商用级全钒液流电池中平行流道与无流道结构的传质与电化学性能对比研究

Comparative Study of Mass Transfer and Electrochemical Performance between Parallel-Flow and Flow-Field-Free Configurations in Commercial-Scale Vanadium Redox Flow Batteries

  • 摘要: 针对活性面积400 mm×900 mm的商用级全钒液流电池(VRFB),采用COMSOL Multiphysics软件建立多物理场模型,对比平行流道和无流道两种导液结构下的流动传质及电化学性能。结果发现:平行流道结构下电极内部电解液传质以扩散为主,压降更小,但电解液电流密度和VO2+浓度分布不均,浓差极化更剧烈,过电势更高,放电电压和电压效率更低;无流道结构下电极中电解液传质以对流为主,电解液电流密度和VO2+浓度分布更均匀;两种导液结构下过电势均随SOC的增大呈现先下降再上升的趋势,且在0.5附近达到极小值;放电电压和电压效率均随着施加电流密度的增大逐渐下降。

     

    Abstract: For a commercial-grade all-vanadium redox flow battery (VRFB) with an active area of 400 mm × 900 mm, a multiphysics model was established using COMSOL Multiphysics software to compare the flow, mass transfer, and electrochemical performance of the battery under two different electrolyte distribution structures: parallel flow channels and a flow-channel-free design. The results showed that under the parallel flow channel structure, the electrolyte flow velocity within the electrode was lower, mass transfer was dominated by diffusion, and the pressure drop was smaller. However, the electrolyte current density and VO2+ concentration distribution were uneven, concentration polarization was more severe, overpotentials were higher, and both discharge voltage and voltage efficiency were lower. Under the flow-channel-free structure, the electrolyte velocity within the electrode was higher, mass transfer was dominated by convection, and the distribution of electrolyte current density and VO2+ was more uniform. As the state of charge (SOC) increased, the overpotentials for both electrolyte distribution structures first decreased and then increased, reaching a minimum around 0.5. With increasing applied current density, both the discharge voltage and voltage efficiency gradually decreased.

     

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