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首页> 外文期刊>Energy Conversion & Management >Syngas/power cogeneration from proton conducting solid oxide fuel cells assisted by dry methane reforming: A thermal-electrochemical modelling study
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Syngas/power cogeneration from proton conducting solid oxide fuel cells assisted by dry methane reforming: A thermal-electrochemical modelling study

机译:质子传导固体氧化物燃料电池在干甲烷重整辅助下的合成气/热电联产:热电化学模型研究

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摘要

A tubular proton conducting solid oxide fuel cell (H-SOFC) integrated with internal dry methane reforming (DMR) layer is numerically studied for power and syngas cogeneration using CO2 and CH4 as fuel by the Finite Element Method. The coupled heat and mass transporting with electrochemical reactions and chemical reactions (DMR, water gas shifting reaction and methane steam reforming) are fully considered. The model is substantially validated with experimental data of DMR catalyst characterization and SOFC button cell electrochemical characterization. The base case analyses are conducted at open circuit voltage (OCV) and 0.7 V of the DMR-SOFC. It is found that the CO2 conversion and CH4 conversion can be increased by 4.8% and 21.6%, respectively, by increasing the operating voltage of DMR-SOFC from OCV to 0.7 V, with the coproduction of electricity (1.5 W). These conversion enhancements were caused by the in-situ integration of the endothermal DMR reaction and exothermal H-2 electrochemical oxidation. Effects of operating voltage and inlet flow rate of feeding gas are evaluated. The voltage is suggested to be higher than 0.5 V to avoid large temperature gradient in the reactor. It is also found that conversion ratios of both CH4 and CO2 decrease from over 90% to be below 60% as the fuel flow rate is increased from 40 cm(3) min(-1) to 80 cm(3) min(-1).
机译:通过有限元方法,利用CO2和CH4作为燃料,对集成有内部干甲烷重整(DMR)层的管状质子传导固体氧化物燃料电池(H-SOFC)进行了动力和合成气热电联产的数值研究。充分考虑了热和质量的传输与电化学反应和化学反应(DMR,水煤气变换反应和甲烷蒸汽重整)的耦合。该模型已通过DMR催化剂表征和SOFC纽扣电池电化学表征的实验数据进行了充分验证。基本案例分析是在DMR-SOFC的开路电压(OCV)和0.7 V下进行的。发现通过将DMR-SOFC的工作电压从OCV提高到0.7 V,同时产生电能(1.5 W),可以分别将CO2转化率和CH4转化率提高4.8%和21.6%。这些转化率的提高是由吸热DMR反应和放热H-2电化学氧化的原位整合引起的。评估工作电压和进料气入口流量的影响。建议该电压高于0.5 V,以避免反应器中较大的温度梯度。还发现,随着燃料流量从40 cm(3)min(-1)增加到80 cm(3)min(-1),CH4和CO2的转化率从90%以上降低到60%以下)。

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