期刊
JOURNAL OF POWER SOURCES
卷 558, 期 -, 页码 -出版社
ELSEVIER
DOI: 10.1016/j.jpowsour.2022.232564
关键词
LDH; Seawater; MEA; Electrolysis
Direct seawater electrolysis faces challenges in suppressing chlorine adsorption/reaction and overcoming degradation of the anion exchange membrane. The solution involves developing selective catalysts and implementing limited operating conditions. Development of active, selective, cost-effective, and stable seawater-splitting catalysts is crucial for commercializing AEM water electrolyzers.
Direct seawater electrolysis faces fundamental electrochemical challenges, such as suppression of chlorine adsorption and/or evolution reactions that poison the current state-of-the-art anode catalysts and accelerate the degradation of the anion exchange membrane (AEM). The technically favored solution path for addressing these issues includes development of novel selective catalysts and implementation of limited operating conditions. Therefore, development of highly active, selective, cost-effective, and stable seawater-splitting catalysts is required for a successful commercialization of the AEM water electrolyzers (AEMWEs). Herein, we report for the first-time an extended operation for over 1000 h of advanced AEMWEs, operating directly with seawater. To fabricate the membrane electrode assemblies (MEAs), catalyst coated electrodes (CCEs) are assembled with Sustainion (R) X37-50 grade T anion exchange membranes. The anode CCEs are fabricated by spraying an ink prepared from nanostructured NiFe-layered double hydroxide (LDH) catalyst that are synthesized by the solvothermal method and deposited directly onto platinized titanium porous transport layers (PTLs). The cathode CCEs are prepared by spraying an ink prepared from commercial Renay-Nickel catalyst onto a nickel fiber felt. As prepared AEM electrolyzer cells operated with seawater and demonstrated better than previously reported in the literature performance of over 1000 h of operation at a constant current density of 300 mA cm-2.
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