Evidence map›Paper›PMID 37459180›Full record

ArticleACS applied materials & interfaces2023

How the Porous Transport Layer Interface Affects Catalyst Utilization and Performance in Polymer Electrolyte Water Electrolysis.

Carl Cesar Weber, Jacob A Wrubel, Lorenz Gubler, Guido Bender, Salvatore De Angelis, Felix N Büchi

Open access · hybridAbstract read
In one paragraph

Article in ACS applied materials & interfaces, 2023. The graph could read no effect estimate from its abstract, so it casts no vote on the map. Cited by 13 papers.

0numbers the graph read from it
0cells of the map it votes in
13citing papers in PubMed
5.4field-weighted citation impact, top 4% of its field
1 · What the graph read from it

What it found

Each row is one number read from the abstract, on the scale the paper reported it, with its interval. Left of the dashed line favours the treatment, right favours the comparator. Under each row is the sentence it came from. New to these charts? A ten-minute tutorial.

The abstract states no effect estimate the extractor could read, or names no intervention and outcome on the map, so this paper lights no cell and moves no belief. It is still indexed, cited and linked below.

2 · The registry

The trial behind it

Trials whose registry record cites this paper, or whose number appears in the abstract. A trial that started after this paper was published is citing it as background, not reporting it.

Neither the registry nor the abstract names a trial number. If this is a trial report, that itself is worth knowing.

3 · Its place in the literature

Who cites it

13 citing papers in PubMed, 73 citations in OpenAlex.

  1. Article
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  6. Review
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  8. Article
  9. Perchlorate Fusion-Hydrothermal Synthesis of Nano-Crystalline IrOSmall (Weinheim an der Bergstrasse, Germany) · 2025
    Article
  10. Review
  11. Article
  12. Photodeposition-Based Synthesis of TiOAdvanced science (Weinheim, Baden-Wurttemberg, Germany) · 2024
    Article
  13. Article
4 · The record

Corrections and comments

PubMed lists nothing against this paper. Absence here is not a guarantee, only a check that was made.

5 · Who and what money

Authors and funding

6 authors at 2 institutions in 2 countries.

Carl Cesar WeberElectrochemistry Laboratory, Paul Scherrer Institut, 5232 Villigen PSI, Switzerland.
Jacob A WrubelNational Renewable Energy Laboratory, Golden, Colorado 80401, United States.
Lorenz GublerElectrochemistry Laboratory, Paul Scherrer Institut, 5232 Villigen PSI, Switzerland.ORCID 0000-0002-8338-6994
Guido BenderNational Renewable Energy Laboratory, Golden, Colorado 80401, United States.
Salvatore De AngelisElectrochemistry Laboratory, Paul Scherrer Institut, 5232 Villigen PSI, Switzerland.ORCID 0000-0002-2777-2129
Felix N BüchiElectrochemistry Laboratory, Paul Scherrer Institut, 5232 Villigen PSI, Switzerland.ORCID 0000-0002-3541-4591
Paul Scherrer Institute · CHNational Laboratory of the Rockies · US

Funding

No grant is acknowledged in the PubMed record.

6 · The paper itself

Abstract

Cost reduction and fast scale-up of electrolyzer technologies are essential for decarbonizing several crucial branches of industry. For polymer electrolyte water electrolysis, this requires a dramatic reduction of the expensive and scarce iridium-based catalyst, making its efficient utilization a key factor. The interfacial properties between the porous transport layer (PTL) and the catalyst layer (CL) are crucial for optimal catalyst utilization. Therefore, it is essential to understand the relationship between this interface and electrochemical performance. In this study, we fabricated a matrix of two-dimensional interface layers with a well-known model structure, integrating them as an additional layer between the PTL and the CL. By characterizing the performance and conducting an in-depth analysis of the overpotentials, we were able to estimate the catalyst utilization at different current densities, correlating them to the geometric properties of the model PTLs. We found that large areas of the CL become inactive at increasing current density either due to dry-out, oxygen saturation (under the PTL), or the high resistance of the CL away from the pore edges. We experimentally estimated the water penetration in the CL under the PTL to be ≈20 μm. Experimental results were corroborated using a 3D-multiphysics model to calculate the current distribution in the CL and estimate the impact of membrane dry-out. Finally, we observed a strong pressure dependency on performance and high-frequency resistance, which indicates that with the employed model PTLs, a significant gas phase accumulates in the CL under the lands, hindering the distribution of liquid water. The findings of this work can be extrapolated to improve and engineer PTLs with advanced interface properties, helping to reach the required target goals in cost and iridium loadings.

Indexed as

active catalyst layercatalyst utilizationhydrogeninterface PTL/CLiridium loadingPEM electrolysispolymer electrolyte water electrolysisporous transport layer

Identifiers

PMID37459180
PMCPMC10375438
OpenAlexW4384522374

What OpenQuestion holds

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LicenceCC BY
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Registered trials

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Read under generation 80e0d062 · epoch 390. Bibliography from PubMed, PubMed Central and OpenAlex; grants from NIH RePORTER; trial links from ClinicalTrials.gov; estimates, votes and beliefs from the OpenQuestion graph.