• edited by
0 0 votes

The transfer function of a Proportional-Integral $\text{(PI)}$ controller $G_{C}(s)$ is given by

\[
G_{C}(s)=K_{C}\left(1+\frac{1}{\tau_{I} s}\right)
\]
where $K_{C}$ is the controller gain, $\tau_{I}$ is the controller integral time constant and $s$ is the Laplace variable. The role of the integral component of the controller is to $\_\_\_\_$.

  1. integrate the difference between the process and manipulated variable
  2. integrate the difference between the set point and disturbance variable
  3. integrate the difference between the set point and the measured variable
  4. integrate the difference between the input and output variable

Please log in or register to answer this question.

Answer:

Related questions

0 0 votes
0 0 answers
gatecse asked Feb 23
In the open-loop process shown in the figure, the input $U(s)$, the transfer function $G_{p}(s)$ and the output $Y(s)$ are given in the Laplace domain in terms of the Lap...
0 0 votes
0 0 answers
Lakshman Bhaiya asked Mar 20, 2022
Which of the following statements are $\text{CORRECT}$ for a controller?In a proportional controller, a control action is proportional to the errorIn an integral controll...
0 0 votes
0 0 answers
go_editor asked Mar 1, 2021
The process and instrumentation diagram for a feedback control strategy to maintain the level $(h)$ of a liquid by regulating a valve $(V)$ in a tank is shown below. $F_1...
0 0 votes
0 0 answers
gatecse asked Feb 23
For a Newtonian fluid, a plot of shear stress (on $\text{Y}$ axis) against shear rate (on $\text{X}$ axis) will result in a straight line $\_\_\_\_$.parallel to the $\tex...
0 0 votes
0 0 answers
gatecse asked Feb 23
In an aerobic fermentation with air sparging, which of the following options can be used to increase the volumetric mass transfer coefficient for oxygen transfer?Using pu...