作者: Masoud Hasany , Mohammad Malakootikhah , Vahid Rahmanian , Soheila Yaghmaei
DOI: 10.1016/J.CJCHE.2015.05.006
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摘要: Abstract A two-dimensional non-isothermal mathematical model has been developed for the ethane dehydrogenation reaction in a fixed-bed catalytic membrane reactor. Since is an equilibrium reaction, removal of produced hydrogen by shifts thermodynamic to ethylene production. For further displacement oxidative method used. endothermic energy consumed reaction. The results show that generated substantial improvement reactor performance terms high conversions and significant saving. It was also established sweep gas velocity shell side one most important factors effectiveness