This study focuses on the kinetics of ethylene/propylene (homo/co)polymerization reactions using a high activity TiCl 4 /MgCl 2 /AlEt 3 catalyst. The reactor system is a gas phase reactor equipped with an on-line composition control scheme. As such, important kinetic data such as the instantaneous r
Kinetic study of gas phase olefin polymerization with a TiCl4/MgCl2 catalyst. II. Kinetic parameter estimation and model building
โ Scribed by M. Hamba; G. C. Han-Adebekun; W. H. Ray
- Publisher
- John Wiley and Sons
- Year
- 1997
- Tongue
- English
- Weight
- 455 KB
- Volume
- 35
- Category
- Article
- ISSN
- 0887-624X
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โฆ Synopsis
Monomer transport and polymerization kinetics are two key phenomena in olefin polymerization with heterogeneous transition metal catalysts. To have a better understanding of these interrelated kinetics and diffusion phenomena, a quantitative calculation of the monomer diffusion directly from experimental study is essential. In this work, a novel temperature-perturbation technique is developed to systematically study the kinetic and diffusion limitations in catalyzed gas phase olefin polymerization. A physical model of the particle growth mechanism as well as its mathematical representation is presented and the diffusion limitations occurring in the system at high temperature are characterized and quantitatively analyzed. Finally, the practical implications of the results of this study on the operation of industrial scale polyolefin reactors are examined.
๐ SIMILAR VOLUMES
Using a high-activity MgCl 2 -supported TiCl 4 catalyst, kinetic studies of ethylene and propylene polymerization are conducted in a semi-batch gas phase stirredbed reactor system. Based on the experimental observations obtained from this study and others in the literature, simple kinetic mechanisms