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Effect of Polymer Growth Rate and Diffusion Resistance on the Behavior of Industrial Polyethylene Fluidized Bed Reactor

โœ Scribed by N. M. Ghasem


Publisher
John Wiley and Sons
Year
2001
Tongue
English
Weight
290 KB
Volume
24
Category
Article
ISSN
0930-7516

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Static and dynamic bifurcation behaviors dominate the operation of fluidized bed catalytic reactors for the production of polyethylene (UNIPOL Process) and have important implications on the safe operating temperature and polyethylene production rate. The investigations show that the multiplicity of