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Calculation procedures for binary batch rectification

✍ Scribed by Charles E. Huckaba; Donald E. Danly


Publisher
American Institute of Chemical Engineers
Year
1960
Tongue
English
Weight
1019 KB
Volume
6
Category
Article
ISSN
0001-1541

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✦ Synopsis


Abstract

A rigorous mathematical description, consisting of differential‐difference equations, is presented for binary batch rectification in the plate type of column. Two approaches are taken to solving these equations for the condition of constant reflux ratio: an integration by numerical means employing an IBM 650 computer, and a hand calculation procedure that involves trial‐and‐error computation of batch‐rectification curves, which is of interest primarily where high‐speed computing equipment is not available.

Enthalpy balances are used to avoid assumption of equal rate of overflow in the tower; weight units are used instead of mole units; means for accounting for holdup in the condenser‐accumulator system are described. Criteria of convergence and stability of the numerical solution are presented. The validity of the results of the proposed calculation procedures is substantiated by the close agreement of experimental and calculated batch‐rectification curves.


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✍ J.P.W. Houtman; Asghar Husain 📂 Article 📅 1956 🏛 Elsevier Science 🌐 English ⚖ 782 KB

The equation developed by ZUIDERWEG [3], relating sharpness of separation in batch distillation to number of theoretical plates, reflux ratio, and holdup of the column, has been analysed. Based upon this, a method is suggested to choose the most useful combination of number of theoretical plates, re