4.13 A horizontal cylindrical tank shown in Fig. E4.13a is used to slow the propagation of liquid flow surges in a processing line. Figure E4.13b illustrates an end view of the tank and w, is the width of the liquid surface, which is a function of its height, both of which can vary with time. Develop a model for the height of liquid h in the tank at any time with the inlet and out- let volumetric flow rates as model inputs. Linearize the model assuming that the process initially is at steady state and that the liquid density p is constant. Chap di vion md-Order Figure E4.13a R-h R- w:/2" W;- Figure E4.136
4.13 A horizontal cylindrical tank shown in Fig. E4.13a is used to slow the propagation of liquid flow surges in a processing line. Figure E4.13b illustrates an end view of the tank and w, is the width of the liquid surface, which is a function of its height, both of which can vary with time. Develop a model for the height of liquid h in the tank at any time with the inlet and out- let volumetric flow rates as model inputs. Linearize the model assuming that the process initially is at steady state and that the liquid density p is constant. Chap di vion md-Order Figure E4.13a R-h R- w:/2" W;- Figure E4.136
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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Transcribed Image Text:4.13 A horizontal cylindrical tank shown in Fig. E4.13a is used
to slow the propagation of liquid flow surges in a processing
line. Figure E4.13b illustrates an end view of the tank and w, is
the width of the liquid surface, which is a function of its height,
both of which can vary with time. Develop a model for the
height of liquid h in the tank at any time with the inlet and out-
let volumetric flow rates as model inputs. Linearize the model
assuming that the process initially is at steady state and that
the liquid density p is constant.
Transcribed Image Text:Chap
di
vion
md-Order
Figure E4.13a
R-h
R-
w:/2"
W;-
Figure E4.136
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