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Numerical Modeling on Catalytic Tri-reforming Reaction of Methane for Syngas Production

descriptionPublicationkeyboard_double_arrow_right Article , Journal 01 May 2017Publisher:Elsevier BVJournal:Energy Procedia, volume 105, pages 4,198-4,203 (issn: 1876-6102,

Authors: Reiyu Chein; K.T. Wu; C.T. Yu;

doi: 10.1016/j.egypro.2017.03.895

Numerical Modeling on Catalytic Tri-reforming Reaction of Methane for Syngas Production

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Abstract

Abstract In this study, a two-dimensional numerical model was built to study the tri-reforming of methane (TRM) in a tubular fixed-bed reactor under various operation pressures, inlet temperatures, and reactant compositions. It was found that TRM cannot be activated if the reactant inlet temperature were too low. With lower O2/CH4, higher H2O/CH4 and lower CO2/CH4 ratios in the reactant composition, higher H2/CO ratio can be obtained. It was also found that water-gas shift (WGS) reaction played an important role for controlling the resulted H2/CO ratio in syngas.

Related Organizations

National Chung Hsing University
Taiwan
National Chung Hsing University
Taiwan
Institute of Nuclear Energy Research
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