Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol (1) - Liquid | Mole fraction of 1-Tert-butoxybutane (2) - Liquid | Mole fraction of 1-Tert-butoxybutane (2) - Gas | Mole fraction of Ethanol (1) - Gas |
386.33 | 0.9354 | 0.0496 | 0.2500 | 0.7051 |
388.38 | 0.9403 | 0.0484 | 0.2042 | 0.7599 |
374.54 | 0.8904 | 0.0980 | 0.4098 | 0.4530 |
377.84 | 0.9007 | 0.0826 | 0.3681 | 0.5182 |
380.92 | 0.9043 | 0.0791 | 0.3347 | 0.5741 |
380.34 | 0.9043 | 0.0764 | 0.3351 | 0.5685 |
371.07 | 0.8603 | 0.1179 | 0.5025 | 0.3887 |
367.34 | 0.8550 | 0.1170 | 0.5673 | 0.3396 |
363.35 | 0.7995 | 0.1682 | 0.6272 | 0.3045 |
361.13 | 0.7651 | 0.2033 | 0.7014 | 0.2574 |
360.99 | 0.7679 | 0.1927 | 0.6909 | 0.2524 |
359.70 | 0.7398 | 0.2237 | 0.7159 | 0.2410 |
360.25 | 0.7456 | 0.2116 | 0.7001 | 0.2469 |
359.33 | 0.7236 | 0.2347 | 0.7242 | 0.2353 |
356.80 | 0.6277 | 0.3403 | 0.7750 | 0.2074 |
354.82 | 0.6241 | 0.3115 | 0.6588 | 0.1927 |
353.92 | 0.6184 | 0.2965 | 0.5890 | 0.1909 |
354.20 | 0.5586 | 0.3747 | 0.6953 | 0.1836 |
352.91 | 0.5424 | 0.3572 | 0.6082 | 0.1759 |
353.26 | 0.5230 | 0.3934 | 0.6646 | 0.1751 |
354.18 | 0.5574 | 0.3705 | 0.6876 | 0.1842 |
354.77 | 0.5658 | 0.3678 | 0.7146 | 0.1870 |
354.51 | 0.5028 | 0.4462 | 0.7743 | 0.1791 |
355.57 | 0.5596 | 0.3917 | 0.7773 | 0.1919 |
354.57 | 0.4846 | 0.4733 | 0.8059 | 0.1778 |
353.20 | 0.4597 | 0.4651 | 0.7222 | 0.1671 |
352.59 | 0.4536 | 0.4455 | 0.6679 | 0.1665 |
351.45 | 0.4268 | 0.4033 | 0.5613 | 0.1653 |
351.44 | 0.3899 | 0.4585 | 0.6091 | 0.1581 |
351.66 | 0.3476 | 0.5290 | 0.6733 | 0.1507 |
351.11 | 0.3335 | 0.4953 | 0.6090 | 0.1523 |
350.77 | 0.3200 | 0.4512 | 0.5454 | 0.1557 |
350.81 | 0.2978 | 0.4921 | 0.5790 | 0.1503 |
350.96 | 0.2680 | 0.5577 | 0.6336 | 0.1431 |
351.04 | 0.2462 | 0.6051 | 0.6784 | 0.1356 |
350.68 | 0.2283 | 0.5534 | 0.6040 | 0.1411 |
350.57 | 0.2118 | 0.5050 | 0.5512 | 0.1474 |
350.54 | 0.2002 | 0.4730 | 0.5209 | 0.1528 |
350.51 | 0.1717 | 0.5516 | 0.5785 | 0.1385 |
350.50 | 0.1519 | 0.6043 | 0.6202 | 0.1270 |
350.54 | 0.1352 | 0.6485 | 0.6577 | 0.1167 |
350.45 | 0.1226 | 0.5956 | 0.6043 | 0.1243 |
350.47 | 0.1087 | 0.5311 | 0.5536 | 0.1362 |
350.55 | 0.0993 | 0.4818 | 0.5217 | 0.1465 |
350.53 | 0.0870 | 0.5375 | 0.5632 | 0.1294 |
350.56 | 0.0786 | 0.5776 | 0.5918 | 0.1166 |
350.59 | 0.0697 | 0.6212 | 0.6299 | 0.1014 |
350.67 | 0.0617 | 0.6601 | 0.6626 | 0.0889 |
350.71 | 0.0551 | 0.6936 | 0.6944 | 0.0779 |
350.82 | 0.0465 | 0.6104 | 0.6345 | 0.0879 |
350.97 | 0.0395 | 0.5409 | 0.5953 | 0.0980 |
351.09 | 0.0340 | 0.4806 | 0.5593 | 0.1119 |
351.03 | 0.0360 | 0.4842 | 0.5609 | 0.1122 |
351.63 | 0.2166 | 0.7318 | 0.8145 | 0.1244 |
352.14 | 0.2957 | 0.6591 | 0.7977 | 0.1414 |
353.00 | 0.3929 | 0.5678 | 0.7847 | 0.1594 |
352.37 | 0.3842 | 0.5528 | 0.7363 | 0.1555 |
351.56 | 0.3416 | 0.5510 | 0.6750 | 0.1514 |
351.59 | 0.3178 | 0.5858 | 0.7031 | 0.1470 |
351.26 | 0.2745 | 0.6175 | 0.7007 | 0.1402 |
350.87 | 0.2239 | 0.6318 | 0.6767 | 0.1340 |
350.92 | 0.1908 | 0.6868 | 0.7215 | 0.1239 |
350.98 | 0.1544 | 0.7479 | 0.7673 | 0.1112 |
350.99 | 0.1226 | 0.7993 | 0.8097 | 0.0962 |
351.01 | 0.1022 | 0.8345 | 0.8396 | 0.0861 |
351.06 | 0.0877 | 0.8588 | 0.8628 | 0.0764 |
350.72 | 0.0784 | 0.7828 | 0.7707 | 0.0808 |
350.66 | 0.0746 | 0.7571 | 0.7446 | 0.0822 |
350.63 | 0.0703 | 0.7247 | 0.7154 | 0.0844 |
350.59 | 0.0941 | 0.7056 | 0.6960 | 0.0989 |
350.57 | 0.1324 | 0.6760 | 0.6738 | 0.1157 |
350.66 | 0.1170 | 0.7175 | 0.7118 | 0.1056 |
350.53 | 0.1046 | 0.6551 | 0.6487 | 0.1121 |
351.38 | 0.1440 | 0.8308 | 0.8725 | 0.1010 |
351.31 | 0.1185 | 0.8605 | 0.8864 | 0.0895 |
351.18 | 0.0759 | 0.8995 | 0.9041 | 0.0676 |
351.10 | 0.0565 | 0.9054 | 0.9022 | 0.0555 |
351.01 | 0.0558 | 0.8861 | 0.8784 | 0.0568 |
350.78 | 0.0491 | 0.7917 | 0.7788 | 0.0616 |
350.75 | 0.0457 | 0.7501 | 0.7395 | 0.0648 |
351.40 | 0.0010 | 0.9912 | 0.9895 | 0.0018 |
351.32 | 0.0164 | 0.9761 | 0.9727 | 0.0191 |
351.21 | 0.0150 | 0.9391 | 0.9325 | 0.0183 |
351.13 | 0.0162 | 0.9121 | 0.9032 | 0.0212 |
350.86 | 0.0451 | 0.8308 | 0.8147 | 0.0553 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol (1) - Liquid | Mole fraction of 1-Tert-butoxybutane (2) - Liquid | Mole fraction of 1-Tert-butoxybutane (2) - Gas | Mole fraction of Ethanol (1) - Gas |
386.33 | 0.9354 | 0.0496 | 0.2500 | 0.7051 |
388.38 | 0.9403 | 0.0484 | 0.2042 | 0.7599 |
374.54 | 0.8904 | 0.0980 | 0.4098 | 0.4530 |
377.84 | 0.9007 | 0.0826 | 0.3681 | 0.5182 |
380.92 | 0.9043 | 0.0791 | 0.3347 | 0.5741 |
380.34 | 0.9043 | 0.0764 | 0.3351 | 0.5685 |
371.07 | 0.8603 | 0.1179 | 0.5025 | 0.3887 |
367.34 | 0.8550 | 0.1170 | 0.5673 | 0.3396 |
363.35 | 0.7995 | 0.1682 | 0.6272 | 0.3045 |
361.13 | 0.7651 | 0.2033 | 0.7014 | 0.2574 |
360.99 | 0.7679 | 0.1927 | 0.6909 | 0.2524 |
359.70 | 0.7398 | 0.2237 | 0.7159 | 0.2410 |
360.25 | 0.7456 | 0.2116 | 0.7001 | 0.2469 |
359.33 | 0.7236 | 0.2347 | 0.7242 | 0.2353 |
356.80 | 0.6277 | 0.3403 | 0.7750 | 0.2074 |
354.82 | 0.6241 | 0.3115 | 0.6588 | 0.1927 |
353.92 | 0.6184 | 0.2965 | 0.5890 | 0.1909 |
354.20 | 0.5586 | 0.3747 | 0.6953 | 0.1836 |
352.91 | 0.5424 | 0.3572 | 0.6082 | 0.1759 |
353.26 | 0.5230 | 0.3934 | 0.6646 | 0.1751 |
354.18 | 0.5574 | 0.3705 | 0.6876 | 0.1842 |
354.77 | 0.5658 | 0.3678 | 0.7146 | 0.1870 |
354.51 | 0.5028 | 0.4462 | 0.7743 | 0.1791 |
355.57 | 0.5596 | 0.3917 | 0.7773 | 0.1919 |
354.57 | 0.4846 | 0.4733 | 0.8059 | 0.1778 |
353.20 | 0.4597 | 0.4651 | 0.7222 | 0.1671 |
352.59 | 0.4536 | 0.4455 | 0.6679 | 0.1665 |
351.45 | 0.4268 | 0.4033 | 0.5613 | 0.1653 |
351.44 | 0.3899 | 0.4585 | 0.6091 | 0.1581 |
351.66 | 0.3476 | 0.5290 | 0.6733 | 0.1507 |
351.11 | 0.3335 | 0.4953 | 0.6090 | 0.1523 |
350.77 | 0.3200 | 0.4512 | 0.5454 | 0.1557 |
350.81 | 0.2978 | 0.4921 | 0.5790 | 0.1503 |
350.96 | 0.2680 | 0.5577 | 0.6336 | 0.1431 |
351.04 | 0.2462 | 0.6051 | 0.6784 | 0.1356 |
350.68 | 0.2283 | 0.5534 | 0.6040 | 0.1411 |
350.57 | 0.2118 | 0.5050 | 0.5512 | 0.1474 |
350.54 | 0.2002 | 0.4730 | 0.5209 | 0.1528 |
350.51 | 0.1717 | 0.5516 | 0.5785 | 0.1385 |
350.50 | 0.1519 | 0.6043 | 0.6202 | 0.1270 |
350.54 | 0.1352 | 0.6485 | 0.6577 | 0.1167 |
350.45 | 0.1226 | 0.5956 | 0.6043 | 0.1243 |
350.47 | 0.1087 | 0.5311 | 0.5536 | 0.1362 |
350.55 | 0.0993 | 0.4818 | 0.5217 | 0.1465 |
350.53 | 0.0870 | 0.5375 | 0.5632 | 0.1294 |
350.56 | 0.0786 | 0.5776 | 0.5918 | 0.1166 |
350.59 | 0.0697 | 0.6212 | 0.6299 | 0.1014 |
350.67 | 0.0617 | 0.6601 | 0.6626 | 0.0889 |
350.71 | 0.0551 | 0.6936 | 0.6944 | 0.0779 |
350.82 | 0.0465 | 0.6104 | 0.6345 | 0.0879 |
350.97 | 0.0395 | 0.5409 | 0.5953 | 0.0980 |
351.09 | 0.0340 | 0.4806 | 0.5593 | 0.1119 |
351.03 | 0.0360 | 0.4842 | 0.5609 | 0.1122 |
351.63 | 0.2166 | 0.7318 | 0.8145 | 0.1244 |
352.14 | 0.2957 | 0.6591 | 0.7977 | 0.1414 |
353.00 | 0.3929 | 0.5678 | 0.7847 | 0.1594 |
352.37 | 0.3842 | 0.5528 | 0.7363 | 0.1555 |
351.56 | 0.3416 | 0.5510 | 0.6750 | 0.1514 |
351.59 | 0.3178 | 0.5858 | 0.7031 | 0.1470 |
351.26 | 0.2745 | 0.6175 | 0.7007 | 0.1402 |
350.87 | 0.2239 | 0.6318 | 0.6767 | 0.1340 |
350.92 | 0.1908 | 0.6868 | 0.7215 | 0.1239 |
350.98 | 0.1544 | 0.7479 | 0.7673 | 0.1112 |
350.99 | 0.1226 | 0.7993 | 0.8097 | 0.0962 |
351.01 | 0.1022 | 0.8345 | 0.8396 | 0.0861 |
351.06 | 0.0877 | 0.8588 | 0.8628 | 0.0764 |
350.72 | 0.0784 | 0.7828 | 0.7707 | 0.0808 |
350.66 | 0.0746 | 0.7571 | 0.7446 | 0.0822 |
350.63 | 0.0703 | 0.7247 | 0.7154 | 0.0844 |
350.59 | 0.0941 | 0.7056 | 0.6960 | 0.0989 |
350.57 | 0.1324 | 0.6760 | 0.6738 | 0.1157 |
350.66 | 0.1170 | 0.7175 | 0.7118 | 0.1056 |
350.53 | 0.1046 | 0.6551 | 0.6487 | 0.1121 |
351.38 | 0.1440 | 0.8308 | 0.8725 | 0.1010 |
351.31 | 0.1185 | 0.8605 | 0.8864 | 0.0895 |
351.18 | 0.0759 | 0.8995 | 0.9041 | 0.0676 |
351.10 | 0.0565 | 0.9054 | 0.9022 | 0.0555 |
351.01 | 0.0558 | 0.8861 | 0.8784 | 0.0568 |
350.78 | 0.0491 | 0.7917 | 0.7788 | 0.0616 |
350.75 | 0.0457 | 0.7501 | 0.7395 | 0.0648 |
351.40 | 0.0010 | 0.9912 | 0.9895 | 0.0018 |
351.32 | 0.0164 | 0.9761 | 0.9727 | 0.0191 |
351.21 | 0.0150 | 0.9391 | 0.9325 | 0.0183 |
351.13 | 0.0162 | 0.9121 | 0.9032 | 0.0212 |
350.86 | 0.0451 | 0.8308 | 0.8147 | 0.0553 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Mole fraction of 1-Tert-butoxybutane (2) - Liquid | Mole fraction of Ethanol (1) - Liquid | Refractive index (Na D-line) - Liquid |
0.0200 | 0.3861 | 1.3649 |
0.0256 | 0.4929 | 1.3662 |
0.0350 | 0.6743 | 1.3665 |
0.0390 | 0.7520 | 1.3662 |
0.0393 | 0.4538 | 1.3677 |
0.0434 | 0.8371 | 1.3654 |
0.0493 | 0.9507 | 1.3639 |
0.0504 | 0.5815 | 1.3686 |
0.0556 | 0.6415 | 1.3686 |
0.0589 | 0.9411 | 1.3646 |
0.0632 | 0.7297 | 1.3684 |
0.0691 | 0.7983 | 1.3679 |
0.0797 | 0.9203 | 1.3665 |
0.1006 | 0.8994 | 1.3678 |
0.1126 | 0.4568 | 1.374 |
0.1302 | 0.5278 | 1.3747 |
0.1466 | 0.5946 | 1.375 |
0.1555 | 0.8445 | 1.3714 |
0.1683 | 0.6827 | 1.3748 |
0.1884 | 0.7639 | 1.3742 |
0.1947 | 0.8053 | 1.3737 |
0.1966 | 0.4659 | 1.3785 |
0.1978 | 0.8022 | 1.3738 |
0.2346 | 0.5561 | 1.3791 |
0.2488 | 0.5898 | 1.3791 |
0.2528 | 0.7472 | 1.3765 |
0.2773 | 0.6574 | 1.3788 |
0.2904 | 0.4418 | 1.3819 |
0.2923 | 0.7077 | 1.3782 |
0.2967 | 0.7033 | 1.3783 |
0.3063 | 0.4660 | 1.3821 |
0.3311 | 0.5037 | 1.3822 |
0.3500 | 0.5325 | 1.3822 |
0.3512 | 0.6488 | 1.3804 |
0.3670 | 0.5584 | 1.3821 |
0.3966 | 0.6034 | 1.3818 |
0.3970 | 0.6030 | 1.3819 |
0.3987 | 0.3989 | 1.3847 |
0.4313 | 0.5687 | 1.3829 |
0.4339 | 0.4340 | 1.3849 |
0.4662 | 0.4664 | 1.3849 |
0.4999 | 0.5001 | 1.3846 |
0.5118 | 0.4882 | 1.3849 |
0.5169 | 0.3514 | 1.3868 |
0.5380 | 0.3657 | 1.3869 |
0.5590 | 0.4410 | 1.386 |
0.5786 | 0.3933 | 1.3868 |
0.5953 | 0.4047 | 1.3867 |
0.5964 | 0.4036 | 1.3867 |
0.6221 | 0.2857 | 1.3884 |
0.6627 | 0.3373 | 1.388 |
0.6643 | 0.3051 | 1.3884 |
0.6853 | 0.3147 | 1.3883 |
0.7044 | 0.2956 | 1.3886 |
0.7432 | 0.2032 | 1.39 |
0.7441 | 0.2559 | 1.3892 |
0.7644 | 0.2090 | 1.3899 |
0.7814 | 0.2186 | 1.3897 |
0.7853 | 0.2147 | 1.3899 |
0.8493 | 0.1507 | 1.3905 |
0.9072 | 0.0928 | 1.3911 |
0.9404 | 0.0596 | 1.3913 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Mole fraction of 1-Tert-butoxybutane (2) - Liquid | Mole fraction of Ethanol (1) - Liquid | Refractive index (Na D-line) - Liquid |
0.0200 | 0.3861 | 1.3649 |
0.0256 | 0.4929 | 1.3662 |
0.0350 | 0.6743 | 1.3665 |
0.0390 | 0.7520 | 1.3662 |
0.0393 | 0.4538 | 1.3677 |
0.0434 | 0.8371 | 1.3654 |
0.0493 | 0.9507 | 1.3639 |
0.0504 | 0.5815 | 1.3686 |
0.0556 | 0.6415 | 1.3686 |
0.0589 | 0.9411 | 1.3646 |
0.0632 | 0.7297 | 1.3684 |
0.0691 | 0.7983 | 1.3679 |
0.0797 | 0.9203 | 1.3665 |
0.1006 | 0.8994 | 1.3678 |
0.1126 | 0.4568 | 1.374 |
0.1302 | 0.5278 | 1.3747 |
0.1466 | 0.5946 | 1.375 |
0.1555 | 0.8445 | 1.3714 |
0.1683 | 0.6827 | 1.3748 |
0.1884 | 0.7639 | 1.3742 |
0.1947 | 0.8053 | 1.3737 |
0.1966 | 0.4659 | 1.3785 |
0.1978 | 0.8022 | 1.3738 |
0.2346 | 0.5561 | 1.3791 |
0.2488 | 0.5898 | 1.3791 |
0.2528 | 0.7472 | 1.3765 |
0.2773 | 0.6574 | 1.3788 |
0.2904 | 0.4418 | 1.3819 |
0.2923 | 0.7077 | 1.3782 |
0.2967 | 0.7033 | 1.3783 |
0.3063 | 0.4660 | 1.3821 |
0.3311 | 0.5037 | 1.3822 |
0.3500 | 0.5325 | 1.3822 |
0.3512 | 0.6488 | 1.3804 |
0.3670 | 0.5584 | 1.3821 |
0.3966 | 0.6034 | 1.3818 |
0.3970 | 0.6030 | 1.3819 |
0.3987 | 0.3989 | 1.3847 |
0.4313 | 0.5687 | 1.3829 |
0.4339 | 0.4340 | 1.3849 |
0.4662 | 0.4664 | 1.3849 |
0.4999 | 0.5001 | 1.3846 |
0.5118 | 0.4882 | 1.3849 |
0.5169 | 0.3514 | 1.3868 |
0.5380 | 0.3657 | 1.3869 |
0.5590 | 0.4410 | 1.386 |
0.5786 | 0.3933 | 1.3868 |
0.5953 | 0.4047 | 1.3867 |
0.5964 | 0.4036 | 1.3867 |
0.6221 | 0.2857 | 1.3884 |
0.6627 | 0.3373 | 1.388 |
0.6643 | 0.3051 | 1.3884 |
0.6853 | 0.3147 | 1.3883 |
0.7044 | 0.2956 | 1.3886 |
0.7432 | 0.2032 | 1.39 |
0.7441 | 0.2559 | 1.3892 |
0.7644 | 0.2090 | 1.3899 |
0.7814 | 0.2186 | 1.3897 |
0.7853 | 0.2147 | 1.3899 |
0.8493 | 0.1507 | 1.3905 |
0.9072 | 0.0928 | 1.3911 |
0.9404 | 0.0596 | 1.3913 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Mole fraction of 1-Tert-butoxybutane (2) - Liquid | Mole fraction of Ethanol (1) - Liquid | Mass density, kg/m3 - Liquid |
0.0200 | 0.3861 | 870.02 |
0.0256 | 0.4929 | 847.87 |
0.0350 | 0.6743 | 818.09 |
0.0390 | 0.7520 | 807.27 |
0.0393 | 0.4538 | 848.08 |
0.0434 | 0.8371 | 796.25 |
0.0493 | 0.9507 | 782.41 |
0.0504 | 0.5815 | 825.62 |
0.0556 | 0.6415 | 816.54 |
0.0589 | 0.9411 | 781.92 |
0.0632 | 0.7297 | 804.36 |
0.0691 | 0.7983 | 795.57 |
0.0797 | 0.9203 | 780.9 |
0.1006 | 0.8994 | 779.92 |
0.1126 | 0.4568 | 822.06 |
0.1302 | 0.5278 | 810.74 |
0.1466 | 0.5946 | 801.27 |
0.1555 | 0.8445 | 777.57 |
0.1683 | 0.6827 | 789.97 |
0.1884 | 0.7639 | 780.35 |
0.1947 | 0.8053 | 776.05 |
0.1966 | 0.4659 | 802.52 |
0.1978 | 0.8022 | 775.98 |
0.2346 | 0.5561 | 790.2 |
0.2488 | 0.5898 | 786.03 |
0.2528 | 0.7472 | 773.99 |
0.2773 | 0.6574 | 777.88 |
0.2904 | 0.4418 | 790.19 |
0.2923 | 0.7077 | 772.71 |
0.2967 | 0.7033 | 772.6 |
0.3063 | 0.4660 | 786.89 |
0.3311 | 0.5037 | 781.96 |
0.3500 | 0.5325 | 778.33 |
0.3512 | 0.6488 | 770.96 |
0.3670 | 0.5584 | 775.16 |
0.3966 | 0.6034 | 769.83 |
0.3970 | 0.6030 | 769.71 |
0.3987 | 0.3989 | 780.6 |
0.4313 | 0.5687 | 768.83 |
0.4339 | 0.4340 | 775.9 |
0.4662 | 0.4664 | 771.7 |
0.4999 | 0.5001 | 767.3 |
0.5118 | 0.4882 | 766.95 |
0.5169 | 0.3514 | 773.08 |
0.5380 | 0.3657 | 770.99 |
0.5590 | 0.4410 | 765.94 |
0.5786 | 0.3933 | 766.97 |
0.5953 | 0.4047 | 765.3 |
0.5964 | 0.4036 | 765.18 |
0.6221 | 0.2857 | 768.62 |
0.6627 | 0.3373 | 763.92 |
0.6643 | 0.3051 | 765.29 |
0.6853 | 0.3147 | 763.6 |
0.7044 | 0.2956 | 763.16 |
0.7432 | 0.2032 | 764.48 |
0.7441 | 0.2559 | 762.45 |
0.7644 | 0.2090 | 763.11 |
0.7814 | 0.2186 | 761.8 |
0.7853 | 0.2147 | 761.72 |
0.8493 | 0.1507 | 760.58 |
0.9072 | 0.0928 | 759.5 |
0.9404 | 0.0596 | 758.85 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Mole fraction of 1-Tert-butoxybutane (2) - Liquid | Mole fraction of Ethanol (1) - Liquid | Mass density, kg/m3 - Liquid |
0.0200 | 0.3861 | 870.02 |
0.0256 | 0.4929 | 847.87 |
0.0350 | 0.6743 | 818.09 |
0.0390 | 0.7520 | 807.27 |
0.0393 | 0.4538 | 848.08 |
0.0434 | 0.8371 | 796.25 |
0.0493 | 0.9507 | 782.41 |
0.0504 | 0.5815 | 825.62 |
0.0556 | 0.6415 | 816.54 |
0.0589 | 0.9411 | 781.92 |
0.0632 | 0.7297 | 804.36 |
0.0691 | 0.7983 | 795.57 |
0.0797 | 0.9203 | 780.9 |
0.1006 | 0.8994 | 779.92 |
0.1126 | 0.4568 | 822.06 |
0.1302 | 0.5278 | 810.74 |
0.1466 | 0.5946 | 801.27 |
0.1555 | 0.8445 | 777.57 |
0.1683 | 0.6827 | 789.97 |
0.1884 | 0.7639 | 780.35 |
0.1947 | 0.8053 | 776.05 |
0.1966 | 0.4659 | 802.52 |
0.1978 | 0.8022 | 775.98 |
0.2346 | 0.5561 | 790.2 |
0.2488 | 0.5898 | 786.03 |
0.2528 | 0.7472 | 773.99 |
0.2773 | 0.6574 | 777.88 |
0.2904 | 0.4418 | 790.19 |
0.2923 | 0.7077 | 772.71 |
0.2967 | 0.7033 | 772.6 |
0.3063 | 0.4660 | 786.89 |
0.3311 | 0.5037 | 781.96 |
0.3500 | 0.5325 | 778.33 |
0.3512 | 0.6488 | 770.96 |
0.3670 | 0.5584 | 775.16 |
0.3966 | 0.6034 | 769.83 |
0.3970 | 0.6030 | 769.71 |
0.3987 | 0.3989 | 780.6 |
0.4313 | 0.5687 | 768.83 |
0.4339 | 0.4340 | 775.9 |
0.4662 | 0.4664 | 771.7 |
0.4999 | 0.5001 | 767.3 |
0.5118 | 0.4882 | 766.95 |
0.5169 | 0.3514 | 773.08 |
0.5380 | 0.3657 | 770.99 |
0.5590 | 0.4410 | 765.94 |
0.5786 | 0.3933 | 766.97 |
0.5953 | 0.4047 | 765.3 |
0.5964 | 0.4036 | 765.18 |
0.6221 | 0.2857 | 768.62 |
0.6627 | 0.3373 | 763.92 |
0.6643 | 0.3051 | 765.29 |
0.6853 | 0.3147 | 763.6 |
0.7044 | 0.2956 | 763.16 |
0.7432 | 0.2032 | 764.48 |
0.7441 | 0.2559 | 762.45 |
0.7644 | 0.2090 | 763.11 |
0.7814 | 0.2186 | 761.8 |
0.7853 | 0.2147 | 761.72 |
0.8493 | 0.1507 | 760.58 |
0.9072 | 0.0928 | 759.5 |
0.9404 | 0.0596 | 758.85 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Mole fraction of 1-Tert-butoxybutane (2) - Liquid | Mole fraction of Ethanol (1) - Liquid | Speed of sound, m/s - Liquid |
0.0200 | 0.3861 | 1352.0 |
0.0256 | 0.4929 | 1302.0 |
0.0350 | 0.6743 | 1234.0 |
0.0390 | 0.7520 | 1208.0 |
0.0393 | 0.4538 | 1294.0 |
0.0434 | 0.8371 | 1180.0 |
0.0493 | 0.9507 | 1141.0 |
0.0504 | 0.5815 | 1248.0 |
0.0556 | 0.6415 | 1229.0 |
0.0589 | 0.9411 | 1139.0 |
0.0632 | 0.7297 | 1201.0 |
0.0691 | 0.7983 | 1179.0 |
0.0797 | 0.9203 | 1139.0 |
0.1006 | 0.8994 | 1136.0 |
0.1126 | 0.4568 | 1208.0 |
0.1302 | 0.5278 | 1193.0 |
0.1466 | 0.5946 | 1179.0 |
0.1555 | 0.8445 | 1133.0 |
0.1683 | 0.6827 | 1159.0 |
0.1884 | 0.7639 | 1141.0 |
0.1947 | 0.8053 | 1132.0 |
0.1966 | 0.4659 | 1175.0 |
0.1978 | 0.8022 | 1132.0 |
0.2346 | 0.5561 | 1160.0 |
0.2488 | 0.5898 | 1153.0 |
0.2528 | 0.7472 | 1129.0 |
0.2773 | 0.6574 | 1139.0 |
0.2904 | 0.4418 | 1156.0 |
0.2923 | 0.7077 | 1127.0 |
0.2967 | 0.7033 | 1128.0 |
0.3063 | 0.4660 | 1153.0 |
0.3311 | 0.5037 | 1146.0 |
0.3500 | 0.5325 | 1141.0 |
0.3512 | 0.6488 | 1125.0 |
0.3670 | 0.5584 | 1135.0 |
0.3966 | 0.6034 | 1124.0 |
0.3970 | 0.6030 | 1124.0 |
0.3987 | 0.3989 | 1142.0 |
0.4313 | 0.5687 | 1123.0 |
0.4339 | 0.4340 | 1137.0 |
0.4662 | 0.4664 | 1130.0 |
0.4999 | 0.5001 | 1122.0 |
0.5118 | 0.4882 | 1121.0 |
0.5169 | 0.3514 | 1133.0 |
0.5380 | 0.3657 | 1131.0 |
0.5590 | 0.4410 | 1120.0 |
0.5786 | 0.3933 | 1123.0 |
0.5953 | 0.4047 | 1119.0 |
0.5964 | 0.4036 | 1119.0 |
0.6221 | 0.2857 | 1127.0 |
0.6627 | 0.3373 | 1118.0 |
0.6643 | 0.3051 | 1122.0 |
0.6853 | 0.3147 | 1120.0 |
0.7044 | 0.2956 | 1118.0 |
0.7432 | 0.2032 | 1122.0 |
0.7441 | 0.2559 | 1117.0 |
0.7644 | 0.2090 | 1120.0 |
0.7814 | 0.2186 | 1117.0 |
0.7853 | 0.2147 | 1118.0 |
0.8493 | 0.1507 | 1116.0 |
0.9072 | 0.0928 | 1115.0 |
0.9404 | 0.0596 | 1115.0 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Mole fraction of 1-Tert-butoxybutane (2) - Liquid | Mole fraction of Ethanol (1) - Liquid | Speed of sound, m/s - Liquid |
0.0200 | 0.3861 | 1352.0 |
0.0256 | 0.4929 | 1302.0 |
0.0350 | 0.6743 | 1234.0 |
0.0390 | 0.7520 | 1208.0 |
0.0393 | 0.4538 | 1294.0 |
0.0434 | 0.8371 | 1180.0 |
0.0493 | 0.9507 | 1141.0 |
0.0504 | 0.5815 | 1248.0 |
0.0556 | 0.6415 | 1229.0 |
0.0589 | 0.9411 | 1139.0 |
0.0632 | 0.7297 | 1201.0 |
0.0691 | 0.7983 | 1179.0 |
0.0797 | 0.9203 | 1139.0 |
0.1006 | 0.8994 | 1136.0 |
0.1126 | 0.4568 | 1208.0 |
0.1302 | 0.5278 | 1193.0 |
0.1466 | 0.5946 | 1179.0 |
0.1555 | 0.8445 | 1133.0 |
0.1683 | 0.6827 | 1159.0 |
0.1884 | 0.7639 | 1141.0 |
0.1947 | 0.8053 | 1132.0 |
0.1966 | 0.4659 | 1175.0 |
0.1978 | 0.8022 | 1132.0 |
0.2346 | 0.5561 | 1160.0 |
0.2488 | 0.5898 | 1153.0 |
0.2528 | 0.7472 | 1129.0 |
0.2773 | 0.6574 | 1139.0 |
0.2904 | 0.4418 | 1156.0 |
0.2923 | 0.7077 | 1127.0 |
0.2967 | 0.7033 | 1128.0 |
0.3063 | 0.4660 | 1153.0 |
0.3311 | 0.5037 | 1146.0 |
0.3500 | 0.5325 | 1141.0 |
0.3512 | 0.6488 | 1125.0 |
0.3670 | 0.5584 | 1135.0 |
0.3966 | 0.6034 | 1124.0 |
0.3970 | 0.6030 | 1124.0 |
0.3987 | 0.3989 | 1142.0 |
0.4313 | 0.5687 | 1123.0 |
0.4339 | 0.4340 | 1137.0 |
0.4662 | 0.4664 | 1130.0 |
0.4999 | 0.5001 | 1122.0 |
0.5118 | 0.4882 | 1121.0 |
0.5169 | 0.3514 | 1133.0 |
0.5380 | 0.3657 | 1131.0 |
0.5590 | 0.4410 | 1120.0 |
0.5786 | 0.3933 | 1123.0 |
0.5953 | 0.4047 | 1119.0 |
0.5964 | 0.4036 | 1119.0 |
0.6221 | 0.2857 | 1127.0 |
0.6627 | 0.3373 | 1118.0 |
0.6643 | 0.3051 | 1122.0 |
0.6853 | 0.3147 | 1120.0 |
0.7044 | 0.2956 | 1118.0 |
0.7432 | 0.2032 | 1122.0 |
0.7441 | 0.2559 | 1117.0 |
0.7644 | 0.2090 | 1120.0 |
0.7814 | 0.2186 | 1117.0 |
0.7853 | 0.2147 | 1118.0 |
0.8493 | 0.1507 | 1116.0 |
0.9072 | 0.0928 | 1115.0 |
0.9404 | 0.0596 | 1115.0 |