Please use this identifier to cite or link to this item: https://scholarbank.nus.edu.sg/handle/10635/67385
DC FieldValue
dc.titleClosed-loop tuning of process control systems
dc.contributor.authorKrishnaswamy, P.R.
dc.contributor.authorChan, B.E.M.
dc.contributor.authorRangaiah, G.P.
dc.date.accessioned2014-06-17T10:00:46Z
dc.date.available2014-06-17T10:00:46Z
dc.date.issued1987
dc.identifier.citationKrishnaswamy, P.R.,Chan, B.E.M.,Rangaiah, G.P. (1987). Closed-loop tuning of process control systems. Chemical Engineering Science 42 (9) : 2173-2182. ScholarBank@NUS Repository.
dc.identifier.issn00092509
dc.identifier.urihttp://scholarbank.nus.edu.sg/handle/10635/67385
dc.description.abstractA technique for tuning PID controllers, involving a single dynamic test (such as a step or pulse change in set point) implemented during closed-loop operation, is proposed. The resulting transient data are used to predict the frequency response of the open-loop process which in turn is used to compute the optimum controller settings. Simulation results reveal that this technique provides reliable tuning constants even when such practical problems as process noise and unanticipated load upsets arise during implementation. A comparison with the recently proposed tuning alternative (Yuwana and Seborg, A.I.Ch.E. J. 28, 434, 1982; Jutan and Rodriguez, Can. J. Chem. Engng 62, 802, 1984) confirms that in general the suggested procedure, apart from being more flexible, yields also relatively better results. © 1987.
dc.sourceScopus
dc.typeArticle
dc.contributor.departmentCHEMICAL ENGINEERING
dc.description.sourcetitleChemical Engineering Science
dc.description.volume42
dc.description.issue9
dc.description.page2173-2182
dc.description.codenCESCA
dc.identifier.isiutNOT_IN_WOS
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