分离器(采油)
迷惑
质子交换膜燃料电池
计算流体力学
机械
氢
尺寸
试验台
压力降
毛细管作用
计算机模拟
材料科学
化学
核工程
机械工程
工程类
燃料电池
热力学
化学工程
复合材料
物理
有机化学
作者
Jiquan Han,Jianmei Feng,Tianfang Hou,Wei Chen,Xueyuan Peng
标识
DOI:10.1080/15435075.2020.1865370
摘要
The gas-water separator is an important auxiliary component of the hydrogen recirculation subsystem for the proton exchange membrane fuel cell (PEMFC) system. This study investigated three baffle separators with different structures used for a 75 kW PEMFC system by computational fluid dynamics (CFD) simulation and experimental validation. An Euler-Lagrange two-phase simulation model was established to investigate the gas-phase flow characteristics and the droplets trajectory and film distribution in separators. Moreover, an experimental bench was set up to test the overall performance of the separators. The results showed that the CFD model can predict the performance of the gas-water separator accurately. Through the comparison of air and mixed hydrogen, it was found that the density of the gas phase fluid has a great influence on the pressure drop. The local gas flow at the baffle bottom where the film fall directly is at high velocity in separator A, resulting in that the liquid film is broken easily to cause more fine droplets being entrained again into the outflow. Besides, thicker liquid film still formed in the top part of the separators A and B compared with separator C, which is not conducive for high separation performance. Thus, the separator C is preferred to be suggested for PEMFC systems.
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