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吴震

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个人简介

教授,博导,西安交通大学青年拔尖人才(A类),化工机械所所长和支部书记。

研究方向为固态储氢与燃料电池,牵头主持国家重点研发计划重点专项项目(2项)、国家重大科技专项项目任务(1项)、国家自然科学基金项目(3项)等国家级项目6项以及陕西省重点研发计划专项项目(3项)等省部级项目10余项。

一作或通讯作者在Chemical Reviews、Journal of Energy Chemistry等期刊发表论文80余篇,获中国发明创业奖成果奖二等奖(第一完成人)、陕西省石化科学技术一等奖、中国发明创业奖人物奖等。


论文成果

Magnesium based metal hydride reactor incorporating helical coil heat exchanger: Simulation study and optimal design

发布时间:2025-04-30  点击次数:

发布时间:2025-04-30

论文名称:Magnesium based metal hydride reactor incorporating helical coil heat exchanger: Simulation study and optimal design

发表刊物:Applied Energy

摘要:Magnesium based metal hydride has been viewed as one of the most commonly-used materials in the practical applications of hydrogen energy systems. The heat and mass transfer processes have significant effects on the hydrogen storage performance of magnesium based metal hydride reactors. Incorporating helical coil heat exchanger into the reactor could be an effective way to improve the performance of heat and mass transfer. In this work, a new three-dimensional model for magnesium based metal hydride reactor with helical coil heat exchanger is proposed and solved using the commercial software package COMSOL Multiphysics V3.5a. The comparison of hydrogen storage behaviors between the reactors incorporating the traditional straight pipe and new helical coil heat exchangers is firstly conducted based on the numerical simulation. The comparison results show that the helical coil heat exchanger has better effect on improving the characteristics of reactor than the straight pipe heat exchanger due to its secondary circulation. The effects of key parameters, including the initial conditions, heat transfer coefficients of heat transfer fluid and helical coil geometry on the characteristics of reactor with the helical coil heat exchanger are also analyzed systematically. It is discovered that larger initial hydrogen pressure and lower initial temperature are beneficial to the improvement of hydrogen absorption kinetics, because of the greater driving force for the hydriding reaction. The results of optimal design suggest that smaller non-dimensional pitch, the ratio of helical pitch to helical diameter, improves the heat and mass transfer performance. The reactor with 0.333 of non-dimensional pitch exhibits the best hydrogen storage behaviors under 3.0 MPa and 523 K, when the heat transfer coefficient of heat transfer fluid is 500 W m−2 K−1. Approximately 95% of hydrogen absorption process is completed within about 1000 s in this case.

合写作者:Zhen Wu, Fusheng Yang, Zaoxiao Zhang*, Zewei Bao

卷号:130

页面范围:712-722

是否译文:否

发表时间:2014-10-01

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