Dynamic optimization of batch emulsion polymerization of vinyl acetate—an orthogonal polynomial initiator policy
A minimum end time initiator addition policy for batch emulsion polymerization of vinyl acetate under a constant reaction temperature is found using a general nonlinear programming solver and orthogonal collocation techniques. The constraints are restrictions on the reaction rate of the polymerizati...
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Published in | Chemical engineering science Vol. 44; no. 3; pp. 515 - 528 |
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Main Authors | , |
Format | Journal Article |
Language | English |
Published |
Oxford
Elsevier Ltd
1989
Elsevier |
Subjects | |
Online Access | Get full text |
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Summary: | A minimum end time initiator addition policy for batch emulsion polymerization of vinyl acetate under a constant reaction temperature is found using a general nonlinear programming solver and orthogonal collocation techniques. The constraints are restrictions on the reaction rate of the polymerization and the total amount of initiator added. A 5-1 jacketed reactor with a computerized temperature control system was used to carry out several experimental runs. Experimental results show a good agreement with theoretical predictions for this complex system. The results also demonstrate that good temperature control can be achieved for this highly exothermic reaction system under these optimal-control policies. The methodology used to solve this fixed initial value constrained optimal-control problem is a modified version of Biegler (1984,
Comput. chem. Engng
8, 243). The modified approach is more promising in cases where state constraints and/or free end time situations exist. |
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ISSN: | 0009-2509 1873-4405 |
DOI: | 10.1016/0009-2509(89)85029-8 |