Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Methyl Alcohol (2) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Methyl Alcohol (2) - Liquid mixture 1 |
298.20 | 0.9995 | 0.0000 | 0.0030 | 0.0000 |
298.20 | 0.9406 | 0.0588 | 0.0038 | 0.0021 |
298.20 | 0.8845 | 0.1143 | 0.0040 | 0.0051 |
298.20 | 0.8475 | 0.1489 | 0.0088 | 0.0120 |
298.20 | 0.7535 | 0.2431 | 0.0098 | 0.0272 |
298.20 | 0.6957 | 0.3004 | 0.0117 | 0.0362 |
298.20 | 0.6522 | 0.3473 | 0.0121 | 0.0408 |
298.20 | 0.4760 | 0.5221 | 0.0279 | 0.1135 |
308.20 | 0.9995 | 0.0000 | 0.0082 | 0.0000 |
308.20 | 0.9427 | 0.0570 | 0.0090 | 0.0056 |
308.20 | 0.8849 | 0.1148 | 0.0091 | 0.0125 |
308.20 | 0.8566 | 0.1431 | 0.0101 | 0.0155 |
308.20 | 0.7479 | 0.2514 | 0.0115 | 0.0343 |
308.20 | 0.6987 | 0.3003 | 0.0129 | 0.0432 |
308.20 | 0.6508 | 0.3477 | 0.0158 | 0.0551 |
308.20 | 0.4760 | 0.5221 | 0.0176 | 0.1145 |
318.20 | 0.9994 | 0.0000 | 0.0201 | 0.0000 |
318.20 | 0.9451 | 0.0539 | 0.0205 | 0.0107 |
318.20 | 0.8874 | 0.1123 | 0.0215 | 0.0250 |
318.20 | 0.8509 | 0.1476 | 0.0226 | 0.0320 |
318.20 | 0.7957 | 0.2035 | 0.0255 | 0.0506 |
318.20 | 0.6526 | 0.3460 | 0.0340 | 0.1015 |
318.20 | 0.5355 | 0.4629 | 0.0434 | 0.1666 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Methyl Alcohol (2) - Liquid mixture 1 | Mole fraction of 9,12-Octadecadienoic acid (Z,Z)-, methyl ester (1) - Liquid mixture 1 |
298.20 | 0.6657 | 0.0011 |
298.20 | 0.7270 | 0.0016 |
298.20 | 0.7487 | 0.0018 |
298.20 | 0.7677 | 0.0023 |
298.20 | 0.7878 | 0.0035 |
298.20 | 0.8117 | 0.0037 |
298.20 | 0.8695 | 0.0079 |
298.20 | 0.9028 | 0.0148 |
298.20 | 0.9131 | 0.0199 |
298.20 | 0.9142 | 0.0230 |
298.20 | 0.9144 | 0.0167 |
308.20 | 0.0738 | 0.8998 |
308.20 | 0.6887 | 0.0011 |
308.20 | 0.7669 | 0.0029 |
308.20 | 0.8505 | 0.0087 |
308.20 | 0.8817 | 0.0820 |
308.20 | 0.8874 | 0.0172 |
308.20 | 0.8880 | 0.0595 |
308.20 | 0.8989 | 0.0416 |
318.20 | 0.4953 | 0.4427 |
318.20 | 0.6734 | 0.0011 |
318.20 | 0.7387 | 0.0025 |
318.20 | 0.8475 | 0.0090 |
318.20 | 0.8571 | 0.0826 |
318.20 | 0.8719 | 0.0196 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Methyl Alcohol (2) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Methyl Alcohol (2) - Liquid mixture 1 |
298.20 | 0.9995 | 0.0000 | 0.0030 | 0.0000 |
298.20 | 0.9406 | 0.0588 | 0.0038 | 0.0021 |
298.20 | 0.8845 | 0.1143 | 0.0040 | 0.0051 |
298.20 | 0.8475 | 0.1489 | 0.0088 | 0.0120 |
298.20 | 0.7535 | 0.2431 | 0.0098 | 0.0272 |
298.20 | 0.6957 | 0.3004 | 0.0117 | 0.0362 |
298.20 | 0.6522 | 0.3473 | 0.0121 | 0.0408 |
298.20 | 0.4760 | 0.5221 | 0.0279 | 0.1135 |
308.20 | 0.9995 | 0.0000 | 0.0082 | 0.0000 |
308.20 | 0.9427 | 0.0570 | 0.0090 | 0.0056 |
308.20 | 0.8849 | 0.1148 | 0.0091 | 0.0125 |
308.20 | 0.8566 | 0.1431 | 0.0101 | 0.0155 |
308.20 | 0.7479 | 0.2514 | 0.0115 | 0.0343 |
308.20 | 0.6987 | 0.3003 | 0.0129 | 0.0432 |
308.20 | 0.6508 | 0.3477 | 0.0158 | 0.0551 |
308.20 | 0.4760 | 0.5221 | 0.0176 | 0.1145 |
318.20 | 0.9994 | 0.0000 | 0.0201 | 0.0000 |
318.20 | 0.9451 | 0.0539 | 0.0205 | 0.0107 |
318.20 | 0.8874 | 0.1123 | 0.0215 | 0.0250 |
318.20 | 0.8509 | 0.1476 | 0.0226 | 0.0320 |
318.20 | 0.7957 | 0.2035 | 0.0255 | 0.0506 |
318.20 | 0.6526 | 0.3460 | 0.0340 | 0.1015 |
318.20 | 0.5355 | 0.4629 | 0.0434 | 0.1666 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Methyl Alcohol (2) - Liquid mixture 1 | Mole fraction of 9,12-Octadecadienoic acid (Z,Z)-, methyl ester (1) - Liquid mixture 1 |
298.20 | 0.6657 | 0.0011 |
298.20 | 0.7270 | 0.0016 |
298.20 | 0.7487 | 0.0018 |
298.20 | 0.7677 | 0.0023 |
298.20 | 0.7878 | 0.0035 |
298.20 | 0.8117 | 0.0037 |
298.20 | 0.8695 | 0.0079 |
298.20 | 0.9028 | 0.0148 |
298.20 | 0.9131 | 0.0199 |
298.20 | 0.9142 | 0.0230 |
298.20 | 0.9144 | 0.0167 |
308.20 | 0.0738 | 0.8998 |
308.20 | 0.6887 | 0.0011 |
308.20 | 0.7669 | 0.0029 |
308.20 | 0.8505 | 0.0087 |
308.20 | 0.8817 | 0.0820 |
308.20 | 0.8874 | 0.0172 |
308.20 | 0.8880 | 0.0595 |
308.20 | 0.8989 | 0.0416 |
318.20 | 0.4953 | 0.4427 |
318.20 | 0.6734 | 0.0011 |
318.20 | 0.7387 | 0.0025 |
318.20 | 0.8475 | 0.0090 |
318.20 | 0.8571 | 0.0826 |
318.20 | 0.8719 | 0.0196 |