dc.creatorGhasem, N. M.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia
dc.creatorHussain, M. A.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia
dc.creatorSata, S. A.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia
dc.date.accessioned2018-02-24T16:01:01Z
dc.date.accessioned2020-04-15T18:08:46Z
dc.date.available2018-02-24T16:01:01Z
dc.date.available2020-04-15T18:08:46Z
dc.date.created2018-02-24T16:01:01Z
dc.date.created2020-04-15T18:08:46Z
dc.identifier2027-1352
dc.identifier0122-7483
dc.identifierhttp://hdl.handle.net/10554/31947
dc.description.abstractThe absence of a stable operational state in polymerization reactors that operates in batches is factor that determine the need of a special control system. In this study, advanced control methodology is implemented for controlling the operation of a batch polymerization reactor for polystyrene production utilizing model predictive control. By utilizing a model of the polymerization process, the necessary operational conditions were determined for producing the polymer within the desired characteristics. The main control objective is to bring the reactor temperature to its target temperature as rapidly as possible with minimal temperature overshoot. Control performance for the proposed method is encouraging. It has been observed that temperature overshoot can be minimized by the proposed method with the use of both reactor and jacket energy balance for reactor temperature control.
dc.languageeng
dc.publisherPontificia Universidad Javeriana
dc.relationhttp://revistas.javeriana.edu.co/index.php/scientarium/article/view/4946/3820
dc.relationUniversitas Scientiarum; Vol 11, No 1 (2006); 49-58
dc.relationUniversitas Scientiarum; Vol 11, No 1 (2006); 49-58
dc.relationUniversitas Scientiarum; Vol 11, No 1 (2006); 49-58
dc.rightsAtribución-NoComercial-SinDerivadas 4.0 Internacional
dc.rightsinfo:eu-repo/semantics/openAccess
dc.rightshttp://purl.org/coar/access_right/c_abf2
dc.subjectnull
dc.subjectcontrol; MPC; polymerization; polystyrene; modeling
dc.subjectnull
dc.titleAPPLICATION OF MODEL PREDICTIVE CONTROL TO BATCH POLYMERIZATION REACTOR


Este ítem pertenece a la siguiente institución