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On the mass transport in membraneless flow batteries with flow-by configuration

机译:具有流通结构的无膜液流电池的批量运输

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Progress on the analysis of the mass transport phenomena in a membraneless redox flow battery with porous electrodes in flow-by configuration is here reported. A species transport model for a typical redox reactant interacting with a porous electrode is proposed. A hybrid numerical-analytical solution is obtained through the Generalized Integral Transform Technique (GITT), adopting a single domain formulation that includes both the porous and pure fluid regions. The influence of the Reynolds number and the thickness of the electrode on the parameters of interest is theoretically examined. The importance of considering the simultaneous development of flow and mass transport is analyzed, and the presence of the transversal convective flux of species proves to have a significant role on the generation of current inside the electrode. A scaling of the limiting current density with ∼Re0.41is demonstrated and some physical conclusions are drawn. Guidelines for the prevention of crossover are also offered, with increasing Reynolds number and decreasing relative thickness of the electrode having a positive effect, as far as avoiding the mixed potentials effects is concerned. The physical insights attained through the present analysis should add to the efforts in achieving membraneless redox flow batteries with performances comparable to membrane-based devices of similar size.
机译:本文报道了在具有流通式构造的多孔电极的无膜氧化还原液流电池中的传质现象分析的进展。提出了一种典型的氧化还原反应物与多孔电极相互作用的物质迁移模型。混合数值分析解决方案是通过广义积分变换技术(GITT)获得的,采用了包含多孔和纯流体区域的单域公式。理论上研究了雷诺数和电极厚度对目标参数的影响。分析了考虑流动和质量传输同时发展的重要性,物质的横向对流通量的存在被证明对电极内部电流的产生具有重要作用。证明了极限电流密度约为Re0.41的比例,并得出了一些物理结论。还提供了防止交叉的准则,就避免混合电势效应而言,雷诺数的增加和电极相对厚度的减小具有积极的作用。通过本分析获得的物理见解应为实现无膜氧化还原液流电池做出更大的努力,其性能可与类似尺寸的基于膜的设备相媲美。

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