10 tips for tuning of pid looops

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10 Tips for Tuning of Pid Looops

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10 Tips for:

Tuning of PID LoopsBy

Steve Mackay

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Welcome to this webinarThere are at least 3 ways to interact with your presenter today:1. Use the Text tab, near bottom left of your screen.

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This 45 minute session will commence shortly!

RH

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Objectives

• Concept of tuning • Ziegler Nichols classical rules • Practical closed and open loop strategies • Cascade loops • Dead time issues

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Concept of Tuning

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1 - Minimize Integral of error

Objectives of Tuning (1)

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2 - Minimize Amplitude of error squared

Objectives of Tuning (2)

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3 - Minimize wear and tear

4 - No overshoot at Start Up

5 - Minimize effect of known disturbances

Other Aspects of Tuning (3,4,5)

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Ziegler Nichols and others

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Loop Controller and Process

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1. Put controller in manual mode

2. Make a step change to the OP value

3. Observe Reaction Curve

4. Calculate timing constants

Reaction curve

Steps of Open Loop Tuning (Reaction Curve)

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P - Control

PI - Control

PID - Control

OP

N L%

0 9

3

. %

int

OPN L

T L

12

20 5

. %

.int

OPN L

T LT Lder

KC

KC

KC

Reaction Curve Calculations

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• Find critical value of K for continuous oscillations• Do not use I or D - control• Observe critical frequency for 180° phase shift• Stabilize loop by reducing K and ensure that I & D• Control still gives a phase lead

Continuous Cycling - Ziegler & Nichols

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P-only for Continuous Cycling Method

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1. Put controller in P - control only2. P - control on ERR = (SP - PV)3. Controller in Auto4. Step change to SP5. Double value of K until continuous cycling6. Calculate tuning constants

Continuous Cycling Method

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P - Control

PI - Control

PID - Control

K KC U 0 5.

K K

T PC U

U

0 45

12

.

.int

K K

T P

T P

C U

U

derU

0 6

2

8

.

int

Calculation of Tuning Constants

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First Order Lag

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First Order Lag Response Curve

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Variation on continuous cycling ....to avoid danger to process ...but damped oscillations are acceptablerequires some subjective evaluation

Damped Cycling Method

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Damped Oscillation Decay Ratio

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1. Put controller in P - control2. P - control on ERR = (SP - PV) 3. Controller into Auto4. Double K until oscillations.5. Terminate immediately6. Calculate tuning constants

Steps of Damped Cycling Method

Estimate damping of oscillationConvert P into Pu using diagram

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Convert P into Pu using diagram

Estimate damping of oscillation

(d) ... 0.5 acceptable

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PI - Control

PID - Control

T

P Rd dint .

12

R Ppd

u

T

P R

TP R

d d

derd d

int

2

8

K determined by good judgement.....

Calculate Tuning Constants

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Tuning for NO Overshoot on Start-up

Variation of continuous cycling method

When no overshoot even for start-up is permitted (manual auto)

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Same as for continuous cyclingFormula for PID – control:

K K

T P

T P

C U

U

derU

0 2

3

2

.

int

Formula for NO Overshoot on Start-up

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Variation of continuous cycling method

No overshoot during normal modulating controlonly

Tuning for SOME Overshoot on Start-up

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Same as for continuous cyclingFormula for PID - control

K K

T P

T P

C U

U

derU

033

2

3

.

int

Formula for Some Overshoot on Start-up

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Cascade Control

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Single Loop Temperature Control

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Two Controller Basic Cascade Control

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Tuning of Cascade Loops (cont…)

• Cascade Control - Secondary Controllers– Mainly flow controller– No D - control as mainly stable– K < 1

• Cascade Control - Primary Controllers– Mainly PID controller– Careful stability considerations

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Long Process Deadtime in Closed Loop Control & The

Smith Predictor

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Process Deadtime

• Difficult problem to overcome long deadtime in feedback control loop

• Especially when deadtime more than 20% of total time taken for PV to settle to its new value after last setpoint change

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Example of Process Deadtime

Illustration of a long conveyor system giving an excessive deadtime to the control loop

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Overcoming Process Deadtime

• Depends on operating requirements of process

• Easiest solution: de-tune controller to slower response rate so that controller will not over compensate unless deadtime excessively long

• Integral mode of controller very sensitive to deadtime since during period of PV inactivity, integrator ramps output

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Level ControlMaintain flow as constant

as possible to downstream equipment

Medium response

Tune as slowly as possible without overfilling or emptyingthe tank

Choice of Tuning Constant (1)

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Flow ControlMaintain constant flowAim for fast responseSmall process lag in systemTune for fast as possible

response

Choice of Tuning Constants (2)

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Temperature ControlMaintain a steady temperatureMajor process lag and dead time in the systemTune as quickly as possible without causing

oscillations

TCPV

SP

T2

O utlet

Inlet

Choice of Tuning Constants (3)

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Thank You For Your Interest

If you are interested in further training, please visit:

IDC Technologies Short Courses:Two-day practical courses available to the public:

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