Geometric Structures of Associating Component Optimized toward Correlation and Prediction of Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanal, Ethanol, and Ethanoic Acid Zhu, D.; Gao, D.; Zhang, H.; Winter, B.; Lücking, P.; Sun, H.; Guan, H.; Chen, H.; Shi, J.; Journal of Chemical & Engineering Data 2013, 58, 7-17
Data
P = 101.325 kPa
T (K) x (mol mol-1) x (mol mol-1) x (mol mol-1) x (mol mol-1)
296.40 0.9050 0.095 0.0047 0.9953
306.86 0.6605 0.0694 0.0078 0.9868
308.47 0.6334 0.0665 0.0084 0.9848
310.29 0.6063 0.0637 0.0091 0.9824
312.43 0.5791 0.0608 0.0099 0.9795
315.00 0.5520 0.058 0.0108 0.9759
318.24 0.5249 0.0551 0.0118 0.9715
321.28 0.4974 0.0522 0.013 0.966
322.82 0.4200 0.5246 0.126 0.8712
324.83 0.3901 0.5517 0.1509 0.8457
325.99 0.3602 0.5788 0.1808 0.8151
297.28 0.8777 0.0922 0.0049 0.9948
328.28 0.3301 0.606 0.2167 0.7782
330.87 0.3001 0.6332 0.2591 0.7346
333.53 0.2700 0.6603 0.3091 0.6832
337.18 0.2400 0.6875 0.3668 0.6238
339.41 0.2101 0.7145 0.4321 0.5563
341.49 0.1801 0.7417 0.505 0.481
344.39 0.1501 0.7688 0.5839 0.3992
346.64 0.1201 0.7959 0.6666 0.3133
349.27 0.0900 0.8232 0.7502 0.2262
350.21 0.0599 0.8504 0.8306 0.1419
298.06 0.8504 0.0893 0.0052 0.9943
350.99 0.0301 0.8774 0.9028 0.0656
364.73 0.0587 0.3599 0.6351 0.1177
365.94 0.0615 0.3299 0.6076 0.1265
366.79 0.0642 0.2999 0.5778 0.1358
367.72 0.0670 0.2699 0.5453 0.1462
368.87 0.0698 0.2399 0.5096 0.1575
370.66 0.0725 0.2098 0.4701 0.17
371.65 0.0753 0.1798 0.4265 0.1835
372.80 0.0780 0.1498 0.3777 0.1983
374.46 0.0808 0.12 0.3229 0.215
298.93 0.8233 0.0865 0.0054 0.9936
376.10 0.0835 0.09 0.2601 0.2337
377.68 0.0862 0.0601 0.1876 0.2548
379.30 0.0890 0.0301 0.1023 0.2797
398.72 0.0521 0.0224 0.0309 0.3632
299.70 0.7962 0.0836 0.0057 0.9929
300.71 0.7691 0.0808 0.0061 0.992
301.94 0.7419 0.0779 0.0064 0.991
303.91 0.7148 0.0751 0.0068 0.9899
305.28 0.6877 0.0722 0.0073 0.9885
22548; ethanol + acetic acid + ethanal; 00051:00071:00726