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PID CONTROLLER
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Contents
Introduction to PID
Modes of Control
1. On-Off Control
2. Proportional Control
3. Proportional + Integral Control
4. Proportional + Derivative Control
5. Proportional + Integral + Derivative Control
Introduction
◦ PID Stands for
◦ –P =Proportional
◦ –I =Integral
◦ –D =Derivative
◦ The usefulness of PID controls lies in their general applicability to most
control systems.
◦ In particular, when the mathematical model of the plant is not known and
therefore analytical design methods cannot be used, PID controls prove to
be most useful.
◦ In the field of process control systems, it is well known that the basic and
modified PID control schemes have proved their usefulness in providing
satisfactory control, although in many given situations they may not provide
optimal control.
◦ It is interesting to note that more than half of the industrial controllers in
use today are PID controllers or modified PID controllers.
◦ Because most PID controllers are adjusted on-site, many different types of
tuning rules have been proposed in the literature.
◦ •Using these tuning rules, delicate and finetuning of PID controllers can be
made on-site.
Four Modes of Controllers
◦ Each mode of control has specific advantages and limitations.
1. On-Off Control
2. Proportional Control
3. Proportional + Integral Control
4. Proportional + Derivative Control
5. Proportional + Integral + Derivative Control
On-Off Control
◦ This is the simplest form of control.
Proportional Control (P)
◦ In proportional mode, there is a continuous linear relation between value of the controlled
variable and position of the final control element.
◦ Output of proportional controller is:
◦ The transfer function can be written as:
◦ As the gain is increased the system
responds faster to changes in set-point
but becomes progressively underdamped
and eventually unstable.
Proportional Plus Integral Controllers (PI)
◦ Integral control describes a controller in which the output rate of change is dependent on the
magnitude of the input.
◦ Specifically, a smaller amplitude input causes a slower rate of change of the output.
◦ Integral signal is sum of all instantaneous values, so when integral and proportional terms are
added the movement get accelerated towards the set point.
◦ The major advantage of integral controllers is that they have the unique
ability to return the controlled variable back to the exact setpoint following
a disturbance.
◦ Disadvantages of the integral control mode are that it responds relatively
slowly to an error signal and that it can initially allow a large deviation at
the instant the error is produced.
◦ This can lead to system instability and cyclic operation . For this reason ,
the integral control mode is not normally used alone, but is combined with
another control mode
◦ The transfer function can be written as:
We Have,
Proportional Plus derivative Control (PD)
◦ The stability and overshoot problems
that arise when a proportional
controller is used at high gain can be
reduced by adding a term
proportional to the time-derivative of
the error signal.
◦ The value of the damping can be
adjusted to achieve acritically
damped response.
Here,
◦ The transfer function can be written as
• The higher the error signal rate of change ,the sooner the final control element is
positioned to the desired value.
• The added derivative action reduces initial overshoot of the measured variable, and
therefore aids in stabilizing the process sooner.
• This control mode is called proportional plus derivative(PD)control because the
derivative section responds to the rate of change of the error signal.
Proportional Plus Integral Plus Derivative
Control (PID)
◦ Although PD control deals neatly with
the overshoot and ringing problems
associated with proportional control
it does not cure the problem with the
steady-state error.
◦ Fortunately it is possible to eliminate
this while using relatively low gain by
adding an integral term to the
control function which becomes
Here,
The transfer function is:
The Characteristics of P, I, and D controllers
CL Response Rise Time Overshoot Settling Time S-S Error
Kp Decrease Increase Small Change Decrease
Ki Decrease Increase Increase Eliminate
Kd Small Change Decrease Decrease Small Change
Designing a PID Controller
!. We obtain an open-loop response and determine what needs to be improved.
2. Then, we add a proportional control to improve the rise time.
3. Now we add a derivative control to improve the overshoot.
4. Then we add an integra lcontrol to eliminate the steady-state error.
5. Finally, we adjust each of Kp, Ki, and Kd until we obtain a desired overall response.

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Everything You Need to Know About PID Controllers

  • 2. Contents Introduction to PID Modes of Control 1. On-Off Control 2. Proportional Control 3. Proportional + Integral Control 4. Proportional + Derivative Control 5. Proportional + Integral + Derivative Control
  • 3. Introduction ◦ PID Stands for ◦ –P =Proportional ◦ –I =Integral ◦ –D =Derivative
  • 4. ◦ The usefulness of PID controls lies in their general applicability to most control systems. ◦ In particular, when the mathematical model of the plant is not known and therefore analytical design methods cannot be used, PID controls prove to be most useful. ◦ In the field of process control systems, it is well known that the basic and modified PID control schemes have proved their usefulness in providing satisfactory control, although in many given situations they may not provide optimal control.
  • 5. ◦ It is interesting to note that more than half of the industrial controllers in use today are PID controllers or modified PID controllers. ◦ Because most PID controllers are adjusted on-site, many different types of tuning rules have been proposed in the literature. ◦ •Using these tuning rules, delicate and finetuning of PID controllers can be made on-site.
  • 6. Four Modes of Controllers ◦ Each mode of control has specific advantages and limitations. 1. On-Off Control 2. Proportional Control 3. Proportional + Integral Control 4. Proportional + Derivative Control 5. Proportional + Integral + Derivative Control
  • 7. On-Off Control ◦ This is the simplest form of control.
  • 8. Proportional Control (P) ◦ In proportional mode, there is a continuous linear relation between value of the controlled variable and position of the final control element.
  • 9. ◦ Output of proportional controller is: ◦ The transfer function can be written as:
  • 10. ◦ As the gain is increased the system responds faster to changes in set-point but becomes progressively underdamped and eventually unstable.
  • 11. Proportional Plus Integral Controllers (PI) ◦ Integral control describes a controller in which the output rate of change is dependent on the magnitude of the input. ◦ Specifically, a smaller amplitude input causes a slower rate of change of the output. ◦ Integral signal is sum of all instantaneous values, so when integral and proportional terms are added the movement get accelerated towards the set point.
  • 12. ◦ The major advantage of integral controllers is that they have the unique ability to return the controlled variable back to the exact setpoint following a disturbance. ◦ Disadvantages of the integral control mode are that it responds relatively slowly to an error signal and that it can initially allow a large deviation at the instant the error is produced. ◦ This can lead to system instability and cyclic operation . For this reason , the integral control mode is not normally used alone, but is combined with another control mode
  • 13.
  • 14. ◦ The transfer function can be written as: We Have,
  • 15. Proportional Plus derivative Control (PD) ◦ The stability and overshoot problems that arise when a proportional controller is used at high gain can be reduced by adding a term proportional to the time-derivative of the error signal. ◦ The value of the damping can be adjusted to achieve acritically damped response.
  • 16. Here,
  • 17. ◦ The transfer function can be written as • The higher the error signal rate of change ,the sooner the final control element is positioned to the desired value. • The added derivative action reduces initial overshoot of the measured variable, and therefore aids in stabilizing the process sooner. • This control mode is called proportional plus derivative(PD)control because the derivative section responds to the rate of change of the error signal.
  • 18. Proportional Plus Integral Plus Derivative Control (PID) ◦ Although PD control deals neatly with the overshoot and ringing problems associated with proportional control it does not cure the problem with the steady-state error. ◦ Fortunately it is possible to eliminate this while using relatively low gain by adding an integral term to the control function which becomes
  • 20. The Characteristics of P, I, and D controllers CL Response Rise Time Overshoot Settling Time S-S Error Kp Decrease Increase Small Change Decrease Ki Decrease Increase Increase Eliminate Kd Small Change Decrease Decrease Small Change
  • 21. Designing a PID Controller !. We obtain an open-loop response and determine what needs to be improved. 2. Then, we add a proportional control to improve the rise time. 3. Now we add a derivative control to improve the overshoot. 4. Then we add an integra lcontrol to eliminate the steady-state error. 5. Finally, we adjust each of Kp, Ki, and Kd until we obtain a desired overall response.