Comprehensive investigation of novel pore-graded gas diffusion layers for high-performance and cost-effective proton exchange membrane electrolyzers

Hydrogen produced by water electrolysis is a promising storage medium for renewable energy. Reducing the capital cost of proton exchange membrane (PEM) electrolyzers without losing efficiency is one of its most pressing challenges. Gas diffusion layers (GDL), such as felts, foams, meshes and sintered plates, are key stack components, but these are either inefficient or expensive. This study presents a new type of GDL produced via vacuum plasma spraying (VPS), which offers a large potential for cost reduction. With this technology, it is possible to introduce a gradient in the pore-size distribution along the thickness of the GDL by varying the plasma parameters and titanium powder particle sizes. This feature was confirmed by cross-section scanning electron microscopy (SEM). X-ray computed tomography (CT) and mercury intrusion porosimetry allowed determining the porosity, pore radii distribution, and pore entry distribution. Pore radii of ca. 10 μm could be achieved in the layers of the GDL close to the bipolar plate, while those in contact with the electrodes were in the range of 5 μm. The thermally sprayed Ti-GDLs allowed achieving PEM electrolyzer performances comparable to those of the state-of-the-art sintered plates and far superior than those of meshes. Moreover, a numerical model showed that the reduced capillary pressure and tortuosity eliminates mass transport limitations at 2 A cm−2. The results presented herein demonstrate a promising solution to reduce the cost of one of the most expensive components of the stack.

[1]  K. Andreas Friedrich,et al.  Highly active anode electrocatalysts derived from electrochemical leaching of Ru from metallic Ir0.7Ru0.3 for proton exchange membrane electrolyzers , 2017 .

[2]  K. A. Friedrich,et al.  Low-Cost and Durable Bipolar Plates for Proton Exchange Membrane Electrolyzers , 2017, Scientific Reports.

[3]  Philipp Lettenmeier,et al.  Wie kommen Wind und Sonne ins Gasnetz? Pilotprojekt zur elektrolytischen Wasserstofferzeugung erfolgreich abgeschlossen , 2017 .

[4]  K. Andreas Friedrich,et al.  Improving the Activity and Stability of Ir Catalysts for PEM Electrolyzer Anodes by SnO2:Sb Aerogel Supports: Does V Addition play an Active Role in Electrocatalysis? , 2017 .

[5]  A. Bazylak,et al.  Influence of limiting throat and flow regime on oxygen bubble saturation of polymer electrolyte membrane electrolyzer porous transport layers , 2017 .

[6]  Scott T. Retterer,et al.  Investigation of thin/well-tunable liquid/gas diffusion layers exhibiting superior multifunctional performance in low-temperature electrolytic water splitting , 2017 .

[7]  Uwe Reimer,et al.  An analysis of degradation phenomena in polymer electrolyte membrane water electrolysis , 2016 .

[8]  T. Morawietz,et al.  Durable Membrane Electrode Assemblies for Proton Exchange Membrane Electrolyzer Systems Operating at High Current Densities , 2016 .

[9]  K. Friedrich,et al.  Uncovering the Stabilization Mechanism in Bimetallic Ruthenium-Iridium Anodes for Proton Exchange Membrane Electrolyzers. , 2016, The journal of physical chemistry letters.

[10]  M. Winter,et al.  Multi-Scale Correlative Tomography of a Li-Ion Battery Composite Cathode , 2016, Scientific Reports.

[11]  K. A. Friedrich,et al.  Towards developing a backing layer for proton exchange membrane electrolyzers , 2016 .

[12]  K. A. Friedrich,et al.  Protective coatings on stainless steel bipolar plates for proton exchange membrane (PEM) electrolysers , 2016 .

[13]  T. Morawietz,et al.  Nanostructured Ir-supported on Ti4O7 as a cost-effective anode for proton exchange membrane (PEM) electrolyzers. , 2016, Physical chemistry chemical physics : PCCP.

[14]  K. Friedrich,et al.  Nanosized IrO(x)-Ir Catalyst with Relevant Activity for Anodes of Proton Exchange Membrane Electrolysis Produced by a Cost-Effective Procedure. , 2016, Angewandte Chemie.

[15]  K. Pinkwart,et al.  Membrane Electrode Assemblies for Water Electrolysis using WO3‐Supported IrxRu1‐xO2 Catalysts , 2016 .

[16]  K. Friedrich,et al.  Coated Stainless Steel Bipolar Plates for Proton Exchange Membrane Electrolyzers , 2016 .

[17]  R. Schlögl,et al.  Molecular Insight in Structure and Activity of Highly Efficient, Low-Ir Ir-Ni Oxide Catalysts for Electrochemical Water Splitting (OER). , 2015, Journal of the American Chemical Society.

[18]  Matthew R. Shaner,et al.  Experimental demonstrations of spontaneous, solar-driven photoelectrochemical water splitting , 2015 .

[19]  Jiangwei Liu,et al.  Residual stresses and final deformation of an alumina coating: Modeling and measurement , 2015 .

[20]  M. Willinger,et al.  Oxide-supported IrNiO(x) core-shell particles as efficient, cost-effective, and stable catalysts for electrochemical water splitting. , 2015, Angewandte Chemie.

[21]  C. Kang,et al.  Fabrication of titanium bipolar plates by rubber forming and performance of single cell using TiN-coated titanium bipolar plates , 2014 .

[22]  Prashanth H. Jampani,et al.  Nanostructured F doped IrO2 electro-catalyst powders for PEM based water electrolysis , 2014 .

[23]  D. Bessarabov,et al.  Failure of PEM water electrolysis cells: Case study involving anode dissolution and membrane thinning , 2014 .

[24]  R. Zengerle,et al.  Tomography based screening of flow field / current collector combinations for PEM water electrolysis , 2014 .

[25]  Aleksandar R. Zeradjanin,et al.  Stability of nanostructured iridium oxide electrocatalysts during oxygen evolution reaction in acidic environment , 2014 .

[26]  Asif Ansar,et al.  Low Cost Bipolar Plates for Large Scale PEM Electrolyzers , 2014 .

[27]  J. Wallace,et al.  Feasibility study of using microfluidic platforms for visualizing bubble flows in electrolyzer gas diffusion layers , 2014 .

[28]  Pierre Millet,et al.  Electrochemical characterization of Polymer Electrolyte Membrane Water Electrolysis Cells , 2014 .

[29]  Tetsuya Yoshida,et al.  Influence of pore structural properties of current collectors on the performance of proton exchange membrane electrolyzer , 2013 .

[30]  D. Stolten,et al.  A comprehensive review on PEM water electrolysis , 2013 .

[31]  Thomas F. Jaramillo,et al.  Addressing the terawatt challenge: scalability in the supply of chemical elements for renewable energy , 2012 .

[32]  Peter Strasser,et al.  Electrocatalytic Oxygen Evolution Reaction (OER) on Ru, Ir, and Pt Catalysts: A Comparative Study of Nanoparticles and Bulk Materials , 2012 .

[33]  V. V. Lopes,et al.  Assessing cell polarity reversal degradation phenomena in PEM fuel cells by electrochemical impedance spectroscopy , 2011 .

[34]  Antonino S. Aricò,et al.  Optimization of components and assembling in a PEM electrolyzer stack , 2011 .

[35]  B. Popov,et al.  High-durability titanium bipolar plate modified by electrochemical deposition of platinum for unitized regenerative fuel cell (URFC) , 2010 .

[36]  Pierre Millet,et al.  Optimization of porous current collectors for PEM water electrolysers , 2009 .

[37]  K. Karan,et al.  Investigation of Charge-Transfer and Mass-Transport Resistances in PEMFCs with Microporous Layer Using Electrochemical Impedance Spectroscopy , 2009 .

[38]  Lorenz Holzer,et al.  Contradicting Geometrical Concepts in Pore Size Analysis Attained with Electron Microscopy and Mercury Intrusion , 2008 .

[39]  I. Baranova,et al.  Optimization of porous current collectors for PEM water electrolysers , 2006 .

[40]  R. Balzer,et al.  The bubble coverage of gas-evolving electrodes in stagnant electrolytes , 2005 .

[41]  Michael D. Abràmoff,et al.  Image processing with ImageJ , 2004 .

[42]  R. Bonnet,et al.  Modeling of the Substrate Temperature Evolution during the APS Thermal Spray Process , 2003, Thermal Spray 2003: Proceedings from the International Thermal Spray Conference.

[43]  Yann Bultel,et al.  Oxygen reduction reaction kinetics and mechanism on platinum nanoparticles inside Nafion , 2001 .

[44]  Markus Hilpert,et al.  Pore-morphology-based simulation of drainage in totally wetting porous media , 2001 .

[45]  E. Herms,et al.  Hydrogen embrittlement of 316L type stainless steel , 1999 .

[46]  A. Kornyshev,et al.  Electrochemical impedance of the cathode catalyst layer in polymer electrolyte fuel cells , 1999 .

[47]  Zeyun Yu,et al.  New algorithms in 3D image analysis and their application to the measurement of a spatialized pore size distribution in soils , 1999 .

[48]  Kornyshe Electrochemical impedance of the cathode catalyst layer in polymer electrolyte fuel cells , 1999 .

[49]  Peter Urban,et al.  Characterization of direct methanol fuel cells by ac impedance spectroscopy , 1998 .

[50]  J. Tarascon,et al.  Comparison of Modeling Predictions with Experimental Data from Plastic Lithium Ion Cells , 1996 .

[51]  H. Vogt The problem of the departure diameter of bubbles at gas-evolving electrodes , 1989 .

[52]  A. R. Troiano,et al.  Hydrogen Embrittlement of Austenitic Stainless Steel , 1965 .