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 experim
Kinetic study of gas phase olefin polymerization with a TiCl4/MgCl2 catalyst I. Effect of polymerization conditions
โ Scribed by G. C. Han-Adebekun; M. Hamba; W. H. Ray
- Publisher
- John Wiley and Sons
- Year
- 1997
- Tongue
- English
- Weight
- 281 KB
- Volume
- 35
- Category
- Article
- ISSN
- 0887-624X
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โฆ Synopsis
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 reaction rate of each monomer is readily obtained. In the investigation, experiments are performed to study the effects of comonomer composition variations, temperature variations, hydrogen concentration variations, and variations in the Al/Ti ratio. It is observed that the ethylene and propylene instantaneous reaction rates show a rather peculiar pattern with the appearance of a second peak. Our work linked the existence of this peak to the Al/Ti ratio used. A theory based on the oxidation state change is proposed. This theory is also used to explain the effects of temperature changes and hydrogen concentration changes on the system. A variety of analytical techniques are employed to study the polymer properties and evidence is provided to support the existence of polymer partial melting at relatively high reaction temperatures. The resulting diffusion limitation is believed to be partially responsible for the observed activity decrease at such elevated temperatures.
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