SCI和EI收录∣中国化工学会会刊

中国化学工程学报 ›› 2024, Vol. 65 ›› Issue (1): 35-42.DOI: 10.1016/j.cjche.2023.07.003

• Full Length Article • 上一篇    下一篇

Filtration performance and modeling of granular bed for dust removal from coal pyrolytic vapors

Shuaiqiang Yang1,2, Lin Du1, Guangchao Ding1, Runguo Liu1, Wenli Song1,3, Songgeng Li1,3   

  1. 1 State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China;
    2 School of Petrochemical Engineering, Yan’an Vocational and Technical College, Yan’an 716000, China;
    3 Sino-Danish College, University of Chinese Academy of Sciences, Beijing 100049, China
  • 收稿日期:2023-02-24 修回日期:2023-07-18 出版日期:2024-01-28 发布日期:2024-04-17
  • 通讯作者: Songgeng Li,E-mail:sgli@ipe.ac.cn
  • 基金资助:
    The authors are grateful to the financial support from the National Key Research and Development Program of China (2018YFB0605003).

Filtration performance and modeling of granular bed for dust removal from coal pyrolytic vapors

Shuaiqiang Yang1,2, Lin Du1, Guangchao Ding1, Runguo Liu1, Wenli Song1,3, Songgeng Li1,3   

  1. 1 State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China;
    2 School of Petrochemical Engineering, Yan’an Vocational and Technical College, Yan’an 716000, China;
    3 Sino-Danish College, University of Chinese Academy of Sciences, Beijing 100049, China
  • Received:2023-02-24 Revised:2023-07-18 Online:2024-01-28 Published:2024-04-17
  • Contact: Songgeng Li,E-mail:sgli@ipe.ac.cn
  • Supported by:
    The authors are grateful to the financial support from the National Key Research and Development Program of China (2018YFB0605003).

摘要: Dust removal from pyrolytic vapors at high temperatures is an obstacle to the industrialization of the coal pyrolysis process. In this work, a granular bed with expanded perlites as filtration media was designed and integrated into a 10 t·d-1 coal pyrolysis facility. The testing results showed that around 97.56% dust collection efficiency was achieved. As a result, dust content in tar was significantly lowered. The pressure drop of the granular bed maintained in the range of 356 Pa to 489 Pa. The dust size in the effluent after filtration exhibited a bimodal distribution, which was attributed to the heterogeneity of the dust components. The effects of filtration bed on pyrolytic product yields were also discussed. A modified filtration model based on the macroscopic phenomenological theory was proposed to describe the performance of the granular bed. The computation results were well agreed with the experimental data.

关键词: Granular bed filtration, Dust removal, Pyrolysis, Filtration, Fixed-bed

Abstract: Dust removal from pyrolytic vapors at high temperatures is an obstacle to the industrialization of the coal pyrolysis process. In this work, a granular bed with expanded perlites as filtration media was designed and integrated into a 10 t·d-1 coal pyrolysis facility. The testing results showed that around 97.56% dust collection efficiency was achieved. As a result, dust content in tar was significantly lowered. The pressure drop of the granular bed maintained in the range of 356 Pa to 489 Pa. The dust size in the effluent after filtration exhibited a bimodal distribution, which was attributed to the heterogeneity of the dust components. The effects of filtration bed on pyrolytic product yields were also discussed. A modified filtration model based on the macroscopic phenomenological theory was proposed to describe the performance of the granular bed. The computation results were well agreed with the experimental data.

Key words: Granular bed filtration, Dust removal, Pyrolysis, Filtration, Fixed-bed