SCI和EI收录∣中国化工学会会刊

Chinese Journal of Chemical Engineering ›› 2022, Vol. 51 ›› Issue (11): 43-52.DOI: 10.1016/j.cjche.2021.12.015

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Numerical simulation and experimental study of gas cyclone–liquid jet separator for fine particle separation

Liwang Wang1, Erwen Chen1, Liang Ma1,2, Zhanghuang Yang1, Zongzhe Li1, Weihui Yang1, Hualin Wang1, Yulong Chang2   

  1. 1. School of Mechanical and Power Engineering, East China University of Science and Technology, Shanghai 200237, China;
    2. College of Architecture and Environment, Sichuan University, Chengdu 610065, China
  • Received:2021-06-28 Revised:2021-12-13 Online:2023-01-18 Published:2022-11-18
  • Contact: Liang Ma,E-mail:maliang@ecust.edu.cn
  • Supported by:
    This research was supported by the National Natural Science Foundation of China (21878099), and the Science and Technology Commission of Shanghai Municipality (19DZ1208000).

Numerical simulation and experimental study of gas cyclone–liquid jet separator for fine particle separation

Liwang Wang1, Erwen Chen1, Liang Ma1,2, Zhanghuang Yang1, Zongzhe Li1, Weihui Yang1, Hualin Wang1, Yulong Chang2   

  1. 1. School of Mechanical and Power Engineering, East China University of Science and Technology, Shanghai 200237, China;
    2. College of Architecture and Environment, Sichuan University, Chengdu 610065, China
  • 通讯作者: Liang Ma,E-mail:maliang@ecust.edu.cn
  • 基金资助:
    This research was supported by the National Natural Science Foundation of China (21878099), and the Science and Technology Commission of Shanghai Municipality (19DZ1208000).

Abstract: To address the shortcomings of existing particulate matter trapping technology, especially the low separation efficiency of fine particles, herein, a novel gas cyclone–liquid jet separator was developed to research fine particle trapping. First, numerical simulation methods were used to investigate the flow field characteristics and dust removal efficiency of the separator under different working conditions, and to determined suitable experimental conditions for subsequent dust removal experiments. Afterward, the separation efficiency of the separator against five kinds of common particles, including g-C3N4, TiO2, SiC, talc, and SiO2, was experimentally studied. A maximum separation efficiency of 99.48% was achieved for particles larger than 13.1 μm, and 96.55% efficiency was achieved for particles larger than 2 μm. The best crushing atomization effect was achieved for the separator when uG was 10 m·s-1 and uL was 3 m·s-1, while the best separation effect was achieved when uG was 10 m·s-1 and uL was 3.75 m·s-1. Studies have shown that the gas cyclone–liquid jet separator has excellent applicability in the separation of fine particles.

Key words: Gas cyclone–liquid jet, Dust removal, Fine particles, Numerical simulation

摘要: To address the shortcomings of existing particulate matter trapping technology, especially the low separation efficiency of fine particles, herein, a novel gas cyclone–liquid jet separator was developed to research fine particle trapping. First, numerical simulation methods were used to investigate the flow field characteristics and dust removal efficiency of the separator under different working conditions, and to determined suitable experimental conditions for subsequent dust removal experiments. Afterward, the separation efficiency of the separator against five kinds of common particles, including g-C3N4, TiO2, SiC, talc, and SiO2, was experimentally studied. A maximum separation efficiency of 99.48% was achieved for particles larger than 13.1 μm, and 96.55% efficiency was achieved for particles larger than 2 μm. The best crushing atomization effect was achieved for the separator when uG was 10 m·s-1 and uL was 3 m·s-1, while the best separation effect was achieved when uG was 10 m·s-1 and uL was 3.75 m·s-1. Studies have shown that the gas cyclone–liquid jet separator has excellent applicability in the separation of fine particles.

关键词: Gas cyclone–liquid jet, Dust removal, Fine particles, Numerical simulation