Zhang Guobin, Qu Zhiguo
MOE Key Laboratory of Thermo-Fluid Science and Engineering, School of Energy and Power Engineering, Xi'an Jiaotong University, Xi'an 710049, China.
Materials (Basel). 2024 Jul 26;17(15):3694. doi: 10.3390/ma17153694.
The oxygen discharge process significantly affects the electrochemical performance of a proton exchange membrane water electrolyzer (PEMWE), which requires an optimal structure of the flow field implemented in the bipolar plate (BP) component. In this study, we numerically investigated the two-phase (liquid water and oxygen) flow in the PEMWE's channel region with different outlet manifold structures utilizing the volume of fluid (VOF) model. Then, the oxygen volume fraction at the liquid/gas diffusion layer (L/GDL) surface, i.e., the interface of the channel and L/GDL, obtained by the liquid water and oxygen flow model was incorporated into a three-dimensional (3D) PEMWE model, which made it possible to predict the influence of the outlet manifold structure on the multiple transfers inside the whole electrolyzer as well as the electrochemical performance. The results indicate that the existence of oxygen in the flow field significantly decreased the electrolyzer voltage at a fixed operation current density and deteriorated the uniform distribution of the oxygen amount, current density (corresponding to the electrochemical reaction rate) and temperature in the membrane electrode assembly (MEA), indicating that the rapid oxygen removal from the flow field is preferred in the operation of the electrolyzer. Moreover, slight increases in the width of the outlet manifold were helpful in relieving the oxygen accumulation in the anode CL and, hence, improved the electrolyzer performance with more uniform distribution characteristics.
氧气排放过程对质子交换膜水电解槽(PEMWE)的电化学性能有显著影响,这就要求在双极板(BP)组件中实现最佳的流场结构。在本研究中,我们利用流体体积(VOF)模型对具有不同出口集管结构的PEMWE通道区域内的两相(液态水和氧气)流动进行了数值研究。然后,将通过液态水和氧气流动模型得到的通道与液/气扩散层(L/GDL)界面处,即L/GDL表面的氧气体积分数纳入三维(3D)PEMWE模型,从而能够预测出口集管结构对整个电解槽内多种传递过程以及电化学性能的影响。结果表明,在固定的运行电流密度下,流场中氧气的存在显著降低了电解槽电压,并恶化了膜电极组件(MEA)中氧气量、电流密度(对应于电化学反应速率)和温度的均匀分布,这表明在电解槽运行中,优先从流场中快速去除氧气。此外,出口集管宽度的轻微增加有助于缓解阳极催化层中的氧气积累,从而改善电解槽性能,并具有更均匀的分布特性。