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PID%20Control%20Loops

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PID Control Loops Guy Zebrick Contents Open & Closed Loops Direct and Reverse Acting Proportional Control Integral Control Derivative Control Definitions Loop Tuning ... – PowerPoint PPT presentation

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Title: PID%20Control%20Loops


1
PID Control Loops
  • Guy Zebrick

2
Contents
  • Open Closed Loops
  • Direct and Reverse Acting
  • Proportional Control
  • Integral Control
  • Derivative Control
  • Definitions
  • Loop Tuning

3
Open Loop Control / Direct Acting
Mathematical Calculation
Input Control Variable
Output Device 0-100
Setpoint
Input Outside Air Temperature Setpoint
50F Output Chiller on/off (0-100) Action
Direct (input output )
4
Open Loop Control / Reverse Acting
Mathematical Calculation
Input Control Variable
Output Device 0-100
Setpoint
Input Outside Air Temperature Setpoint
60F Output Boiler on/off (0-100) Action
Reverse (input output )
5
Closed Loop Control Reverse Acting
Mathematical Calculation
Input Control Variable
Output Device 0-100
Setpoint
Input Room Temperature Setpoint 70F Output
Radiator Valve (0-100)
6
PID Control by Mathematical calculation
  • Proportional
  • Output varies in PROPORTION to input error
  • Integral
  • Output varies over TIME based on input error
  • Derivative
  • Output varies based RATE of CHANGE of input error
  • P control
  • P I control
  • P I D control (not used in our industry!)

7
PID closed loop control driving at speed
0 P
30 PID
40 PI
60 PI
0 PID
40 PID
70 PI
25 PID
40 PI
8
Definition (SETPOINT)
  • The desired value of the input variable

9
Definition OFFSET (error)
  • The DIFFERENCE between the input variable and the
    desired setpoint.

10
Definition Throttling Range (Proportional Band)
Amount of Change in INPUT that equals a 0-100
change in OUTPUT
100
ControllerOutput
50
0
70
75
65
Setpoint
Throttling Range (Proportional Band) (10F)
11
Proportional Control (with Offset Error)
Control Point
Setpoint
Offset
0100
Time
12
Proportional Integral Control (eliminates
offset)
Control Point
Setpoint
Offset
0100
Time
13
Derivative Calculation based on RATE of CHANGE
Control Point
Setpoint
Offset
D
P I D Not used in our industry!
Time
14
Integral Windup Condition
Setpoint
100
Control Point
Time
Prevented by Disabling Loop when system is OFF
15
PID Enhancements
  • Setpoint Reset
  • Setpoint Recovery Ramp
  • Setpoint Demand Limit BUMP
  • Setpoint Select(s)
  • PID Output BIAS
  • PID Output Start Point
  • PID Output Start Ramp
  • PID Output Adjust Delay
  • PID Output Adjust Threshold
  • PID AUXILLARY Output
  • PID Output Sequencer

16
Definition PID Output Bias
50
0
100
100
50
50
0
0
T1
T2
T3
T4
T5
T6
T1
T2
T3
T4
T5
T6
Output 50 at Setpoint
Output 0 at Setpoint
17
PID Setpoint RESET
  • Requires RESET sensor (typically outside air)
  • Automatically adjusts setpoint

18
PID Setpoint Recovery Ramp
  • Degrees/Hr
  • Requires multiple schedule information
  • Current State (occupied/unoccupied)
  • Next State (occupied/unoccupied)
  • Time until next state (minutes)

UNOCC
Setpoint
OCC
OCC
Time
19
PID options (not available on ALL PID loops)
  • Output Start Value ()
  • Provides starting value for initial control
  • Output Start Ramp (seconds)
  • limits action during initial startup to prevent
    overshoot
  • Output Dead Band ()
  • Output Adjust Delay Threshold
  • Prevents repeated minor adjustment to output
  • Prevents needless wear tear on mechanical
    devices

20
Definition Hunting (over-reacting)
100
ControllerOutput
50
0
70
Setpoint
69
71
Proportional BandThrottling Range (2F)
Time
21
Tuning Hints
  • PI control for closed-loop applications only.
  • The narrower (smaller) the throttling range, the
    more precise the control operation. The wider
    (larger) the throttling range, the more stable
    the control action.
  • Generally the throttling range required for PI
    control is greater than what is used for
    proportional control only.
  • The integral time value is set in seconds. A slow
    process such as space temperature control
    requires a long integral time (600 seconds or
    more), while a fast process such as static
    pressure control requires a short integral time.
  • An integral time of 0 eliminates the integral
    function for the control loop.

22
Typical Values
  • From Engineering Manual
  • Default Space Temperature Control
  • (CV AHU controller)

23
Field Tuning
  • Integral Time to Zero
  • Throttling Range ½ Input Sensor Range
  • Adjust Throttling Range to point where about
    first begins to hunt.
  • Increase Throttling Range 1.5 X
  • Add Integral Time based on system response time
  • (typically 60 2500 seconds)
  • Check for Stable Operation

24
PID POP Quiz
  • Define open loop
  • Define closed loop
  • A cooling loop is (direct/reverse) acting
  • An AHU static pressure control loop is
    (direct/reverse) acting
  • Define P, I, D
  • Define throttling range
  • Define integral time
  • When do you use Differential control?
  • What adjustment(s) reduce hunting?

25
Questions?
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