h and optimal controller design for the shell control problem d. chang, e.s. meadows, and s.l....

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H and Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering University of Alberta CSChE Annual Meeting 2002

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Page 1: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

H and Optimal Controller Design for the Shell Control

Problem

D. Chang, E.S. Meadows, and S.L. ShahDepartment of Chemical and Materials

EngineeringUniversity of Alberta

CSChE Annual Meeting 2002

Page 2: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 2

Outline

Shell control problem descriptionKey objectivesDesign criteria and methodologyH and optimal controller results

Prototype test case resultsConclusions

Page 3: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 3

Shell Control Problem

Prett and Morari. Shell Process Control Workshop, 1987.

Page 4: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 4

Key Objectives

Design a robustly stable controller satisfying the following constraints:

top end point and bottom reflux temperature is constrained between 0.5 and –0.5

top draw, side draw and bottoms reflux duty is constrained between 0.5 and –0.5

Manipulated variables have maximum move sizes between 0.05 and –0.05

Page 5: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 5

Generalized Plant Structure

Page 6: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 6

Block Singularity

0

)(

212

12111

21

DC

DDC

BBA

sPspy(D) spy(D’)

I

D0

12 ID 021 and

Avoid singular control problems

Meaning D12 must be full column and D21 must be full row rank. (Zhou, Doyle, and Glover, 1996)D before addition of setpoints

D’ after addition of setpoints

Page 7: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 7

Exogenous Inputs Revisited

Prett and Morari. Shell Process Control Workshop, 1987.

Page 8: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 8

Open Loop Characteristics

Page 9: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 9

Exogenous Output Weights

2

1

1

Cs

BsAsw

Performance weight•Crossover = 0.006 rad/sec 167 sec

•10% S.S. offset

Controller output weight•Crossover = 0.9 rad/sec 1.1 sec

Page 10: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 10

H Controller Response

Page 11: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 11

Robust Stability of H Controller

Page 12: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 12

Optimal Response

iteration 1

iteration 2iteration 3

iteration 4

Page 13: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 13

Prototype Test Cases

Worst case uncertainty set calculated by Matlab :

1= 1 2= -1, 3= -0.7585, 4= -0.5549, 5= 0.2497

Page 14: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 14

Optimal Time Response

Page 15: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 15

Worst Case Input Frequency

w 0.2754 rad/s

Page 16: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 16

Input and Rate Responses

Page 17: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 17

Conclusions

A robustly stable multivariate controller can be designed with relative ease

All of the input, output and rate constraints were met for the Shell control problem

analysis provides a consistent framework for evaluating robust performance for all controllers

Page 18: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 18

Acknowledgements

Dr. E.S. MeadowsDr. S.L. ShahCPC group at U of ANSERCiCore

Page 19: H  and  Optimal Controller Design for the Shell Control Problem D. Chang, E.S. Meadows, and S.L. Shah Department of Chemical and Materials Engineering

CSChE Annual Meeting 2002: Vancouver, BC 19

Questions?