Operational conditions:
Mole fraction of Isopropyl Alcohol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0095 | -0.0559 |
0.0169 | -0.1105 |
0.0243 | -0.1634 |
0.0315 | -0.2156 |
0.0386 | -0.2659 |
0.0456 | -0.3152 |
0.0526 | -0.3634 |
0.0594 | -0.4119 |
0.0661 | -0.4592 |
0.0727 | -0.5054 |
0.0793 | -0.5504 |
0.0857 | -0.5950 |
0.0921 | -0.6386 |
0.0983 | -0.6811 |
0.1045 | -0.7233 |
0.1106 | -0.7643 |
0.1166 | -0.8049 |
0.1225 | -0.8451 |
0.1284 | -0.8840 |
0.1342 | -0.9217 |
0.1413 | -0.9633 |
0.1469 | -0.9987 |
0.1524 | -1.0372 |
0.1579 | -1.0732 |
0.1633 | -1.1054 |
0.1686 | -1.1394 |
0.1738 | -1.1764 |
0.1790 | -1.205 |
0.1842 | -1.2375 |
0.1892 | -1.2692 |
0.1942 | -1.3004 |
0.1992 | -1.3306 |
0.2040 | -1.3601 |
0.2088 | -1.3896 |
0.2136 | -1.4178 |
0.2183 | -1.4458 |
0.2230 | -1.4731 |
0.2276 | -1.5003 |
0.2321 | -1.5266 |
0.2366 | -1.5518 |
0.2421 | -1.5742 |
0.2465 | -1.5995 |
0.2508 | -1.6235 |
0.2551 | -1.6475 |
0.2593 | -1.6702 |
0.2635 | -1.6931 |
0.2676 | -1.7155 |
0.2717 | -1.7377 |
0.2757 | -1.7595 |
0.2797 | -1.7789 |
0.2837 | -1.8002 |
0.2876 | -1.8131 |
0.2914 | -1.8339 |
0.2952 | -1.8541 |
0.3028 | -1.8888 |
0.3065 | -1.9052 |
0.3131 | -1.9359 |
0.3192 | -1.9632 |
0.3253 | -1.9906 |
0.3312 | -2.0138 |
0.3371 | -2.0402 |
0.3428 | -2.0609 |
0.3485 | -2.0807 |
0.3540 | -2.1004 |
0.3595 | -2.1191 |
0.3648 | -2.1373 |
0.3701 | -2.1547 |
0.3753 | -2.1712 |
0.3804 | -2.1893 |
0.3854 | -2.2079 |
0.3903 | -2.2237 |
0.3952 | -2.2426 |
0.4000 | -2.2564 |
0.4047 | -2.2699 |
0.4093 | -2.2832 |
0.4139 | -2.2961 |
0.4228 | -2.3212 |
0.4315 | -2.3446 |
0.4398 | -2.3659 |
0.4480 | -2.3857 |
0.4559 | -2.3984 |
0.4636 | -2.4188 |
0.4711 | -2.4294 |
0.4784 | -2.4454 |
0.4854 | -2.4564 |
0.4923 | -2.4651 |
0.4990 | -2.4757 |
0.5055 | -2.4849 |
0.5104 | -2.4935 |
0.5119 | -2.4932 |
0.5181 | -2.5006 |
0.5242 | -2.5073 |
0.5280 | -2.5109 |
0.5300 | -2.5132 |
0.5358 | -2.5181 |
0.5414 | -2.5226 |
0.5445 | -2.5244 |
0.5469 | -2.5264 |
0.5522 | -2.5292 |
0.5575 | -2.5314 |
0.5598 | -2.5293 |
0.5626 | -2.5331 |
0.5675 | -2.5301 |
0.5742 | -2.5294 |
0.5876 | -2.5271 |
0.6002 | -2.5211 |
0.6121 | -2.5118 |
0.6233 | -2.4992 |
0.6338 | -2.4841 |
0.6438 | -2.468 |
0.6533 | -2.4501 |
0.6622 | -2.4359 |
0.6707 | -2.4157 |
0.6788 | -2.3993 |
0.6865 | -2.3769 |
0.6939 | -2.3542 |
0.7009 | -2.3312 |
0.7076 | -2.3079 |
0.7140 | -2.2893 |
0.7201 | -2.2706 |
0.7260 | -2.2467 |
0.7316 | -2.2228 |
0.7422 | -2.1852 |
0.7678 | -2.0694 |
0.7854 | -1.9794 |
0.8005 | -1.9023 |
0.8135 | -1.8285 |
0.8250 | -1.7593 |
0.8352 | -1.6931 |
0.8442 | -1.6304 |
0.8523 | -1.5707 |
0.8596 | -1.5144 |
0.8778 | -1.3785 |
0.8815 | -1.3471 |
0.8852 | -1.3168 |
0.8890 | -1.2852 |
0.8928 | -1.2506 |
0.9005 | -1.1785 |
0.9045 | -1.1443 |
0.9084 | -1.1027 |
0.9125 | -1.0656 |
0.9164 | -1.0222 |
0.9204 | -0.9778 |
0.9245 | -0.9373 |
0.9287 | -0.8894 |
0.9287 | -0.8894 |
0.9328 | -0.8488 |
0.9328 | -0.8488 |
0.9370 | -0.7999 |
0.9412 | -0.7566 |
0.9455 | -0.7086 |
0.9498 | -0.6584 |
0.9542 | -0.6069 |
0.9586 | -0.5544 |
0.9630 | -0.4991 |
0.9675 | -0.4435 |
0.9720 | -0.3855 |
0.9766 | -0.3268 |
0.9812 | -0.2614 |
0.9858 | -0.1948 |
0.9905 | -0.1315 |
0.9952 | -0.0667 |
Operational conditions:
Mole fraction of Isopropyl Alcohol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0095 | -0.0559 |
0.0169 | -0.1105 |
0.0243 | -0.1634 |
0.0315 | -0.2156 |
0.0386 | -0.2659 |
0.0456 | -0.3152 |
0.0526 | -0.3634 |
0.0594 | -0.4119 |
0.0661 | -0.4592 |
0.0727 | -0.5054 |
0.0793 | -0.5504 |
0.0857 | -0.5950 |
0.0921 | -0.6386 |
0.0983 | -0.6811 |
0.1045 | -0.7233 |
0.1106 | -0.7643 |
0.1166 | -0.8049 |
0.1225 | -0.8451 |
0.1284 | -0.8840 |
0.1342 | -0.9217 |
0.1413 | -0.9633 |
0.1469 | -0.9987 |
0.1524 | -1.0372 |
0.1579 | -1.0732 |
0.1633 | -1.1054 |
0.1686 | -1.1394 |
0.1738 | -1.1764 |
0.1790 | -1.205 |
0.1842 | -1.2375 |
0.1892 | -1.2692 |
0.1942 | -1.3004 |
0.1992 | -1.3306 |
0.2040 | -1.3601 |
0.2088 | -1.3896 |
0.2136 | -1.4178 |
0.2183 | -1.4458 |
0.2230 | -1.4731 |
0.2276 | -1.5003 |
0.2321 | -1.5266 |
0.2366 | -1.5518 |
0.2421 | -1.5742 |
0.2465 | -1.5995 |
0.2508 | -1.6235 |
0.2551 | -1.6475 |
0.2593 | -1.6702 |
0.2635 | -1.6931 |
0.2676 | -1.7155 |
0.2717 | -1.7377 |
0.2757 | -1.7595 |
0.2797 | -1.7789 |
0.2837 | -1.8002 |
0.2876 | -1.8131 |
0.2914 | -1.8339 |
0.2952 | -1.8541 |
0.3028 | -1.8888 |
0.3065 | -1.9052 |
0.3131 | -1.9359 |
0.3192 | -1.9632 |
0.3253 | -1.9906 |
0.3312 | -2.0138 |
0.3371 | -2.0402 |
0.3428 | -2.0609 |
0.3485 | -2.0807 |
0.3540 | -2.1004 |
0.3595 | -2.1191 |
0.3648 | -2.1373 |
0.3701 | -2.1547 |
0.3753 | -2.1712 |
0.3804 | -2.1893 |
0.3854 | -2.2079 |
0.3903 | -2.2237 |
0.3952 | -2.2426 |
0.4000 | -2.2564 |
0.4047 | -2.2699 |
0.4093 | -2.2832 |
0.4139 | -2.2961 |
0.4228 | -2.3212 |
0.4315 | -2.3446 |
0.4398 | -2.3659 |
0.4480 | -2.3857 |
0.4559 | -2.3984 |
0.4636 | -2.4188 |
0.4711 | -2.4294 |
0.4784 | -2.4454 |
0.4854 | -2.4564 |
0.4923 | -2.4651 |
0.4990 | -2.4757 |
0.5055 | -2.4849 |
0.5104 | -2.4935 |
0.5119 | -2.4932 |
0.5181 | -2.5006 |
0.5242 | -2.5073 |
0.5280 | -2.5109 |
0.5300 | -2.5132 |
0.5358 | -2.5181 |
0.5414 | -2.5226 |
0.5445 | -2.5244 |
0.5469 | -2.5264 |
0.5522 | -2.5292 |
0.5575 | -2.5314 |
0.5598 | -2.5293 |
0.5626 | -2.5331 |
0.5675 | -2.5301 |
0.5742 | -2.5294 |
0.5876 | -2.5271 |
0.6002 | -2.5211 |
0.6121 | -2.5118 |
0.6233 | -2.4992 |
0.6338 | -2.4841 |
0.6438 | -2.468 |
0.6533 | -2.4501 |
0.6622 | -2.4359 |
0.6707 | -2.4157 |
0.6788 | -2.3993 |
0.6865 | -2.3769 |
0.6939 | -2.3542 |
0.7009 | -2.3312 |
0.7076 | -2.3079 |
0.7140 | -2.2893 |
0.7201 | -2.2706 |
0.7260 | -2.2467 |
0.7316 | -2.2228 |
0.7422 | -2.1852 |
0.7678 | -2.0694 |
0.7854 | -1.9794 |
0.8005 | -1.9023 |
0.8135 | -1.8285 |
0.8250 | -1.7593 |
0.8352 | -1.6931 |
0.8442 | -1.6304 |
0.8523 | -1.5707 |
0.8596 | -1.5144 |
0.8778 | -1.3785 |
0.8815 | -1.3471 |
0.8852 | -1.3168 |
0.8890 | -1.2852 |
0.8928 | -1.2506 |
0.9005 | -1.1785 |
0.9045 | -1.1443 |
0.9084 | -1.1027 |
0.9125 | -1.0656 |
0.9164 | -1.0222 |
0.9204 | -0.9778 |
0.9245 | -0.9373 |
0.9287 | -0.8894 |
0.9287 | -0.8894 |
0.9328 | -0.8488 |
0.9328 | -0.8488 |
0.9370 | -0.7999 |
0.9412 | -0.7566 |
0.9455 | -0.7086 |
0.9498 | -0.6584 |
0.9542 | -0.6069 |
0.9586 | -0.5544 |
0.9630 | -0.4991 |
0.9675 | -0.4435 |
0.9720 | -0.3855 |
0.9766 | -0.3268 |
0.9812 | -0.2614 |
0.9858 | -0.1948 |
0.9905 | -0.1315 |
0.9952 | -0.0667 |