Experimental studies and thermodynamic analysis of isobaric vapor-liquid-liquid equilibria of 2-propanol + water system using n-propyl acetate and isopropyl acetate as entrainers Janakey Devi, V.; Sai, P.; Balakrishnan, A.; Fluid Phase Equilibria 2017, 454, 22-34
Data
P = 101 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)
350.4 0.1007 0.8889 0.291 0.5365 0.19 0.3783
349.2 0.0278 0.9663 0.106 0.2632 0.0922 0.401
349.1 0.0222 0.974 0.0894 0.2373 0.083 0.399
348.9 0.0136 0.976 0.0557 0.235 0.0585 0.4059
348.8 0.0166 0.9768 0.0278 0.2245 0.0341 0.4101
348.6 0.0053 0.9776 0.011 0.2184 0.0188 0.4112
350.3 0.0725 0.9127 0.2742 0.4821 0.181 0.3803
350.2 0.0613 0.9229 0.2517 0.4352 0.1688 0.3864
350.0 0.0557 0.9258 0.2295 0.4024 0.1565 0.3873
349.9 0.0557 0.9306 0.207 0.3652 0.1412 0.3922
349.8 0.05 0.9334 0.1845 0.3355 0.132 0.3943
349.6 0.0444 0.9509 0.1623 0.2981 0.1229 0.3935
349.4 0.0332 0.9542 0.1397 0.285 0.1166 0.394
349.3 0.0278 0.9543 0.1274 0.2702 0.0983 0.3954
15529; 1-methylethyl ethanoate + propan-2-ol + water; 00004:00082:00200