SCI和EI收录∣中国化工学会会刊

Chinese Journal of Chemical Engineering ›› 2013, Vol. 21 ›› Issue (8): 906-913.DOI: 10.1016/S1004-9541(13)60551-0

• 化工热力学 • 上一篇    下一篇

Estimation on Global Reaction Heat for the Aromatization Process of Liquefied Petroleum Gas

黎小辉1, 朱建华1, 郝代军2   

  1. 1 College of Chemical Engineering, China University of Petroleum (Beijing), Beijing 102249, China;
    2 Luoyang Petrochemical Engineering Corporation, SINOPEC, Luoyang 471003, China
  • 收稿日期:2012-02-12 修回日期:2012-08-11 出版日期:2013-08-28 发布日期:2013-08-24
  • 通讯作者: ZHU Jianhua

Estimation on Global Reaction Heat for the Aromatization Process of Liquefied Petroleum Gas

LI Xiaohui1, ZHU Jianhua1, HAO Daijun2   

  1. 1 College of Chemical Engineering, China University of Petroleum (Beijing), Beijing 102249, China;
    2 Luoyang Petrochemical Engineering Corporation, SINOPEC, Luoyang 471003, China
  • Received:2012-02-12 Revised:2012-08-11 Online:2013-08-28 Published:2013-08-24

摘要: The reaction heat effect analysis for the aromatization process of Liquefied Petroleum Gas (LPG) was completed in this paper. In order to characterize this complex reaction system, one set of independent reactions was determined by means of atomic coefficient matrix method. Based on reaction thermodynamic and stoichiometric knowledge, the heat effect, Gibbs free energy change and equilibrium constant for each independent reaction was calculated for the specified conditions. Under these conditions, based on the initial and final composition data from LPG aromatization experiments, the actual extent of reaction for each independent reaction was determined. Furthermore, the global reaction heat and adiabatic temperature rise of LPG aromatization reaction system could be estimated. This work would provide a theoretical guidance for the design and scale-up of reactor for LPG aromatization process, as well as for the selection of proper operating conditions.

关键词: global reaction heat, aromatization process, liquefied petroleum gas

Abstract: The reaction heat effect analysis for the aromatization process of Liquefied Petroleum Gas (LPG) was completed in this paper. In order to characterize this complex reaction system, one set of independent reactions was determined by means of atomic coefficient matrix method. Based on reaction thermodynamic and stoichiometric knowledge, the heat effect, Gibbs free energy change and equilibrium constant for each independent reaction was calculated for the specified conditions. Under these conditions, based on the initial and final composition data from LPG aromatization experiments, the actual extent of reaction for each independent reaction was determined. Furthermore, the global reaction heat and adiabatic temperature rise of LPG aromatization reaction system could be estimated. This work would provide a theoretical guidance for the design and scale-up of reactor for LPG aromatization process, as well as for the selection of proper operating conditions.

Key words: global reaction heat, aromatization process, liquefied petroleum gas