001     905047
005     20240712113256.0
020 _ _ |a 978-3-95806-603-8
024 7 _ |2 Handle
|a 2128/30165
024 7 _ |2 URN
|a urn:nbn:de:0001-2022020848
037 _ _ |a FZJ-2022-00346
100 1 _ |0 P:(DE-Juel1)173820
|a Liu, Chang
|b 0
|e Corresponding author
245 _ _ |a Noble Metal Coated Porous Transport Layers for Polymer Electrolyte Membrane Water Electrolysis
|f - 2021-07-01
260 _ _ |a Jülich
|b Forschungszentrum Jülich GmbH Zentralbibliothek, Verlag
|c 2021
300 _ _ |a 139
336 7 _ |2 DataCite
|a Output Types/Dissertation
336 7 _ |0 PUB:(DE-HGF)3
|2 PUB:(DE-HGF)
|a Book
|m book
336 7 _ |2 ORCID
|a DISSERTATION
336 7 _ |2 BibTeX
|a PHDTHESIS
336 7 _ |0 2
|2 EndNote
|a Thesis
336 7 _ |0 PUB:(DE-HGF)11
|2 PUB:(DE-HGF)
|a Dissertation / PhD Thesis
|b phd
|m phd
|s 1642001266_14168
336 7 _ |2 DRIVER
|a doctoralThesis
490 0 _ |a Schriften des Forschungszentrums Jülich Reihe Energie & Umwelt / Energy & Environment
|v 562
502 _ _ |a Dissertation, RWTH Aachen University, 2021
|b Dissertation
|c RWTH Aachen University
|d 2021
520 _ _ |a Polymer electrolyte membrane (PEM) water electrolyzers are electrochemical energyconversion devices that split water into its constituent elements of hydrogen and oxygen. Titaniumbasedporous transport layers (PTL) are widely used due to their good bulk conductivity, highcorrosion resistivity, and excellent mechanical strength. However, titanium-based PTLs situatedat the anode side of PEM electrolyzers are subjected to harsh oxidizing conditions such as highanode overpotential, low pH and oxygen evolution. Under these conditions, titanium (Ti0) changesits oxidation state over time, which induces the formation of a thin but continuously growing layerof passivated titanium (TiOx). Consequently, the contact resistance of titanium PTLs is adverselyaffected, critically decreasing cell performance and durability.In this thesis, a very simple and scalable method is used to protect the titanium-based PTL frompassivation by sputtering very thin layers of noble metal coatings such as Ir, Pt, or Au onto thePTLs. The 20 to 50 nm thick noble metal coatings on the titanium fibers significantly decreasedinterfacial contact resistance between the PTL and catalyst layer, and improved cell performance.The single cells assembled with Ir- or Pt-coated PTLs delivered higher cell performance than cellswith Au-coated PTLs, and nearly identical cell performance as carbon paper, which is prone tocarbon corrosion under these operating conditions.The high cost of using noble metal coatings can be decreased by reducing the loading of thenoble metals. The loading of Ir as a protective layer on the PTL has an impact on the cellperformance. The amount of iridium on one side of the PTL was reduced to 0.025 mgIr∙cm-2 andshowed identical cell performance as Ir-coated PTLs with higher iridium loading, whicheffectively reduced the cost of the Ir. The total amount of iridium is 40 times less compared towhat is usually used in an anode catalyst layer, and 20 times less than Au or Pt typically used asprotective layers in contemporary and commercial electrolyzers.The critical passivation of the bare titanium-based PTL is also one significant factor thatrestricts the durability of a PEM water electrolyzer. In order to investigate the durability of noblemetal coatings (Ir, Pt, Au) on the PTLs, a series of long-term measurements were performed under2 V and 80 °C on the single cells assembled with Ir-coated, Pt-coated and Au-coated PTLs,respectively. Compared to the cell without the coatings, the cell assembled with iridium andplatinum coatings showed degradation rates close to zero, while the identical cell performance wasobserved after 4000 hours with a cell voltage of 2 V. These results demonstrate that iridium andplatinum coatings on titanium-based PTLs are highly effective at protecting the PTL againstpassivation, ultimately improving cell performance and durability.
536 _ _ |0 G:(DE-HGF)POF4-1231
|a 1231 - Electrochemistry for Hydrogen (POF4-123)
|c POF4-123
|f POF IV
|x 0
856 4 _ |u https://juser.fz-juelich.de/record/905047/files/Energie_Umwelt_562.pdf
|y OpenAccess
909 C O |o oai:juser.fz-juelich.de:905047
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910 1 _ |0 I:(DE-588b)5008462-8
|6 P:(DE-Juel1)173820
|a Forschungszentrum Jülich
|b 0
|k FZJ
910 1 _ |0 I:(DE-588b)36225-6
|6 P:(DE-Juel1)173820
|a RWTH Aachen
|b 0
|k RWTH
913 1 _ |0 G:(DE-HGF)POF4-123
|1 G:(DE-HGF)POF4-120
|2 G:(DE-HGF)POF4-100
|3 G:(DE-HGF)POF4
|4 G:(DE-HGF)POF
|9 G:(DE-HGF)POF4-1231
|a DE-HGF
|b Forschungsbereich Energie
|l Materialien und Technologien für die Energiewende (MTET)
|v Chemische Energieträger
|x 0
914 1 _ |y 2021
915 _ _ |0 StatID:(DE-HGF)0510
|2 StatID
|a OpenAccess
915 _ _ |0 LIC:(DE-HGF)CCBY4
|2 HGFVOC
|a Creative Commons Attribution CC BY 4.0
920 _ _ |l yes
920 1 _ |0 I:(DE-Juel1)IEK-14-20191129
|k IEK-14
|l Elektrochemische Verfahrenstechnik
|x 0
980 1 _ |a FullTexts
980 _ _ |a phd
980 _ _ |a VDB
980 _ _ |a UNRESTRICTED
980 _ _ |a book
980 _ _ |a I:(DE-Juel1)IEK-14-20191129
981 _ _ |a I:(DE-Juel1)IET-4-20191129


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