液体和蒸汽水膜加湿器水传递的实验和模拟研究

S. Mull , M. Pollak , L. Weiß , W. Tegethoff , J. Koehler , M. Wensing
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摘要

聚合物电解质膜(PEM)燃料电池需要精确的水管理来实现高性能和长使用寿命。水的管理是由进入阴极气体的主动加湿控制的。这通常是通过膜加湿器作为植物平衡的一部分来实现的。膜加湿器是被动组件,将水从阴极排气流转移到阴极进口流。移动燃料电池系统中加湿器的工作模式在气到气或少量液态水到气输送的气体之间变化。工作模式的变化主要取决于燃料电池的工作点。膜式加湿器的气-气输运模式已被广泛研究,但对膜式加湿器中少量液态水-气输运的气体的实验和模拟研究仍然不足。到目前为止,只有我们自己的少量液态水-气输运测点的气体实验数据发表。本文提出了一个新的实验数据集,该数据集由39个气变气和86个气变气和少量液态水-气输运测点组成。改变实验数据的边界条件如下:温度、压力、气态水、液态水、氮气质量流量。提出的数据证实了以前的工作:液态水在所有边界条件下都显著增强了质量输运。此外,本文还提出了一种新的以Modelica为建模语言的一维仿真方法。通过调整两个拟合因子,将现有的气对气加湿器模型扩展为两相流模型。本文给出的实验数据验证了这一点。该模型与整个实验数据集的匹配精度很高,R2 = 0.90。这显示了从气对气加湿器模型到两相流模型的简单扩展的通用方法。使用这种建模方法将导致更准确的加湿器性能预测,从而更准确地控制整个燃料电池系统的水管理。此外,它显示了积极使用液态水来增强加湿器性能的潜力。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Experimental and simulative investigation of water transfer in membrane humidifiers operating with liquid and vaporous water
Polymer electrolyte membrane (PEM) fuel cells require exact water management to achieve high performance and long service lifetimes. The water management is controlled by the active humidification of the incoming cathode gas. This is commonly achieved by a membrane humidifier as part of the balance of plant. Membrane humidifiers are passive components that transfer water from the cathode exhaust stream to the cathode inlet stream. The operating modes of a humidifier in a mobile fuel cell system vary between gas-to-gas or gas with a small amount of liquid water-to-gas transport. The change of operating modes depends primarily on the operating point of the fuel cell. The gas-to-gas transport mode is widely investigated, but experimental and simulative studies of gas with a small amount of liquid water-to-gas transfer in membrane humidifiers are still insufficient. So far, only our own experimental data from gas with a small amount of liquid water-to-gas transport measurement points have been published. This paper presents a new experimental data set that consists of 39 gas-to-gas and 86 gas with a small amount of liquid water-to-gas transport measurement points. The following boundary conditions for the experimental data are varied: Temperature, pressure, gaseous water, liquid water, and nitrogen mass flow rate. The data presented confirm previous work: That liquid water significantly enhances mass transport for all boundary conditions. Additionally, this paper presents a new 1D simulation approach using Modelica as the modeling language. An existing gas-to-gas humidifier model was extended to a 2-phase flow model by adjusting 2 fit factors. The experimental data presented here enable the validation. The model matches the overall experimental data set with a high accuracy of R2 = 0.90. This shows a generic approach for a simple extension from a gas-to-gas humidifier model to a 2-phase flow model. Using this modeling approach will result in more accurate humidifier performance prediction and therefore more accurate water management control for the entire fuel cell system. Moreover, it shows the potential of actively using liquid water to enhance the humidifier’s performance.
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