叶青, 宋洁, 侯坤, 郭志远, 徐桂芝, 邓占锋, 李宝让. 质子交换膜电解制氢氢气渗透研究进展[J]. 工程科学学报, 2022, 44(7): 1274-1281. DOI: 10.13374/j.issn2095-9389.2021.08.02.003
引用本文: 叶青, 宋洁, 侯坤, 郭志远, 徐桂芝, 邓占锋, 李宝让. 质子交换膜电解制氢氢气渗透研究进展[J]. 工程科学学报, 2022, 44(7): 1274-1281. DOI: 10.13374/j.issn2095-9389.2021.08.02.003
YE Qing, SONG Jie, HOU Kun, GUO Zhi-yuan, XU Gui-zhi, DENG Zhan-feng, LI Bao-rang. Review of hydrogen permeation in PEM water electrolysis[J]. Chinese Journal of Engineering, 2022, 44(7): 1274-1281. DOI: 10.13374/j.issn2095-9389.2021.08.02.003
Citation: YE Qing, SONG Jie, HOU Kun, GUO Zhi-yuan, XU Gui-zhi, DENG Zhan-feng, LI Bao-rang. Review of hydrogen permeation in PEM water electrolysis[J]. Chinese Journal of Engineering, 2022, 44(7): 1274-1281. DOI: 10.13374/j.issn2095-9389.2021.08.02.003

质子交换膜电解制氢氢气渗透研究进展

Review of hydrogen permeation in PEM water electrolysis

  • 摘要: 由于膜的吸水特性,高压质子交换膜(PEM)制氢(尤其是差压式,氢侧高压/氧侧常压)存在氢气渗透问题,影响电解堆的运行安全与效率。基于菲克定律描述的渗透通量与渗透率、分压差的关系,综述了温度/压力、膜水合程度、氢气分压差对氢气渗透的影响规律。在常规运行压力范围(3.5 MPa)内,扩散系数与溶解度主要受温度影响,温度升高则渗透率增大;氢气渗透率随膜水合程度的增加而增大;氢气分压差对渗透的影响表现出线性(渗透池环境)与非线性(电解制氢环境)两种关系,非线性可能源于膜透水性提升与水通道结构改变引起的对流渗透。考虑到电解制氢实际工况存在电流,综述了电流密度对氢渗透的影响,氢气渗透率随运行电流密度的升高而增大,氢过饱和是可能的影响机理,高电流密度下氢过饱和度升高,导致氢气通过膜的渗透增加。

     

    Abstract: Hydrogen has the advantages of high energy density, no pollution, and long-term storage. As an important medium for the transformation of energy interconnection, it helps to promote the clean and efficient use of traditional fossil energy, support the large-scale development of renewable energy, and achieve large-scale deep decarbonization. With the excellent responsiveness to intermittent and fluctuating power supplies, proton exchange membrane (PEM) water electrolysis has been a research hotspot in the field of hydrogen production with renewable energy and will be one of the main technical routes for effective hydrogen supply in the future. The high-pressure operation of PEM electrolyzers has been successfully realized and commercialized, considering PEM’s outstanding mechanical strength and gas separation properties. However, due to the water-absorbing properties of the membrane, an important problem in high-pressure PEM water electrolysis (especially under differential pressure conditions and high pressure in the cathode compartment/atmospheric pressure in the anode compartment) is the permeation of hydrogen through the membrane, which affects safety and efficiency. In this article, the research progress of hydrogen permeation in PEM electrolysis was reviewed. First, the theory of permeation was introduced. Second, considering the relationship among the permeation flux, permeability, and partial pressure difference described by Fick’s law, the effects of temperature/pressure, hydration degree of the membrane, and partial pressure difference on hydrogen permeation were reviewed. In the normal operating pressure range (<3.5 MPa) for hydrogen production through PEM electrolysis, the diffusion coefficient and solubility are mainly affected by temperature, and the permeability increases with increasing temperature. The permeability of hydrogen in water is approximately 5–10 times that of a dry film, and the permeability increases with increases in the relative humidity of the membrane. The influence of partial pressure difference in hydrogen permeation shows a linear dependence in permeation cell and quadratic dependence in real electrolysis. The quadratic dependence may be attributed to the convective permeation caused by the increase in membrane water permeability and changes in the water channel. Third, considering the current in real operating conditions of electrolysis, the effect of current density on hydrogen permeation was reviewed. The permeability increases with the increase in current density, which may be attributed to the increase in hydrogen supersaturation in the cathode. At a high current density, the hydrogen concentration within the ionomer at the cathode catalyst particles become higher, and the high concentration gradient causes hydrogen to diffuse from cathode to anode.

     

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