Phase equilibria and excess properties for binary systems in reactive distillation processes. Part II. Ethyl acetate synthesis Brandt, S.; Horstmann, S.; Steinigeweg, S.; Gmehling, J.; Fluid Phase Equilibria 2014, 376, 48-54
Data
T = 323.15 K
x (mol mol-1) P (kPa)
0 7.61
0.0384 8.9
0.0526 9.38
0.0699 9.97
0.0904 10.67
0.1163 11.56
0.1455 12.55
0.1781 13.66
0.2133 14.85
0.2505 16.1
0.2895 17.39
0.0012 7.65
0.3287 18.65
0.3298 18.7
0.3677 19.89
0.3702 20.0
0.4104 21.21
0.4109 21.28
0.4572 22.64
0.5073 24.13
0.5601 25.66
0.6150 27.21
0.0022 7.69
0.6710 28.76
0.7260 30.25
0.7793 31.67
0.8243 32.87
0.8647 33.96
0.8993 34.88
0.9275 35.67
0.9502 36.31
0.9654 36.76
0.9760 37.08
0.0035 7.73
0.9842 37.33
0.9897 37.5
0.9952 37.68
0.9976 37.76
1 37.85
0.0057 7.8
0.0082 7.88
0.0125 8.03
0.0184 8.23
0.0272 8.52
3410; acetic acid + ethyl ethanoate; 00019:00051