Polymerization of olefins through heterogeneous catalysis. XVIII. A kinetic explanation for unusual effects
β Scribed by W. K. Alex Shaffer; W. Harmon Ray
- Publisher
- John Wiley and Sons
- Year
- 1997
- Tongue
- English
- Weight
- 417 KB
- Volume
- 65
- Category
- Article
- ISSN
- 0021-8995
No coin nor oath required. For personal study only.
β¦ Synopsis
The development of a detailed kinetic model describing some of the unusual effects observed in catalyzed olefin polymerization is presented. Based on the method of moments, the model describes the rate effects of hydrogen and comonomers, as well as the ability of certain systems to incorporate long chain branches via internal and/ or terminal double bond polymerization. Examples are provided demonstrating the model's ability to predict rates and degrees of polymerization with ethylene, propylene, and 1-hexene monomers. In the case of propylene, multiple insertion mechanisms are modeled and compared with experimental sequence length and end group data. In other examples the model is used to simulate an oscillating metallocene catalyst and a metallocene catalyst capable of branch addition via terminal double bond polymerization.
π SIMILAR VOLUMES
A novel lab-scale stirred bed gas phase reactor system has been designed and constructed for investigating the kinetic behaviour of olefin copolymerization reactions using heterogeneous catalysts. The system, equipped for basic temperature and pressure control, also includes an on-line composition c
Equation (8) on page 5454 read: ( 8 ) (8) kla = 9.85 x 10-4~0.6N1.2g-0.053ul-0.45Q0.76~~0.72( F 1 ~, ) -0.6 I It should read: kIa = 9-85 x 1 0 -4 D 0 . 6 ~l . 2 g -0 . ~ -0.45~0.360;;0.72( F p ) -o.6 I 01 1 2
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