The modeling of the semibatch emulsion polymerization of styrene and its validation against data obtained from a reactor facility is presented. The model, which describes the growth of a monodisperse polystyrene seed as neat monomer is fed to the reactor, incorporates recent findings in radical diff
On-line calorimetric control of emulsion polymerization reactors
✍ Scribed by I. Saenz De Buruaga; M. Arotçarena; P.D. Armitage; L.M. Gugliotta; J.R. Leiza; J.M. Asua
- Publisher
- Elsevier Science
- Year
- 1996
- Tongue
- English
- Weight
- 407 KB
- Volume
- 51
- Category
- Article
- ISSN
- 0009-2509
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✦ Synopsis
Reaction calorimetery was used to monitor and control unseeded semi-batch emulsion copolymerization of VAc and BuA. An external PC, using the information derived from a commercial reaction calorimeter, calculated on-line the thermal and material balances of the calorimetric reactor, and thus the monomer conversions. For a desired copolymer composition profile, previously calculated conversion-dependent monomer feed profiles were used to determine the rates of monomer addition every 20 seconds. Gas chromatography and gravimetry confirmed that copolymers having the desired variable composition profiles were successfully obtained. The control strategy devised lends itself to polymer quality control and safe operation, since variable monomer inhibitor levels or sudden inhibition during the reaction do not lead either to the formation of off-composition polymer nor to monomer accumulation in the reactor. Furthermore, the rate of polymerization can be reduced by fixing upper limits for monomer concentrations in the polymer particles, useful in cases where the minimum-time optimal feed profile, which corresponds to maximum swelling, might lead to thermal runaway.
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