Designing of Decoupler for a 44 Distillation Column Processes with PID Controller

Please use this identifier to cite or link to this item: http://hdl.handle.net/2080/1710

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DC Field	Value	Language
dc.contributor.author	Sethi, M K	-
dc.contributor.author	Dan, T K	-
dc.date.accessioned	2012-05-25T11:14:16Z	-
dc.date.available	2012-05-25T11:14:16Z	-
dc.date.issued	2012-05	-
dc.identifier.citation	International Conference on Electrical Engineering and Computer Science, May 5, 2012, Goa India	en
dc.identifier.isbn	978-93-81693-98-8	-
dc.identifier.uri	http://hdl.handle.net/2080/1710	-
dc.description	Copyright belongs to proceeding publisher	en
dc.description.abstract	This paper extend the concept of relative normalized gain array (RNGA) and an Equivalent Transfer Function (ETF) for each element in the transfer function matrix was derived for the closed-loop control system and proposes a systematic approach to designing decentralized PID control for distillation column process containing integrators and/or differentiators. The decoupler could be easily determined with each element in the First-Order-plus-Time-Delay (FOPTD) form and resulted in a stable, proper and causal decoupled matrix. The main advantage of this method is its simplicity; it reduces excessive calculation.	en
dc.format.extent	223151 bytes	-
dc.format.mimetype	application/pdf	-
dc.language.iso	en	-
dc.title	Designing of Decoupler for a 44 Distillation Column Processes with PID Controller	en
dc.type	Article	en
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