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Simulation of velocity profiles in a laboratory electrolyser using computational fluid dynamics

机译:使用计算流体动力学模拟实验室电解器中的速度分布

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A commercial CFD code, Fluent, has been used to analyse the design of a filter-press reactor operating with characteristic linear flow velocities between 0.024 and 0.192 ms~(-1). Electrolyte flow through the reactor channel was numerically calculated using a finite volume approach to solve the Navier-Stokes equations. The length of the channel was divided into 7 sections corresponding to distances of 0, 0.01, 0.04, 0.08, 0.12, 0.14 and 0.15 m from the electrode edge nearest to the inlet. The depth of the channel was divided into three planes parallel to the channel bottom. For each channel section, a velocity profile was obtained at each depth together with the average velocity in each plane. The flow predictions show that the flow development, as the electrolyte passes through the cell, is strongly affected by the manifold causing strong vortex structures at the entrance and exit of the channel. Although the flow disturbances are a function of the flow rate, they gradually disappear downstream along the channel length. Simulated velocity profiles are considered for the typical current density range used in the FM01-LC reactor.
机译:商业CFD码,流畅,已用于分析滤波器压力机的设计,其特征线性流速在0.024和0.192ms〜(-1)之间。使用电抗器通道的电解质流动使用有限体积方法来解决Navier-Stokes方程。通道的长度分为与最近入口最近的电极边缘的0,0.01,0.04,0.08,0.12,0.14和0.15μs的7个部分。通道的深度被分成三个平行于通道底部的平面。对于每个通道部分,在每个深度下一起获得速度分布,以及每个平面中的平均速度。流程预测表明,随着电解质通过电池的流动开发,受到歧管的强烈影响,该歧管在通道的入口和出口处引起强烈的涡流结构。虽然流动干扰是流速的函数,但它们沿着沟道长度逐渐消失。模拟速度曲线被认为是FM01-LC反应器中使用的典型电流密度范围。

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