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Effect of Swirl on Gasification Characteristics in an Entrained-flow Coal Gasifier

Authors
  • Li, Rongbin1
  • Xie, Mingzhuang1
  • Jin, Hui2
  • Guo, Liejin2
  • Liu, Fengqin1
  • 1 University of Science and Technology Beijing, 100083 , (China)
  • 2 Xi’an Jiaotong University, 710049 , (China)
Type
Published Article
Journal
International Journal of Chemical Reactor Engineering
Publisher
De Gruyter
Publication Date
Feb 28, 2020
Volume
18
Issue
3
Identifiers
DOI: 10.1515/ijcre-2019-0203
Source
De Gruyter
Keywords
License
Yellow

Abstract

The three-dimensional (3-D) comprehensive mathematical model was developed to simulate the coal gasification process in an entrained flow gasifier with a swirl burner. The models employed or developed includes the coal devolatilization model, the char combustion and gasification model, the gas homogeneous reaction model, the random-trajectory model, gas turbulence model, and the P-1 radiation model. The solution of models was executed based on the computational fluid dynamics (CFD). By qualitatively comparing the results at different swirl number, the significant influences of swirl on characteristics of coal gasification such as flow distributions, gas temperature and product composition including hydrogen (H2), carbon monoxide (CO), etc., and on the performance of coal gasification such as averaged exit product composition, carbon conversion rate and cold gas efficiency, were in detail discussed. Especially, a proper swirl number (S ≤ 0.65) in favor of gasification was found for the investigated gasifier in this paper.

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