25
Chapter 14 Frequency Response Force dynamic process with A sin t , 2 2 ) ( s A s U Chapter 14 14. 1 1

[PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Embed Size (px)

Citation preview

Page 1: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Chapter 14Frequency ResponseForce dynamic process with A sin t , 22)(

sAsU

Cha

pter

14

14.1

1

Page 2: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Input: Output: is the normalized amplitude ratio (AR) is the phase angle, response angle (RA)AR and are functions of ωAssume G(s) known and let

tsinA

tAsinˆ

1 2

2 21 2

2

1

arctan

s j G j K K j

G AR K K

KGK

Cha

pter

14

AA /ˆ

2

Page 3: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Example 14.1:Example 14.1:

21 1 ( 1)1 1

jG j jj j

11

G ss

2 2 2 2

11 1

G j j

K1 K2

Cha

pter

14

3

Page 4: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Cha

pter

14

4

Page 5: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

(plot of log |G| vs. log and vs. log )

2 2

0

1

1arctan

as , 90

G

Use a Bode plot to illustrate frequency response

log coordinates:

1 2 3

1 2 3

1 2 3

1 2 3

1

2

1 2

1 2

log log log log

log log log

G G G G

G G G G

G G G G

G G G GGGG

G G G

G G G

Cha

pter

14

5

Page 6: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Figure 14.4 Bode diagram for a time delay, e-s.

Cha

pter

14

6

Page 7: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Cha

pter

14

Example 14.30.55(0.5 1)( )

(20 1)(4 1)

ss eG ss s

7

Page 8: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

The Bode plot for a PI controller is shown in next slide.Note b = 1/I . Asymptotic slope ( 0) is -1 on log-log plot.

Recall that the F.R. is characterized by:1. Amplitude Ratio (AR)2. Phase Angle ()

F.R. Characteristics of Controllers

For any T.F., G(s)

A) Proportional Controller

B) PI Controller

For

( )

( )

AR G j

G j

( ) , 0C C CG s K AR K

2 2

1

1 1( ) 1 1

1tan

C C CI I

I

G s K AR Ks

Cha

pter

14

8

Page 9: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Cha

pter

14

9

Page 10: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Series PID Controller. The simplest version of the series PID controller is

Series PID Controller with a Derivative Filter. The series controller with a derivative filter was described in Chapter 8

τ 1 τ 1 (14-50)τI

c c DI

sG s K ss

τ 1 τ 1 (14-51)τ ατ 1I D

c cI D

s sG s Ks s

Cha

pter

14

Ideal PID Controller.1( ) (1 ) (14 48)c c DI

G s K ss

10

Page 11: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Figure 14.6 Bode plots of ideal parallel PID controller and series PID controller with derivative filter (α = 1).

Ideal parallel:

Series with Derivative Filter:

10 1 4 1210 0.4 1cs sG s

s s

12 1 410cG s s

s C

hapt

er 1

4

11

Page 12: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Advantages of FR Analysis for Controller Design:1. Applicable to dynamic model of any order

(including non-polynomials).2. Designer can specify desired closed-loop response

characteristics.3. Information on stability and sensitivity/robustness is provided.

Disadvantage:The approach tends to be iterative and hence time-consuming

-- interactive computer graphics desirable (MATLAB)

Cha

pter

14

12

Page 13: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Controller Design by Frequency Response- Stability Margins

Analyze GOL(s) = GCGVGPGM (open loop gain)

Three methods in use:

(1) Bode plot |G|, vs. (open loop F.R.) - Chapter 14

(2)Nyquist plot - polar plot of G(j) - Appendix J

(3)Nichols chart |G|, vs. G/(1+G) (closed loop F.R.) - Appendix J

Advantages:• do not need to compute roots of characteristic equation• can be applied to time delay systems• can identify stability margin, i.e., how close you are to instability.

Cha

pter

14

13

Page 14: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Cha

pter

14

14.8

14

Page 15: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Frequency Response Stability CriteriaTwo principal results:1. Bode Stability Criterion2. Nyquist Stability Criterion

I) Bode stability criterionA closed-loop system is unstable if the FR of the open-loop T.F. GOL=GCGPGVGM, has an amplitude ratio greater than one at the critical frequency, . Otherwise the closed-loop system is stable.

• Note: where the open-loop phase angle is -1800. Thus,

• The Bode Stability Criterion provides info on closed-loop stability from open-loop FR info.

• Physical Analogy: Pushing a child on a swing or bouncing a ball.

C

value of C

Cha

pter

14

15

Page 16: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Example 1:Example 1:A process has a T.F.,

And GV = 0.1, GM = 10 . If proportional control is used, determine

closed-loop stability for 3 values of Kc: 1, 4, and 20.

Solution:Solution:The OLTF is GOL=GCGPGVGM or...

The Bode plots for the 3 values of Kc shown in Fig. 14.9.Note: the phase angle curves are identical. From the Bodediagram:KC AROL Stable?1 0.25 Yes4 1.0 Conditionally stable20 5.0 No

3

2( )(0.5 1)

COL

KG ss

3

2( )(0.5 1)pG s

s

Cha

pter

14

16

Page 17: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Figure 14.9 Bode plots for GOL = 2Kc/(0.5s + 1)3.

Cha

pter

14

17

Page 18: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

• For proportional-only control, the ultimate gain Kcu is defined to be the largest value of Kc that results in a stable closed-loop system.

• For proportional-only control, GOL= KcG and G = GvGpGm.AROL(ω)=Kc ARG(ω) (14-58)

where ARG denotes the amplitude ratio of G.

• At the stability limit, ω = ωc, AROL(ωc) = 1 and Kc= Kcu.

1 (14-59)(ω )cu

G cK

ARC

hapt

er 1

4

18

Page 19: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Example 14.7:Example 14.7:Determine the closed-loop stability of the system,

Where GV = 2.0, GM = 0.25 and GC =KC . Find C from theBode Diagram. What is the maximum value of Kc for a stablesystem?

Solution:Solution:The Bode plot for Kc= 1 is shown in Fig. 14.11. Note that:

154)(

sesG

s

p

OL

max

1.69 rad min

0.235

1 1= 4.250.235

C

C

COL

AR

KAR

Cha

pter

14

19

Page 20: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Cha

pter

14

14.11

20

Page 21: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Ultimate Gain and Ultimate Period

• Ultimate Gain: KCU = maximum value of |KC| that results in a stable closed-loop system when proportional-only control is used.

• Ultimate Period:

• KCU can be determined from the OLFR when proportional-only control is used with KC =1. Thus

• Note: First and second-order systems (without time delays) do not have a KCU value if the PID controller action is correct.

2U

C

P

1 for 1C

CU COL

K KAR

Cha

pter

14

21

Page 22: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Gain and Phase Margins• The gain margin (GM) and phase margin (PM) provide measures of how close a system is to a stability limit.

• Gain Margin: Let AC = AROL at = C. Then the gain margin is

defined as: GM = 1/AC

According to the Bode Stability Criterion, GM >1 stability

• Phase Margin: Let g = frequency at which AROL = 1.0 and the corresponding phase angle is g . The phase margin is defined as: PM = 180° + g

According to the Bode Stability Criterion, PM >0 stability

See Figure 14.12.

Cha

pter

14

22

Page 23: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Cha

pter

14

23

Page 24: [PPT]No Slide Title - McKetta Department of Chemical …che.utexas.edu/course/che360/lecture_notes/chapter_14.ppt · Web viewTitle No Slide Title Author Preferred Customer Last modified

Rules of Thumb:A well-designed FB control system will have:

Closed-Loop FR Characteristics:An analysis of CLFR provides useful information about control system performance and robustness. Typical desired CLFR for disturbance and setpoint changes and the corresponding step response are shown in Appendix J.

1.7 2.0 30 45GM PM

Cha

pter

14

24