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    微细腔内甲烷-湿空气重整特性试验与数值模拟

    Experimental and Numerical Study on Characteristics of Methane-Wet Air Reforming in a Micro-combustor

    • 摘要: 针对甲烷-湿空气在微细腔内的自热重整,建立了直径为2 mm的微细直管试验系统,采用试验研究和三维数值计算两种方法分析了微反应器内甲烷-湿空气自热重整转化特性,并重点分析了反应温度、原料气组分比例变化对重整反应中甲烷转化率和氢气产率的影响.结果表明:在相同的甲烷流量工况下,随着温度的升高以及空/碳比和水/碳比的增大,甲烷转化率和氢气产率均增大,其中空-碳比对甲烷转化率的影响比对氢气产率的影响大;进气质量流量较小的体系比较大的体系在重整产氢方面的效果好.试验和数值模拟得到的结果比较一致.

       

      Abstract: To study the auto-thermal reforming process of methane-wet air in a micro-combustor, a straight tube experimental system has been established with a tube diameter of 2 mm, based on which experimental tests and 3D numerical simulation are performed to analyze the conversion characteristics of the reforming, focusing on the influence of reaction temperature and feed gas ratio on the methane conversion rate and H2 yield. Study results show that at the same mass flow of methane, both the methane conversion rate and H2 yield increase with rising temperature, air-methane ratio and steam-methane ratio; the influence of air-methane ratio on methane conversion rate is greater than on H2 yield. The system with low mass flow of feed gas is more efficient than that with high mass flow in H2 yield during methane-wet air reforming. Test results agree well with that of the numerical simulation.

       

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