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In relation to this article, we declare that there is no conflict of interest.
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Received June 29, 2001
Accepted September 24, 2001
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Characteristics of Slug Flow in a Fluidized Bed of Polyethylene Particles

Department of Chemical Engineering, Sungkyunkwan University, Suwon 440-746, Korea 1Hanwha Petrochemical Co., Daejeon 305-345, Korea
Korean Journal of Chemical Engineering, January 2002, 19(1), 183-189(7), 10.1007/BF02706893
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Abstract

The slug flow behavior of polyethylene particles was examined in a fluidized bed of 7 cm ID and 50 cm in height. The employed polymer particles were high density polyethylene (HDPE) with the average particle size of 603 mm. The slugging flow of polyethylene particles was analyzed from the measured pressure drop signals by classical statistical methods such as absolute average deviation, probability density function, power spectrum, auto-correlation, and cross-correlation. The results show that in spite of high dielectric constant of polymer particles, the slugging_x000D_ phenomena such as incipient slugging velocity, slugging frequency and slugging rise velocity were very similar to the Geldart B type non-polymeric particles. It was observed that slug frequencies decreased with gas velocity and the limiting slug frequency was observed for the gas velocities in this study.

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