2.4 Consider a liquid flow system consisting of a sealed tank with noncondensible gas s above the liquid as shown in Fig. E2.4. Derive an unsteady-state model relating the liquid level h to the input flow rate q;. Is operation of this system independent of the ambient pressure P,? What about for a system open to the atmosphere? You may make the following assumptions: (i) The gas obeys the ideal gas law. A constant amount of mJM moles of gas is present in the tank. (ii) The operation is isothermal. (iii) A square root relation holds for flow through the valve. di Pg Ра th Н h ic to Cy ne Cross-sectional area = A nd

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
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Just perform degree of freedom analysis identifying all model constants, input variables and output variables. 

 

Book: Process Dynamics and Control, Third Edition or Fourth Edition, by D. E. Seborg, T. F. Edgar, D. A. Mellichamp, F. J. Doyle III, John Wiley & Sons, Inc, 2011

 

2.4 Consider a liquid flow system consisting of a sealed tank
with noncondensible gas above the liquid as shown in Fig. E2.4.
Derive an unsteady-state model relating the liquid level h to
the input flow rate q;. Is operation of this system independent
of the ambient pressure P,? What about for a system open to
the atmosphere?
You
may
make the following assumptions:
(i) The gas obeys the ideal gas law. A constant amount of
m.JM moles of gas is present in the tank.
(ii) The operation is isothermal.
(iii) A square root relation holds for flow through the valve.
di
Pg
Ра
th
Н
ic
to
Cy
ne
Cross-sectional
area = A
nd
Transcribed Image Text:2.4 Consider a liquid flow system consisting of a sealed tank with noncondensible gas above the liquid as shown in Fig. E2.4. Derive an unsteady-state model relating the liquid level h to the input flow rate q;. Is operation of this system independent of the ambient pressure P,? What about for a system open to the atmosphere? You may make the following assumptions: (i) The gas obeys the ideal gas law. A constant amount of m.JM moles of gas is present in the tank. (ii) The operation is isothermal. (iii) A square root relation holds for flow through the valve. di Pg Ра th Н ic to Cy ne Cross-sectional area = A nd
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