Flow field design for high-pressure PEM electrolysis cells
| Autor: | Anders Christian Olesen, Søren Knudsen Kær |
|---|---|
| Jazyk: | angličtina |
| Rok vydání: | 2017 |
| Zdroj: | Olesen, A C & Kær, S K 2017, ' Flow field design for high-pressure PEM electrolysis cells ', 1st International Conference on Electrolysis, Copenhagen, Denmark, 13/06/2017-15/06/2017 . Aalborg University |
| Popis: | With the increasing interest in producing hydrogen through water electrolysis, the importance of understanding the transport phenomena governing its operation increases. To ensure optimal operating conditions for PEM electrolysis, it is particularly important to understand how the liquid feed-water distributes. Water not only serves a reactant, it also aids in cooling due to its high specific heat capacity. The movement of liquid water at the anode is difficult to model, since it is highly coupled to the formation of gas bubbles. To capture the complex two-phase flow behaviour that takes place within micro-channels and porous media, our research group has developed an Euler-Euler model in the computational fluid dynamics modelling framework of ANSYS CFX. In addition to two-phase flow, the model accounts for turbulence, species transport in the gas phase, heat transport in all three phases (i.e. solid, gas and liquid), as well as charge transport of electrons and ions. Our recent improvements have focused on the models ability to account for phase change and electrochemistry as well as the modelling of two-phase flow regimes. For comparison, an interdigitated and parallel channel flow field will be investigated with regard to how well they distribute gas and heat. To obtain a high durability when operating at high current densities, it is essential that liquid water and temperature is evenly distribution over the entire active surface area. In Figure 1, a contour plot of the temperature distribution within an interdigitated flow field is presented as an example. The axis-symmetric simulation shows that the formation of hot spots in the order of 8◦C above the inlet temperature can occur for a current density of 3 A/cm2 and a water stoichiometry of 350. These spots are primarily located underneath the outlet channels. To avoid them, an in-depth design and simulation study is necessary. With the increasing interest in producing hydrogen through water electrolysis, the importance of understanding the transport phenomena governing its operation increases. To ensure optimal operating conditions for PEM electrolysis, it is particularly important to understand how the liquid feed-water distributes. Water not only serves a reactant, it also aids in cooling due to its high specific heat capacity. The movement of liquid water at the anode is difficult to model, since it is highly coupled to the formation of gas bubbles. To capture the complex two-phase flow behaviour that takes place within micro-channels and porous media, our research group has developed an Euler-Euler model in the computational fluid dynamics modelling framework of ANSYS CFX. In addition to two-phase flow, the model accounts for turbulence, species transport in the gas phase, heat transport in all three phases (i.e. solid, gas and liquid), as well as charge transport of electrons and ions. Our recent improvements have focused on the models ability to account for phase change and electrochemistry as well as the modelling of two-phase flow regimes. For comparison, an interdigitated and parallel channel flow field will be investigated with regard to how well they distribute gas and heat. To obtain a high durability when operating at high current densities, it is essential that liquid water and temperature is evenly distribution over the entire active surface area. In Figure 1, a contour plot of the temperature distribution within an interdigitated flow field is presented as an example. The axis-symmetric simulation shows that the formation of hot spots in the order of 8◦C above the inlet temperature can occur for a current density of 3 A/cm2 and a water stoichiometry of 350. These spots are primarily located underneath the outlet channels. To avoid them, an in-depth design and simulation study is necessary. |
| Databáze: | OpenAIRE |
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