Mixture of Ethane, 1,1'-oxybis[2-methoxy- + Propane, 1,1,1,3,3,3-hexafluoro-
Datasets
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Pvap - Vapor or sublimation pressure, kPa (2)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Propane, 1,1,1,3,3,3-hexafluoro- (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.15 |
0.3500 |
32.10 |
293.15 |
0.4621 |
52.70 |
293.15 |
0.5718 |
75.90 |
293.15 |
0.6783 |
103.10 |
293.15 |
0.7501 |
121.90 |
293.15 |
0.8403 |
146.60 |
293.15 |
0.8890 |
163.90 |
303.15 |
0.3102 |
36.10 |
303.15 |
0.4076 |
59.10 |
303.15 |
0.5132 |
89.60 |
303.15 |
0.5978 |
113.20 |
303.15 |
0.6560 |
133.90 |
303.15 |
0.7164 |
155.10 |
303.15 |
0.7701 |
175.80 |
303.15 |
0.8239 |
195.70 |
303.15 |
0.8668 |
217.50 |
313.15 |
0.2750 |
42.50 |
313.15 |
0.3681 |
69.60 |
313.15 |
0.4564 |
99.70 |
313.15 |
0.5310 |
128.10 |
313.15 |
0.6411 |
172.80 |
313.15 |
0.7200 |
209.70 |
313.15 |
0.8002 |
252.90 |
313.15 |
0.8974 |
317.90 |
323.15 |
0.2303 |
47.10 |
323.15 |
0.3561 |
92.50 |
323.15 |
0.4335 |
126.50 |
323.15 |
0.5213 |
168.60 |
323.15 |
0.5834 |
199.70 |
323.15 |
0.6796 |
252.60 |
323.15 |
0.7664 |
312.30 |
323.15 |
0.8283 |
359.30 |
323.15 |
0.8866 |
407.20 |
333.15 |
0.1797 |
49.30 |
333.15 |
0.3022 |
101.30 |
333.15 |
0.4191 |
158.90 |
333.15 |
0.5188 |
221.60 |
333.15 |
0.6598 |
321.50 |
333.15 |
0.7692 |
409.30 |
333.15 |
0.8751 |
512.70 |
343.15 |
0.1565 |
61.70 |
343.15 |
0.2526 |
112.20 |
343.15 |
0.3627 |
175.70 |
343.15 |
0.4474 |
232.80 |
343.15 |
0.5425 |
311.60 |
343.15 |
0.6429 |
397.50 |
343.15 |
0.7500 |
497.00 |
343.15 |
0.8664 |
633.90 |
353.15 |
0.1375 |
77.90 |
353.15 |
0.2827 |
179.10 |
353.15 |
0.3964 |
273.50 |
353.15 |
0.5573 |
423.60 |
353.15 |
0.6800 |
559.00 |
353.15 |
0.7550 |
650.00 |
353.15 |
0.8517 |
780.90 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Propane, 1,1,1,3,3,3-hexafluoro- (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.15 |
0.3500 |
32.10 |
293.15 |
0.4621 |
52.70 |
293.15 |
0.5718 |
75.90 |
293.15 |
0.6783 |
103.10 |
293.15 |
0.7501 |
121.90 |
293.15 |
0.8403 |
146.60 |
293.15 |
0.8890 |
163.90 |
303.15 |
0.3102 |
36.10 |
303.15 |
0.4076 |
59.10 |
303.15 |
0.5132 |
89.60 |
303.15 |
0.5978 |
113.20 |
303.15 |
0.6560 |
133.90 |
303.15 |
0.7164 |
155.10 |
303.15 |
0.7701 |
175.80 |
303.15 |
0.8239 |
195.70 |
303.15 |
0.8668 |
217.50 |
313.15 |
0.2750 |
42.50 |
313.15 |
0.3681 |
69.60 |
313.15 |
0.4564 |
99.70 |
313.15 |
0.5310 |
128.10 |
313.15 |
0.6411 |
172.80 |
313.15 |
0.7200 |
209.70 |
313.15 |
0.8002 |
252.90 |
313.15 |
0.8974 |
317.90 |
323.15 |
0.2303 |
47.10 |
323.15 |
0.3561 |
92.50 |
323.15 |
0.4335 |
126.50 |
323.15 |
0.5213 |
168.60 |
323.15 |
0.5834 |
199.70 |
323.15 |
0.6796 |
252.60 |
323.15 |
0.7664 |
312.30 |
323.15 |
0.8283 |
359.30 |
323.15 |
0.8866 |
407.20 |
333.15 |
0.1797 |
49.30 |
333.15 |
0.3022 |
101.30 |
333.15 |
0.4191 |
158.90 |
333.15 |
0.5188 |
221.60 |
333.15 |
0.6598 |
321.50 |
333.15 |
0.7692 |
409.30 |
333.15 |
0.8751 |
512.70 |
343.15 |
0.1565 |
61.70 |
343.15 |
0.2526 |
112.20 |
343.15 |
0.3627 |
175.70 |
343.15 |
0.4474 |
232.80 |
343.15 |
0.5425 |
311.60 |
343.15 |
0.6429 |
397.50 |
343.15 |
0.7500 |
497.00 |
343.15 |
0.8664 |
633.90 |
353.15 |
0.1375 |
77.90 |
353.15 |
0.2827 |
179.10 |
353.15 |
0.3964 |
273.50 |
353.15 |
0.5573 |
423.60 |
353.15 |
0.6800 |
559.00 |
353.15 |
0.7550 |
650.00 |
353.15 |
0.8517 |
780.90 |
Sources
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Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of 1,1,1,3,3-Pentafluoropropane + N,N-Dimethylacetamide and 1,1,1,3,3,3-Hexafluoropropane + N,N-Dimethylacetamide/Diethylene Glycol Dimethyl Ether Systems