(a):
Let the plant transfer function be Gp.
E(s) = R(s)-Y(s);
F(s) = Gc(s)*E(s)
Y(s) = Gp(s)*(D(s)+F(s)) = Gp(s)*(D(s)+ Gc(s)*E(s)) = Gp(s)*(D(s)+ Gc(s)*R(s)- Gc(s)*Y(s))
= Gp(s)*D(s)+ Gp(s)*Gc(s)*R(s)- Gp(s)*Gc(s)*Y(s)
=>Y(s)(1+Gp(s)*Gc(s)) = Gp(s)*D(s)+ Gp(s)*Gc(s)*R(s)
Transfer function from r to y is:
(b):
Steady state value for a unit step input can be obtained by setting the parameter 's' in the transfer function to 0.
Therefore, the steady state values is:
Steady state error is:
For this value to be with in 5% and for the system to be stable,
=> Kp>1.9
(c):
So, the time constant is
which is the time required to reach 63%. For this to be equal to 1,
Kp = 0.9.
(d):
For the steady state error to be less, the value of the proportional controller should be high to have enough influence and reduce the error. But this would also lead to faster response of the system. This means the time constant would be small. Therefore, it is not possible to satisfy both the conditions in this case.
An integral controller in addition to the proportional part would solve the issue. The proportional part which has a major influence on time constant can be reduced, where as the integral part can reduce the steady state error.
(e):
the steady state values is:
Therefore, the steady state error is 0.
(f):
The characteristic equation is s2+0.1s+Ki = 0. Comparing it to the standard equation gives,
The overshoot is given by:
=> Ki = 0.00715
(g):
Settling time for 2% range is approximately given by:
Ts = 1 => Ki = 45.762
(h):
The transfer function between E and D is:
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