A modified form of the Discrete Maximum Principle (DMP) is derived for systems with finite memory. It is shown that this form of the DMP may be used for the optimal control of nonlinear continuous dynamics systems, when the control policies are bound to be piecewise constant. In this case the modifi
Composition control of batch copolymerization reactors
β Scribed by Matthew Tirrell; Kevin Gromley
- Publisher
- Elsevier Science
- Year
- 1981
- Tongue
- English
- Weight
- 876 KB
- Volume
- 36
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
β¦ Synopsis
Abstrac+-Composition control of free-radically initiated batch copolymerization reactor by temperature manipulation is investigated through a program of calculation and experiment. The work of Ray and Gall is extended to explicit calculation of temperature vs time policies which eliminate or minimize composition drift. Both continuous and discrete, oiecewise-constant oolicies have been computed. The former are disjoint policies which can bc found . simply by manipulating the monomer mass balances; the tatter are found through &Ii&ion of the discrete version of the maximum principle. Calculations are compared to experiments done on the system styrene-acrylonitrile. It is demonstrated that implementation of some of Ihe computed policies is feasible and quite beneficial. The time discrete policies with smalt numbers of stages (less than -six) perform much more poorly than the continuous policies indicating that the copolymerization reactor is much more sensitive to deviations from optimal&y than batch reactors operating with other reaction schemes. Thus, effective implementation of the lype of control studied here will necessitate use of controllers capable of closely tracking a continuous trajectory.
π SIMILAR VOLUMES
In this article a highly exothermic batch polymerization reactor is considered. The reactor is simplified as a mixing tank with the internal heat generation treated as a disturbance. A fuzzy-hybrid-PID-feedback (FH-PID) control structure is developed in which the output of fuzzy hybrid portion is us
Although reactant addition induces unavoidable temperature changes in semi-batch reactors, it is shown that adaptive-predictive techniques may offer a means of balancing them successfully. To this end, appropriate data filtering must be integrated to the estimation algorithm, so that parameters rema
In this paper, a digital PID controller, derived in the partial state reference model (PSRM) adaptive control spirit, is used to control the temperature in batch and semi-batch chemical reactors.This controller consists in the combination of a performance-oriented linear quadratic control design met