Problem 1. For the figure shown below: U(s) 10 s+5 Controller Plant s+ 1 Sensor a)...
Q4. The feedback system shown below has a plant, a controller, and sensor transfer functions as G(s), Gc(s) and H(s), respectively. Find the output Y(s) and the input U(s) as a function of the inputs and transfer functions. (2 Points) D(s) R(s) + U(s) Gc (s) O G(s) - Y(s) H(S)
C(8) for the system shown in Figure 1. R(S Find the equivalent transfer function, Geg (s) 1 Cix) Figure 1. Block diagram 2s+1 s(5s+6Ge(s) = and Figure 2 shows a closed-loop transfer function, where G(s) 2. proper H(s) K+s. Find the overall closed-loop transfer function and express is as rational function. C(s) Ea (s) Controller R(s) +/ Plant G(s) Ge (s) Feedback H(s) Figure 2. Closed loop transfer function Construct the actuation Error Transfer Function associated with the system shown...
Problem 4) (20 Pts.) A Proportional controller is simply a gain block. In figure below, it is the block with gain 2nd order underdamped plant as shown. Kc which is behind the a) Simplify below block diagram to obtain the overall feedback system transfer funion)R(G) b) Choose Kc so that the overall feedback system transfer function G(s) has 50% overshoot due to a step input (called quarter decay ratio tuning) d) The feedback system transfer function Gs)- is faster than...
Implement a PID controller to control the transfer function
shown below. The PID controller and plant transfer function should
be in a closed feedback loop. Assume the feedback loop has a Gain
of 5 associated with it i.e. . The Transfer function of a PID
controller is also given below. Start by:
6. Implement a PID controller to control the transfer function shown below. The PID feedback loop has a Gain of 5 associated with it i.e. (HS) = 5)....
7.16C). Given the control system shown in Figure P7.16 where the plant transfer function G(o) is given by 2.0 design a PID controller for this system. Cis) R(s) 2.0 sis+ 1)(s+3) Plant PID controller FIGURE P7.16
7.16C). Given the control system shown in Figure P7.16 where the plant transfer function G(o) is given by 2.0 design a PID controller for this system. Cis) R(s) 2.0 sis+ 1)(s+3) Plant PID controller FIGURE P7.16
1. Consider a feedback system given below: T(s) Disturbance Controller Dynamics R(S) + Gc(s) G.(s) U(s) Sensor H(s) IMs) Sensor noise where the input and transfer functions are given as follows: R(s) = –,7,(s) = 0, N(s) = 0, G, - 15,6, -_- , and H(s) = 1. s's + 3) a. Derive the system transfer function Y(s)/R(s) = G,, poles, $, On, and, from the response function y(t), the performance measures: rise time Tr, peak time Tp, percent overshoot...
on Matlab please!!!!
Problem 1- (a) Design a controller for a plant with transfer function, G(s)-(+ to obtain (i) estep(00)s 0, (ii) T12%) < 1 s, and (iii) an-5 rad/s (4 points). (b) Plot the unit step response of the closed-loop system you design and find the percentage of overshoot, the time to the first peak, settling time and eramp[oo) (4 points). (c) Can you modify your design, without compromising design specifications, in order to further shorten T1296) while keeping...
10.Represent the translational mechanical system shown in the Figure in state- space, where xX3(t) is the output IN- 11.Find the state equations and output equation for the phase-variable representation of the transfer function G(s) 2s+1/(s2+7s+ 9) 12. Convert the state and output equations shown to a transfer function. -1.5 2 u(t) X = X 4 0 Y [1.5 0.625]x 13. For each system shown, write the state equations and the output equation for the phase- variable representation 8s10 sh25 t26...
Given the control system shown in Figure P7.I6 where the plant transfer function Gis) is given by лис, 2.0 Ds + 3) ss design a PID controller for this system. Cis) 2.0 sis + 1)(s+3 R(s) Plant PID controller FIGURE P7.16
Given the control system shown in Figure P7.I6 where the plant transfer function Gis) is given by лис, 2.0 Ds + 3) ss design a PID controller for this system. Cis) 2.0 sis + 1)(s+3 R(s) Plant PID controller...
15.3 A conventional controller is to be used in the scheme shown below in Figure P15.1 for controlling the exit temperature of the industrial heat exchanger first introduced in Problem 14.2. Assuming that Tz, the brine temperature (in °C), remains constant, the transfer function relations for the process have been previously given as: 1 -0.5e-10* (40s I)(15s)(BB (P14.3b) Assume that the valve dynamics are negligible. (a) Use the provided model in a control system simulation package to obtain a process...