 0.8688 |
268.15 |
1834.10 |
| 0.8736 |
283.15 |
2691.20 |
| 0.8741 |
293.15 |
3421.90 |
| 0.8752 |
275.15 |
2206.80 |
| 0.8938 |
258.15 |
1471.30 |
| 0.8979 |
283.15 |
2823.20 |
| 0.8985 |
263.15 |
1701.40 |
| 0.9028 |
268.15 |
1936.50 |
| 0.9053 |
275.15 |
2328.40 |
Sources