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A Performance Evaluation of a Microchannel Reactor for the Production of Hydrogen from Formic Acid for Electrochemical Energy Applications

机译:微通道反应器从甲酸生产氢气用于电化学能源的性能评估

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An experimental evaluation of a microchannel reactor was completed to assess the reactor performance for the catalytic decomposition of vaporised formic acid (FA) for H2 production. Initially, X-ray powder diffraction (XRD), elemental mapping using SEM-EDS and BET surface area measurements were done to characterise the commercial Au/Al2O3 catalyst. The reactor was evaluated using pure (99.99%) and diluted (50/50 vol.%) FA at reactor temperatures of 250–350°C and inlet vapour flow rates of 12–48 mL.min-1. Satisfactory reactor performance was demonstrated at 350°C as near- equilibrium FA conversion (>98%) was obtained for all flow rates investigated. The best operating -1 point was identified as 350°C and 48 mL.min (pure FA feed) with a H2 yield of 68.7%. At these conditions the reactor performed well in comparison to conventional systems, achieving a H2 -1 -1 production rate of 11.8 NL.gcat .h . This paper therefore highlights important considerations for ongoing design and development of microchannel reactors for the decomposition of FA for H2 production.
机译:完成了对微通道反应器的实验评估,以评估用于气化甲酸(FA)催化分解以生产H2的反应器性能。最初,进行了X射线粉末衍射(XRD),使用SEM-EDS进行元素标测和BET表面积测量,以表征商用Au / Al2O3催化剂。在250–350°C的反应器温度和12–48 mL.min-1的入口蒸汽流速下,使用纯(99.99%)和稀释(50/50 vol。%)FA评估反应堆。由于在所有研究流量下均获得了接近平衡的FA转化率(> 98%),因​​此在350°C时,反应器性能令人满意。最佳工作-1点为350°C和48 mL.min(纯FA进料),氢气产率为68.7%。在这些条件下,该反应器与常规系统相比运行良好,实现了H2 -1 -1的生产率为11.8 NL.gcat .h。因此,本文重点介绍了正在进行的设计和开发用于分解用于生产H2的FA的微通道反应器的重要考虑因素。

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