Model-based synthesis of nonlinear PI and PID controllers
dc.contributor.author | Wright, Raymond A. | en_US |
dc.contributor.author | Kravaris, Costas | en_US |
dc.contributor.author | Kazantzis, Nikolaos | en_US |
dc.date.accessioned | 2007-01-17T15:56:16Z | |
dc.date.available | 2007-01-17T15:56:16Z | |
dc.date.issued | 2001-08 | en_US |
dc.identifier.citation | Wright, Raymond A.; Kravaris, Costas; Kazantzis, Nikolaos (2001)."Model-based synthesis of nonlinear PI and PID controllers." AIChE Journal 47(8): 1805-1818. <http://hdl.handle.net/2027.42/49316> | en_US |
dc.identifier.issn | 0001-1541 | en_US |
dc.identifier.issn | 1547-5905 | en_US |
dc.identifier.uri | https://hdl.handle.net/2027.42/49316 | |
dc.description.abstract | PI and PID controllers continue to be popular methods in industrial applications. It is well known that linear PI and PID controllers result from the application of model-based controller design methods to linear first- and second-order systems. It is shown that nonlinear PI and PID controllers result from the application of nonlinear controller design methods to nonlinear first- and second-order systems. As a result, the controllers resulting from nonlinear model-based control theory are put in a convenient form, more amenable to industrial implementation. Additionally, the quantities used in the controller are useful for monitoring the process and quantifying modeling error. Chemical engineering examples are used to illustrate the resulting control laws. A simulation example further demonstrates the performance of the nonlinear controllers, as well as their useful process monitoring quantities. | en_US |
dc.format.extent | 257855 bytes | |
dc.format.extent | 3118 bytes | |
dc.format.mimetype | application/pdf | |
dc.format.mimetype | text/plain | |
dc.language.iso | en_US | |
dc.publisher | Wiley Subscription Services, Inc., A Wiley Company | en_US |
dc.subject.other | Chemistry | en_US |
dc.subject.other | Chemical Engineering | en_US |
dc.title | Model-based synthesis of nonlinear PI and PID controllers | en_US |
dc.type | Article | en_US |
dc.rights.robots | IndexNoFollow | en_US |
dc.subject.hlbsecondlevel | Chemical Engineering | en_US |
dc.subject.hlbtoplevel | Engineering | en_US |
dc.subject.hlbtoplevel | Science | en_US |
dc.description.peerreviewed | Peer Reviewed | en_US |
dc.contributor.affiliationum | Dept. of Chemical Engineering, The University of Michigan, Ann Arbor, MI 48109 | en_US |
dc.contributor.affiliationother | The Dow Chemical Company, Midland, MI 48667 ; The Dow Chemical Company, Midland, MI 48667 | en_US |
dc.contributor.affiliationother | Dept. of Chemical Engineering, Texas A&M University, College Station, TX 77843 | en_US |
dc.description.bitstreamurl | http://deepblue.lib.umich.edu/bitstream/2027.42/49316/1/690470812_ftp.pdf | en_US |
dc.identifier.doi | http://dx.doi.org/10.1002/aic.690470812 | en_US |
dc.identifier.source | AIChE Journal | en_US |
dc.owningcollname | Interdisciplinary and Peer-Reviewed |
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