DocumentCode
3204007
Title
Quantitative synthesis for a 3×3 distillation column to achieve performance robustness
Author
Nataraj, P.S.V. ; Joshi, Jitendra B.
Author_Institution
Syst. & Control Eng. Group, Indian Inst. of Technol., Bombay, India
fYear
1995
fDate
5-7Jan 1995
Firstpage
161
Lastpage
166
Abstract
In this paper, quantitative synthesis of a multivariable two-matrix-degree-of-freedom feedback system for a 3×3 distillation column with sidestreams example having significant plant parameter uncertainty, is performed. The synthesis procedure is that of multi-input multi-output (MIMO) quantitative feedback theory (QFT). From the given MIMO problem, equivalent single-loop problems are derived whose solution guarantees the solution of the original problem. Using the basic single-input single-output (SISO) QFT procedure, the single-loop problems are then solved to satisfy the frequency domain specifications on the tracking and disturbance-rejection properties. The design is verified in both frequency and time domains for 81 plants picked randomly from the set of uncertain plants. The results show that the performance specifications are successfully achieved for the range of parameter uncertainty considered
Keywords
MIMO systems; chemical industry; control system synthesis; distillation; feedback; process control; MIMO quantitative feedback theory; distillation column; disturbance rejection; frequency domain specifications; multivariable feedback system; parameter uncertainty; performance robustness; single-loop problems; tracking; Control engineering; Control system synthesis; Control systems; Distillation equipment; Feedback; Frequency domain analysis; MIMO; Robustness; Uncertain systems; Uncertainty;
fLanguage
English
Publisher
ieee
Conference_Titel
Industrial Automation and Control, 1995 (I A & C'95), IEEE/IAS International Conference on (Cat. No.95TH8005)
Conference_Location
Hyderabad
Print_ISBN
0-7803-2081-6
Type
conf
DOI
10.1109/IACC.1995.465849
Filename
465849
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