Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Fixed | Measured | |||||
|---|---|---|---|---|---|---|
| Temperature, K - Liquid mixture 1 | Mole fraction of 2-Propanol (1) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of 2-Propanol (1) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of 2-Propanol (1) - Gas | Mole fraction of Water (3) - Gas |
| 350.40 | 0.1007 | 0.8889 | 0.2910 | 0.5365 | 0.1900 | 0.3783 |
| 350.30 | 0.0725 | 0.9127 | 0.2742 | 0.4821 | 0.1810 | 0.3803 |
| 350.20 | 0.0613 | 0.9229 | 0.2517 | 0.4352 | 0.1688 | 0.3864 |
| 350.00 | 0.0557 | 0.9258 | 0.2295 | 0.4024 | 0.1565 | 0.3873 |
| 349.90 | 0.0557 | 0.9306 | 0.2070 | 0.3652 | 0.1412 | 0.3922 |
| 349.80 | 0.0500 | 0.9334 | 0.1845 | 0.3355 | 0.1320 | 0.3943 |
| 349.60 | 0.0444 | 0.9509 | 0.1623 | 0.2981 | 0.1229 | 0.3935 |
| 349.40 | 0.0332 | 0.9542 | 0.1397 | 0.2850 | 0.1166 | 0.3940 |
| 349.30 | 0.0278 | 0.9543 | 0.1274 | 0.2702 | 0.0983 | 0.3954 |
| 349.20 | 0.0278 | 0.9663 | 0.1060 | 0.2632 | 0.0922 | 0.4010 |
| 349.10 | 0.0222 | 0.9740 | 0.0894 | 0.2373 | 0.0830 | 0.3990 |
| 348.90 | 0.0136 | 0.9760 | 0.0557 | 0.2350 | 0.0585 | 0.4059 |
| 348.80 | 0.0166 | 0.9768 | 0.0278 | 0.2245 | 0.0341 | 0.4101 |
| 348.60 | 0.0053 | 0.9776 | 0.0110 | 0.2184 | 0.0188 | 0.4112 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
| Fixed | Measured | |||
|---|---|---|---|---|
| Temperature, K - Liquid mixture 2 | Mass fraction of Water (3) - Liquid mixture 1 | Mass fraction of Isopropyl acetate (2) - Liquid mixture 1 | Mass fraction of Water (3) - Liquid mixture 2 | Mass fraction of Isopropyl acetate (2) - Liquid mixture 2 |
| 298.15 | 0.9729 | 0.0271 | 0.0168 | 0.9832 |
| 298.15 | 0.9402 | 0.0328 | 0.0397 | 0.9395 |
| 298.15 | 0.9165 | 0.0337 | 0.0515 | 0.9047 |
| 298.15 | 0.8937 | 0.0341 | 0.0576 | 0.8735 |
| 298.15 | 0.8607 | 0.0371 | 0.0629 | 0.8151 |
| 298.15 | 0.8466 | 0.0392 | 0.0673 | 0.7848 |
| 298.15 | 0.8355 | 0.0384 | 0.0757 | 0.7511 |
| 298.15 | 0.8242 | 0.0380 | 0.0846 | 0.7180 |
| 298.15 | 0.8134 | 0.0394 | 0.0963 | 0.6842 |
| 303.15 | 0.9742 | 0.0258 | 0.0176 | 0.9824 |
| 303.15 | 0.9255 | 0.0480 | 0.0291 | 0.9464 |
| 303.15 | 0.9043 | 0.0462 | 0.0322 | 0.9175 |
| 303.15 | 0.8870 | 0.0439 | 0.0402 | 0.8832 |
| 303.15 | 0.8656 | 0.0492 | 0.0529 | 0.8428 |
| 303.15 | 0.8542 | 0.0462 | 0.0611 | 0.8067 |
| 303.15 | 0.8387 | 0.0505 | 0.0734 | 0.7681 |
| 303.15 | 0.8309 | 0.0470 | 0.0856 | 0.7294 |
| 303.15 | 0.8112 | 0.0488 | 0.1110 | 0.6573 |
| 308.15 | 0.9767 | 0.0233 | 0.0209 | 0.9791 |
| 308.15 | 0.9436 | 0.0324 | 0.0253 | 0.9518 |
| 308.15 | 0.9151 | 0.0412 | 0.0378 | 0.9135 |
| 308.15 | 0.8971 | 0.0415 | 0.0469 | 0.8779 |
| 308.15 | 0.8573 | 0.0413 | 0.0742 | 0.7721 |
| 308.15 | 0.8448 | 0.0426 | 0.0828 | 0.7374 |
| 308.15 | 0.8404 | 0.0384 | 0.0909 | 0.7043 |
| 308.15 | 0.8252 | 0.0436 | 0.1058 | 0.6674 |
| 308.15 | 0.8129 | 0.0480 | 0.1151 | 0.6378 |
| 313.15 | 0.9779 | 0.0221 | 0.0228 | 0.9772 |
| 313.15 | 0.9303 | 0.0470 | 0.0324 | 0.9407 |
| 313.15 | 0.9067 | 0.0502 | 0.0408 | 0.9039 |
| 313.15 | 0.8891 | 0.0502 | 0.0541 | 0.8617 |
| 313.15 | 0.8699 | 0.0540 | 0.0623 | 0.8241 |
| 313.15 | 0.8555 | 0.0554 | 0.0765 | 0.7805 |
| 313.15 | 0.8474 | 0.0519 | 0.0895 | 0.7398 |
| 313.15 | 0.8314 | 0.0572 | 0.1043 | 0.6985 |
| 313.15 | 0.8188 | 0.0601 | 0.1205 | 0.6578 |
| 318.15 | 0.9782 | 0.0218 | 0.0232 | 0.9768 |
| 318.15 | 0.9353 | 0.0432 | 0.0294 | 0.9438 |
| 318.15 | 0.9161 | 0.0431 | 0.0353 | 0.9099 |
| 318.15 | 0.8780 | 0.0496 | 0.0495 | 0.8280 |
| 318.15 | 0.8635 | 0.0523 | 0.0634 | 0.7951 |
| 318.15 | 0.8541 | 0.0504 | 0.0779 | 0.7534 |
| 318.15 | 0.8452 | 0.0491 | 0.0873 | 0.7180 |
| 318.15 | 0.8375 | 0.0483 | 0.0993 | 0.6818 |
| 318.15 | 0.8232 | 0.0535 | 0.1119 | 0.6472 |
| 323.15 | 0.9789 | 0.0211 | 0.0254 | 0.9746 |
| 323.15 | 0.9407 | 0.0369 | 0.0367 | 0.9331 |
| 323.15 | 0.9150 | 0.0420 | 0.0448 | 0.8966 |
| 323.15 | 0.8928 | 0.0454 | 0.0506 | 0.8624 |
| 323.15 | 0.8781 | 0.0491 | 0.0576 | 0.8243 |
| 323.15 | 0.8647 | 0.0499 | 0.0684 | 0.7904 |
| 323.15 | 0.8329 | 0.0533 | 0.0852 | 0.7401 |
| 323.15 | 0.8226 | 0.0533 | 0.0922 | 0.7071 |
| 323.15 | 0.8085 | 0.0593 | 0.1106 | 0.6629 |
Operational conditions:
| Mole fraction of Isopropyl acetate (2) - Liquid mixture 1 | Mole fraction of 2-Propanol (1) - Liquid mixture 1 |
|---|---|
| 0.0052 | 0.0430 |
| 0.0161 | 0.0869 |
| 0.0259 | 0.1055 |
| 0.0359 | 0.1192 |
| 0.0459 | 0.1335 |
| 0.0616 | 0.1546 |
| 0.0777 | 0.1730 |
| 0.1040 | 0.1997 |
| 0.0963 | 0.1923 |
| 0.1284 | 0.2180 |
| 0.1905 | 0.2498 |
| 0.2753 | 0.2588 |
Operational conditions:
| Fixed | Measured | ||
|---|---|---|---|
| Mole fraction of 2-Propanol (1) - Liquid mixture 2 | Mole fraction of Isopropyl acetate (2) - Liquid mixture 2 | Mole fraction of 2-Propanol (1) - Liquid mixture 1 | Mole fraction of Isopropyl acetate (2) - Liquid mixture 1 |
| 0.0000 | 0.0031 | 0.0000 | 0.8822 |
| 0.0157 | 0.0031 | 0.1044 | 0.7072 |
| 0.0327 | 0.0035 | 0.1940 | 0.5456 |
| 0.0320 | 0.0042 | 0.2161 | 0.4881 |
| 0.0396 | 0.0056 | 0.2364 | 0.4070 |
| 0.0446 | 0.0058 | 0.2363 | 0.3270 |
| Fixed | Measured | |
|---|---|---|
| Mole fraction of 2-Propanol (1) - Liquid | Mole fraction of Water (3) - Liquid | Azeotropic temperature, K - Liquid |
| 0.0922 | 0.4010 | 349.20 |
Note: These property values are available through the Cheméo API. A free account gives you an access key.