Consider the storage tank. Assume that flow rates of all free streams are linear function of corresponding liquid leve It is known that F, =2 (ft³) xh (ft) uSEngen eeee ft-min. Flow rates given in the figure are steady state values ft³ F; = 3- min min genusEngeniuSEngeniusEngenjus h igenusEngenuSEngenusEngenus Pump A = 2ft? If a transfer function is developed between Ħ (s) = TpS+1 K, {F(6) + F()} it Then Kp = 1, Tp = ; 2 - Kp = ;,Tp 2 ● Kp = ,Tp Tp = 2 = 1 genu 3 ° Kp = = 1, Tp | 2 ||

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
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Problem 1.1P
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Consider the storage tank. Assume that flow rates of all free streams are linear function of corresponding liquid level.
F2
It is known that
(ft³)
EngenusEngeniusEngeniusEngenust
xh (ft)
eeee
eeee
=2
ft-min.
Flow rates given in the figure are steady state values
ft
ft³
= 1-
min
%3D
F = 3-
min
genusEngenuSEngeniusEngenjusE
genusEngeniuSEngenusEngenusE
Pump
eee e
= 2ft?
If a transfer function is developed between
Kp
H (s)
{F(6) + F,()}
TpS +1
Then
Ingen
© Kp
Кр
= 1,tp = ;
2
1
1
Kp = ;,Tp
ngenu
2
2
Кр
1
||
Tp =
genu
3
Кр — 1, Тр
%3
Transcribed Image Text:Consider the storage tank. Assume that flow rates of all free streams are linear function of corresponding liquid level. F2 It is known that (ft³) EngenusEngeniusEngeniusEngenust xh (ft) eeee eeee =2 ft-min. Flow rates given in the figure are steady state values ft ft³ = 1- min %3D F = 3- min genusEngenuSEngeniusEngenjusE genusEngeniuSEngenusEngenusE Pump eee e = 2ft? If a transfer function is developed between Kp H (s) {F(6) + F,()} TpS +1 Then Ingen © Kp Кр = 1,tp = ; 2 1 1 Kp = ;,Tp ngenu 2 2 Кр 1 || Tp = genu 3 Кр — 1, Тр %3
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