Datasets
-
Temperature, K x Mole fraction (8)
-
Azeotropic temperature, K (2)
Temperature, K x Mole fraction
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 2 |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 1 |
Mole fraction of Isopropyl Alcohol (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 |
Temperature, K x Mass fraction
[ref]
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 |
Mole fraction of Isopropyl Alcohol (1)
[ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid mixture 1)
- Pressure, kPa = 100 (Liquid mixture 1)
Mole fraction of Isopropyl acetate (2) - Liquid mixture 1 |
Mole fraction of Isopropyl Alcohol (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 |
Mole fraction
[ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid mixture 1)
- Pressure, kPa = 100 (Liquid mixture 2)
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 2 |
Mole fraction of Isopropyl acetate (2) - Liquid mixture 2 |
Mole fraction of Isopropyl Alcohol (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 |
Temperature, K x Mole fraction
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 2 |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 1 |
Mole fraction of Isopropyl Alcohol (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 |
Temperature, K x Mass fraction
[ref]
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 |
Mole fraction of Isopropyl Alcohol (1)
[ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid mixture 1)
- Pressure, kPa = 100 (Liquid mixture 1)
Mole fraction of Isopropyl acetate (2) - Liquid mixture 1 |
Mole fraction of Isopropyl Alcohol (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 |
Mole fraction
[ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid mixture 1)
- Pressure, kPa = 100 (Liquid mixture 2)
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 2 |
Mole fraction of Isopropyl acetate (2) - Liquid mixture 2 |
Mole fraction of Isopropyl Alcohol (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 |
Azeotropic temperature, K
[ref]
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Mole fraction of Water (3) - Liquid |
Azeotropic temperature, K - Liquid |
0.0922 |
0.4010 |
349.20 |
Azeotropic temperature, K
[ref]
Fixed |
Measured |
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Mole fraction of Water (3) - Liquid |
Azeotropic temperature, K - Liquid |
0.0922 |
0.4010 |
349.20 |
Sources