Vapor-Liquid-Liquid Equilibria Measurements for the Dehydration of Ethanol, Isopropanol, and n-Propanol via Azeotropic Distillation Using DIPE and Isooctane as Entrainers Pienaar, C.; Schwarz, C.E.; Knoetze, J.H.; Burger, A.J.; Journal of Chemical & Engineering Data 2013, 58, 537-550
Data
P = 101.3 kPa
T (K) x (mol mol-1) x (mol mol-1) x (mol mol-1) x (mol mol-1) x (mol mol-1) x (mol mol-1)
335.31 0.0476 0.9524 0.9991 0.0009 0.7814 0.2186
334.56 0.152 0.5959 0.8852 0.0036 0.6299 0.1927
334.47 0.1635 0.5899 0.8852 0.0042 0.6188 0.1731
334.55 0.1738 0.5667 0.8798 0.0044 0.6306 0.1881
334.77 0.1951 0.5081 0.8644 0.0043 0.6196 0.1891
334.84 0.2599 0.4197 0.853 0.0019 0.6195 0.1866
334.92 0.2629 0.4157 0.8365 0.0077 0.6147 0.1798
335.03 0.3408 0.3132 0.8201 0.0108 0.6081 0.1886
335.04 0.3473 0.2972 0.7858 0.0178 0.5982 0.1889
335.37 0.3813 0.2594 0.7761 0.0208 0.6034 0.1821
335.22 0.3941 0.2551 0.759 0.0211 0.6081 0.188
334.53 0.0605 0.8805 0.9636 0.0012 0.7049 0.21
335.39 0.7927 0.0131 0.7954 0.0127 0.584 0.1945
336.29 0.7644 0.016 0.7674 0.0141 0.577 0.207
334.40 0.0644 0.8498 0.951 0.0016 0.6945 0.201
334.16 0.0877 0.7844 0.9231 0.0015 0.667 0.1974
334.25 0.0997 0.7194 0.9161 0.0024 0.6631 0.1861
334.27 0.1051 0.7134 0.9221 0.0019 0.6597 0.1888
334.19 0.1168 0.6733 0.9128 0.0011 0.6219 0.1826
334.42 0.1232 0.6499 0.9004 0.0029 0.6447 0.1879
334.38 0.1451 0.6029 0.8845 0.0038 0.6391 0.1944
22556; ethanol + diisopropyl ether + water; 00004:00071:00250