001     1037736
005     20250203103244.0
024 7 _ |a 10.1149/MA2023-02422138mtgabs
|2 doi
024 7 _ |a 1091-8213
|2 ISSN
024 7 _ |a 2151-2043
|2 ISSN
037 _ _ |a FZJ-2025-00896
082 _ _ |a 540
100 1 _ |a Galkina, Irina
|0 P:(DE-Juel1)179530
|b 0
|u fzj
111 2 _ |a 244th ECS Meeting
|c Gothenburg
|d 2023-10-08 - 2023-10-12
|w Sweden
245 _ _ |a Promoting AEM Water Electrolyzer Performance and Reproducibility by Tumbler Milling of Ni 3 fe-LDH OER Catalyst
260 _ _ |c 2023
336 7 _ |a Abstract
|b abstract
|m abstract
|0 PUB:(DE-HGF)1
|s 1737526193_30426
|2 PUB:(DE-HGF)
336 7 _ |a Conference Paper
|0 33
|2 EndNote
336 7 _ |a INPROCEEDINGS
|2 BibTeX
336 7 _ |a conferenceObject
|2 DRIVER
336 7 _ |a Output Types/Conference Abstract
|2 DataCite
336 7 _ |a OTHER
|2 ORCID
520 _ _ |a Anion exchange membrane water electrolysis is an attractive clean energy technology for producing hydrogen for energy storage, transport 1,2 and numerous other applications. Rational choice of highly active and stable catalysts as well as the proper design of catalyst layers are crucial to achieve technical relevance of electrolyser systems. The establishment of clear understanding of optimal catalyst treatment and methods of implementation are key steps towards optimized electrolyzer performance and durability. One aspect of catalyst performance in catalyst layers is the catalyst size distribution. A multimodal size distribution of catalyst particles or agglomerates can jeopardize the layer homogeneity and thus electrode performance.In this work, the effect of high-energy ball tumbling milling on the promising Ni3Fe-LDH OER catalyst followed by catalyst dispersion control was correlated to the microstructure of the catalyst layer, the achieved catalyst activity and utilization, and the resulting single cell performance and stability. Physico-chemical characterization confirmed the stable layered double hydroxide structure of the catalyst. By milling, a 300-fold reduction of catalyst agglomerate size, and an 8.8-fold increase of the geometrical surface was achieved. The optimized solvent compositions effectively increased the catalyst ink stability. We found that a significantly decreased catalyst agglomerate size resulted in very homogeneous mixtures of catalyst and ionomer. By tailoring the electrode structure design, lower internal electronic resistances of the electrodes, decreased charge-transfer resistances (Rct) of the membrane electrode assembly, and stable single cell durability of 1000 h with a minor degradation rate of 57 µV h-1 were accomplished.This work presents a facile and scalable approach of NiFe-LDH catalyst treatment and dispersion control and provides a guideline to follow for further electrode development and increased AEM water electrolyzer performances.
536 _ _ |a 1231 - Electrochemistry for Hydrogen (POF4-123)
|0 G:(DE-HGF)POF4-1231
|c POF4-123
|f POF IV
|x 0
588 _ _ |a Dataset connected to CrossRef, Journals: juser.fz-juelich.de
700 1 _ |a Faid, Alaa Y.
|0 P:(DE-HGF)0
|b 1
700 1 _ |a Grigorev, Nikita
|0 P:(DE-Juel1)172675
|b 2
700 1 _ |a Jiang, Wulyu
|0 P:(DE-HGF)0
|b 3
700 1 _ |a Borowski, Patrick
|0 P:(DE-HGF)0
|b 4
700 1 _ |a Sunde, Svein
|0 P:(DE-HGF)0
|b 5
700 1 _ |a Shviro, Meital
|0 P:(DE-Juel1)165174
|b 6
700 1 _ |a Lehnert, Werner
|0 P:(DE-Juel1)129883
|b 7
700 1 _ |a Mechler, Anna K.
|0 P:(DE-Juel1)175122
|b 8
|u fzj
700 1 _ |a Scheepers, Fabian
|0 P:(DE-Juel1)166215
|b 9
|u fzj
773 _ _ |a 10.1149/MA2023-02422138mtgabs
|0 PERI:(DE-600)2438749-6
|y 2023
|g Vol. MA2023-02, no. 42, p. 2138 - 2138
|x 2151-2043
909 C O |o oai:juser.fz-juelich.de:1037736
|p VDB
910 1 _ |a Forschungszentrum Jülich
|0 I:(DE-588b)5008462-8
|k FZJ
|b 0
|6 P:(DE-Juel1)179530
910 1 _ |a Forschungszentrum Jülich
|0 I:(DE-588b)5008462-8
|k FZJ
|b 8
|6 P:(DE-Juel1)175122
910 1 _ |a Forschungszentrum Jülich
|0 I:(DE-588b)5008462-8
|k FZJ
|b 9
|6 P:(DE-Juel1)166215
913 1 _ |a DE-HGF
|b Forschungsbereich Energie
|l Materialien und Technologien für die Energiewende (MTET)
|1 G:(DE-HGF)POF4-120
|0 G:(DE-HGF)POF4-123
|3 G:(DE-HGF)POF4
|2 G:(DE-HGF)POF4-100
|4 G:(DE-HGF)POF
|v Chemische Energieträger
|9 G:(DE-HGF)POF4-1231
|x 0
914 1 _ |y 2024
920 _ _ |l yes
920 1 _ |0 I:(DE-Juel1)IEK-14-20191129
|k IEK-14
|l Elektrochemische Verfahrenstechnik
|x 0
920 1 _ |0 I:(DE-Juel1)IET-4-20191129
|k IET-4
|l Elektrochemische Verfahrenstechnik
|x 1
980 _ _ |a abstract
980 _ _ |a VDB
980 _ _ |a I:(DE-Juel1)IEK-14-20191129
980 _ _ |a I:(DE-Juel1)IET-4-20191129
980 _ _ |a UNRESTRICTED


LibraryCollectionCLSMajorCLSMinorLanguageAuthor
Marc 21