Mixture of 1,1,1,2,3,3,3-heptafluoropropane + Norflurane
Datasets
-
Mole fraction
-
Vapor or sublimation pressure, kPa
Mole fraction of Norflurane (2)
[ref]
| Fixed |
Measured |
| Mole fraction of Norflurane (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Norflurane (2) - Gas |
| 0.0000 |
283.15 |
0.0000 |
| 0.0730 |
283.15 |
0.1080 |
| 0.2228 |
283.15 |
0.3057 |
| 0.3238 |
283.15 |
0.4143 |
| 0.4314 |
283.15 |
0.5287 |
| 0.5297 |
283.15 |
0.6168 |
| 0.7004 |
283.15 |
0.7643 |
| 0.8099 |
283.15 |
0.8517 |
| 0.8854 |
283.15 |
0.9093 |
| 1.0000 |
283.15 |
1.0000 |
| 0.0000 |
293.15 |
0.0000 |
| 0.0730 |
293.15 |
0.1064 |
| 0.2228 |
293.15 |
0.2998 |
| 0.3238 |
293.15 |
0.4098 |
| 0.4314 |
293.15 |
0.5226 |
| 0.5297 |
293.15 |
0.6132 |
| 0.7004 |
293.15 |
0.7599 |
| 0.8099 |
293.15 |
0.8483 |
| 0.8854 |
293.15 |
0.9084 |
| 1.0000 |
293.15 |
1.0000 |
| 0.0000 |
303.15 |
0.0000 |
| 0.0730 |
303.15 |
0.1043 |
| 0.2228 |
303.15 |
0.2957 |
| 0.3238 |
303.15 |
0.4062 |
| 0.4314 |
303.15 |
0.5160 |
| 0.5297 |
303.15 |
0.6089 |
| 0.7004 |
303.15 |
0.7564 |
| 0.8099 |
303.15 |
0.8462 |
| 0.8854 |
303.15 |
0.9076 |
| 1.0000 |
303.15 |
1.0000 |
| 0.0000 |
313.15 |
0.0000 |
| 0.0720 |
313.15 |
0.1012 |
| 0.2228 |
313.15 |
0.2914 |
| 0.3238 |
313.15 |
0.3961 |
| 0.4332 |
313.15 |
0.5106 |
| 0.5297 |
313.15 |
0.6010 |
| 0.7004 |
313.15 |
0.7520 |
| 0.8099 |
313.15 |
0.8428 |
| 0.8854 |
313.15 |
0.9056 |
| 1.0000 |
313.15 |
1.0000 |
| 0.0000 |
323.15 |
0.0000 |
| 0.0720 |
323.15 |
0.0984 |
| 0.2228 |
323.15 |
0.2832 |
| 0.3218 |
323.15 |
0.3934 |
| 0.4332 |
323.15 |
0.5030 |
| 0.5297 |
323.15 |
0.5932 |
| 0.7004 |
323.15 |
0.7477 |
| 0.8099 |
323.15 |
0.8404 |
| 0.8854 |
323.15 |
0.9031 |
| 1.0000 |
323.15 |
1.0000 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Norflurane (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Gas |
| 0.0000 |
283.15 |
278.90 |
| 0.0730 |
283.15 |
292.60 |
| 0.2228 |
283.15 |
317.80 |
| 0.3238 |
283.15 |
335.10 |
| 0.4314 |
283.15 |
349.10 |
| 0.5297 |
283.15 |
363.40 |
| 0.7004 |
283.15 |
384.00 |
| 0.8099 |
283.15 |
396.70 |
| 0.8854 |
283.15 |
405.60 |
| 1.0000 |
283.15 |
414.00 |
| 0.0000 |
293.15 |
388.00 |
| 0.0730 |
293.15 |
406.60 |
| 0.2228 |
293.15 |
441.20 |
| 0.3238 |
293.15 |
463.40 |
| 0.4314 |
293.15 |
484.10 |
| 0.5297 |
293.15 |
502.10 |
| 0.7004 |
293.15 |
529.80 |
| 0.8099 |
293.15 |
546.20 |
| 0.8854 |
293.15 |
558.70 |
| 1.0000 |
293.15 |
571.50 |
| 0.0000 |
303.15 |
524.50 |
| 0.0730 |
303.15 |
548.10 |
| 0.2228 |
303.15 |
595.10 |
| 0.3238 |
303.15 |
624.70 |
| 0.4314 |
303.15 |
653.00 |
| 0.5297 |
303.15 |
679.20 |
| 0.7004 |
303.15 |
713.80 |
| 0.8099 |
303.15 |
736.30 |
| 0.8854 |
303.15 |
751.40 |
| 1.0000 |
303.15 |
767.00 |
| 0.0000 |
313.15 |
699.00 |
| 0.0720 |
313.15 |
728.10 |
| 0.2228 |
313.15 |
788.80 |
| 0.3238 |
313.15 |
824.00 |
| 0.4332 |
313.15 |
859.60 |
| 0.5297 |
313.15 |
890.80 |
| 0.7004 |
313.15 |
939.70 |
| 0.8099 |
313.15 |
969.20 |
| 0.8854 |
313.15 |
988.40 |
| 1.0000 |
313.15 |
1013.00 |
| 0.0000 |
323.15 |
912.40 |
| 0.0720 |
323.15 |
945.70 |
| 0.2228 |
323.15 |
1028.80 |
| 0.3218 |
323.15 |
1070.80 |
| 0.4332 |
323.15 |
1116.90 |
| 0.5297 |
323.15 |
1156.30 |
| 0.7004 |
323.15 |
1219.30 |
| 0.8099 |
323.15 |
1257.60 |
| 0.8854 |
323.15 |
1282.70 |
| 1.0000 |
323.15 |
1314.70 |
Sources
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Vapor-liquid equilibria for the 1,1,1,2 -tetrafluoroethane (HFC-134a) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) and 1,1,1-trifluoroethane (HFC-143a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) systems