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Concentrated Solution Model of Transport in All Vanadium Redox Flow Battery Membrane Separator

机译:所有钒氧化还原流量电池膜分离器中的集中溶液运输模型

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A model of transport across the ion-exchange membrane in all-vanadium redox flow batteries has been proposed based on concentrated solution theory for species with high concentration. The model is based upon the Stefan-Maxwell multicomponent diffusion equation where the fluxes of the species including protons (H~+), bisulfate (HSO_4~-), water (H_2O) and the sulfonate functional groups (-SO_3~-) are fully coupled. The driving force for species transport has been modeled in terms of concentration and electrostatic potential gradients. The ionic transference numbers as well as water electro-osmosis drag coefficient has been calculated for different acid concentrations.
机译:基于高浓度的物种的浓缩溶液理论,提出了全钒氧化还原电池中的离子交换膜的运输模型。该模型基于Stefan-Maxwell多组分扩散方程,其中物种的助熔剂(H〜+),双硫酸氢盐(HSO_4〜 - ),水(H_2O)和磺酸族官能团(-SO_3〜 - )是完全的耦合。物种传输的驱动力已经在浓度和静电潜在梯度方面进行了建模。针对不同的酸浓度计算了离子转移数以及水电渗荷载系数。

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