A multi-scale model of methane catalytic combustion was built by a series of balance equations and diffusion equations, and these equations were solved through the computational fluid dynamics (CFD) software. The difference between this work and previous model is the diffusion process in catalyst coating was considered. By analyzing the methane conversion, temperature distribution and mass fraction contours of every component, the performance of multi-scale model was compared with that of the pure CFD model without diffusion. The effects of diffusion, methane concentration, flow rate on the methane conversion and temperature distribution of monolithic reactor were also evaluated and discussed by the multi-scale model. The multi-scale model showed better accuracy than the pure CFD model without diffusion process. Different methane concentrations and gas flow rates had enormous effects on the methane conversion and temperature. Therefore, it was beneficial to the reaction process to adjust the methane concentration and gas flow rate appropriately.
机构:
Univ Paris 06, CNRS, Inst Jean Rond Alembert, UMR 7190, F-75252 Paris 05, FranceUniv Paris 06, CNRS, Inst Jean Rond Alembert, UMR 7190, F-75252 Paris 05, France
Ozhan, Cansu
Fuster, Daniel
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Univ Paris 06, CNRS, Inst Jean Rond Alembert, UMR 7190, F-75252 Paris 05, FranceUniv Paris 06, CNRS, Inst Jean Rond Alembert, UMR 7190, F-75252 Paris 05, France
Fuster, Daniel
Da Costa, Patrick
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Univ Paris 06, CNRS, Inst Jean Rond Alembert, UMR 7190, F-75252 Paris 05, FranceUniv Paris 06, CNRS, Inst Jean Rond Alembert, UMR 7190, F-75252 Paris 05, France
机构:
Jiangsu Normal Univ, Sch Math & Stat, Xuzhou 221000, Jiangsu, Peoples R China
Jiangsu Normal Univ, Res Inst Math Sci, Xuzhou 221000, Jiangsu, Peoples R ChinaJiangsu Normal Univ, Sch Math & Stat, Xuzhou 221000, Jiangsu, Peoples R China
Xie, Longjie
Yang, Li
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Shandong Univ, Sch Math, Jinan 250100, Shandong, Peoples R ChinaJiangsu Normal Univ, Sch Math & Stat, Xuzhou 221000, Jiangsu, Peoples R China