Influence of external operating parameters on the hydrothermal transport and performance in proton exchange membrane water electrolyzer

被引:0
|
作者
An, Zhoujian [1 ,2 ]
Yao, Minchao [1 ,2 ]
Du, Xiaoze [1 ,2 ]
Li, Qingliang [3 ]
Jian, Binghao [1 ,2 ]
Zhang, Dong [1 ,2 ]
机构
[1] Lanzhou Univ Technol, Coll Energy & Power Engn, Lanzhou 730050, Peoples R China
[2] Lanzhou Univ Technol, Key Lab Adv Pumps Valves & Fluid Control Syst, Minist Educ, Lanzhou 730050, Peoples R China
[3] TianDi Shanghai Min Equipment Technol Co Ltd, Shanghai 200030, Peoples R China
基金
中国国家自然科学基金;
关键词
Proton exchange membrane water electrolyzer; Single-channel serpentine flow field; External environmental parameters; Water distribution; Hydrothermal transport; HIGH-PRESSURE; 2-PHASE FLOW; CURRENT-DENSITY; GAS-LIQUID; FUEL-CELL; PEM; TEMPERATURE; DEGRADATION; PLATE; POWER;
D O I
10.1007/s11581-024-05688-x
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The single-channel-serpentine proton exchange membrane water electrolyzer (PEMWE) has the potential to be a crucial element in the linking of power, transport, heating, and chemical industries in the foreseeable future of sustainable energy systems. Its performance is influenced by a number of factors. Within the many factors affecting their performance, the external operating parameters have a significant effect on the temperature distribution of the internal components as well as the moisture distribution. In this paper, a single-channel-serpentine flow field electrolyzer (SFFE) is built to address the simulation deficiencies of a conventional single-channel proton exchange membrane electrolyzer, and to more intuitively represent the effects of single-channel-serpentine external environmental parameters on the internal performance of the electrolyzer, in order to assess the effects of different voltages, operating temperatures, and inlet flow rates on the distribution of heat, the distribution of liquid water and gases, and the susceptibility to cross-penetration sites. The results show that when the operating voltage drops below 2.2 V, the liquid-saturated water undergoes a greater impact. Specifically, the voltage increase from 1.6 to 2.2 V results in a significant decrease from 0.97 to 0.79, corresponding to an 18.6% drop. That is, when the voltage is 2.2 V, the liquid water content ensures the adequacy of the reaction, while the inhibitory effect of bubble formation occurs at the beginning. Therefore, 338.15 K and 2.2 V are the most recommended experimental conditions.
引用
收藏
页码:6253 / 6266
页数:14
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