EXTRACTIVE DISTILLATION EMPLOYING A DISSOLVED SALT AS SEPARATING AGENT

被引：50

作者：

COOK, RA

FURTER, WF

机构：

[1] Department of Chemical Engineering, Royal Military College of Canada, Kingston, Ontario

来源：

CANADIAN JOURNAL OF CHEMICAL ENGINEERING | 1968年 / 46卷 / 02期

关键词：

D O I：

10.1002/cjce.5450460209

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

A process of extractive distillation, employing a dissolved salt rather than a liquid solvent as separating agent, was studied on a pilot plant scale. Aqueous ethanol was fractionated in a 12‐tray, bubble cap column with potassium acetate present in the liquid phase. Even relatively small concentrations of salt eliminated the azeotrope. An overhead product completely free of separating agent was obtained directly from the column. A technique is described for metering salt at a steady rate, and for achieving rapid solution of the salt in the reflux stream. Copyright © 1968 Canadian Society for Chemical Engineering

引用

页码：119 / &