Steady state multiobjective optimization of continuous copolymerization reactors
- 1 April 1986
- journal article
- research article
- Published by Wiley in Polymer Engineering & Science
- Vol. 26 (7) , 499-507
- https://doi.org/10.1002/pen.760260708
Abstract
The multiobjective nature of optimization problems related to homopolymerizaton and copolymerization processes implies a vector objective formulation for a correct approach. Two copolymerization systems, methyl methacrylate‐vinyl acetate (MMA‐VA) and styrene‐acrylonitrile (ST‐AN) are simulated, and some aspects of the steady state optimality of continuous operation are analyzed. The determination of non‐inferior sets through the concept of Pareto optimality permits a clear decision on trade‐offs related to operating conditions and product specifications.Keywords
This publication has 16 references indexed in Scilit:
- Multiobjective dynamic optimization of semibatch copolymerization reactorsChemical Engineering Science, 1982
- Composition control of batch copolymerization reactorsChemical Engineering Science, 1981
- Multi-level, multi-objective optimization in process engineeringChemical Engineering Science, 1981
- Mathematical programming with multiple objectives: A tutorialComputers & Operations Research, 1980
- Kuhn-Tucker multipliers as trade-offs in multiobjective decision-making analysisAutomatica, 1979
- Multiple‐Objective Optimization in Water Resource SystemsWater Resources Research, 1974
- On the Mathematical Modeling of Polymerization ReactorsJournal of Macromolecular Science, Part C: Polymer Reviews, 1972
- Molecular Weight Distributions in Copolymer Systems. II. Free Radical CopolymerizationMacromolecules, 1971
- The optimal control of polymerisation reactorsThe Canadian Journal of Chemical Engineering, 1969
- The Control of Copolymer Composition Distributions in Batch and Tubular ReactorsMacromolecules, 1969