𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Design calculations for batch distillation column

✍ Scribed by J.P.W. Houtman; Asghar Husain


Publisher
Elsevier Science
Year
1956
Tongue
English
Weight
782 KB
Volume
5
Category
Article
ISSN
0009-2509

No coin nor oath required. For personal study only.

✦ Synopsis


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, reflux ratio, and holdup, in order to obtain a required separation. A nomograph is provided to simplify the calculations. Directions are given for selecting the best column out of the available ones, or for adjusting the amount of charge in case only one column is available. RBsumB-On snalyse l'equation developpee par ZurDEawEo [S] en indiquant le rappart entre l'exactitude de separation dans la distillation discontinue d'une part et le nombre de plateaux theoriques, le rapport du reflux et le sejour dans la colonne d'autre part. En se basant sur ce qui p&&de, on propose une methode pour choisir la combinaison la plus utile du nombre de plateaux theoriques, du rapport de reflux et du sejour afin d'obtenir la separation requise. Ensuite on donne une nomographie pour simplifier les calculs. Sont donnees encore des directives pour choisir la meilleure des colonnes disponibles ou de mettre au point la quantite de la charge en cas qu'il n'y ait qu'une seule colonne de disponible.


πŸ“œ SIMILAR VOLUMES


An efficient design method for binary, a
✍ Urmila M. Diwekar πŸ“‚ Article πŸ“… 1991 πŸ› American Institute of Chemical Engineers 🌐 English βš– 667 KB

## Abstract Using rigorous models to simulate batch distillation involves the solution of many stiff differential equations. The dimensionality of the problem also increases with an increase in the number of plates and components, which imposes limitations on the use of rigorous models. Furthermore

Backstepping-based cascade control schem
✍ Rosendo Monroy-Loperena; Jose Alvarez-Ramirez πŸ“‚ Article πŸ“… 2004 πŸ› American Institute of Chemical Engineers 🌐 English βš– 267 KB πŸ‘ 3 views

## Abstract Nonstationary dynamics, finite‐time operation, large thermodynamical uncertainty and delayed composition measurements make the control of batch distillation processes a challenging and interesting problem. In this paper, a cascade control design to regulate the overhead composition of a