Butadiene polymerization in the gas phase is modeled by a polymeric multilayer model. Intraparticle mass and heat transfer effects are studied. The effects of catalyst size and diffusivity of butadiene on the radial profile of monomer concentration in polymeric particles and on the rate of particle
Modeling of particle growth and morphology in the gas phase polymerization of butadiene. II. Simulation and discussion
โ Scribed by Junzi Zhao; Jianzhong Sun; Qiyun Zhou; Zuren Pan
- Publisher
- John Wiley and Sons
- Year
- 2001
- Tongue
- English
- Weight
- 358 KB
- Volume
- 81
- Category
- Article
- ISSN
- 0021-8995
- DOI
- 10.1002/app.1490
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โฆ Synopsis
Abstract
The improved multigrain model was used to simulate the gas phase polymerization of butadiene catalyzed by lowโ, mediumโ, and highโactivity catalysts, respectively. For the lowโactivity catalyst, the mass and heat transfer resistances in the particle were negligible. The morphology of the polymeric particles was uniform. For the mediumโactivity catalyst, the overall mass transfer effectiveness was > 90%, the maximal temperature rise was 8K, and the heat transfer resistance in the particle was negligible. Mass transfer resistance does not affect the morphology of product particle significantly. For the highโactivity catalyst, the overall mass transfer effectiveness was within the range of 70โ96%, the morphology of the product particle was affected by the mass transfer resistance to some extent. The maximal temperature rise was 21K; the heat transfer resistance in the particle was negligible as well. However, there was some severe mass transfer resistance in the particle, and the maximal temperature rise was โค 30K for the large catalyst particle with the same activity. Thus, the polymeric particle morphology was comparatively poor, with the occurrence of particle softening and sticking. ยฉ 2001 John Wiley & Sons, Inc. J Appl Polym Sci 81: 730โ741, 2001
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