Mixture of Propane, 1,1,1,3,3,3-hexafluoro- + N,N-Dimethylacetamide
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- (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.15 |
0.3900 |
42.90 |
293.15 |
0.4603 |
55.50 |
293.15 |
0.5559 |
72.20 |
293.15 |
0.6240 |
87.70 |
293.15 |
0.6902 |
103.20 |
293.15 |
0.7513 |
123.60 |
293.15 |
0.8233 |
149.20 |
293.15 |
0.8874 |
178.90 |
303.15 |
0.4226 |
65.00 |
303.15 |
0.4978 |
83.20 |
303.15 |
0.5633 |
100.60 |
303.15 |
0.6229 |
119.20 |
303.15 |
0.6811 |
136.60 |
303.15 |
0.7359 |
163.00 |
303.15 |
0.8198 |
201.50 |
303.15 |
0.8978 |
252.70 |
313.15 |
0.3784 |
75.10 |
313.15 |
0.4532 |
96.50 |
313.15 |
0.5555 |
133.20 |
313.15 |
0.6308 |
160.10 |
313.15 |
0.6935 |
189.50 |
313.15 |
0.7546 |
223.50 |
313.15 |
0.8173 |
267.70 |
313.15 |
0.8992 |
329.10 |
323.15 |
0.2520 |
55.80 |
323.15 |
0.3284 |
79.10 |
323.15 |
0.4300 |
119.00 |
323.15 |
0.5241 |
157.50 |
323.15 |
0.6225 |
205.50 |
323.15 |
0.6809 |
243.10 |
323.15 |
0.7285 |
278.70 |
323.15 |
0.8052 |
336.90 |
323.15 |
0.8578 |
382.20 |
323.15 |
0.9030 |
440.90 |
333.15 |
0.2753 |
79.20 |
333.15 |
0.3506 |
113.90 |
333.15 |
0.4370 |
155.30 |
333.15 |
0.5172 |
197.90 |
333.15 |
0.5853 |
243.60 |
333.15 |
0.6926 |
325.60 |
333.15 |
0.7875 |
407.30 |
333.15 |
0.8799 |
521.70 |
343.15 |
0.2591 |
96.00 |
343.15 |
0.3517 |
144.20 |
343.15 |
0.4761 |
223.80 |
343.15 |
0.6055 |
325.70 |
343.15 |
0.7113 |
429.30 |
343.15 |
0.7765 |
512.70 |
343.15 |
0.8540 |
603.90 |
353.15 |
0.2397 |
112.00 |
353.15 |
0.3400 |
182.00 |
353.15 |
0.4239 |
246.20 |
353.15 |
0.5137 |
323.60 |
353.15 |
0.6192 |
429.30 |
353.15 |
0.7320 |
573.70 |
353.15 |
0.8364 |
739.90 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Propane, 1,1,1,3,3,3-hexafluoro- (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.15 |
0.3900 |
42.90 |
293.15 |
0.4603 |
55.50 |
293.15 |
0.5559 |
72.20 |
293.15 |
0.6240 |
87.70 |
293.15 |
0.6902 |
103.20 |
293.15 |
0.7513 |
123.60 |
293.15 |
0.8233 |
149.20 |
293.15 |
0.8874 |
178.90 |
303.15 |
0.4226 |
65.00 |
303.15 |
0.4978 |
83.20 |
303.15 |
0.5633 |
100.60 |
303.15 |
0.6229 |
119.20 |
303.15 |
0.6811 |
136.60 |
303.15 |
0.7359 |
163.00 |
303.15 |
0.8198 |
201.50 |
303.15 |
0.8978 |
252.70 |
313.15 |
0.3784 |
75.10 |
313.15 |
0.4532 |
96.50 |
313.15 |
0.5555 |
133.20 |
313.15 |
0.6308 |
160.10 |
313.15 |
0.6935 |
189.50 |
313.15 |
0.7546 |
223.50 |
313.15 |
0.8173 |
267.70 |
313.15 |
0.8992 |
329.10 |
323.15 |
0.2520 |
55.80 |
323.15 |
0.3284 |
79.10 |
323.15 |
0.4300 |
119.00 |
323.15 |
0.5241 |
157.50 |
323.15 |
0.6225 |
205.50 |
323.15 |
0.6809 |
243.10 |
323.15 |
0.7285 |
278.70 |
323.15 |
0.8052 |
336.90 |
323.15 |
0.8578 |
382.20 |
323.15 |
0.9030 |
440.90 |
333.15 |
0.2753 |
79.20 |
333.15 |
0.3506 |
113.90 |
333.15 |
0.4370 |
155.30 |
333.15 |
0.5172 |
197.90 |
333.15 |
0.5853 |
243.60 |
333.15 |
0.6926 |
325.60 |
333.15 |
0.7875 |
407.30 |
333.15 |
0.8799 |
521.70 |
343.15 |
0.2591 |
96.00 |
343.15 |
0.3517 |
144.20 |
343.15 |
0.4761 |
223.80 |
343.15 |
0.6055 |
325.70 |
343.15 |
0.7113 |
429.30 |
343.15 |
0.7765 |
512.70 |
343.15 |
0.8540 |
603.90 |
353.15 |
0.2397 |
112.00 |
353.15 |
0.3400 |
182.00 |
353.15 |
0.4239 |
246.20 |
353.15 |
0.5137 |
323.60 |
353.15 |
0.6192 |
429.30 |
353.15 |
0.7320 |
573.70 |
353.15 |
0.8364 |
739.90 |
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