Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of o-Xylene (3) - Liquid mixture 1 | Mole fraction of Ethanol, 2,2'-oxybis- (2) - Liquid mixture 1 | Mole fraction of Ethanol, 2,2'-oxybis- (2) - Liquid mixture 2 | Mole fraction of o-Xylene (3) - Liquid mixture 2 |
288.15 | 0.0000 | 0.0004 | 0.9950 | 0.0000 |
288.15 | 0.1066 | 0.0012 | 0.9850 | 0.0100 |
288.15 | 0.1867 | 0.0010 | 0.9776 | 0.0175 |
288.15 | 0.3344 | 0.0015 | 0.9665 | 0.0290 |
288.15 | 0.4266 | 0.0020 | 0.9581 | 0.0373 |
288.15 | 0.4980 | 0.0023 | 0.9527 | 0.0431 |
288.15 | 0.5641 | 0.0028 | 0.9471 | 0.0490 |
298.15 | 0.0000 | 0.0024 | 0.9946 | 0.0000 |
298.15 | 0.1018 | 0.0030 | 0.9852 | 0.0097 |
298.15 | 0.1953 | 0.0038 | 0.9777 | 0.0174 |
298.15 | 0.3529 | 0.0044 | 0.9658 | 0.0297 |
298.15 | 0.4048 | 0.0049 | 0.9566 | 0.0385 |
298.15 | 0.5380 | 0.0052 | 0.9474 | 0.0479 |
298.15 | 0.5282 | 0.0054 | 0.9472 | 0.0475 |
298.15 | 0.5747 | 0.0053 | 0.9441 | 0.0515 |
308.15 | 0.0000 | 0.0048 | 0.9928 | 0.0000 |
308.15 | 0.0992 | 0.0053 | 0.9834 | 0.0098 |
308.15 | 0.1787 | 0.0058 | 0.9742 | 0.0183 |
308.15 | 0.3112 | 0.0061 | 0.9629 | 0.0302 |
308.15 | 0.3997 | 0.0081 | 0.9504 | 0.0422 |
308.15 | 0.4750 | 0.0088 | 0.9418 | 0.0509 |
318.15 | 0.0000 | 0.0051 | 0.9926 | 0.0000 |
318.15 | 0.1024 | 0.0065 | 0.9827 | 0.0097 |
318.15 | 0.1827 | 0.0053 | 0.9752 | 0.0175 |
318.15 | 0.3162 | 0.0055 | 0.9637 | 0.0293 |
318.15 | 0.4083 | 0.0060 | 0.9530 | 0.0400 |
318.15 | 0.4606 | 0.0060 | 0.9451 | 0.0480 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of o-Xylene (3) - Liquid mixture 1 | Mole fraction of Ethanol, 2,2'-oxybis- (2) - Liquid mixture 1 | Mole fraction of Ethanol, 2,2'-oxybis- (2) - Liquid mixture 2 | Mole fraction of o-Xylene (3) - Liquid mixture 2 |
288.15 | 0.0000 | 0.0004 | 0.9950 | 0.0000 |
288.15 | 0.1066 | 0.0012 | 0.9850 | 0.0100 |
288.15 | 0.1867 | 0.0010 | 0.9776 | 0.0175 |
288.15 | 0.3344 | 0.0015 | 0.9665 | 0.0290 |
288.15 | 0.4266 | 0.0020 | 0.9581 | 0.0373 |
288.15 | 0.4980 | 0.0023 | 0.9527 | 0.0431 |
288.15 | 0.5641 | 0.0028 | 0.9471 | 0.0490 |
298.15 | 0.0000 | 0.0024 | 0.9946 | 0.0000 |
298.15 | 0.1018 | 0.0030 | 0.9852 | 0.0097 |
298.15 | 0.1953 | 0.0038 | 0.9777 | 0.0174 |
298.15 | 0.3529 | 0.0044 | 0.9658 | 0.0297 |
298.15 | 0.4048 | 0.0049 | 0.9566 | 0.0385 |
298.15 | 0.5380 | 0.0052 | 0.9474 | 0.0479 |
298.15 | 0.5282 | 0.0054 | 0.9472 | 0.0475 |
298.15 | 0.5747 | 0.0053 | 0.9441 | 0.0515 |
308.15 | 0.0000 | 0.0048 | 0.9928 | 0.0000 |
308.15 | 0.0992 | 0.0053 | 0.9834 | 0.0098 |
308.15 | 0.1787 | 0.0058 | 0.9742 | 0.0183 |
308.15 | 0.3112 | 0.0061 | 0.9629 | 0.0302 |
308.15 | 0.3997 | 0.0081 | 0.9504 | 0.0422 |
308.15 | 0.4750 | 0.0088 | 0.9418 | 0.0509 |
318.15 | 0.0000 | 0.0051 | 0.9926 | 0.0000 |
318.15 | 0.1024 | 0.0065 | 0.9827 | 0.0097 |
318.15 | 0.1827 | 0.0053 | 0.9752 | 0.0175 |
318.15 | 0.3162 | 0.0055 | 0.9637 | 0.0293 |
318.15 | 0.4083 | 0.0060 | 0.9530 | 0.0400 |
318.15 | 0.4606 | 0.0060 | 0.9451 | 0.0480 |