There has been such a bewildering flow of information, dealing especially with the principles of stage calculations, that the engineer who is not a distillation expert finds himself at a loss as to how to select the best procedures for solving his distillation problems. The literature abounds with information on all phases of distillation calculations and design. Printed and bound by Q u i i - Woorib'ine. Library of Congress Cataloging in Publication Data Henley, Ernest J Equilibrium-stage separation operations in chemical engineering.

Requests for permission or further information should be addressed to the Permissions Department, John Wiley & Sons. Reproduction or translation of any part of this work beyond that permitted by Sections 107 and 108 of the 1976 United States Copyright Act without the permission of the copyright owner is unlawful. Column shown was designed by one of the authors.ĭIPARTIMENTQ Dl INGEGNERIA CHlMK DEl PROCESS1 E DEI MATERIAL1Ĭopyright 1981, by John Wiley & Sons, Inc. Macco Refinery and Chemical Division, California, was the prime contractor for construction. The lift was one of the heaviest ever accomplished in the U.S.with a load of this type. Seader Professor of Chemical Engineering University of UtahĪ 350-ton deisobutanizer distillation column, 212 feet high, was raised into position in one piece at the El Segundo refinery of Standard Oil Co. Henley Professor of Chemical Engineering University of Houston Equilibrium-Stage Separation Operations in Chemical Engineering Ernest J.

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