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The Catalyst Loading Effects on the Feed Rate of NaBH 4 Solution for the Hydrogen Production Rate and Conversion Efficiency

机译:催化剂负荷对纳米4溶液的进料速率进行氢气生产率和转化效率

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The research in this study focused on the operating parameters for a high efficiency hydrogen production rate system, with the aim to design a hydrolysis of the NaBH 4 hydrogen production module for lightweight and efficient hydrogen production and conversion. The experiment used a reactor, where the reaction volume was about 12 mL. The parameters on the feed rate of the NaBH 4 solution and the catalyst loading for the hydrogen production rate and conversion efficiency were investigated. The catalyst is sufficient to allow the release of hydrogen in the 1 g/min solution, but the efficiency of hydrogen production at high flow rates has been shown to be low in previous studies. Therefore, the aim is to increase the catalyst to improve the reaction efficiency in this study. The results show that at the high temperature reaction condition, solid NaBO 2 will not generate on the catalyst surface to influence the hydrogen production rate when using the five pcs catalyst. When the reaction temperature was 108 °C, the average hydrogen production rate was 1.72 L/min, and the conversion efficiency was 91.2%.
机译:该研究的研究重点是高效氢生产率系统的操作参数,目的是设计纳米4氢生产模块的水解,用于轻质和高效的氢气产生和转化。实验使用反应器,反应体积为约12mL。研究了NaBH 4溶液进料速率的参数和氢气产生率和转化效率的催化剂负载。催化剂足以允许在1g / min溶液中释放氢,但在先前的研究中,高流速下的氢气产生的效率已经很低。因此,目的是增加催化剂以提高该研究的反应效率。结果表明,在高温反应条件下,固体NaBO 2在使用五种PCS催化剂时不会产生催化剂表面以影响氢气产生速率。当反应温度为108℃时,平均氢气产生速率为1.72升/分钟,转化效率为91.2%。

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