Operational conditions:
Mole fraction of 1-Propanol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0101 | -0.0873 |
0.0201 | -0.1720 |
0.0298 | -0.2544 |
0.0394 | -0.3340 |
0.0487 | -0.4112 |
0.0579 | -0.4862 |
0.0669 | -0.5559 |
0.0758 | -0.6294 |
0.0844 | -0.6975 |
0.0930 | -0.7638 |
0.1013 | -0.8288 |
0.1095 | -0.8923 |
0.1176 | -0.9550 |
0.1255 | -1.0158 |
0.1332 | -1.0758 |
0.1409 | -1.1348 |
0.1484 | -1.1922 |
0.1557 | -1.249 |
0.1630 | -1.3043 |
0.1701 | -1.3583 |
0.1771 | -1.4056 |
0.1840 | -1.452 |
0.1908 | -1.4974 |
0.1974 | -1.5419 |
0.2040 | -1.5855 |
0.2104 | -1.6331 |
0.2167 | -1.6797 |
0.2230 | -1.7204 |
0.2291 | -1.7607 |
0.2320 | -1.7867 |
0.2352 | -1.8051 |
0.2385 | -1.8272 |
0.2454 | -1.8849 |
0.2470 | -1.8864 |
0.2527 | -1.9233 |
0.2603 | -1.9874 |
0.2685 | -2.0326 |
0.2772 | -2.1006 |
0.2865 | -2.1615 |
0.2964 | -2.2255 |
0.3071 | -2.2928 |
0.3185 | -2.3634 |
0.3309 | -2.4376 |
0.3442 | -2.5152 |
0.3586 | -2.5964 |
0.3743 | -2.687 |
0.3915 | -2.7767 |
0.3960 | -2.7992 |
0.4006 | -2.8218 |
0.4053 | -2.8446 |
0.4102 | -2.8674 |
0.4151 | -2.8902 |
0.4202 | -2.9122 |
0.4254 | -2.9359 |
0.4307 | -2.9636 |
0.4362 | -2.9884 |
0.4418 | -3.0142 |
0.4476 | -3.0366 |
0.4535 | -3.0589 |
0.4595 | -3.0809 |
0.4657 | -3.1026 |
0.4721 | -3.1242 |
0.4787 | -3.1455 |
0.4855 | -3.1661 |
0.4924 | -3.1896 |
0.4996 | -3.2151 |
0.5069 | -3.2323 |
0.5145 | -3.2514 |
0.5223 | -3.2736 |
0.5304 | -3.2887 |
0.5339 | -3.3028 |
0.5387 | -3.3131 |
0.5394 | -3.3129 |
0.5451 | -3.327 |
0.5509 | -3.3306 |
0.5568 | -3.3361 |
0.5628 | -3.3407 |
0.5690 | -3.3492 |
0.5753 | -3.3567 |
0.5817 | -3.3653 |
0.5883 | -3.3628 |
0.5950 | -3.3675 |
0.6019 | -3.3656 |
0.6090 | -3.3641 |
0.6162 | -3.3623 |
0.6236 | -3.3585 |
0.6312 | -3.3523 |
0.6389 | -3.3435 |
0.6469 | -3.3321 |
0.6550 | -3.3127 |
0.6634 | -3.291 |
0.6719 | -3.2692 |
0.6808 | -3.2424 |
0.6852 | -3.2296 |
0.6898 | -3.2144 |
0.6944 | -3.1979 |
0.6991 | -3.1803 |
0.7038 | -3.1609 |
0.7086 | -3.1402 |
0.7135 | -3.1183 |
0.7184 | -3.0945 |
0.7234 | -3.0695 |
0.7285 | -3.0429 |
0.7336 | -3.0144 |
0.7388 | -2.9846 |
0.7441 | -2.9528 |
0.7495 | -2.9188 |
0.7549 | -2.8878 |
0.7604 | -2.8503 |
0.7660 | -2.8153 |
0.7671 | -2.8049 |
0.7698 | -2.7859 |
0.7717 | -2.7735 |
0.7725 | -2.7668 |
0.7753 | -2.7468 |
0.7775 | -2.7293 |
0.7780 | -2.7259 |
0.7808 | -2.7058 |
0.7836 | -2.6839 |
0.7864 | -2.6624 |
0.7892 | -2.6394 |
0.7920 | -2.6163 |
0.7949 | -2.5934 |
0.7978 | -2.5686 |
0.8007 | -2.5441 |
0.8036 | -2.5184 |
0.8066 | -2.492 |
0.8096 | -2.4648 |
0.8125 | -2.4368 |
0.8156 | -2.4084 |
0.8186 | -2.3793 |
0.8217 | -2.3497 |
0.8248 | -2.3198 |
0.8279 | -2.2893 |
0.8310 | -2.2574 |
0.8342 | -2.2249 |
0.8373 | -2.1914 |
0.8405 | -2.1564 |
0.8438 | -2.1258 |
0.8470 | -2.0939 |
0.8503 | -2.0578 |
0.8536 | -2.0209 |
0.8569 | -1.9819 |
0.8603 | -1.9434 |
0.8637 | -1.9107 |
0.8659 | -1.8826 |
0.8682 | -1.8568 |
0.8705 | -1.8303 |
0.8728 | -1.8029 |
0.8751 | -1.7757 |
0.8775 | -1.7489 |
0.8798 | -1.7198 |
0.8822 | -1.6906 |
0.8845 | -1.6614 |
0.8869 | -1.6326 |
0.8917 | -1.5736 |
0.8941 | -1.5435 |
0.8966 | -1.5084 |
0.8990 | -1.4778 |
0.9015 | -1.4469 |
0.9040 | -1.4096 |
0.9065 | -1.3822 |
0.9090 | -1.3447 |
0.9115 | -1.3118 |
0.9140 | -1.2808 |
0.9165 | -1.2475 |
0.9191 | -1.2105 |
0.9217 | -1.1758 |
0.9243 | -1.1402 |
0.9276 | -1.0984 |
0.9302 | -1.0678 |
0.9328 | -1.0234 |
0.9355 | -0.9905 |
0.9381 | -0.9545 |
0.9407 | -0.9176 |
0.9434 | -0.8797 |
0.9461 | -0.8408 |
0.9488 | -0.8013 |
0.9515 | -0.7607 |
0.9542 | -0.7216 |
0.9569 | -0.6817 |
0.9597 | -0.6406 |
0.9625 | -0.5986 |
0.9653 | -0.5557 |
0.9681 | -0.5106 |
0.9709 | -0.4615 |
0.9737 | -0.4257 |
0.9766 | -0.3802 |
0.9794 | -0.3343 |
0.9823 | -0.2882 |
0.9852 | -0.2415 |
0.9881 | -0.1939 |
0.9911 | -0.1485 |
0.9940 | -0.1040 |
0.9970 | -0.0536 |
Operational conditions:
Mole fraction of 1-Propanol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0101 | -0.0873 |
0.0201 | -0.1720 |
0.0298 | -0.2544 |
0.0394 | -0.3340 |
0.0487 | -0.4112 |
0.0579 | -0.4862 |
0.0669 | -0.5559 |
0.0758 | -0.6294 |
0.0844 | -0.6975 |
0.0930 | -0.7638 |
0.1013 | -0.8288 |
0.1095 | -0.8923 |
0.1176 | -0.9550 |
0.1255 | -1.0158 |
0.1332 | -1.0758 |
0.1409 | -1.1348 |
0.1484 | -1.1922 |
0.1557 | -1.249 |
0.1630 | -1.3043 |
0.1701 | -1.3583 |
0.1771 | -1.4056 |
0.1840 | -1.452 |
0.1908 | -1.4974 |
0.1974 | -1.5419 |
0.2040 | -1.5855 |
0.2104 | -1.6331 |
0.2167 | -1.6797 |
0.2230 | -1.7204 |
0.2291 | -1.7607 |
0.2320 | -1.7867 |
0.2352 | -1.8051 |
0.2385 | -1.8272 |
0.2454 | -1.8849 |
0.2470 | -1.8864 |
0.2527 | -1.9233 |
0.2603 | -1.9874 |
0.2685 | -2.0326 |
0.2772 | -2.1006 |
0.2865 | -2.1615 |
0.2964 | -2.2255 |
0.3071 | -2.2928 |
0.3185 | -2.3634 |
0.3309 | -2.4376 |
0.3442 | -2.5152 |
0.3586 | -2.5964 |
0.3743 | -2.687 |
0.3915 | -2.7767 |
0.3960 | -2.7992 |
0.4006 | -2.8218 |
0.4053 | -2.8446 |
0.4102 | -2.8674 |
0.4151 | -2.8902 |
0.4202 | -2.9122 |
0.4254 | -2.9359 |
0.4307 | -2.9636 |
0.4362 | -2.9884 |
0.4418 | -3.0142 |
0.4476 | -3.0366 |
0.4535 | -3.0589 |
0.4595 | -3.0809 |
0.4657 | -3.1026 |
0.4721 | -3.1242 |
0.4787 | -3.1455 |
0.4855 | -3.1661 |
0.4924 | -3.1896 |
0.4996 | -3.2151 |
0.5069 | -3.2323 |
0.5145 | -3.2514 |
0.5223 | -3.2736 |
0.5304 | -3.2887 |
0.5339 | -3.3028 |
0.5387 | -3.3131 |
0.5394 | -3.3129 |
0.5451 | -3.327 |
0.5509 | -3.3306 |
0.5568 | -3.3361 |
0.5628 | -3.3407 |
0.5690 | -3.3492 |
0.5753 | -3.3567 |
0.5817 | -3.3653 |
0.5883 | -3.3628 |
0.5950 | -3.3675 |
0.6019 | -3.3656 |
0.6090 | -3.3641 |
0.6162 | -3.3623 |
0.6236 | -3.3585 |
0.6312 | -3.3523 |
0.6389 | -3.3435 |
0.6469 | -3.3321 |
0.6550 | -3.3127 |
0.6634 | -3.291 |
0.6719 | -3.2692 |
0.6808 | -3.2424 |
0.6852 | -3.2296 |
0.6898 | -3.2144 |
0.6944 | -3.1979 |
0.6991 | -3.1803 |
0.7038 | -3.1609 |
0.7086 | -3.1402 |
0.7135 | -3.1183 |
0.7184 | -3.0945 |
0.7234 | -3.0695 |
0.7285 | -3.0429 |
0.7336 | -3.0144 |
0.7388 | -2.9846 |
0.7441 | -2.9528 |
0.7495 | -2.9188 |
0.7549 | -2.8878 |
0.7604 | -2.8503 |
0.7660 | -2.8153 |
0.7671 | -2.8049 |
0.7698 | -2.7859 |
0.7717 | -2.7735 |
0.7725 | -2.7668 |
0.7753 | -2.7468 |
0.7775 | -2.7293 |
0.7780 | -2.7259 |
0.7808 | -2.7058 |
0.7836 | -2.6839 |
0.7864 | -2.6624 |
0.7892 | -2.6394 |
0.7920 | -2.6163 |
0.7949 | -2.5934 |
0.7978 | -2.5686 |
0.8007 | -2.5441 |
0.8036 | -2.5184 |
0.8066 | -2.492 |
0.8096 | -2.4648 |
0.8125 | -2.4368 |
0.8156 | -2.4084 |
0.8186 | -2.3793 |
0.8217 | -2.3497 |
0.8248 | -2.3198 |
0.8279 | -2.2893 |
0.8310 | -2.2574 |
0.8342 | -2.2249 |
0.8373 | -2.1914 |
0.8405 | -2.1564 |
0.8438 | -2.1258 |
0.8470 | -2.0939 |
0.8503 | -2.0578 |
0.8536 | -2.0209 |
0.8569 | -1.9819 |
0.8603 | -1.9434 |
0.8637 | -1.9107 |
0.8659 | -1.8826 |
0.8682 | -1.8568 |
0.8705 | -1.8303 |
0.8728 | -1.8029 |
0.8751 | -1.7757 |
0.8775 | -1.7489 |
0.8798 | -1.7198 |
0.8822 | -1.6906 |
0.8845 | -1.6614 |
0.8869 | -1.6326 |
0.8917 | -1.5736 |
0.8941 | -1.5435 |
0.8966 | -1.5084 |
0.8990 | -1.4778 |
0.9015 | -1.4469 |
0.9040 | -1.4096 |
0.9065 | -1.3822 |
0.9090 | -1.3447 |
0.9115 | -1.3118 |
0.9140 | -1.2808 |
0.9165 | -1.2475 |
0.9191 | -1.2105 |
0.9217 | -1.1758 |
0.9243 | -1.1402 |
0.9276 | -1.0984 |
0.9302 | -1.0678 |
0.9328 | -1.0234 |
0.9355 | -0.9905 |
0.9381 | -0.9545 |
0.9407 | -0.9176 |
0.9434 | -0.8797 |
0.9461 | -0.8408 |
0.9488 | -0.8013 |
0.9515 | -0.7607 |
0.9542 | -0.7216 |
0.9569 | -0.6817 |
0.9597 | -0.6406 |
0.9625 | -0.5986 |
0.9653 | -0.5557 |
0.9681 | -0.5106 |
0.9709 | -0.4615 |
0.9737 | -0.4257 |
0.9766 | -0.3802 |
0.9794 | -0.3343 |
0.9823 | -0.2882 |
0.9852 | -0.2415 |
0.9881 | -0.1939 |
0.9911 | -0.1485 |
0.9940 | -0.1040 |
0.9970 | -0.0536 |