2 0 2009 san nos 0 journal Original Sanjari, S.[Samaneh] Nosrati, M.[Mohsen] Haghtalab, A.[Ali] Fluid Phase Equilib. 2009 2009-04-01 Osmotic coefficient data and an excess Gibbs energy function for single-phase complex system of glucose + alcohol +water Excess Gibbs-free energy NRTL-NRF model Water activity Isopiestic method Osmotic coefficient Activity coefficient Glucose Ethylene glycol Glycerol 2,3 Butanediol 10.1016/j.fluid.2008.11.016 277 107-113 1 D(+)-glucose C6H12O6 1 Commercial source 2 glycerol C3H8O3 1 Commercial source 3 1,2-ethanediol C2H6O2 1 Commercial source 4 2,3-butanediol C4H10O2 1 Commercial source 5 water H2O 1 Commercial source 1 99.5 3 Estimated by the compiler 1 1 2 1 5 1 Principal objective of the work PW TRC 3/5/2009 1 Osmotic coefficient Isopiestic method Liquid Direct value, X 5 Author Standard deviation of a single value (unbiased) Liquid Gas Temperature, K 298.15 5 1 Molality, mol/kg 2 Liquid 5 2 Molality, mol/kg 1 Liquid 5 1 .087 2 2 .436 3 1 .811 3 .0003244 1 1 .165 3 2 .413 3 1 .687 3 .0002748 1 1 .428 3 2 .428 3 1 .483 3 .0001932 1 1 .902 3 2 .451 3 1 .382 3 .0001528 1 1 1.322 4 2 .441 3 1 .323 3 .0001292 1 1 1.886 4 2 .472 3 1 .284 3 .0001136 1 1 2.188 4 2 .438 3 1 .255 3 .000102 1 1 2.614 4 2 .436 3 1 .234 3 .0000936 1 1 3.045 4 2 .435 3 1 .217 3 .0000868 1 1 3.464 4 2 .433 3 1 .203 3 .0000812 1 1 3.951 4 2 .439 3 1 .19 3 .000076 1 1 4.351 4 2 .435 3 1 .179 3 .0000716 1 1 .092 2 2 .917 3 1 .823 3 .0003292 1 1 .18 3 2 .9 3 1 .758 3 .0003032 1 1 .488 3 2 .976 3 1 .612 3 .0002448 1 1 1.05 4 2 1.05 4 1 .451 3 .0001804 1 1 1.461 4 2 .974 3 1 .402 3 .0001608 1 1 1.959 4 2 .98 3 1 .36 3 .000144 1 1 2.459 4 2 .984 3 1 .325 3 .00013 1 1 3.103 4 2 1.034 4 1 .297 3 .0001188 1 1 3.84 4 2 1.097 4 1 .275 3 .00011 1 1 4.651 4 2 1.163 4 1 .258 3 .0001032 1 1 5.279 4 2 1.173 4 1 .248 3 .0000992 1 1 5.656 4 2 1.131 4 1 .243 3 .0000972 1 1 .087 2 2 1.748 4 1 .911 3 .0003644 1 1 .255 3 2 2.055 4 1 .821 3 .0003284 1 1 .522 3 2 2.088 4 1 .722 3 .0002888 1 1 1.037 4 2 2.074 4 1 .601 3 .0002404 1 1 1.839 4 2 2.452 4 1 .502 3 .0002008 1 1 2.456 4 2 2.456 4 1 .454 3 .0001816 1 1 4.146 4 2 3.317 4 1 .369 3 .0001476 1 1 5.1 4 2 3.4 4 1 .333 3 .0001332 1 1 5.425 4 2 3.1 4 1 .32 3 .000128 1 1 5.825 4 2 2.913 4 1 .309 3 .0001236 1 1 6.168 4 2 2.741 4 1 .298 3 .0001192 1 1 6.471 4 2 2.588 4 1 .289 3 .0001156 1 1 .1 3 2 3.984 4 1 .907 3 .0003628 1 1 .33 3 2 4.17 4 1 .822 3 .0003288 1 1 .539 3 2 4.312 4 1 .758 3 .0003032 1 1 1.266 4 2 5.064 4 1 .601 3 .0002404 1 1 2.242 4 2 5.979 4 1 .481 3 .0001924 1 1 3.1 4 2 6.2 4 1 .415 3 .000166 1 1 4.536 4 2 7.258 4 1 .338 3 .0001352 1 1 5.169 4 2 6.892 4 1 .311 3 .0001244 1 1 6.982 4 2 7.048 4 1 .248 3 .0000992 1 1 7.263 4 2 6.932 4 1 .24 3 .000096 1 1 7.515 4 2 7.011 4 1 .233 3 .0000932 1 1 7.793 4 2 7.167 4 1 .226 3 .0000904 1 1 1 3 1 5 1 Principal objective of the work PW TRC 3/5/2009 1 Osmotic coefficient Isopiestic method Liquid Direct value, X 5 Author Standard deviation of a single value (unbiased) Liquid Gas Temperature, K 298.15 5 1 Molality, mol/kg 3 Liquid 5 2 Molality, mol/kg 1 Liquid 5 1 .091 2 2 .457 3 1 .775 3 .0019375 1 1 .16 3 2 .4 3 1 .698 3 .001745 1 1 .51 3 2 .51 3 1 .497 3 .0012425 1 1 1.026 4 2 .513 3 1 .385 3 .0009625 1 1 1.401 4 2 .467 3 1 .336 3 .00084 1 1 1.761 4 2 .44 3 1 .304 3 .00076 1 1 2.132 4 2 .426 3 1 .281 3 .0007025 1 1 2.495 4 2 .416 3 1 .264 3 .00066 1 1 2.789 4 2 .398 3 1 .252 3 .00063 1 1 3.081 4 2 .385 3 1 .243 3 .0006075 1 1 3.401 4 2 .378 3 1 .236 3 .00059 1 1 3.876 4 2 .388 3 1 .233 3 .0005825 1 1 .088 2 2 .88 3 1 .879 3 .0021975 1 1 .181 3 2 .905 3 1 .822 3 .002055 1 1 .516 3 2 1.032 4 1 .677 3 .0016925 1 1 1.043 4 2 1.043 4 1 .542 3 .001355 1 1 1.542 4 2 1.028 4 1 .474 3 .001185 1 1 1.876 4 2 .938 3 1 .443 3 .0011075 1 1 2.205 4 2 .882 3 1 .417 3 .0010425 1 1 2.592 4 2 .864 3 1 .396 3 .00099 1 1 3.007 4 2 .859 3 1 .378 3 .000945 1 1 3.455 4 2 .864 3 1 .363 3 .0009075 1 1 3.872 4 2 .86 3 1 .352 3 .00088 1 1 4.318 4 2 .864 3 1 .343 3 .0008575 1 1 .089 2 2 1.78 4 1 .914 3 .002285 1 1 .156 3 2 1.56 4 1 .869 3 .0021725 1 1 .488 3 2 1.952 4 1 .721 3 .0018025 1 1 1.042 4 2 2.084 4 1 .612 3 .00153 1 1 2.105 4 2 2.807 4 1 .498 3 .001245 1 1 2.407 4 2 2.407 4 1 .477 3 .0011925 1 1 4.051 4 2 3.241 4 1 .417 3 .0010425 1 1 4.312 4 2 2.875 4 1 .41 3 .001025 1 1 4.652 4 2 2.658 4 1 .403 3 .0010075 1 1 5.012 4 2 2.506 4 1 .396 3 .00099 1 1 5.295 4 2 2.353 4 1 .391 3 .0009775 1 1 5.687 4 2 2.275 4 1 .385 3 .0009625 1 1 .102 3 2 4.08 4 1 .905 3 .0022625 1 1 .135 3 2 4.185 4 1 .852 3 .00213 1 1 .599 3 2 4.792 4 1 .699 3 .0017475 1 1 1.221 4 2 4.884 4 1 .625 3 .0015625 1 1 2.435 4 2 6.493 4 1 .502 3 .001255 1 1 3.181 4 2 6.362 4 1 .449 3 .0011225 1 1 4.655 4 2 7.448 4 1 .389 3 .0009725 1 1 6.515 4 2 8.687 4 1 .334 3 .000835 1 1 7.639 4 2 8.73 4 1 .311 3 .0007775 1 1 7.81 4 2 7.81 4 1 .308 3 .00077 1 1 7.931 4 2 7.779 4 1 .306 3 .000765 1 1 8.2 4 2 7.74 4 1 .303 3 .0007575 1 1 1 4 1 5 1 Principal objective of the work PW TRC 3/5/2009 1 Osmotic coefficient Isopiestic method Liquid Direct value, X 5 Author Standard deviation of a single value (unbiased) Liquid Gas Temperature, K 298.15 5 1 Molality, mol/kg 4 Liquid 5 2 Molality, mol/kg 1 Liquid 5 1 .087 2 2 .437 3 1 .789 3 .00000789 1 1 .195 3 2 .488 3 1 .632 3 .00000632 1 1 .512 3 2 .512 3 1 .42 3 .0000042 1 1 .995 3 2 .498 3 1 .327 3 .00000327 1 1 1.421 4 2 .474 3 1 .272 3 .00000272 1 1 1.929 4 2 .482 3 1 .236 3 .00000236 1 1 2.482 4 2 .496 3 1 .211 3 .00000211 1 1 3.024 4 2 .504 3 1 .193 3 .00000193 1 1 3.524 4 2 .503 3 1 .18 3 .0000018 1 1 3.98 4 2 .498 3 1 .17 3 .0000017 1 1 4.461 4 2 .496 3 1 .161 3 .00000161 1 1 4.861 4 2 .486 3 1 .154 3 .00000154 1 1 .092 2 2 .923 3 1 .795 3 .00000795 1 1 .134 3 2 1.076 4 1 .749 3 .00000749 1 1 .522 3 2 1.044 4 1 .521 3 .00000521 1 1 1.147 4 2 1.147 4 1 .388 3 .00000388 1 1 1.813 4 2 1.209 4 1 .322 3 .00000322 1 1 2.394 4 2 1.197 4 1 .289 3 .00000289 1 1 2.963 4 2 1.185 4 1 .264 3 .00000264 1 1 3.515 4 2 1.172 4 1 .244 3 .00000244 1 1 4.005 4 2 1.144 4 1 .229 3 .00000229 1 1 4.471 4 2 1.118 4 1 .216 3 .00000216 1 1 4.831 4 2 1.074 4 1 .207 3 .00000207 1 1 5.167 4 2 1.033 4 1 .199 3 .00000199 1 1 .09 2 2 1.798 4 1 .892 3 .00000892 1 1 .23 3 2 2.3 4 1 .822 3 .00000822 1 1 .512 3 2 2.048 4 1 .692 3 .00000692 1 1 1.173 4 2 2.346 4 1 .487 3 .00000487 1 1 1.84 4 2 2.453 4 1 .385 3 .00000385 1 1 3.143 4 2 3.143 4 1 .299 3 .00000299 1 1 3.53 4 2 2.824 4 1 .283 3 .00000283 1 1 4.01 4 2 2.673 4 1 .27 3 .0000027 1 1 4.725 4 2 2.7 4 1 .258 3 .00000258 1 1 5.532 4 2 2.766 4 1 .247 3 .00000247 1 1 6.338 4 2 2.817 4 1 .238 3 .00000238 1 1 7.242 4 2 2.897 4 1 .228 3 .00000228 1 1 .1 3 2 3.996 4 1 .899 3 .00000899 1 1 .232 3 2 4.64 4 1 .841 3 .00000841 1 1 .562 3 2 4.496 4 1 .724 3 .00000724 1 1 1.478 4 2 5.912 4 1 .52 3 .0000052 1 1 2.299 4 2 6.131 4 1 .428 3 .00000428 1 1 4.426 4 2 8.852 4 1 .312 3 .00000312 1 1 5.101 4 2 8.162 4 1 .289 3 .00000289 1 1 8.132 4 2 10.843 5 1 .217 3 .00000217 1 1 8.75 4 2 10 5 1 .207 3 .00000207 1 1 9.524 4 2 9.524 4 1 .197 3 .00000197 1 1 10.455 5 2 9.293 4 1 .188 3 .00000188 1 1 12.124 5 2 9.699 4 1 .18 3 .0000018 1