## Abstract We developed a mathematical model to describe the behavior of semibatch styrene suspension polymerization processes, where the constituents of a typical emulsion polymerization process are added into the reaction vessel during the course of a typical suspension reaction. This technique
Modeling and optimization of suspension SAN polymerization re actors
β Scribed by M. J. R. Cavalcanti; J. C. Pinto
- Publisher
- John Wiley and Sons
- Year
- 1997
- Tongue
- English
- Weight
- 422 KB
- Volume
- 65
- Category
- Article
- ISSN
- 0021-8995
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β¦ Synopsis
A detailed mathematical model is developed to describe the operation of batch-modified SAN [ styrene (ST) /acrylonitrile (AN )/a-methylstyrene (AMS )] terpolymerization reactors. The model is validated by comparing simulation results with published and plant experimental data. Optimal temperature policies and initiator feed concentrations are then computed. It is shown that optimal operation conditions may be extremely sensitive to small perturbations, so that optimal operation conditions may actually be unfeasible. It is also shown that average polymer molecular weight may be properly controlled by adding small amounts of inhibitor into the polymerization medium, which is usually cheaper than using chain transfer agents to control the average polymer molecular weight.
π SIMILAR VOLUMES
On the basis of a population balance and the kinetic mechanism of free-radical suspension polymerization, a mathematical model of the suspension polymerization process is proposed. The population balance model which describes a mechanism involving the particle size distribution (PSD) in disperse sys