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Elucidating the Role of Hydroxide Electrolyte on Anion-Exchange-Membrane Water Electrolyzer Performance

Jiangjin LiuEnergy Conversion Group, Lawrence Berkeley National Laboratory, Berkeley, California 94720, United States of AmericaZhenye KangChemistry and Nanoscience Center, National Renewable Energy Laboratory, Golden, Colorado 80401, United States of AmericaDongguo LiMPA-11: Material Synthesis and Integrated Devices, Los Alamos National Laboratory, Los Alamos, New Mexico 87545, United States of AmericaMagnolia PakChemistry and Nanoscience Center, National Renewable Energy Laboratory, Golden, Colorado 80401, United States of AmericaShaun M AliaChemistry and Nanoscience Center, National Renewable Energy Laboratory, Golden, Colorado 80401, United States of AmericaCy FujimotoNanoscale Sciences Department, Sandia National Laboratories, Albuquerque, New Mexico 87185, United States of AmericaGuido BenderChemistry and Nanoscience Center, National Renewable Energy Laboratory, Golden, Colorado 80401, United States of AmericaYu Seung KimMPA-11: Material Synthesis and Integrated Devices, Los Alamos National Laboratory, Los Alamos, New Mexico 87545, United States of AmericaAdam Z. WeberEnergy Conversion Group, Lawrence Berkeley National Laboratory, Berkeley, California 94720, United States of America
2021en
ABI

Аннотация

Many solid-state devices, especially those requiring anion conduction, often add a supporting electrolyte to enable efficient operation. The prototypical case is that of anion-exchange-membrane water electrolyzers (AEMWEs), where addition of an alkali metal solution improves performance. However, the specific mechanism of this performance improvement is currently unknown. This work investigates the functionality of the alkali metal solution in AEMWEs using experiments and mathematical models. The results show that additional hydroxide plays a key role not only in ohmic resistance of the membrane and catalyst layer but also in the reaction kinetics. The modeling suggests that the added liquid electrolyte creates an additional electrochemical interface with the electrocatalyst that provides ion-transport pathways and distributes product gas bubbles; the total effective electrochemical active surface area in the cell with 1 M KOH is 5 times higher than that of the cell with DI water. In the cell with 1 M KOH, more than 80% of the reaction current is associate with the liquid electrolyte. These results indicate the importance of high pH of electrolyte and catalyst/electrolyte interface in AEMWEs. The understanding of the functionality of the alkali metal solution presented in this study should help guide the design and optimization of AEMWEs.

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