DocumentCode :
1601472
Title :
Nonlinear control of a batch polymerization reactor: an experimental study
Author :
Soroush, Masoud ; Kravaris, Costas
Author_Institution :
Dept. of Chem. Eng., Michigan Univ., Ann Arbor, MI, USA
fYear :
1992
Firstpage :
66
Abstract :
The experimental application of the globally linearizing control method to a batch polymerization reactor is studied. The nonlinear controller is implemented on a microcomputer to start up the reactor and then track a precalculated optimal temperature profile. The reactor temperature is controlled by manipulating two coordinated inputs. A reduced-order observer is used to estimate the concentrations of initiator and monomer. The experimental results show the excellent servo and regulatory performance of the nonlinear controller in the presence of observer initialization error and active manipulated input constraints
Keywords :
batch processing (industrial); chemical technology; linearisation techniques; microcomputer applications; nonlinear control systems; polymerisation; process computer control; temperature control; GLC; batch polymerization reactor; globally linearizing control; initiator concentration; microcomputer; monomer concentration; nonlinear controller; observer initialization error; optimal temperature profile; reduced-order observer; regulatory performance; servo performance; temperature profile tracking; Chemical engineering; Control system synthesis; Control systems; Inductors; Nonlinear control systems; Polymers; Pressure control; Servomechanisms; Temperature control; Valves;
fLanguage :
English
Publisher :
ieee
Conference_Titel :
Control Applications, 1992., First IEEE Conference on
Conference_Location :
Dayton, OH
Print_ISBN :
0-7803-0047-5
Type :
conf
DOI :
10.1109/CCA.1992.269897
Filename :
269897
Link To Document :
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