Tuning proportional-integral controllers for processes with both inverse response and deadtime

Industrial and Engineering Chemistry Research

Volumn 39, Issue 4, 2000, Pages 973-976

  Luyben, William L ^a  

^a Lehigh University   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

CHEMICAL REACTORS; FEEDBACK CONTROL; FURNACES; HEAT EXCHANGERS; MATHEMATICAL MODELS; TEMPERATURE CONTROL;

DEADTIME; INTEGRAL CONTROLLERS; INVERSE RESPONSE; TUNING METHOD;

PROCESS CONTROL;

ARTICLE; CHEMICAL ENGINEERING; CHEMICAL INDUSTRY; HEAT EXCHANGE; REACTOR; TEMPERATURE;

EID: 0034128554     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie9906114     Document Type: Article

References (8)

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2. Ho, W. K.; Hang, C. C.; Zhou, J. Performance and gain and phase margins of well-known PI tuning formulas. IEEE Trans. Control Syst. Technol. 1995, 3, 245-248.
3. Marlin, T. E. Process Control; McGraw-Hill: New York, 1995.
4. Chien, I. L.; Fruehauf, P. S. Consider IMC tuning to improve performance. Chem. Eng. Prog. 1990, Oct, 33-41.
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6. Waller, K. V. T.; Nygardas, C. G. On inverse response in process control. Ind. Eng. Chem. Fundam. 1975, 14 (3), 221-223.
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8. Ogunnaike, B. A.; Ray, W. H. Process Dynamics, Modeling and Control; Oxford University Press: Oxford, U.K., 1994; p 608.