Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Benzonitrile (1) - Liquid mixture 2 | Mole fraction of Benzonitrile (1) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 1 |
288.15 | 0.0268 | 0.9336 | 0.0041 | 0.9566 |
288.15 | 0.0371 | 0.8753 | 0.0065 | 0.9170 |
288.15 | 0.0521 | 0.8040 | 0.0118 | 0.8709 |
288.15 | 0.0689 | 0.7486 | 0.0143 | 0.8434 |
288.15 | 0.0805 | 0.6962 | 0.0215 | 0.8023 |
288.15 | 0.1006 | 0.6502 | 0.0251 | 0.7792 |
288.15 | 0.1236 | 0.5964 | 0.0312 | 0.7487 |
288.15 | 0.1426 | 0.5569 | 0.0366 | 0.7233 |
288.15 | 0.1737 | 0.4955 | 0.0427 | 0.6916 |
288.15 | 0.3020 | 0.3290 | 0.0750 | 0.6230 |
288.15 | 0.4897 | 0.1401 | 0.1401 | 0.4897 |
298.15 | 0.0495 | 0.9075 | 0.0055 | 0.9583 |
298.15 | 0.0652 | 0.8383 | 0.0092 | 0.9158 |
298.15 | 0.0795 | 0.7892 | 0.0123 | 0.8895 |
298.15 | 0.0901 | 0.7217 | 0.0172 | 0.8477 |
298.15 | 0.1006 | 0.6800 | 0.0215 | 0.8196 |
298.15 | 0.1162 | 0.6424 | 0.0263 | 0.7982 |
298.15 | 0.1373 | 0.5913 | 0.0323 | 0.7681 |
298.15 | 0.1924 | 0.4955 | 0.0454 | 0.7226 |
298.15 | 0.2125 | 0.4577 | 0.0508 | 0.6988 |
298.15 | 0.2711 | 0.3817 | 0.0649 | 0.6630 |
298.15 | 0.5270 | 0.1349 | 0.1349 | 0.5270 |
308.15 | 0.0799 | 0.8711 | 0.0073 | 0.9576 |
308.15 | 0.0875 | 0.8227 | 0.0099 | 0.9289 |
308.15 | 0.0968 | 0.7711 | 0.0128 | 0.9012 |
308.15 | 0.1049 | 0.7426 | 0.0154 | 0.8862 |
308.15 | 0.1152 | 0.6864 | 0.0199 | 0.8540 |
308.15 | 0.1524 | 0.5877 | 0.0318 | 0.8018 |
308.15 | 0.1948 | 0.5151 | 0.0411 | 0.7685 |
308.15 | 0.2306 | 0.4592 | 0.0520 | 0.7372 |
308.15 | 0.2601 | 0.4107 | 0.0564 | 0.7177 |
308.15 | 0.3356 | 0.3219 | 0.0651 | 0.6898 |
308.15 | 0.5599 | 0.1303 | 0.1303 | 0.5599 |
318.15 | 0.1006 | 0.8495 | 0.0097 | 0.9605 |
318.15 | 0.1007 | 0.8161 | 0.0125 | 0.9396 |
318.15 | 0.1120 | 0.7669 | 0.0149 | 0.9157 |
318.15 | 0.1211 | 0.7278 | 0.0181 | 0.8966 |
318.15 | 0.1250 | 0.7030 | 0.0204 | 0.8826 |
318.15 | 0.1448 | 0.6497 | 0.0251 | 0.8595 |
318.15 | 0.1752 | 0.5775 | 0.0294 | 0.8350 |
318.15 | 0.2007 | 0.5242 | 0.0377 | 0.8001 |
318.15 | 0.2650 | 0.4230 | 0.0522 | 0.7513 |
318.15 | 0.3249 | 0.3401 | 0.0675 | 0.7076 |
318.15 | 0.6008 | 0.1187 | 0.1187 | 0.6008 |
328.15 | 0.1176 | 0.8323 | 0.0102 | 0.9637 |
328.15 | 0.1221 | 0.7981 | 0.0128 | 0.9492 |
328.15 | 0.1322 | 0.7463 | 0.0165 | 0.9264 |
328.15 | 0.1479 | 0.6872 | 0.0205 | 0.9041 |
328.15 | 0.1641 | 0.6327 | 0.0248 | 0.8765 |
328.15 | 0.1848 | 0.5815 | 0.0282 | 0.8555 |
328.15 | 0.2181 | 0.5181 | 0.0351 | 0.8300 |
328.15 | 0.2478 | 0.4647 | 0.0401 | 0.8067 |
328.15 | 0.2816 | 0.4130 | 0.0502 | 0.7787 |
328.15 | 0.3429 | 0.3324 | 0.0598 | 0.7474 |
328.15 | 0.6354 | 0.1152 | 0.1152 | 0.6354 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Benzonitrile (1) - Liquid mixture 2 | Mole fraction of Benzonitrile (1) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 1 |
288.15 | 0.0268 | 0.9336 | 0.0041 | 0.9566 |
288.15 | 0.0371 | 0.8753 | 0.0065 | 0.9170 |
288.15 | 0.0521 | 0.8040 | 0.0118 | 0.8709 |
288.15 | 0.0689 | 0.7486 | 0.0143 | 0.8434 |
288.15 | 0.0805 | 0.6962 | 0.0215 | 0.8023 |
288.15 | 0.1006 | 0.6502 | 0.0251 | 0.7792 |
288.15 | 0.1236 | 0.5964 | 0.0312 | 0.7487 |
288.15 | 0.1426 | 0.5569 | 0.0366 | 0.7233 |
288.15 | 0.1737 | 0.4955 | 0.0427 | 0.6916 |
288.15 | 0.3020 | 0.3290 | 0.0750 | 0.6230 |
288.15 | 0.4897 | 0.1401 | 0.1401 | 0.4897 |
298.15 | 0.0495 | 0.9075 | 0.0055 | 0.9583 |
298.15 | 0.0652 | 0.8383 | 0.0092 | 0.9158 |
298.15 | 0.0795 | 0.7892 | 0.0123 | 0.8895 |
298.15 | 0.0901 | 0.7217 | 0.0172 | 0.8477 |
298.15 | 0.1006 | 0.6800 | 0.0215 | 0.8196 |
298.15 | 0.1162 | 0.6424 | 0.0263 | 0.7982 |
298.15 | 0.1373 | 0.5913 | 0.0323 | 0.7681 |
298.15 | 0.1924 | 0.4955 | 0.0454 | 0.7226 |
298.15 | 0.2125 | 0.4577 | 0.0508 | 0.6988 |
298.15 | 0.2711 | 0.3817 | 0.0649 | 0.6630 |
298.15 | 0.5270 | 0.1349 | 0.1349 | 0.5270 |
308.15 | 0.0799 | 0.8711 | 0.0073 | 0.9576 |
308.15 | 0.0875 | 0.8227 | 0.0099 | 0.9289 |
308.15 | 0.0968 | 0.7711 | 0.0128 | 0.9012 |
308.15 | 0.1049 | 0.7426 | 0.0154 | 0.8862 |
308.15 | 0.1152 | 0.6864 | 0.0199 | 0.8540 |
308.15 | 0.1524 | 0.5877 | 0.0318 | 0.8018 |
308.15 | 0.1948 | 0.5151 | 0.0411 | 0.7685 |
308.15 | 0.2306 | 0.4592 | 0.0520 | 0.7372 |
308.15 | 0.2601 | 0.4107 | 0.0564 | 0.7177 |
308.15 | 0.3356 | 0.3219 | 0.0651 | 0.6898 |
308.15 | 0.5599 | 0.1303 | 0.1303 | 0.5599 |
318.15 | 0.1006 | 0.8495 | 0.0097 | 0.9605 |
318.15 | 0.1007 | 0.8161 | 0.0125 | 0.9396 |
318.15 | 0.1120 | 0.7669 | 0.0149 | 0.9157 |
318.15 | 0.1211 | 0.7278 | 0.0181 | 0.8966 |
318.15 | 0.1250 | 0.7030 | 0.0204 | 0.8826 |
318.15 | 0.1448 | 0.6497 | 0.0251 | 0.8595 |
318.15 | 0.1752 | 0.5775 | 0.0294 | 0.8350 |
318.15 | 0.2007 | 0.5242 | 0.0377 | 0.8001 |
318.15 | 0.2650 | 0.4230 | 0.0522 | 0.7513 |
318.15 | 0.3249 | 0.3401 | 0.0675 | 0.7076 |
318.15 | 0.6008 | 0.1187 | 0.1187 | 0.6008 |
328.15 | 0.1176 | 0.8323 | 0.0102 | 0.9637 |
328.15 | 0.1221 | 0.7981 | 0.0128 | 0.9492 |
328.15 | 0.1322 | 0.7463 | 0.0165 | 0.9264 |
328.15 | 0.1479 | 0.6872 | 0.0205 | 0.9041 |
328.15 | 0.1641 | 0.6327 | 0.0248 | 0.8765 |
328.15 | 0.1848 | 0.5815 | 0.0282 | 0.8555 |
328.15 | 0.2181 | 0.5181 | 0.0351 | 0.8300 |
328.15 | 0.2478 | 0.4647 | 0.0401 | 0.8067 |
328.15 | 0.2816 | 0.4130 | 0.0502 | 0.7787 |
328.15 | 0.3429 | 0.3324 | 0.0598 | 0.7474 |
328.15 | 0.6354 | 0.1152 | 0.1152 | 0.6354 |