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@ARTICLE{Liu:891123,
author = {Liu, Chang and Wippermann, Klaus and Rasinski, Marcin and
Suo, Yanpeng and Shviro, Meital and Carmo, Marcelo and
Lehnert, Werner},
title = {{C}onstructing a {M}ultifunctional {I}nterface between
{M}embrane and {P}orous {T}ransport {L}ayer for {W}ater
{E}lectrolyzers},
journal = {ACS applied materials $\&$ interfaces},
volume = {13},
number = {14},
issn = {1944-8244},
address = {Washington, DC},
publisher = {Soc.},
reportid = {FZJ-2021-01375},
pages = {16182 - 16196},
year = {2021},
abstract = {The cell performance and durability of polymer electrolyte
membrane (PEM) water electrolyzers are limited by the
surface passivation of titanium-based porous transport
layers (PTLs). In order to ensure stable performance
profiles over time, large amounts (≥1 mg·cm–2) of noble
metals (Au, Pt, Ir) are most widely used to coat
titanium-based PTLs. However, their high cost is still a
major obstacle toward commercialization and widespread
application. In this paper, we assess different loadings of
iridium, ranging from 0.005 to 0.05 mg·cm–2 in titanium
PTLs, that consequently affect the investment costs of PEM
water electrolyzers. Concerning a reduction in the precious
metal costs, we found that Ir as a protective layer with a
loading of 0.025 mg·cm–2 on the PTLs would be sufficient
to achieve the same cell performance as PTLs with a higher
Ir loading. This Ir loading is a 40-fold reduction over the
Au or Pt loading typically used for protective layers in
current commercial PEM water electrolyzers. We show that the
Ir protective layer here not only decreases the Ohmic
resistance significantly, which is the largest part of the
gain in performance, but moreover, the oxygen evolution
reaction activity of the iridium layer makes it promising as
a cost-effective catalyst layer. Our work also confirms that
the proper construction of a multifunctional interface
between a membrane and a PTL indeed plays a crucial role in
guaranteeing the superior performance and efficiency of
electrochemical devices.},
cin = {IEK-14 / IEK-4},
ddc = {600},
cid = {I:(DE-Juel1)IEK-14-20191129 / I:(DE-Juel1)IEK-4-20101013},
pnm = {134 - Electrolysis and Hydrogen (POF3-134) / 1231 -
Electrochemistry for Hydrogen (POF4-123)},
pid = {G:(DE-HGF)POF3-134 / G:(DE-HGF)POF4-1231},
typ = {PUB:(DE-HGF)16},
pubmed = {33798332},
UT = {WOS:000641156600020},
doi = {10.1021/acsami.0c20690},
url = {https://juser.fz-juelich.de/record/891123},
}