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Question 2 A steam heated stirred tank ( similar to the one shown in Figure Q 3 ) has the following operating conditions and constant

Question 2
A steam heated stirred tank (similar to the one shown in Figure Q3) has the following operating
conditions and constant parameters:
Mass flow rate, w=104kghr
Density, =1000kgm3
Volume of the tank, V=100m3
Heat capacity, C=1kcalkg.C
Latent heat of vaporization, Hv=600kcalkg
Figure Q2: Steam-heated stirred-tank system.
The controlled variable, CV, is the tank temperature (T), the manipulated variable, MV, is the
steam rate (ws), and the disturbance variable DV, is the inlet temperature ({:Ti). The set point of
the CV is Tsp=150C and the steady state inlet temperature ?bar(T)i is 40C.
(i) Process Modelling and transfer function
(a) Develop a dynamic model for this system that will describe transient operation and that
can be used to find the tank temperature T.
(b) What is the steady state steam flow rate at the set point temperature?
(c) Write the dynamic model in terms of deviation variables and derive the process transfer
function, GP=T'sW'(s) and the disturbance transfer function
Gd=T'sTi'(s) for this process. What are the orders of both transfer function?
Define and calculate the values of process gains and time constants for both transfer
functions (include units)?
(ii) Process control design
(a) It is desired to control the tank outlet temperature, T :
Propose a feedback control method and sketch the schematic diagram
Suggest a feedforward control method and sketch the schematic diagram.
(b) Construct the block diagram of the feedback control system.
(c) Determine the closed-loop transfer function TsTi(s) of the system and using the
final value theorem calculate the offset for a unit step changes in disturbance.
(d) Determine the closed-loop transfer function [TsTsp(s)] of the system and using the
final value theorem calculate the offset for a unit step changes in set-point.
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