In this study the controller for three tank multi loop system is designed using coefficient Diagram
method. Coefficient Diagram Method is one of the polynomial methods in control design. The
controller designed by using CDM technique is based on the coefficients of the characteristics
polynomial of the closed loop system according to the convenient performance such as equivalent
time constant, stability indices and stability limit. Controller is designed for the three tank process
by using CDM Techniques; the simulation results show that the proposed control strategies have
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• PID tunning by MATLAB.
• Comparative performance analysis of PI, PD and PID Controllers
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Objective:
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In this study the controller for three tank multi loop system is designed using coefficient Diagram method. Coefficient Diagram Method is one of the polynomial methods in control design. The controller designed by using CDM technique is based on the coefficients of the characteristics polynomial of the closed loop system according to the convenient performance such as equivalent time constant, stability indices and stability limit. Controller is designed for the three tank process by using CDM Techniques; the simulation results show that the proposed control strategies have good set point tracking and better response capability.
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synchronous Buck Converter. The proposed control involves one voltage
control loop. Analog Type-3 controller is designed for Buck Converter using
standard frequency response techniques.Type-3 analog controller transforms
to 3P3Z controller in discrete domain.Matlab/Simulink model of the Buck
Converter with digital controller is developed. Simualtion results for steady
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Liquid level tanks are employed in many industrial and chemical areas. Their level must be keep
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depending on the sizes of the liquid level tank. According to some proportional-integralderivative
(PID) parameters, the model was simulated by using MATLAB/Simulink program.
After that, data of the liquid level tank were taken into a computer by employing data
acquisition cards (DAQs). Lastly, the computer-controlled liquid level control was successfully
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6. The figure shows the digital control system. When controller
gain K is unity and sampling time is 0.5 sec determine :
a) The open loop pulse transfer function
b) The closed loop pulse transfer function
c) Difference equation for discrete time response
d) Steady state value of system output
Example-1
17. Example-1
• Using the three approximation methods to find the discrete-
time equivalent of a lead compensator.
• Compare the approximation result by plotting the frequency
response of the continuous-time controller and the discrete-
time approximation for sampling periods T = 1, 0.5 and 0.1.
17
𝐺 𝑠 =
10𝑠 + 1
𝑠 + 1
18. Example-1
• Solution: The approximations give the following relations:
• Using Euler’s approximation method
18
𝐺 𝑧 =
10(
𝑧 − 1
𝑇
) + 1
𝑧 − 1
𝑇
+ 1
=
10 𝑧 − 1 + 𝑇
𝑍 − 1 + 𝑇
19. Example-1
• Solution: The approximations give the following relations:
• Using Backward Difference approximation method
19
𝐺 𝑧 =
10(
𝑧 − 1
𝑧𝑇
) + 1
𝑧 − 1
𝑧𝑇
+ 1
=
10 𝑧 − 1 + 𝑧𝑇
𝑍 − 1 + 𝑧𝑇
24. PI Controller
• Figure shows the diagram of a PI type analog controller.
• The controller contains two channels (a proportional channel
and an integral channel) that process the error between the
reference signal and the output.
24
25. Digital PI Controller
• Digital PI control law can even be obtained by the
discretization of a PI analog controller.
• The control law for an analog PI controller is given by
• Using Tustin’s Approximation method
25
𝐶(𝑠) = 𝐾 1 +
1
𝑇𝑖𝑠
𝑖. 𝑒 𝑠 =
2
𝑇
𝑧 − 1
𝑧 + 1
𝐶(𝑧) = 𝐾 1 +
1
𝑇𝑖
2
𝑇
𝑧 − 1
𝑧 + 1
26. Digital PID Controller
• Many practical control problems are solved by PID controllers
or their variants.
• The continuous-time transfer function of a PID controller can
be obtained by taking the Laplace transform of above eq
• PID controller is non-causal and cannot, and should not, be
implemented.
26
𝑢(𝑡) = 𝐾𝑝 𝑒 𝑡 +
1
𝑇𝑖
න
𝑜
𝑡
𝑒 𝑡 𝑑𝑡 + 𝑇𝑑
𝑑𝑒(𝑡)
𝑑𝑡
𝐶𝑝𝑖𝑑(𝑠) =
𝐾𝑝(𝑇𝑖𝑇𝐷𝑠2
+ 𝑇𝑖𝑠 + 1)
𝑇𝑖𝑠
27. Digital PID Controller
• The main reason is that the derivative term is non-causal and that
it amplifies high frequency noise in the measured signals.
• Hence, the gain of the derivative action must be limited.
• This can be achieved by introducing an additional low-pass filter
to the derivative action:
27
𝐶𝑝𝑖𝑑(𝑠) =
𝐾𝑝(𝑇𝑖𝑇𝐷𝑠2
+ 𝑇𝑖𝑠 + 1)
𝑇𝑖𝑠
𝐾𝐷𝑠 ≈
𝐾𝐷𝑠
𝜏𝐿𝑠 + 1
28. Digital PID Controller
• With the augmentation of a low pass filter, the modified
continuous-time PID controller can be written as
• which introduced two zeros, a pole at the origin and another
“fast” pole.
• Any of the previous approximation methods can be used to
approximate the PID controller.
28
𝐶𝑝𝑖𝑑(𝑠) =
𝐾𝑝(𝑇𝑖𝑇𝐷𝑠2
+ 𝑇𝑖𝑠 + 1)
𝑇𝑖𝑠
𝐾𝐷𝑠 ≈
𝐾𝐷𝑠
𝜏𝐿𝑠 + 1
𝐶𝑝𝑖𝑑(𝑠) =
𝐾𝑝(𝑇𝑖𝑇𝐷𝑠2
+ 𝑇𝑖𝑠 + 1)
𝑇𝑖𝑠(𝜏𝐿𝑠 + 1)