Please use this identifier to cite or link to this item:
|Title:||A multiple models based predictive control strategy applied in polymerization reactor control|
|Authors:||Zhuang, H. |
|Source:||Zhuang, H.,Ohshima, M.,Chiu, M.-S. (2003). A multiple models based predictive control strategy applied in polymerization reactor control. Computer Aided Chemical Engineering 15 (C) : 1147-1152. ScholarBank@NUS Repository. https://doi.org/10.1016/S1570-7946(03)80463-7|
|Abstract:||By making use of the multiple models to predict the process outputs in future time instants, a generalized predictive controller design is developed in this paper. However, the resulting nonlinear optimization problem cannot be solved straightforwardly because the values of the weighting functions in the prediction horizon are dependent on the future values of the process outputs and inputs. To circumvent this problem, an iterative procedure is developed. The proposed design is illustrated by considering the control of a polymerization reactor, in which an isothermal free-radical polymerization of methyl methacrylate is carried out using azo-bis-isobutyronitrile as initiator and toluene as solvent. © 2003 Elsevier B.V. All rights reserved.|
|Source Title:||Computer Aided Chemical Engineering|
|Appears in Collections:||Staff Publications|
Show full item record
Files in This Item:
There are no files associated with this item.
checked on Dec 8, 2017
Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.