Refer to the image below of a Proportional-Integral (PI) Controller: d(s) 1 K. (1 + ) Yap (s). TpS + 1 Tms + 1 If t, = T, = Tm = 1 and K. = 2: a) Determine the overall transfer function for a servo problem using the. b) Determine the overall transfer function for a regulatory problem. c) Response to a unit step change for a change in the set point at the t-domain as y(t)?

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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Refer to the image below of a Proportional-Integral (PI) Controller:
d(s)
Yep (S).
K. (1+ T5)
-y(s)
Tps + 1
1
Tms + 1
If t, = Tp = Tm
= 1 and K. = 2:
a) Determine the overall transfer function for a servo problem using the.
b) Determine the overall transfer function for a regulatory problem.
c) Response to a unit step change for a change in the set point at the t-domain as y(t)?
d) Response to a unit step change for regulatory at the t-domain as y(t)?
Transcribed Image Text:Refer to the image below of a Proportional-Integral (PI) Controller: d(s) Yep (S). K. (1+ T5) -y(s) Tps + 1 1 Tms + 1 If t, = Tp = Tm = 1 and K. = 2: a) Determine the overall transfer function for a servo problem using the. b) Determine the overall transfer function for a regulatory problem. c) Response to a unit step change for a change in the set point at the t-domain as y(t)? d) Response to a unit step change for regulatory at the t-domain as y(t)?
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