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Development of a novel compact reformer for PEMFC.

机译:新型用于PEMFC的紧凑型重整器的开发。

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A compact reformer to produce hydrogen for portable fuel cell applications is presented in this thesis. This reformer is a conventional single-path tubular reactor type that is packed with granular catalyst particles. The catalyst is used to induce catalytic partial oxidation reaction (CPOX) and steam reforming reaction (SR) in series using a mixture of methanol, water and oxygen as the feed. One of the important features of the reformer is the interlaced flow path for efficient heat transfer between the reactor sections where the endothermic SR reaction and the exothermic CPOX reaction may be taking place, respectively. Flow simulation has been conducted to determine various design features including the dimension of the reformer that can be used for a PEMFC with the energy production capacity of 10 Watt at 50% efficiency. Subsequently, a prototype reformer has been built to confirm the simulation results and to assess the efficacies of new design features.;Experiment with a commercial catalyst (CuO/ZnO/Al2O3 ) showed a methanol conversion of about 85% at the feed rate enough to generate energy production capacity of 10 Watt at 50% efficiency with an operating temperature of 250°C or below, and a hydrogen concentration of approximately 72--73% in the product gas when SR is the only hydrogen generation reaction. When oxygen is fed to the reformer as an additional reactant, CPOX reaction also takes place and the hydrogen concentration decreases slightly as a result. The current study showed a hydrogen concentration of approximately 67%--72% at 250ºC at various oxygen feed rates. These hydrogen concentrations in the product gas are in reasonable agreement with theoretical predictions and indicate that the CPOX reaction does indeed take place before the SR reaction. The experiments indicated that only 5 of the maximum 19 reformer channels filled with catalyst are not sufficient to complete both the CPOX and SR reactions under the conditions used in this study.;The experimental results support that the prototype reformer is capable of meeting the preset requirements to produce enough hydrogen for 10W PEMFC application. The results also suggest that proper insulation of the reformer is essential for self-sustainability.
机译:本文提出了一种紧凑的重整炉,可生产用于便携式燃料电池的氢气。该重整装置是填充有颗粒状催化剂颗粒的常规单程管式反应器类型。使用甲醇,水和氧气的混合物作为进料,使用该催化剂连续引发催化部分氧化反应(CPOX)和蒸汽重整反应(SR)。重整器的重要特征之一是在反应器段之间进行有效传热的交错流动路径,在反应器段之间可能分别发生吸热SR反应和放热CPOX反应。已经进行了流动模拟以确定各种设计特征,包括可用于PEMFC的重整炉的尺寸,其能量生产能力为10瓦,效率为50%。随后,建立了原型重整器,以确认模拟结果并评估新设计特征的效率。用商用催化剂(CuO / ZnO / Al2O3)进行的实验显示,进料速率足以达到约80%的甲醇转化率当SR是唯一的氢生成反应时,在250°C或更低的工作温度下以50%的效率产生10瓦的能量生产能力,并且在产物气体中氢浓度约为72--73%。当将氧气作为另外的反应物供入重整器时,也会发生CPOX反应,结果氢浓度会略有下降。当前的研究表明,在250ºC下,各种氧气进料速率下的氢气浓度约为67%-72%。产物气中的这些氢浓度与理论预测合理地吻合,并且表明CPOX反应确实在SR反应之前发生。实验表明,在本研究使用的条件下,最多19个重整器通道中只有5个通道不足以完成CPOX和SR反应。;实验结果支持原型重整器能够满足预设要求产生足够的氢气用于10W PEMFC应用。结果还表明,重整器的适当绝缘对于自我维持至关重要。

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