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Naji, M. |
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Motta, Antonella |
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Aletan, Dirar |
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Mohamed, Tarek |
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Ertürk, Emre |
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Taccardi, Nicola |
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Kononenko, Denys |
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Petrov, R. H. | Madrid |
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Alshaaer, Mazen | Brussels |
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Bih, L. |
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Casati, R. |
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Muller, Hermance |
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Kočí, Jan | Prague |
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Šuljagić, Marija |
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Kalteremidou, Kalliopi-Artemi | Brussels |
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Azam, Siraj |
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Ospanova, Alyiya |
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Blanpain, Bart |
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Ali, M. A. |
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Popa, V. |
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Rančić, M. |
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Ollier, Nadège |
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Azevedo, Nuno Monteiro |
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Landes, Michael |
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Rignanese, Gian-Marco |
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Bjerrum, Niels Janniksen
Technical University of Denmark
in Cooperation with on an Cooperation-Score of 37%
Topics
Publications (25/25 displayed)
- 2022Pressurized solid phosphate electrolyzer for medium temperature water splittingcitations
- 2020CsH2PO4 as Electrolyte for the Formation of CH4 by Electrochemical Reduction of CO2citations
- 2016Amino-Functional Polybenzimidazole Blends with Enhanced Phosphoric Acid Mediated Proton Conductivity as Fuel Cell Electrolytescitations
- 2014Hydrogen evolution activity and electrochemical stability of selected transition metal carbides in concentrated phosphoric acidcitations
- 2014The Chemical Vapour Deposition of Tantalum - in long narrow channels
- 2014Intermediate Temperature Steam Electrolysis with Phosphate-Based Electrolytes
- 2014Development of Non-Platinum Catalysts for Intermediate Temperature Water Electrolysis
- 2014Invited: A Stability Study of Alkali Doped PBI Membranes for Alkaline Electrolyzer Cells
- 2014High Surface Area Tungsten Carbides: Synthesis, Characterization and Catalytic Activity towards the Hydrogen Evolution Reaction in Phosphoric Acid at Elevated Temperatures
- 2013Catalyst Degradation in High Temperature Proton Exchange Membrane Fuel Cells Based on Acid Doped Polybenzimidazole Membranescitations
- 2013Development and Study of Tantalum and Niobium Carbides as Electrocatalyst Supports for the Oxygen Electrode for PEM Water Electrolysis at Elevated Temperaturescitations
- 2012Nickel and its alloys as perspective materials for intermediate temperature steam electrolysers operating on proton conducting solid acids as electrolyte
- 2012WC as a non-platinum hydrogen evolution electrocatalyst for high temperature PEM water electrolyserscitations
- 2012Development of Refractory Ceramics for The Oxygen Evolution Reaction (OER) Electrocatalyst Support for Water Electrolysis at elevated temperaturescitations
- 2011Corrosion behaviour of construction materials for high temperature steam electrolyserscitations
- 2011New Construction and Catalyst Support Materials for Water Electrolysis at Elevated Temperatures
- 2011Oxidative degradation of polybenzimidazole membranes as electrolytes for high temperature proton exchange membrane fuel cellscitations
- 20101.7 nm Platinum Nanoparticles: Synthesis with Glucose Starch, Characterization and Catalysiscitations
- 2010Strategic surface topographies for enhanced lubrication in sheet forming of stainless steelcitations
- 2007Corrosion monitoring in a straw-fired power plant using an electrochemical noise probecitations
- 2005Electrochemical noise measurements of steel corrosion in the molten NaCl-K2SO4 systemcitations
- 2004Development of strategic surface topographies for lubrication in sheet forming of stainless steel
- 2001Phosphoric acid doped polybenzimidazole membranes: Physiochemical characterization and fuel cell applications [PEM fuel cells]
- 2000On the chemical nature of boundary lubrication of stainless steel by chlorine - and sulfur-containing EP-additivescitations
- 2000Cold Forging of Stainless Steel with FeCl3 based lubricants
Places of action
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document
Development of Non-Platinum Catalysts for Intermediate Temperature Water Electrolysis
Abstract
Water electrolysis is recognized as an efficient energy storage (in the form of hydrogen) supplement in renewable energy production. However, industrial alkaline water electrolyzers are rather ineffective and space requiring for a commercial use in connection with energy storage. The most effective modern water electrolyzers are based on polymeric proton-conducting membrane electrolytes (PEM), e.g. Nafion®, a perfluorocarbon-sulfonic acid polymer. These electrolyzers work at temperatures up to around 80 °C, and, in extreme cases, up to 130-140 °C. The most developed PEM electrolyzers are at the stage of commercial development. However, there is a great challenge for their widespread commercialization: high cost and low abundance of the electrocatalytic materials (Pt, IrO2) and use of Ti or other expensive construction materials. On the cathode side, the most active catalyst is Pt exhibiting the best compromise in metal-hydrogen bond strength1,2. Due to economic reasons there is a huge interest in replacing Pt by cheaper alternatives and much effort have been made in finding novel catalysts for Hydrogen Evolution Reaction (HER)3,4. Many anhydrous proton conductors have been investigated as electrolytes for the intermediate temperature applications, such as CsHSO4, KHSO45. The most successful systems have been developed with CsH2PO4 (solid acid fuel cells (SAFCs) and Sn0.9In0.1P2O7 electrolytes6,7. While developing materials for the promising medium temperature electrolysis systems it is important to simulate conditions of those presented in the assembled operational electrolyzer. In this work a molten KH2PO4 will be used as an electrolyte while screening performance of various transition metals and their carbides at higher temperature (Figure 1). In this work will be shown that coatings of transition metal carbides not only improve the stability of pure metals but also enhance electrocatalytic efficiency of materials towards HER and Oxygen Evolution Reaction (OER) at intermediate temperatures (Figure 2). The increase of the electrocatalytic activity of tungsten carbide in the electrochemical hydrogen reduction between 120 and 150 °C was recently demonstrated to be several times more intensive than for platinum8. Tests were performed at 260 °C to confirm the reported tendency. As was foreseen, at 260 °C in molten KH2PO4WC demonstrated better performance than Pt as an electrocatalyst for hydrogen evolution reaction (HER) (Figure 3). 1 J.K.. Nørskov et al. J. Electrochem. Soc., 252:J23, 2005. 2 J. Greeley, T.F. Jaramillo, J. Bonde, I. Chorkendorff, J.K. Norskov, Nat. Mater., 5:909-913, 2006. 3 N. Armaroli, V. Balzani ChemSusChem, 4:21-36, 2011. 4 I.E.L. Stephens, I Chorkendorff, Angew. Chem. Int. Ed. 50: 1476-1477, 2011 5 T. Norby, Nature, 410:877-878, 2001. 6 H. Muroyama, K. Katsukawa, T. Matsui, K. Eguchi, J Electrochem Soc, 158(9): B1072-B1075, 2011 7 P. Heo, T. Y. Kim, J. Ha, K. H. Choi, H. Chang, S. Kang, Journal of Power Sources, 198:117–121, 2012. 7 P. Heo, T. Y. Kim, J. Ha, K. H. Choi, H. Chang, S. Kang, Journal of Power Sources, 198:117–121, 2012. 8 A.V. Nikiforov et al. Int. J. Hydrogen Energy 37:18591–18597, 2012. [Formula]