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Integrated glycerol processor and proton exchange membrane fuel cell (PEMFC) systems for stationary applications

机译:集成甘油处理器和质子交换膜燃料电池(PEMFC)系统,用于固定应用

摘要

This work presents the performance and efficiency analysis of an integrated glycerol processing and proton exchange membrane fuel cell (PEMFC) system. Glycerol processing as one of the renewable fuel system is employed for hydrogen production. The hydrogen produced from glycerol processing is then fed to the PEMFC system to produce the desired electricity. Here, a PEMFC power generation system composed of two subsystems: fuel reforming and fuel cell stack. A fuel reforming is regarded as a suitable process to produce hydrogen for stationary application of fuel cells because of its high hydrogen yield which subsequently is used to generate electricity through the fuel cell stack by producing a desired power outcome. The system was simulated and optimized into 3 cases. The first one involves the high temperature proton exchange membrane fuel cell (HT-PEMFC) and a glycerol reformer without water gas shift reactor whereas in the second case, a water gas shift reactor is included to improve its overall system efficiency. The third case involves low temperature proton exchange membrane fuel cell (LT-PEMFC) with a glycerol reformer, water gas shift reactor and preferential oxidation reactor. In this study, a direct comparison between the performance of HT-PEMFC and LT-PEMFC systems integrated with a glycerol steam reformer with and without a water gas shift reactor is shown. The target power output of both the HT-PEMFC and LT-PEMFC systems for stationary application is in the range of 1-8 kW, which is sufficient for small household application. Based on result, HT-PEMFC system with water gas shift reactor shows the highest composition of hydrogen that give amount of 80.79% which operates at 1063.15 K and 3 atm with carbon to steam ratio of 2. Compared with HT-PEMFC without water gas shift reactor and LT-PEMFC, both gave 44.76% and 66.26% of hydrogen composition respectively. In term of the system efficiency, it is found that the highest system efficiency is also obtained from HT-PEMFC system with water gas shift reactor followed by LT-PEMFC system and HT-PEMFC system without water gas shift reactor. The highest system efficiency obtained is 59.89% efficiency due to its high energy required to generate for the system.
机译:这项工作介绍了集成的甘油处理和质子交换膜燃料电池(PEMFC)系统的性能和效率分析。作为可再生燃料系统之一的甘油加工被用于制氢。然后将甘油加工产生的氢气供入PEMFC系统中,以产生所需的电。在这里,PEMFC发电系统由两个子系统组成:燃料重整和燃料电池堆。燃料重整被认为是生产用于燃料电池固定应用的氢的合适方法,因为其高的氢产率随后被用于通过产生期望的功率结果通过燃料电池堆发电。对系统进行了仿真,并将其优化为3种情况。第一个涉及高温质子交换膜燃料电池(HT-PEMFC)和不带水煤气变换反应器的甘油重整器,而在第二种情况下,包括水煤气变换反应器以提高其整体系统效率。第三种情况涉及带有甘油重整器,水煤气变换反应器和优先氧化反应器的低温质子交换膜燃料电池(LT-PEMFC)。在这项研究中,显示了带有和不带有水煤气变换反应器的,带有甘油蒸汽重整器的HT-PEMFC和LT-PEMFC系统的性能之间的直接比较。固定应用的HT-PEMFC和LT-PEMFC系统的目标输出功率在1-8 kW的范围内,足以满足小型家庭应用的需求。根据结果​​,带水煤气变换反应器的HT-PEMFC系统显示出最高的氢组成,氢的含量为80.79%,在1063.15 K和3个大气压下运行,碳汽比为2。反应器和LT-PEMFC的氢组成分别为44.76%和66.26%。在系统效率方面,发现具有水煤气变换反应器的HT-PEMFC系统,其次是具有水煤气变换反应器的LT-PEMFC系统和HT-PEMFC系统也获得了最高的系统效率。由于产生系统所需的高能量,因此获得的最高系统效率为59.89%。

著录项

  • 作者

    Noor Afiqah Sharifmuddin;

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  • 年度 2015
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