Abstract
A method for adaptive control of a nonisothermal continuous stirred tank reactor with output temperature constraint is developed. The control system is a multivariable nonlinear one. Indirect adaptive control is applied. Based on an allowable temperature rise, the control variables are determined. The reactor temperature is under a constraint to prevent the temperature from overshooting. Simulation studies give satisfactory results.
Original language | English |
---|---|
Pages (from-to) | 187-197 |
Number of pages | 11 |
Journal | Chemical Engineering Communications |
Volume | 110 |
Issue number | 1 |
DOIs | |
Publication status | Published - 1991 Dec |
All Science Journal Classification (ASJC) codes
- General Chemistry
- General Chemical Engineering