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INDUSTRIAL AUTOMATION

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Contents. PID Controller. Implementation of PID Controller. Response under actuator Saturation. PID with Anti Reset windup. Tuning methods of PID Controller. – PowerPoint PPT presentation

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Title: INDUSTRIAL AUTOMATION


1
INDUSTRIAL AUTOMATION
  • (Getting Started week -1)

2
Contents
  • PID Controller.
  • Implementation of PID Controller.
  • Response under actuator Saturation.
  • PID with Anti Reset windup.
  • Tuning methods of PID Controller.

3
PID controller
  • Consists of three
  • modes
  • Proportional.
  • Intigral.
  • Derivative.

4
PID Contd.
  • the output of the PID controller u(t) can be
    expressed in terms of the input e(t).

5
Basic terms related to PID
  • Kp Proportional gain. PB Proportional
    Band
  • Ki Intigral gain Kp/Ti
  • Kd Derivative gain Kp.Td
  • where,
  • TiIntigral Time Time taken to repeat the
    proportional control for a step
    signal(min/repeat).
  • TdDerivative time Time taken for the
    proportional term to equal the derivative term
    for a ramp signal.

6
Implementation of PID Controller
  • Integrator Windup under Actuator Saturation

7
Implementation Contd.
  • PID Controller with anti reset Windup.

8
Tuning of PID Controller
  • Involves selection of the proper values of
    Kc,Tau_I and Tau_d.
  • Best method, Ziegler-Nichols method of tuning.
  • the values of controller parameters that bring
    the closed-loop system to the verge of
    instability by
  • 1. Simulation.
  • 2. Root Locus Technique.
  • 3. Direct substitution.

9
Contd.
  • Using Proportional only control, determine Kc
    Ku (ultimate controller gain)
  • the period of the sustained oscillations Pu
    (ultimate period of oscillations).
  • Pu
    2p/?co
  • If the Kc is increased the process dynamics
    goes through the following sequence of behaviour

10
Tuning methods Contd.
  • By using the values of Ku and Pu, determine the
    other parameters
  • of PID Controller. summarized as below.

11
Contd.
  • Dynamic changes as Kc is increased for a FOPDT
    process.

12
Controller Tuning In Time Domain
  • This is done by approx. model based on the
    Process Reaction Curve(open -loop).

13
Contd.
  • The other parameters of controller can be
    caluclated as folows.

14
Example
  • The given transfer function is as follows. By
    using SIMULINK/MATLAB.
  • we can get the parametes of PID controller.
  • By the Zeigler-Nichols method, the tuning of PID
    is done.

15
Example Contd
  • The characteristic eqn of the system is given by
  • By using the method of substitution , for P
    controller only calculate the Ultimate gain.

16
Example Contd.
17
Example Contd.
18
Example contd.
  • By the measuring ultimate gain and ultimate
    period we can get the other parameters by Z-N
    method.
  • Z-N tuning will be
  • P Kc 0.5Ku 0.83
  • PI Kc 0.45Ku 0.75 Tau_I Pu /1.2
    10.5 min
  • PID Kc 0.6Ku 1.0 Tau_I Pu /2 6.3
    min
  • Tau_D Pu /8 1.6

19
Example contd.
  • Final Response for PID controller.

20
Thank you
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