Download presentation

Presentation is loading. Please wait.

Published byHeidi Babbit Modified over 2 years ago

1
Control Systems for Robots Prof. Robert Marmelstein CPSC 527 – Robotics Spring 2010

2
Introduction to Robot Control We want robots to do things that might otherwise be done by intelligent, physical beings Biological nervous systems are often thought of as control systems for living organisms To control a robot in this manner, we need to: Define the state of the robot Sense the state of the robot Compare the state of the robot to a desired state Decide what actions need to be taken to achieve the desired state and issue the associated commands Translate those command into physical action Measure the effect of those physical actions

3
Robot State Description Physical States: Position Orientation (pose) Velocity Acceleration Sensor states Actuator States Internal States: Plans Tasks Behaviors Assumed vs. Actual

4
Control Engineering Control engineering is the application of mathematical techniques to the design of algorithms and devices to control processes or pieces of machinery. It almost always requires a model of the entity that is being controlled If a system can be modeled by a set of linear differential equations there are well understood techniques for getting exact analytical solutions, and so designing controllers so that the output of the system is the required one

5
Example: Forced Spring A forced spring can be modeled by a linear differential equation

6
Real-World Systems Unfortunately, most real-world systems are non-linear in nature Example: Pendulum In these cases, the nonlinear system is often approximated by a linear system For the Pendulum, assume sin( ), which yields:

7
Control System Components Target Value – The desired operating point of the overall system, which is speed. Measured Value – The actual operating point of the system. It is affected by external factors such as hills, and internal factors such as the amount of fuel delivered to the engine. Difference Value – This is the difference between the target value and the measured value. Translates into feedback. Control Input – This is the main adjusting point of the control system. The amount of fuel delivered to the engine is the primary control input to the cruise control Control Algorithm – Determines how to best regulate the control input to make the difference value as close to zero as possible. It does this by periodically looking at the difference value and adjusting the control input

8
Feedback Defined Feedback: continuous monitoring of the sensors and reacting to their changes. Feedback control = self-regulation Two kinds of feedback: positive and negative Negative feedback acts to regulate the state/output of the system e.g., if too high, turn down, if too low, turn up thermostats, toilets, bodies, robots... Positive feedback acts to amplify the state/output of the system e.g., the more there is, the more is added lynch mobs, stock market, ant trails... Often results in system instability

9
Open Loop Controller The Open Loop Controller (OLC) is the simplest kind The controller sends an input signal to the plant It does not compensate for disturbances that occur after the control stage Actual effects are assumed – not measured No feedback to match actual to intended

10
Open Loop Controller (cont.) The OLC is commonly used for behavior-based systems If a trigger condition is met, then the behavior is activated Behavior is performed until the condition is no longer met If the condition is not met, the (assumedly) some other behavior is activated You would likely use an OLC if you have no way of measuring your operating point (e.g., the value you are trying to control)

11
Problem with Open Loop Controllers The effectiveness of OLCs are very context dependent The amount of force that is applied has different effects dependent on the surface type

12
Closed Loop Controller In Closed-loop control, the output is sensed and compared with the reference. The resulting error signal is fed back to the controller [feedback]. Components: Reference – Desired State Controller – Issues Commands Plant – Actuator

13
Closed Loop Controller (cont.) [Negative] Feedback keeps the operation of the system smooth and stable Closed Loop Controller issues: How quickly will the system respond to error? How long will it take the system to reach equilibrium? What, if any, residual error will remain? Under what conditions will the system become unstable?

14
Example of a Closed Loop Controller Computation (Brain) Actuator Control (Auto Pedals) Velocity (Engine Power) Sensing (Eyes) - + Error Input Output Desired Position Actual Position Velocity Time Velocity Velocity decreases as the car gets closer to the desired position

15
Bang-Bang Controller (BBC) The simplest type of closed-loop controller is the Bang-Bang controller. It typically consists of two states and a target value The BBC typically monitors one item (quantity) of interestits job is to keep that quantity at a certain target value If the quantity is too high or low (vs. the target) the BBC compensates to change it The system continually transitions between states, often abruptly OFFON temp < target temp > target

16
Taking the Edge off Bang-Bang Control with Hysteresis Hysteresis provides a sort of "guard band" around the desired set point of the system. In other words, when the temperature goes above (or below) the desired control point, there is a margin which needs to be exceeded before compensation is applied The result a lag which causes the system to run much smoother, avoiding the jerkiness of a purely Bang- Bang controller

17
Leveraging Hysteresis Single Threshold System (no hysteresis) Use of temperature dead zone to induce hysteresis

18
Closed Loop Controller Issues Low Gain – Sluggish High Gain – Unstable JLJ Text – Fig 2.5

19
Proportional Integral Derivative (PID) Controller Closed loop controllers that only use proportional control can easily become unstable if the gain is too high or sluggish if the gain is set too low PID controllers help solve this problem It use the measured error compute an input to the Plant based on three distinct controls: Proportional, Integral and Derivative (see right) Proportional control – Computed based on the actual error (times a gain factor). Thus, The larger the error, the bigger correction the control will make Serves to control response time to error For high gains or large errors, tends to overshoot and oscillate the desired output There is typically a steady state error that cannot be corrected

20
Proportional Integral Derivative (PID) Controller Integral control – Reduces steady- state error by adding (integrating) the actual errors over time. Once the error reaches a predetermined threshold, the controller will compensates Too little can result in undershoot; too much can result in overshoot Derivative (D) control – Computed based of difference between current and previous error. Thus, the output of this control is proportional to the change in error Prevents oscillations due to overshoot Reduced settling time by giving a better dynamical response Generally, this control has a positive effect

21
PID Controller (cont.) The tunable factors are: K p – Proportional Gain factor K I – Integral Gain Factor K D – Differential Gain Factor These factors are cross-coupled, so the performance of the system cannot be optimized by tuning each factor independently Some systems can be engineered without all three PID components The P components is always required, but P controllers alone can result in instability PI is not accurate but converges quickly PD converges relatively quickly reducing oscillations as it approaches the goal. PID accurately maintains a position, but isnt very fast.

22
Helpful PID Terms Gain(s) --The parameter(s) that determine the magnitude of the systems response. Gain values determine whether or not the system stabilizes or fluctuates. Finding effective gains is a trial and error process, requiring testing and recalibration. Proportional Gain – When the value of the gain is proportional to the error. Damping – The process of systematically decreasing a systems fluctuations A system is damped if it does not oscillate out of control. Generally, the gains have to be adjusted for a system to be damped Steady State Error – The amount of error that remains after the system has reached equilibrium

23
PID Controller (cont.) K P – Proportional Gain K I – Integral Gain K D – Derivative Gain

24
PID Controller Response Curve Settling time Overshoot Controlled variable Time Reference % Steady StateTransient State Steady state error

25
PID Response Curve (cont.) Rise Time (T r ) – The time for the plant output y to rise beyond 90% of the desired level for the first time Overshoot – How much the peak level is higher than the steady state, normalized against the steady state The time required for the output to reach its maximum level is called the Peak Time (T p ) Settling Time (T s ) – The time it takes for the system to converge to its steady state Transient State – The period from the detection of error until its approximate correction, resulting in the steady state Steady-state Error – The difference between the steady-state output and the desired output.

26
Effect of Increasing PID Factors KPKP KIKI KDKD NT: No trend

27
K P = 20 K P = 200 K P = 500 Control Performance – Proportional Control Source: CUNY – Dr. Jizhong Xiao K P = 50

28
K I = 200 Control Performance – Integral Control (K P = 100) K I = 50 Source: CUNY – Dr. Jizhong Xiao

29
K D = 5 K D = 20 K D = 10 K D = 2 Control Performance – Derivative Control (K P = 100, K I =200) Source: CUNY – Dr. Jizhong Xiao

30
Optimizing Performance PID Tuning – By Hand Boost K p until it oscillates Boost K D to stop oscillation, back off Kp by 10% Dial in K I to Hold position or velocity smooth Trial and error PID tuning – By Design Zeigler-Nichols Method (next slide) Other: Work to minimize environmental interference and sensor error (two are typically coupled) Smart design helps too

31
Zeigler-Nichols Tuning Rule for PID Controllers Yields ~25% overshoot and good settling time

32
Why Care about the PID Controller? Because PID Controllers are everywhere! Due to its simplicity and excellent if not optimal performance in many applications, PID controllers are used in more than 95% of closed-loop industrial processes. It can be tuned by operators without extensive background in Controls, unlike many other modern controllers that are much more complex but often provide only marginal improvement. In fact, most PID controllers are tuned on-site. The lengthy calculations for an initial guess of PID parameters can often be circumvented if we know a few useful tuning rules. This is especially useful when the system is unknown

33
Non-Linear Control Linear controllers are generally valid only over small operational ranges. Hard non-linearity cannot even be approximated by linear systems. Model uncertainties can sometime be tolerated by the addition of non-linear terms. Non-linear systems often have multiple equilibrium points, plus periodic, or chaotic attractors. In these systems, small disturbances (even noise) can induce radically different behaviors.

34
Control System Non-Linearity Issues Saturation – Occurs when the input signal to a certain device exceeds the ability of the device to process it Input – sensors Output – motors For output, saturation means that the required compensation can no longer be applied to the control system In general, it is good practice to limit the signal to the saturation value in software When an input reaches the saturation point, it no longer provides a reliable estimate of the real world

35
Non-Linearity Issues (cont.) Backlash – Term describing actuator hesitation and overshoot caused by small gaps between motor gears Can result in small, but unnecessary, oscillations of the actuator position Dead Zone – Because the sensitivity of actuators is limited, not every non-zero input will result in action. The Dead Zone is the +/- region above a zero (0) input that will result in no actuator movement.

36
Self-Balancing Robot Lab Problem – Create a PID controller that will keep an NXT robot balanced on two wheels Use a light sensor to determine balance: Light diminishes as it tilts backward Light gets stronger as it tilts forward Collect reference value when the robot is perfectly balanced PID controller will use the light sensor data to compute the compensation for the motors (plant) Move backward if tilting back Move forward if tilting forward

37
Self-Balancing Robot (Pics) Light Sensor

38
[Simplified] PID Controller Algorithm // Get Balance Reading for Light Sensor midVal = Sensor_Read(LS_Port); // Now Compute Power (PID) Value for Balancing Robot while (true) { lightVal = Sensor_Read(LS_Port); error = lightVal – midVal; diffErr = error – prevError; intErr = intErr + error; pVal = k p * error; iVal = (k i *intErr)*dampFactor; dVal = k d *diffErr; prevErr = error; power = (pVal+iVal+dVal)*scale; MotorFWD(motorPorts, power); }

39
Other Material PID Controller for Dead Reckoning CMU PID Tutorial DePaul Self-Balancing Robots – Trials and Tribulations DePaul Self-Balancing Robots – Trials and Tribulations

40
Questions?

Similar presentations

© 2016 SlidePlayer.com Inc.

All rights reserved.

Ads by Google