Coolant C AT Feed R D Steam S N AT XB В R S Run (Ib/min) (lb/min) Xp XB 1 125 22 0.97 0.04 150 22 0.95 0.05 3 175 22 0.93 0.06 4 150 20 0.94 0.06 5 150 24 0.96 0.04
Coolant C AT Feed R D Steam S N AT XB В R S Run (Ib/min) (lb/min) Xp XB 1 125 22 0.97 0.04 150 22 0.95 0.05 3 175 22 0.93 0.06 4 150 20 0.94 0.06 5 150 24 0.96 0.04
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Question
A conventional multiloop control scheme consisting of two PI controllers is to be used to control the product compo-sition sxD and xB of the distillation column shown in Fig.The manipulated variables are the reflux flow rate R and thesteam flow rate to the reboiler S. Experimental data for a num-ber of steady-state conditions are summarized below. Use thisinformation to do the following:(a)Calculate the RGA and determine the recommended pair-ing between controlled and manipulated variables.(b)Does this pairing seem appropriate from dynamic consid-erations? Justify your answer
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