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CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS
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CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

Dec 17, 2015

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Page 1: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

CHE 185 – PROCESS CONTROL AND DYNAMICS

FREQUENCY RESPONSE ANALYSIS

Page 2: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

FREQUENCY RESPONSE ANALYSIS

• IS THE RESPONSE OF A PROCESS TO A SINUSOIDAL INPUT

• CONSIDERS THE EFFECT OF THE TIME SCALE OF THE INPUT.

• IMPORTANT FOR UNDERSTANDING THE PROPAGATION OF VARIABILITY THROUGH A PROCESS.

• IMPORTANT FOR TERMINOLOGY OF THE PROCESS CONTROL FIELD.

• BUT IT IS NOT NORMALLY USED FOR TUNING OR DESIGN OF INDUSTRIAL CONTROLLERS.

Page 3: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

FREQUENCY RESPONSE ANALYSIS

• PROCESS EXPOSED TO A SINUSOIDAL INPUT.

Page 4: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

FREQUENCY RESPONSE ANALYSIS

• KEY COMPONENTS – INPUT FREQUENCY, AMPLITUDE RATIO, PHASE ANGLE.

Page 5: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

FREQUENCY RESPONSE ANALYSIS

• EFFECT OF FREQUENCY ON Ar AND Φ

• PEAK TIME DIFFERENCE

Page 6: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

FREQUENCY GRAPHICS

• BODE PLOT OF Ar AND Φ VERSUS FREQUENCY ω

Page 7: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• BASIS OF BODE PLOT IS A MEASURE OF RELATIVE AMPLITUDE AND PHASE LAG BETWEEN A REGULAR (SINUSOIDAL) SET POINT CHANGE AND THE OUTPUT SIGNAL

• THIS TECHNIQUE INDICATES STABILITY OF THE SYSTEM

• THE ANALYSIS IS COMPLETED WITH AN OPEN LOOP

Gc(s) Ga(s) Gp(s)

Gs(s)

Ysp(s)

Ys(s)

Y(s)

Page 8: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE GENERATION

• WAYS TO GENERATE BODE PLOT INCLUDE:

• DIRECT EXCITATION OF PROCESS.• COMBINE TRANSFER FUNCTION OF

THE PROCESS WITH SINUSOIDAL INPUT.

• SUBSTITUTE s=i w INTO GP(s) AND CONVERT INTO REAL AND IMAGINARY COMPONENTS WHICH YIELD Ar(w) AND f(w).– SEE APPLICATION METHOD IN EXAMPLES

11.1 AND 11.2

• APPLY A PULSE TEST.

Page 9: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• A SINUSOIDAL SETPOINT IS SENT TO THE LOOP

• AFTER THE SYSTEM REACHES STEADY STATE, THERE IS A LAG, CALLED THE PHASE LAG, BETWEEN THE AMPLITUDE PEAK OF THE INLET SIGNAL AND THE AMPLITUDE PEAK OF THE OUTLET SIGNAL

• THE FREQUENCY IS ADJUSTED SO THE PHASE LAG OF THE OUTLET SIGNAL IS 180° BEHIND THE INPUT SIGNAL

Page 10: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• THE RESULTS ARE THEN APPLIED TO A CLOSED LOOP

• THE SETPOINT IS CHANGED TO A CONSTANT VALUE

• SINCE THE ERROR SIGNAL IS 180° OUT OF PHASE AND IS NEGATIVE RELATIVE TO THE INPUT SIGNAL, IT REINFORCES THE PREVIOUS ERROR SIGNAL

Gc(s) Ga(s) Gp(s)

Gs(s)

Ysp(s)

Ys(s)

Y(s)

Page 11: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• THE AMPLITUDE OF THE ERROR SIGNAL BECOMES THE OTHER FACTOR– IF THE AMPLITUDE OF THE ERROR SIGNAL TO THE

AMPLITUDE OF THE ORIGINAL SINUSOID SETPOINT, CALLED THE AMPLITUDE RATIO, IS LESS THAN ONE THEN THE ERROR WILL DECAY TO ZERO OVER TIME,

– IF THE AMPLITUDE RATIO WAS EQUAL TO ONE, A PERMANENT STANDING WAVE WILL RESULT

– IF THE AMPLITUDE RATIO WAS GREATER THAN ONE, THE ERROR WILL GROW WITHOUT LIMIT.

Page 12: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• BODE’S STABILITY CRITERION SAYS:• WHEN THE AMPLITUDE RATIO IS LESS THAN

ONE, THE SYSTEM IS STABLE• WHEN THE AMPLITUDE RATIO IS GREATER

THAN ONE, THE SYSTEM IS UNSTABLE• THE AMPLITUDE RATIO IS DEFINED AS:

WHERE Ar REFERS TO AMPLITUDE AS SHOWN IN FIGURES 11.2.1 AND 11.2.2 IN THE TEXT AND ω IS THE FREQUENCY OF THE SINUSOID

Aa

ary

c

Page 13: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• BODE PLOTS– THESE ARE SHOWN FOR FOPDT PROCESSES IN

FIGURES 11.2.2 AND 11.3.2– A SECOND ORDER PLOT IS FIGURE 11.3.3

• GENERAL TECHNIQUE TO PLOT– WRITE THE TRANSFER FUNCTION IN PROPER FORM

(UNIT VALUE FOR LOWEST ORDER TERM IN DENOMINATOR)

– SEPARATE THE TRANSFER FUNCTION INTO PARTS BASED ON POLES AND ZEROS

– DRAW BODE DIAGRAM FOR EACH PART– SUM THE PARTS TO GET THE FINAL PLOT

Page 14: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE PLOT CREATION EXAMPLE(HTTP://LPSA.SWARTHMORE.EDU/BODE/BODEEXAMPLES.HTML#EX3)

• TRANSFER FUNCTION IN PROPER FORM OR

• PARTS ARE BASED ON POLE AT AND CONSTANT OF 3.3

• POLE PLOT IS CONSTANT 0 dB UP TO BREAK ω, THEN DROPS OFF

• CONSTANT HAS VALUE OF 10.4 dB

Page 15: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE PLOT CREATION EXAMPLE(HTTP://LPSA.SWARTHMORE.EDU/BODE/BODEEXAMPLES.HTML#EX3)

• FUNCTION WITH REAL POLES AND ZEROS

Page 16: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE PLOT CREATION EXAMPLE(HTTP://LPSA.SWARTHMORE.EDU/BODE/BODEEXAMPLES.HTML#EX3)

• FUNCTION WITH REAL POLES AND ZEROS

Page 17: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE PLOT CREATION EXAMPLE(HTTP://LPSA.SWARTHMORE.EDU/BODE/BODEEXAMPLES.HTML#EX3)

• FUNCTION WITH POLE AT ORIGIN

Page 18: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE PLOT CREATION EXAMPLE(HTTP://LPSA.SWARTHMORE.EDU/BODE/BODEEXAMPLES.HTML#EX3)

• FUNCTION WITH REPEATED REAL POLES,NEGATIVE CONSTANT

Page 19: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE PLOT CREATION EXAMPLE(HTTP://LPSA.SWARTHMORE.EDU/BODE/BODEEXAMPLES.HTML#EX3)

• FUNCTION WITH COMPLEX CONJUGATE POLES

Page 20: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE PLOT CREATION EXAMPLE(HTTP://LPSA.SWARTHMORE.EDU/BODE/BODEEXAMPLES.HTML#EX3)

• FUNCTION WITH MULTIPLE POLES ATORIGIN, COMPLEX CONJUGATE ZEROS

Page 21: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE PLOT CREATION EXAMPLE(HTTP://LPSA.SWARTHMORE.EDU/BODE/BODEEXAMPLES.HTML#EX3)

• FUNCTION WITH MULTIPLE POLES ATORIGIN, COMPLEX CONJUGATE ZEROS

Page 22: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE PLOT CREATION EXAMPLE(HTTP://LPSA.SWARTHMORE.EDU/BODE/BODEEXAMPLES.HTML#EX3)

• FUNCTION WITH TIME DELAY

Page 23: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• DEVELOPING A BODE PLOT FROM THE TRANSFER FUNCTION

Page 24: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT• DERIVATION FOR A FIRST ORDER

PROCESS

Page 25: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT• PROPERTIES OF BODE PLOTS

Page 26: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT• BODE PLOT OF COMPLEX TRANSFER

FUNCTIONS• BREAK TRANSFER FUNCTION INTO A

PRODUCT OF SIMPLE TRANSFER FUNCTIONS.• IDENTIFY Ar(ω) AND Φ(ω) OF EACH SIMPLE

TRANSFER FUNCTION FROM TABLE 11.1.• COMBINE TO GET Ar(ω) AND Φ(ω) FOR

COMPLEX TRANSFER FUNCTION ACCORDING TO PROPERTIES.

• PLOT RESULTS AS A FUNCTION OF ω.

Page 27: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• BODE PLOTS CAN BE PLOTTED FROM TRANSFER FUNCTIONS– WE CAN SET UP THE TRANSFER

FUNCTION: Y(s) – Gp(s)C(s) WHERE C(s) IS THE SINUSOIDAL INPUT

– AN INVERSE LaPLACE TRANSFORM OF THE RESULT THEN PROVIDES A TIME FUNCTION

Page 28: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• TAKING THIS TO A LIMIT TO ELIMINATE TRANSIENTS THAT WILL DECAY LEAVES THE STANDING WAVE FUNCTION– THIS CAN BE USED TO EVALUATE Ar

AS A FUNCTION OF ω– AND Φ AS A FUNCTION OF ω– TABLE 11.1 PROVIDES FUNCTIONS TO

CALCULATE Ar AND Φ FOR A NUMBER OF COMMON TRANSFER FUNCTIONS

Page 29: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• GAIN MARGIN AND PHASE MARGIN– THE BODE STABILITY CRITERION IS

EVALUATED AT THE POINT WHERE Φ IS EQUAL TO -180°.

– THE FREQUENCY AT THIS POINT IS CALLED THE CRITICAL FREQUENCY

Page 30: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• GAIN MARGIN AND PHASE MARGIN– THE VALUE OF Ar CALCULATED AT

THE CRITICAL FREQUENCY, Ar* DETERMINES THE PROCESS STABILITY

– THIS IS EXPRESSED AS THE GAIN MARGIN:

– WHEN GM > 1, THE SYSTEM IS STABLE

GMAr

1*

Page 31: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• GAIN MARGIN AND PHASE MARGIN– THE PHASE MARGIN IS THE VALUE

OF THE PHASE ANGLE AT THE POINT WHERE Ar = 1 AND IS RELATIVE TO THE PHASE ANGLE OF -180°:

(EQUATION 11.3.2)– THE FREQUENCY WHERE THIS

CONDITION OCCURS IS CALLED THE CROSSOVER FREQUENCY

PM * ( )180

Page 32: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• PULSE TEST• THIS IS AN OPEN LOOP TEST USED TO

OBTAIN THE VALUES NECESSARY TO CREATE A BODE PLOT

• RESULTS COMPARE THE AMPLITUDE AND THE DURATION TIMES FOR THE INPUT AND OUTPUT VALUES FOR AN OPEN LOOP.

• THESE ARE USED WITH EQUATIONS 11.4.1 THROUGH 11.4.8 TO OBTAIN THE BODE PLOT

Page 33: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• PULSE TEST EXAMPLE

Page 34: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• DEVELOPING A PULSE TEST PROCESS TRANSFER FUNCTION

Page 35: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

BODE STABILITY PLOT

• LIMITATIONS OF TRANSFER FUNCTIONS DEVELOPED FROM PULSE TESTS– THEY REQUIRE AN OPEN LOOP TIME

CONSTANT TO COMPLETE.– DISTURBANCES CAN CORRUPT THE

RESULTS.– BODE PLOTS DEVELOPED FROM PULSE

TESTS TEND TO BE NOISY NEAR THE CROSSOVER FREQUENCY WHICH AFFECTS GM AND PM CALCULATIONS.

Page 36: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

NYQUIST DIAGRAM

• PULSE TEST• COMBINES THE VALUE OF Ar AND Φ ON

A SINGLE DIAGRAM• OTHERWISE IT HAS NO ADVANTAGE

OVER THE BODE PLOTS

Page 37: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

CLOSED LOOP FREQUENCY RESPONSE

• REFERENCE FIGURE 11.6.1

Page 38: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

EXAMPLE OF A CLOSED LOOP BODE PLOT

• REFERENCE FIGURE 11.6.2

Page 39: CHE 185 – PROCESS CONTROL AND DYNAMICS FREQUENCY RESPONSE ANALYSIS.

ANALYSIS OF CLOSED LOOP BODE PLOT

• REFERENCE FIGURE 11.6.2– AT LOW FREQUENCIES, THE CONTROLLER

HAS TIME TO REJECT THE DISTURBANCES, I.E., Ar IS SMALL.

– AT HIGH FREQUENCIES, THE PROCESS FILTERS (AVERAGES) OUT THE VARIATIONS AND Ar IS SMALL.

– AT INTERMEDIATE FREQUENCIES, THE CONTROLLED SYSTEM IS MOST SENSITIVE TO DISTURBANCES.

– THE PEAK FREQUENCY INDICATES THE FREQUENCY FOR WHICH A CONTROLLER IS MOST SENSITIVE.