SCI和EI收录∣中国化工学会会刊

Chinese Journal of Chemical Engineering ›› 2022, Vol. 47 ›› Issue (7): 71-78.DOI: 10.1016/j.cjche.2021.07.012

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Enhancement of acetylene and ethylene yields in partially decoupled oxidation of ethane by changing the composition of heat carrier

Tianpeng LiZhou, Jiajia Luo, Tiefeng Wang   

  1. Beijing Key Laboratory of Green Reaction Engineering and Technology, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
  • Received:2021-04-17 Revised:2021-06-14 Online:2022-08-19 Published:2022-07-28
  • Contact: Tiefeng Wang,E-mail:wangtf@tsinghua.edu.cn
  • Supported by:
    This work was supported by the National Natural Science Foundation of China (21276135), and by Project of Chinese Ministry of Education (113004A).

Enhancement of acetylene and ethylene yields in partially decoupled oxidation of ethane by changing the composition of heat carrier

Tianpeng LiZhou, Jiajia Luo, Tiefeng Wang   

  1. Beijing Key Laboratory of Green Reaction Engineering and Technology, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
  • 通讯作者: Tiefeng Wang,E-mail:wangtf@tsinghua.edu.cn
  • 基金资助:
    This work was supported by the National Natural Science Foundation of China (21276135), and by Project of Chinese Ministry of Education (113004A).

Abstract: In our previous work, a partially decoupled process (PDP) was proposed for efficient conversion of ethane to increase the ethylene yield and a new structural reactor called forward-impinging-back reactor (FIB) was proposed for scale-up. In this work, the influence of changing the composition and temperature of the heat carrier was investigated by simulations with detailed chemistry to further increase of the C2 (C2H2 + C2H4) yield in the PDP of ethane. At ideal mixing conditions, the C2 yield is 75.3% without steam addition and it is 82.9% at steam addition ratio of β=1.4. In comparison, the C2 yield in an FIB reactor is 62.4% without steam addition and it increases to 78.5% with steam addition (β=1.4). The requirement of high mixing efficiency is diminished by steam addition, which is favorable for reactor scale-up.

Key words: Partially decoupled process (PDP), Ethane, Computational fluid dynamics (CFD), Steam addition

摘要: In our previous work, a partially decoupled process (PDP) was proposed for efficient conversion of ethane to increase the ethylene yield and a new structural reactor called forward-impinging-back reactor (FIB) was proposed for scale-up. In this work, the influence of changing the composition and temperature of the heat carrier was investigated by simulations with detailed chemistry to further increase of the C2 (C2H2 + C2H4) yield in the PDP of ethane. At ideal mixing conditions, the C2 yield is 75.3% without steam addition and it is 82.9% at steam addition ratio of β=1.4. In comparison, the C2 yield in an FIB reactor is 62.4% without steam addition and it increases to 78.5% with steam addition (β=1.4). The requirement of high mixing efficiency is diminished by steam addition, which is favorable for reactor scale-up.

关键词: Partially decoupled process (PDP), Ethane, Computational fluid dynamics (CFD), Steam addition