2003-79-ctrl
In the case of a feed-forward control scheme, which of the following is NOT true?
2005-11-ctrl
Cascade control comes under the control configuration which uses
2007-62-ctrl
Consider the following instrumentation diagram for a chemical reactor. \(C_{SP}\) represents a concentration setpoint.
Match the items in column A with the corresponding items given in column B.
Column A |
Column B |
---|---|
P) control strategy |
1) feed forward control |
Q) primary control variable |
2) cascade control |
R) slowest controller |
3) concentration in the reactor |
S) fastest controller |
4) reactor temperature |
5) jacket temperature |
|
6) concentration controller |
|
7) reactor temperature controller |
|
8) jacket temperature controller |
|
9) flow controller |
|
10) selective control |
2004-81-ctrl
The process and disturbance transfer functions for a system are given by
\( \begin{align*} G_p(s) &= \frac{\bar{y}(s)}{m(s)} = \frac{2}{(2s+1)(5s+1)} \\ G_d(s) &= \frac{\bar{y}(s)}{d(s)} = \frac{1}{(2s+1)(5s+1)} \end{align*} \)
The feed forward controller transfer function that will keep the process output constant for changes in disturbance is
2014-46-ctrl
Given below is a simplified block diagram of a feedforward control system.
The transfer function of the process is \(G_p(s)=\dfrac{5}{s+1}\) and the disturbance transfer function is \(G_d(s)=\dfrac{1}{s^2+2s+1}\). The transfer function of the PERFECT feedforward controller, \(G_f(s)\) is
Match the following:
GROUP 1 | GROUP 2 |
(P) Ziegler Nichols | (1) Process reaction curve |
(Q) Under damped response | (2) Decay ratio |
(R) Feed-forward control | (3) Frequency response |
(4) Disturbance measurement |
Last Modified on: 02-May-2024
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