continuous stirred tank reactor was used for studying the kinetics of mesophase formation from a petroleum pitch. The conversion of the pitch was analysed by determination of the tetrahydrofuran insolubles and the mesophase content, the glass transition temperature, the density, and the coke yield o
A theoretical investigation of the production of branched copolymers in continuous stirred tank reactors
โ Scribed by Apostolis Baltsas; Dimitris S. Achilias; Costas Kiparissides
- Publisher
- John Wiley and Sons
- Year
- 1996
- Tongue
- English
- Weight
- 811 KB
- Volume
- 5
- Category
- Article
- ISSN
- 1022-1344
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โฆ Synopsis
Abstract
A comprehensive mathematical model for freeโradical copolymerization reactions has been developed for a homogeneous continuous stirred tank reactor. The present model is based on a fairly general copolymerization scheme accounting for the formation of linear and branched copolymer chains. Both chain transfer to polymer and terminal double bond reactions are considered in order to predict the long chain branching frequency. Changes in molecular weight, composition and degree of branching occurring during the copolymerization reaction are modelled using the method of moments. To breakโdown the dependence of the moment equations on higher order moments two different closure methods are considered. The predictive capabilities of the model are examined in relation to the solution copolymerization of methyl methacrylate with vinyl acetate. It is shown that both chain transfer to polymer and terminal double bond reactions significantly contribute to the broadening of the molecular weight and degree of branching distributions. Furthermore, the terminal double bond reaction effects significantly the copolymer numberโaverage molecular weight and the concentration of terminal double bonds.
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The influence of enforced periodic concentration variations on a continuous stirred tank reactor was studied theoretically. The unsteady-state-processing becomes advantageous under certain conditions. This can be shown for an irreversible consecutive-competing reaction. The yield and selectivitv of