Influence of Supporting Electrolyte on Hydroxide Exchange Membrane Water Electrolysis Performance: Catholyte

Aleksandr Kiessling, Julie C. Fornaciari, Grace Anderson, Xiong Peng, Andreas Gerstmayr, Michael Gerhardt, Samuel McKinney, Alexey Serov, Adam Z. Weber, Yu Seung Kim, Barr Zulevi, Nemanja Danilovic

Research output: Contribution to journalArticlepeer-review

21 Scopus citations

Abstract

Alkaline or hydroxide exchange membrane water electrolysis (HEMWE) is a promising technology for green hydrogen production using platinum group metal-free catalysts and stainless steel, an advantage of alkaline water electrolysis (AWE), and a gasimpermeable membrane, a parallel to proton exchange membrane electrolysis (PEMWE). However, the HEMWE requires supporting electrolytes and there is minimal understanding of their role on the respective reactions. Without SELs, HEMWE performance and durability are worse than PEMWE systems. Herein, consistently feeding potassium hydroxide anolyte, we systematically study the effects of catholyte SELs in HEMWEs including dry vs. wet operation, cation effects, anion effects, and cation/OH ratios on cell potential and stability. We report that (i) hydration of the cathode improves high current density operation by preventing dehydration of the hydroxide exchange membrane (HEM), (ii) there was no correlation between cation type and cell potential, (iii) cell potential and high frequency resistance did not correlate with SEL conductivity, (iv) cathodic carbonate SEL had a significant negative effect on cell performance, (v) increased cation/OH ratio also caused increased cell potentials. Overall, this study concludes that feeding water or potassium hydroxide solution is desirable to improve the AEMWE performance.

Original languageEnglish
Article number024510
JournalJournal of the Electrochemical Society
Volume169
Issue number2
DOIs
StatePublished - 2022
Externally publishedYes

Funding

A.K. gratefully acknowledges funding from the German Fulbright Commission and the Studienstiftung des deutschen Volkes. A.K. thanks the Office for International Education for continuous support during this stay in the US and Prof. Hubert Gasteiger for fruitful discussions. N.D., M.R.G., X.P., A.Z.W., J.C.F., Y.S.K. and G.A. gratefully acknowledge research support from the HydroGEN Advanced Water Splitting Materials Consortium, established as part of the Energy Materials Network under the U.S. Department of Energy, Office of Energy Efficiency and Renewable Energy, Fuel Cell Technologies Office, under Contract Number DE-AC02–05CH11231 (LBNL) and 89233218CNA000001 (LANL). JCF thanks the National Science Foundation (grant DGE1106400) for support. S.M., B.Z. and A.S. also acknowledge Advanced Research Projects Agency-Energy under contract DE-AR000688. The authors would like to thank Nel Hydrogen for supplying titanium porous transport layers.

FundersFunder number
German Fulbright Commission
National Science FoundationDGE1106400
U.S. Department of Energy
Advanced Research Projects Agency - EnergyDE-AR000688
Office of Energy Efficiency and Renewable Energy
Los Alamos National Laboratory
Hydrogen and Fuel Cell Technologies Office89233218CNA000001, DE-AC02–05CH11231
Studienstiftung des Deutschen Volkes

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