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Semiconductor and pharmaceutical industries often produce waste alcohol mixtures. This study discusses a reactive distillation process of a mixed alcohol feed containing n-amyl alcohol and n-hexanol to react with acetic acid to produce useful esters. In an earlier paper (Lee et al. Ind. Eng. Chem. Res. 2009 48, 7186–7204), optimal design of the same Type-III mixed-alcohol reactive distillation process containing n-butanol and n-amyl alcohol was developed. In that paper, the indirect sequence containing a reactive distillation column with heavier amyl acetate bottom product and a second column to produce butyl acetate gives the lowest total annual cost. In this study, with different mixed alcohol feed (although of the same reaction type), it is found that an alternative direct sequence design is much more economically favorable with 34% reduction in total annual cost as compared to the indirect sequence. The reason for the seemingly contradictory results can be explained by differences in relative volatili...

Manufacturing processes in the semiconductor and pharmaceutical industries often produce alcohol mixture byproducts. Therefore, the esterification of alcohol mixtures may be an important step in re...

Vapor-liquid equilibria were measured for the three binary systems made of methyl ethyl ketone with acetone, methyl acetate, or n-amyl alcohol at 100 kPa of pressure by the dew-point-bubble-point temperature apparatus previously proposed by the authors was modified in the present study. Combining the experimental dew-point and bubble-point temperature curves, vapor-liquid equilibria were obtained without using any analytical instrument

Vapor-llquld equHMwn data for the blnary 8ystems ethylene glycol (1,?4hanedbl) wlth n-amyl alcohol (1-pentanol) and ethylene glycol wlth Isoamyl alcohol (3-methyi-l-bulanol) have been measured at 100 mmHg (13.33 kPa) by ushg a reclrculatbn stll a8 propowd by Rbck and Sleg. From these data, Uquld-phare activity coetfldents were flttod by wing the MarguJes, van Laar, Wilson, and UNIQUAC equations. Vapor-prereure meawr(MIBnts of the pure substances were carrled out, and the data were correlated wlth the Antolne equatlon. The Wnaty data were used for the determlnatlon of UNIFAC parameters.