作者: Nada Abdulrazzaq , Baseem Al-Sabbagh , Julia M. Rees , William B. Zimmerman
DOI: 10.1002/AIC.15097
关键词: Mass transfer 、 Distillation 、 Azeotrope 、 Analytical chemistry 、 Evaporation 、 Chemistry 、 Zeotropic mixture 、 Batch distillation 、 Mole fraction 、 Bubble
摘要: The feasibility of separating the azeotropic mixture ethanol-water using microbubble-mediated batch distillation is presented. effects depth liquid in bubble tank and inlet air microbubble temperature on process efficiency were investigated. enrichment ethanol vapor phase was higher than that achieved at equilibrium conditions for all mole fractions considered, including azeotrope. On decreasing increasing microbubbles, separation improved. Ethanol with purity about 98.2 vol % obtained lowest level (3 mm) conjunction highest (90°C). Separation a small rise (4°C) 3 mm evaporation time 90 min making this system suitable treating thermally sensitive mixtures. © 2015 American Institute Chemical Engineers AIChE J, 62: 1192–1199, 2016