首页> 外文期刊>Proceedings of the ASME Advanced Energy Systems Division >ANODE GAS AND STEAM RECYCLING FOR INTERNAL METHANE REFORMING SOFCs: ANALYSIS OF CARBON DEPOSITION
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ANODE GAS AND STEAM RECYCLING FOR INTERNAL METHANE REFORMING SOFCs: ANALYSIS OF CARBON DEPOSITION

机译:内部甲烷重整SOFC的阳极气体和蒸汽再循环:碳沉积分析

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The development of solid oxide fuel cell (SOFCs) systems capable of direct internal reforming (DIR) of methane and higher hydrocarbons is being actively pursued. However, a major challenge with current state-of-the-art nickel-based anodes is their propensity to form deteriorous carbon deposits in DIR, unless excess steam is introduced in the fuel. Reduced fuel humidification levels are desirable from the viewpoints of cell performance, reliability and plant economics. This study explores the use of anodic fuel and steam recycling schemes as possible mitigation strategies against carbon deposits at fuel steam-to-carbon (S:C) ratios less than unity. Using a detailed computational fluid dynamics (CFD) model which couples momentum, heat, mass and charge transport with electrochemical and chemical reactions, the operation of a an internal reforming SOFC and spatial extent of carbon deposition within the anode are analyzed based on a thermodynamic analysis accounting for both the cracking and Boudouard reactions, for several fuel humidification and recycling conditions. 50percent (mass percent) fuel recycling is shown to be an effective mitigation strategy against carbon deposition at inlet xH_(2)O/xCH_(4) ratios of 0.5 to 1, with only a minor portion of the cell inlet region affected by coking. For lower recycling ratios at the same fuel compositions, fuel recycling reduces the risk of coking, but does not eliminate it. For the SOFC configuration studied, at a S:C of 0.5, steam recycling is found to reduce the extent of carbon deposits by a magnitude comparable to that obtained using fuel recycling, providing that steam recycling ratios on order 25percent higher than the fuel recycling ratios are applied. Steam recycling may therefore be considered advantageous, in terms of reduced overall mass flow. For a S:C velence 0.5, the mitigating effect of steam recycling on the susceptibility to coking is through the directions of the cracking and Boudouard reactions, while fuel recycling has a positive impact on the cracking reaction only. The anodic gas recycling strategies considered could help extend the operational range of DIR-SOFCs to lower fuel humidification levels than typically considered, with reduced thermal stresses and risks of carbon deposits, while reducing system cost and complexity in terms of steam production.
机译:能够直接进行甲烷和高级碳氢化合物内部重整(DIR)的固体氧化物燃料电池(SOFC)系统的开发正在积极进行中。但是,当前最先进的镍基阳极面临的主要挑战是,除非在燃料中引入过量的蒸汽,否则它们易于在DIR中形成积碳。从电池性能,可靠性和工厂经济性的观点来看,降低燃料的加湿水平是理想的。这项研究探索了使用阳极燃料和蒸汽再循环方案作为在燃料蒸汽碳比(S:C)小于1的情况下针对碳沉积的可能缓解策略。使用详细的计算流体动力学(CFD)模型,将动量,热量,质量和电荷传输与电化学和化学反应耦合在一起,基于热力学分析来分析内部重整SOFC的操作以及阳极内碳沉积的空间范围包括裂化反应和Boudouard反应,以及几种燃料加湿和再循环条件。 50%(质量百分比)的燃料再循环被证明是一种有效的缓解策略,可防止入口xH_(2)O / xCH_(4)的比率为0.5到1时积碳,只有小部分电池入口区域受焦化影响。对于在相同燃料成分下较低的回收率,燃料回收减少了结焦的风险,但并没有消除。对于研究的SOFC配置,在S:C为0.5的情况下,发现蒸汽再循环可以将碳沉积的程度降低到与使用燃料再循环获得的程度相当的程度,前提是蒸汽再循环比率要比燃料再循环比率高25%被应用。因此,就减少总质量流量而言,蒸汽再循环可被认为是有利的。对于S:C velence 0.5,蒸汽循环对焦化敏感性的缓解作用是通过裂化和Boudouard反应的方向,而燃料循环仅对裂化反应有积极影响。所考虑的阳极气体再循环策略可以帮助扩大DIR-SOFC的运行范围,使其比通常所考虑的更低的燃料加湿水平,从而降低热应力和积碳风险,同时降低系统成本和蒸汽生产方面的复杂性。

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