Mixture of Ethane + Fluoroform
Datasets
-
Mole fraction (12)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Vapor or sublimation pressure, kPa (6)
Mole fraction of Ethane (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Ethane (1) - Liquid |
Mole fraction of Ethane (1) - Gas |
| 173.86 |
0.0000 |
0.0000 |
| 173.96 |
0.0076 |
0.1937 |
| 174.00 |
0.0161 |
0.3238 |
| 174.07 |
0.0289 |
0.4237 |
| 174.02 |
0.0699 |
0.5656 |
| 173.82 |
0.1296 |
0.6266 |
| 173.88 |
0.9218 |
0.6494 |
| 173.87 |
0.9366 |
0.6687 |
| 173.88 |
0.9609 |
0.7225 |
| 173.82 |
0.9829 |
0.8164 |
| 173.63 |
1.0000 |
1.0000 |
| 177.11 |
0.0000 |
0.0000 |
| 177.20 |
0.0180 |
0.2976 |
| 177.25 |
0.0568 |
0.4865 |
| 177.27 |
0.0911 |
0.5594 |
| 177.28 |
0.8723 |
0.6203 |
| 177.29 |
0.9573 |
0.7428 |
| 177.27 |
0.9744 |
0.8157 |
| 177.24 |
1.0000 |
1.0000 |
| 183.20 |
0.0000 |
0.0000 |
| 183.19 |
0.0000 |
0.0000 |
| 183.27 |
0.0273 |
0.3184 |
| 183.28 |
0.0407 |
0.3939 |
| 183.30 |
0.0948 |
0.5275 |
| 183.34 |
0.2602 |
0.5991 |
| 183.30 |
0.8853 |
0.6293 |
| 183.32 |
0.9151 |
0.6571 |
| 183.29 |
0.9435 |
0.7195 |
| 183.30 |
0.9784 |
0.8521 |
| 183.28 |
1.0000 |
1.0000 |
| 228.83 |
0.0000 |
0.0000 |
| 228.85 |
0.0150 |
0.0794 |
| 228.94 |
0.0464 |
0.1938 |
| 228.92 |
0.1193 |
0.3325 |
| 228.91 |
0.2053 |
0.4120 |
| 228.89 |
0.3465 |
0.4801 |
| 228.94 |
0.3750 |
0.4892 |
| 228.94 |
0.7511 |
0.6104 |
| 228.89 |
0.8956 |
0.7249 |
| 228.91 |
0.9774 |
0.9023 |
| 228.82 |
1.0000 |
1.0000 |
Mole fraction of Ethane (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane (1) - Liquid mixture 2 |
| 173.56 |
0.1300 |
| 177.20 |
0.1649 |
| 177.20 |
0.1646 |
| 179.63 |
0.1893 |
| 182.72 |
0.2436 |
| 183.26 |
0.2609 |
| 184.76 |
0.3064 |
| 186.22 |
0.4879 |
Mole fraction of Ethane (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane (1) - Liquid mixture 1 |
| 173.56 |
0.8934 |
| 177.20 |
0.8518 |
| 177.20 |
0.8516 |
| 179.63 |
0.8328 |
| 182.72 |
0.7769 |
| 183.26 |
0.7543 |
| 184.76 |
0.7069 |
Mole fraction of Ethane (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane (1) - Gas |
| 173.56 |
0.6306 |
| 177.20 |
0.6122 |
| 177.20 |
0.6131 |
| 179.63 |
0.6130 |
| 182.72 |
0.6059 |
| 183.26 |
0.5986 |
| 184.76 |
0.6010 |
| 186.22 |
0.5968 |
Azeotropic composition: mole fraction of Ethane (1)
[ref]
| Temperature, K - Liquid |
Azeotropic composition: mole fraction of Ethane (1) - Liquid |
| 188.31 |
0.5874 |
| 193.28 |
0.5805 |
| 198.66 |
0.5728 |
| 212.84 |
0.5540 |
| 228.50 |
0.5337 |
| 243.76 |
0.5170 |
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 |
188.31 |
0.0000 |
| 0.0000 |
193.28 |
0.0000 |
| 0.0000 |
198.66 |
0.0000 |
| 0.0000 |
212.84 |
0.0000 |
| 0.0000 |
228.50 |
0.0000 |
| 0.0000 |
243.76 |
0.0000 |
| 0.0871 |
212.84 |
0.3526 |
| 0.0941 |
198.66 |
0.4468 |
| 0.1037 |
193.28 |
0.4880 |
| 0.1182 |
243.76 |
0.2787 |
| 0.1208 |
228.50 |
0.3424 |
| 0.1439 |
188.31 |
0.5340 |
| 0.2468 |
212.84 |
0.4791 |
| 0.2617 |
243.76 |
0.3971 |
| 0.2717 |
198.66 |
0.5363 |
| 0.2774 |
188.31 |
0.5699 |
| 0.2858 |
228.50 |
0.4530 |
| 0.2861 |
193.28 |
0.5625 |
| 0.3925 |
212.84 |
0.5167 |
| 0.3936 |
188.31 |
0.5795 |
| 0.3962 |
198.66 |
0.5563 |
| 0.4022 |
193.28 |
0.5755 |
| 0.4049 |
243.76 |
0.4721 |
| 0.4258 |
228.50 |
0.5037 |
| 0.4956 |
243.76 |
0.5043 |
| 0.5009 |
228.50 |
0.5251 |
| 0.5023 |
188.31 |
0.5829 |
| 0.5063 |
198.66 |
0.5661 |
| 0.5069 |
243.76 |
0.5100 |
| 0.5114 |
212.84 |
0.5422 |
| 0.5171 |
193.28 |
0.5785 |
| 0.5195 |
243.76 |
0.5147 |
| 0.5247 |
228.50 |
0.5317 |
| 0.5385 |
228.50 |
0.5349 |
| 0.5505 |
212.84 |
0.5498 |
| 0.5687 |
198.66 |
0.5714 |
| 0.5688 |
212.84 |
0.5551 |
| 0.5737 |
193.28 |
0.5806 |
| 0.5753 |
198.66 |
0.5720 |
| 0.5755 |
188.31 |
0.5844 |
| 0.5825 |
193.28 |
0.5811 |
| 0.5919 |
188.31 |
0.5862 |
| 0.6119 |
243.76 |
0.5537 |
| 0.6120 |
212.84 |
0.5644 |
| 0.6164 |
228.50 |
0.5586 |
| 0.6221 |
188.31 |
0.5872 |
| 0.6242 |
198.66 |
0.5768 |
| 0.6319 |
193.28 |
0.5851 |
| 0.7957 |
198.66 |
0.6128 |
| 0.7967 |
193.28 |
0.6089 |
| 0.7968 |
188.31 |
0.6069 |
| 0.8036 |
212.84 |
0.6274 |
| 0.8166 |
228.50 |
0.6460 |
| 0.8255 |
243.76 |
0.6730 |
| 1.0000 |
188.31 |
1.0000 |
| 1.0000 |
193.28 |
1.0000 |
| 1.0000 |
198.66 |
1.0000 |
| 1.0000 |
212.84 |
1.0000 |
| 1.0000 |
228.50 |
1.0000 |
| 1.0000 |
243.76 |
1.0000 |
Mole fraction of Ethane (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Ethane (1) - Liquid |
Mole fraction of Ethane (1) - Gas |
| 173.86 |
0.0000 |
0.0000 |
| 173.96 |
0.0076 |
0.1937 |
| 174.00 |
0.0161 |
0.3238 |
| 174.07 |
0.0289 |
0.4237 |
| 174.02 |
0.0699 |
0.5656 |
| 173.82 |
0.1296 |
0.6266 |
| 173.88 |
0.9218 |
0.6494 |
| 173.87 |
0.9366 |
0.6687 |
| 173.88 |
0.9609 |
0.7225 |
| 173.82 |
0.9829 |
0.8164 |
| 173.63 |
1.0000 |
1.0000 |
| 177.11 |
0.0000 |
0.0000 |
| 177.20 |
0.0180 |
0.2976 |
| 177.25 |
0.0568 |
0.4865 |
| 177.27 |
0.0911 |
0.5594 |
| 177.28 |
0.8723 |
0.6203 |
| 177.29 |
0.9573 |
0.7428 |
| 177.27 |
0.9744 |
0.8157 |
| 177.24 |
1.0000 |
1.0000 |
| 183.20 |
0.0000 |
0.0000 |
| 183.19 |
0.0000 |
0.0000 |
| 183.27 |
0.0273 |
0.3184 |
| 183.28 |
0.0407 |
0.3939 |
| 183.30 |
0.0948 |
0.5275 |
| 183.34 |
0.2602 |
0.5991 |
| 183.30 |
0.8853 |
0.6293 |
| 183.32 |
0.9151 |
0.6571 |
| 183.29 |
0.9435 |
0.7195 |
| 183.30 |
0.9784 |
0.8521 |
| 183.28 |
1.0000 |
1.0000 |
| 228.83 |
0.0000 |
0.0000 |
| 228.85 |
0.0150 |
0.0794 |
| 228.94 |
0.0464 |
0.1938 |
| 228.92 |
0.1193 |
0.3325 |
| 228.91 |
0.2053 |
0.4120 |
| 228.89 |
0.3465 |
0.4801 |
| 228.94 |
0.3750 |
0.4892 |
| 228.94 |
0.7511 |
0.6104 |
| 228.89 |
0.8956 |
0.7249 |
| 228.91 |
0.9774 |
0.9023 |
| 228.82 |
1.0000 |
1.0000 |
Mole fraction of Ethane (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane (1) - Liquid mixture 2 |
| 173.56 |
0.1300 |
| 177.20 |
0.1649 |
| 177.20 |
0.1646 |
| 179.63 |
0.1893 |
| 182.72 |
0.2436 |
| 183.26 |
0.2609 |
| 184.76 |
0.3064 |
| 186.22 |
0.4879 |
Mole fraction of Ethane (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane (1) - Liquid mixture 1 |
| 173.56 |
0.8934 |
| 177.20 |
0.8518 |
| 177.20 |
0.8516 |
| 179.63 |
0.8328 |
| 182.72 |
0.7769 |
| 183.26 |
0.7543 |
| 184.76 |
0.7069 |
Mole fraction of Ethane (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane (1) - Gas |
| 173.56 |
0.6306 |
| 177.20 |
0.6122 |
| 177.20 |
0.6131 |
| 179.63 |
0.6130 |
| 182.72 |
0.6059 |
| 183.26 |
0.5986 |
| 184.76 |
0.6010 |
| 186.22 |
0.5968 |
Azeotropic composition: mole fraction of Ethane (1)
[ref]
| Temperature, K - Liquid |
Azeotropic composition: mole fraction of Ethane (1) - Liquid |
| 188.31 |
0.5874 |
| 193.28 |
0.5805 |
| 198.66 |
0.5728 |
| 212.84 |
0.5540 |
| 228.50 |
0.5337 |
| 243.76 |
0.5170 |
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 |
188.31 |
0.0000 |
| 0.0000 |
193.28 |
0.0000 |
| 0.0000 |
198.66 |
0.0000 |
| 0.0000 |
212.84 |
0.0000 |
| 0.0000 |
228.50 |
0.0000 |
| 0.0000 |
243.76 |
0.0000 |
| 0.0871 |
212.84 |
0.3526 |
| 0.0941 |
198.66 |
0.4468 |
| 0.1037 |
193.28 |
0.4880 |
| 0.1182 |
243.76 |
0.2787 |
| 0.1208 |
228.50 |
0.3424 |
| 0.1439 |
188.31 |
0.5340 |
| 0.2468 |
212.84 |
0.4791 |
| 0.2617 |
243.76 |
0.3971 |
| 0.2717 |
198.66 |
0.5363 |
| 0.2774 |
188.31 |
0.5699 |
| 0.2858 |
228.50 |
0.4530 |
| 0.2861 |
193.28 |
0.5625 |
| 0.3925 |
212.84 |
0.5167 |
| 0.3936 |
188.31 |
0.5795 |
| 0.3962 |
198.66 |
0.5563 |
| 0.4022 |
193.28 |
0.5755 |
| 0.4049 |
243.76 |
0.4721 |
| 0.4258 |
228.50 |
0.5037 |
| 0.4956 |
243.76 |
0.5043 |
| 0.5009 |
228.50 |
0.5251 |
| 0.5023 |
188.31 |
0.5829 |
| 0.5063 |
198.66 |
0.5661 |
| 0.5069 |
243.76 |
0.5100 |
| 0.5114 |
212.84 |
0.5422 |
| 0.5171 |
193.28 |
0.5785 |
| 0.5195 |
243.76 |
0.5147 |
| 0.5247 |
228.50 |
0.5317 |
| 0.5385 |
228.50 |
0.5349 |
| 0.5505 |
212.84 |
0.5498 |
| 0.5687 |
198.66 |
0.5714 |
| 0.5688 |
212.84 |
0.5551 |
| 0.5737 |
193.28 |
0.5806 |
| 0.5753 |
198.66 |
0.5720 |
| 0.5755 |
188.31 |
0.5844 |
| 0.5825 |
193.28 |
0.5811 |
| 0.5919 |
188.31 |
0.5862 |
| 0.6119 |
243.76 |
0.5537 |
| 0.6120 |
212.84 |
0.5644 |
| 0.6164 |
228.50 |
0.5586 |
| 0.6221 |
188.31 |
0.5872 |
| 0.6242 |
198.66 |
0.5768 |
| 0.6319 |
193.28 |
0.5851 |
| 0.7957 |
198.66 |
0.6128 |
| 0.7967 |
193.28 |
0.6089 |
| 0.7968 |
188.31 |
0.6069 |
| 0.8036 |
212.84 |
0.6274 |
| 0.8166 |
228.50 |
0.6460 |
| 0.8255 |
243.76 |
0.6730 |
| 1.0000 |
188.31 |
1.0000 |
| 1.0000 |
193.28 |
1.0000 |
| 1.0000 |
198.66 |
1.0000 |
| 1.0000 |
212.84 |
1.0000 |
| 1.0000 |
228.50 |
1.0000 |
| 1.0000 |
243.76 |
1.0000 |
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 |
188.31 |
85.40 |
| 0.0000 |
193.28 |
115.20 |
| 0.0000 |
198.66 |
153.30 |
| 0.0000 |
212.84 |
307.80 |
| 0.0000 |
228.50 |
591.50 |
| 0.0000 |
243.76 |
1028.00 |
| 0.0871 |
212.84 |
469.10 |
| 0.0941 |
198.66 |
273.50 |
| 0.1037 |
193.28 |
216.20 |
| 0.1182 |
243.76 |
1389.60 |
| 0.1208 |
228.50 |
864.10 |
| 0.1439 |
188.31 |
179.80 |
| 0.2468 |
212.84 |
546.10 |
| 0.2617 |
243.76 |
1548.10 |
| 0.2717 |
198.66 |
306.40 |
| 0.2774 |
188.31 |
189.90 |
| 0.2858 |
228.50 |
968.80 |
| 0.2861 |
193.28 |
241.20 |
| 0.3925 |
212.84 |
564.40 |
| 0.3936 |
188.31 |
191.40 |
| 0.3962 |
198.66 |
312.10 |
| 0.4022 |
193.28 |
244.10 |
| 0.4049 |
243.76 |
1609.50 |
| 0.4258 |
228.50 |
995.40 |
| 0.4956 |
243.76 |
1619.20 |
| 0.5009 |
228.50 |
1000.20 |
| 0.5023 |
188.31 |
191.50 |
| 0.5063 |
198.66 |
313.00 |
| 0.5069 |
243.76 |
1620.60 |
| 0.5114 |
212.84 |
568.50 |
| 0.5171 |
193.28 |
244.30 |
| 0.5195 |
243.76 |
1620.40 |
| 0.5247 |
228.50 |
1000.80 |
| 0.5385 |
228.50 |
1001.20 |
| 0.5505 |
212.84 |
568.90 |
| 0.5687 |
198.66 |
313.30 |
| 0.5688 |
212.84 |
568.70 |
| 0.5737 |
193.28 |
244.40 |
| 0.5753 |
198.66 |
313.30 |
| 0.5755 |
188.31 |
191.60 |
| 0.5825 |
193.28 |
244.50 |
| 0.5919 |
188.31 |
191.60 |
| 0.6119 |
243.76 |
1610.40 |
| 0.6120 |
212.84 |
566.50 |
| 0.6164 |
228.50 |
998.40 |
| 0.6221 |
188.31 |
191.40 |
| 0.6242 |
198.66 |
312.50 |
| 0.6319 |
193.28 |
244.10 |
| 0.7957 |
198.66 |
305.30 |
| 0.7967 |
193.28 |
239.70 |
| 0.7968 |
188.31 |
189.20 |
| 0.8036 |
212.84 |
544.60 |
| 0.8166 |
228.50 |
940.80 |
| 0.8255 |
243.76 |
1484.90 |
| 1.0000 |
188.31 |
123.80 |
| 1.0000 |
193.28 |
159.00 |
| 1.0000 |
198.66 |
204.70 |
| 1.0000 |
212.84 |
374.30 |
| 1.0000 |
228.50 |
665.40 |
| 1.0000 |
243.76 |
1084.00 |
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 |
188.31 |
85.40 |
| 0.0000 |
193.28 |
115.20 |
| 0.0000 |
198.66 |
153.30 |
| 0.0000 |
212.84 |
307.80 |
| 0.0000 |
228.50 |
591.50 |
| 0.0000 |
243.76 |
1028.00 |
| 0.0871 |
212.84 |
469.10 |
| 0.0941 |
198.66 |
273.50 |
| 0.1037 |
193.28 |
216.20 |
| 0.1182 |
243.76 |
1389.60 |
| 0.1208 |
228.50 |
864.10 |
| 0.1439 |
188.31 |
179.80 |
| 0.2468 |
212.84 |
546.10 |
| 0.2617 |
243.76 |
1548.10 |
| 0.2717 |
198.66 |
306.40 |
| 0.2774 |
188.31 |
189.90 |
| 0.2858 |
228.50 |
968.80 |
| 0.2861 |
193.28 |
241.20 |
| 0.3925 |
212.84 |
564.40 |
| 0.3936 |
188.31 |
191.40 |
| 0.3962 |
198.66 |
312.10 |
| 0.4022 |
193.28 |
244.10 |
| 0.4049 |
243.76 |
1609.50 |
| 0.4258 |
228.50 |
995.40 |
| 0.4956 |
243.76 |
1619.20 |
| 0.5009 |
228.50 |
1000.20 |
| 0.5023 |
188.31 |
191.50 |
| 0.5063 |
198.66 |
313.00 |
| 0.5069 |
243.76 |
1620.60 |
| 0.5114 |
212.84 |
568.50 |
| 0.5171 |
193.28 |
244.30 |
| 0.5195 |
243.76 |
1620.40 |
| 0.5247 |
228.50 |
1000.80 |
| 0.5385 |
228.50 |
1001.20 |
| 0.5505 |
212.84 |
568.90 |
| 0.5687 |
198.66 |
313.30 |
| 0.5688 |
212.84 |
568.70 |
| 0.5737 |
193.28 |
244.40 |
| 0.5753 |
198.66 |
313.30 |
| 0.5755 |
188.31 |
191.60 |
| 0.5825 |
193.28 |
244.50 |
| 0.5919 |
188.31 |
191.60 |
| 0.6119 |
243.76 |
1610.40 |
| 0.6120 |
212.84 |
566.50 |
| 0.6164 |
228.50 |
998.40 |
| 0.6221 |
188.31 |
191.40 |
| 0.6242 |
198.66 |
312.50 |
| 0.6319 |
193.28 |
244.10 |
| 0.7957 |
198.66 |
305.30 |
| 0.7967 |
193.28 |
239.70 |
| 0.7968 |
188.31 |
189.20 |
| 0.8036 |
212.84 |
544.60 |
| 0.8166 |
228.50 |
940.80 |
| 0.8255 |
243.76 |
1484.90 |
| 1.0000 |
188.31 |
123.80 |
| 1.0000 |
193.28 |
159.00 |
| 1.0000 |
198.66 |
204.70 |
| 1.0000 |
212.84 |
374.30 |
| 1.0000 |
228.50 |
665.40 |
| 1.0000 |
243.76 |
1084.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Ethane (1) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
| 173.86 |
0.0000 |
34.35 |
| 173.96 |
0.0076 |
42.75 |
| 174.00 |
0.0161 |
50.12 |
| 174.07 |
0.0289 |
58.20 |
| 174.02 |
0.0699 |
73.49 |
| 173.82 |
0.1296 |
82.97 |
| 173.88 |
0.9218 |
80.13 |
| 173.87 |
0.9366 |
78.30 |
| 173.88 |
0.9609 |
73.48 |
| 173.82 |
0.9829 |
65.84 |
| 173.63 |
1.0000 |
53.57 |
| 177.11 |
0.0000 |
41.46 |
| 177.20 |
0.0180 |
58.77 |
| 177.25 |
0.0568 |
79.89 |
| 177.27 |
0.0911 |
91.58 |
| 177.28 |
0.8723 |
100.97 |
| 177.29 |
0.9573 |
87.56 |
| 177.27 |
0.9744 |
80.29 |
| 177.24 |
1.0000 |
66.42 |
| 183.20 |
0.0000 |
62.29 |
| 183.19 |
0.0000 |
62.33 |
| 183.27 |
0.0273 |
90.74 |
| 183.28 |
0.0407 |
101.90 |
| 183.30 |
0.0948 |
127.28 |
| 183.34 |
0.2602 |
144.40 |
| 183.30 |
0.8853 |
139.97 |
| 183.32 |
0.9151 |
135.73 |
| 183.29 |
0.9435 |
126.09 |
| 183.30 |
0.9784 |
108.76 |
| 183.28 |
1.0000 |
94.31 |
| 228.83 |
0.0000 |
600.35 |
| 228.85 |
0.0150 |
651.63 |
| 228.94 |
0.0464 |
738.77 |
| 228.92 |
0.1193 |
862.24 |
| 228.91 |
0.2053 |
939.15 |
| 228.89 |
0.3465 |
993.90 |
| 228.94 |
0.3750 |
1001.08 |
| 228.94 |
0.7511 |
985.98 |
| 228.89 |
0.8956 |
889.01 |
| 228.91 |
0.9774 |
743.70 |
| 228.82 |
1.0000 |
673.93 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Gas |
| 173.56 |
80.59 |
| 177.20 |
101.11 |
| 177.20 |
101.20 |
| 179.63 |
116.87 |
| 182.72 |
139.54 |
| 183.26 |
143.85 |
| 184.76 |
156.08 |
| 186.22 |
168.93 |
Azeotropic pressure, kPa
[ref]
| Temperature, K - Liquid |
Azeotropic pressure, kPa - Liquid |
| 188.31 |
190.80 |
| 193.28 |
243.90 |
| 198.66 |
313.40 |
| 212.84 |
568.50 |
| 228.50 |
1003.10 |
| 243.76 |
1625.90 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Ethane (1) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
| 173.86 |
0.0000 |
34.35 |
| 173.96 |
0.0076 |
42.75 |
| 174.00 |
0.0161 |
50.12 |
| 174.07 |
0.0289 |
58.20 |
| 174.02 |
0.0699 |
73.49 |
| 173.82 |
0.1296 |
82.97 |
| 173.88 |
0.9218 |
80.13 |
| 173.87 |
0.9366 |
78.30 |
| 173.88 |
0.9609 |
73.48 |
| 173.82 |
0.9829 |
65.84 |
| 173.63 |
1.0000 |
53.57 |
| 177.11 |
0.0000 |
41.46 |
| 177.20 |
0.0180 |
58.77 |
| 177.25 |
0.0568 |
79.89 |
| 177.27 |
0.0911 |
91.58 |
| 177.28 |
0.8723 |
100.97 |
| 177.29 |
0.9573 |
87.56 |
| 177.27 |
0.9744 |
80.29 |
| 177.24 |
1.0000 |
66.42 |
| 183.20 |
0.0000 |
62.29 |
| 183.19 |
0.0000 |
62.33 |
| 183.27 |
0.0273 |
90.74 |
| 183.28 |
0.0407 |
101.90 |
| 183.30 |
0.0948 |
127.28 |
| 183.34 |
0.2602 |
144.40 |
| 183.30 |
0.8853 |
139.97 |
| 183.32 |
0.9151 |
135.73 |
| 183.29 |
0.9435 |
126.09 |
| 183.30 |
0.9784 |
108.76 |
| 183.28 |
1.0000 |
94.31 |
| 228.83 |
0.0000 |
600.35 |
| 228.85 |
0.0150 |
651.63 |
| 228.94 |
0.0464 |
738.77 |
| 228.92 |
0.1193 |
862.24 |
| 228.91 |
0.2053 |
939.15 |
| 228.89 |
0.3465 |
993.90 |
| 228.94 |
0.3750 |
1001.08 |
| 228.94 |
0.7511 |
985.98 |
| 228.89 |
0.8956 |
889.01 |
| 228.91 |
0.9774 |
743.70 |
| 228.82 |
1.0000 |
673.93 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Gas |
| 173.56 |
80.59 |
| 177.20 |
101.11 |
| 177.20 |
101.20 |
| 179.63 |
116.87 |
| 182.72 |
139.54 |
| 183.26 |
143.85 |
| 184.76 |
156.08 |
| 186.22 |
168.93 |
Azeotropic pressure, kPa
[ref]
| Temperature, K - Liquid |
Azeotropic pressure, kPa - Liquid |
| 188.31 |
190.80 |
| 193.28 |
243.90 |
| 198.66 |
313.40 |
| 212.84 |
568.50 |
| 228.50 |
1003.10 |
| 243.76 |
1625.90 |
Sources
