SCI和EI收录∣中国化工学会会刊

Chin.J.Chem.Eng. ›› 2015, Vol. 23 ›› Issue (8): 1316-1325.DOI: 10.1016/j.cjche.2015.05.006

• CATALYSIS, KINETICS AND REACTION ENGINEERING • Previous Articles     Next Articles

Effect of hydrogen combustion reaction on the dehydrogenation of ethane in a fixed-bed catalytic membrane reactor

Masoud Hasany, Mohammad Malakootikhah, Vahid Rahmanian, Soheila Yaghmaei   

  1. Department of Chemical and Petroleum Engineering, Sharif University of Technology, Tehran, Iran
  • Received:2014-10-15 Revised:2015-05-03 Online:2015-09-26 Published:2015-08-28
  • Contact: Masoud Hasany

Effect of hydrogen combustion reaction on the dehydrogenation of ethane in a fixed-bed catalytic membrane reactor

Masoud Hasany, Mohammad Malakootikhah, Vahid Rahmanian, Soheila Yaghmaei   

  1. Department of Chemical and Petroleum Engineering, Sharif University of Technology, Tehran, Iran
  • 通讯作者: Masoud Hasany

Abstract: A two-dimensional non-isothermal mathematical model has been developed for the ethane dehydrogenation reaction in a fixed-bed catalytic membrane reactor. Since ethane dehydrogenation is an equilibrium reaction, removal of produced hydrogen by the membrane shifts the thermodynamic equilibriumto ethylene production. For further displacement of the dehydrogenation reaction, oxidative dehydrogenation method has been used. Since ethane dehydrogenation is an endothermic reaction, the energy produced by the oxidative dehydrogenation method is consumed by the dehydrogenation reaction. The results show that the oxidative dehydrogenation method generated a substantial improvement in the reactor performance in terms of high conversions and significant energy saving. It was also established that the sweep gas velocity in the shell side of the reactor is one of the most important factors in the effectiveness of the reactor.

Key words: Catalytic membrane reactor, Mathematical modeling, Ethane dehydrogenation, Hydrogen combustion

摘要: A two-dimensional non-isothermal mathematical model has been developed for the ethane dehydrogenation reaction in a fixed-bed catalytic membrane reactor. Since ethane dehydrogenation is an equilibrium reaction, removal of produced hydrogen by the membrane shifts the thermodynamic equilibriumto ethylene production. For further displacement of the dehydrogenation reaction, oxidative dehydrogenation method has been used. Since ethane dehydrogenation is an endothermic reaction, the energy produced by the oxidative dehydrogenation method is consumed by the dehydrogenation reaction. The results show that the oxidative dehydrogenation method generated a substantial improvement in the reactor performance in terms of high conversions and significant energy saving. It was also established that the sweep gas velocity in the shell side of the reactor is one of the most important factors in the effectiveness of the reactor.

关键词: Catalytic membrane reactor, Mathematical modeling, Ethane dehydrogenation, Hydrogen combustion