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Research on catalytic combustion of low concentration methane in combustion channel of compact reformer

机译:紧凑型重整器燃烧通道低浓度甲烷催化燃烧研究

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The combustion channel of compact methane reformer includes fuel flow duct, porous layer and solid connector. There are heat transport and multi-component species diffusion/convection processes in porous structure. The transfer processes are coupled with methane catalytic combustion, and affect the performance and stability of reformer. A 3D in-house code has been developed to simulate the mass and heat transfer processes involving chemical reactions in the reformer channel in specific condition (mass fraction of CH_4 Y_(CH_4) is less than 1% in the mixture of methane and air). It shows that, catalytic combustion reactions mainly tack place on the porous layer near inlet with a higher temperature area, the biggest heat flux region from the bottom wall is found near the higher temperature area. The reaction rate of methane, temperature of porous layer and heat flux increase with the increase of Y_(CH_4). In general, 0.4% is an adequate value for Y_(CH_4). The research has a benefit meaning to provide a guideline for the improvement and design for compact methane reformer.
机译:紧致甲烷重整器的燃烧通道包括燃料流管,多孔层和实心连接器。多孔结构中存在热传输和多组分物种扩散/对流过程。转移过程与甲烷催化燃烧偶联,并影响重整器的性能和稳定性。已经开发了一种3D内部代码来模拟涉及在特定条件下的重整器通道中的化学反应的质量和传热过程(CH_4 Y_(CH_4)的质量分数小于甲烷和空气的混合物中的1%)。结果表明,催化燃烧反应主要在较高温度面积的入口附近的多孔层上的粘土,从底壁的最大热通量区域在较高温度面积附近找到。甲烷的反应速率,多孔层温度和热通量随着Y_(CH_4)的增加而增加。通常,0.4%是Y_(CH_4)的足够值。该研究具有福利意义,为紧致甲烷重整器的改进和设计提供了指导。

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