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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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Chatzichristodoulou, Christodoulos
Technical University of Denmark
in Cooperation with on an Cooperation-Score of 37%
Topics
Publications (37/37 displayed)
- 2024Operando Electron Microscopy and Impedance Analysis of Solid Oxide Electrolysis and Fuel Cellscitations
- 2021Development of high-temperature electrochemical TEM and its application on solid oxide electrolysis cells
- 2021Development of high-temperature electrochemical TEM and its application on solid oxide electrolysis cells
- 2020Polysulfone-polyvinylpyrrolidone blend membranes as electrolytes in alkaline water electrolysiscitations
- 2020(Invited) Advanced Alkaline Electrolysis Cells for the Production of Sustainable Fuels and Chemicals
- 2017Oxygen transport properties of tubular Ce 0.9 Gd 0.1 O 1.95 -La 0.6 Sr 0.4 FeO 3−d composite asymmetric oxygen permeation membranes supported on magnesium oxidecitations
- 2017Ionic/Electronic Conductivity, Thermal/Chemical Expansion and Oxygen Permeation in Pr and Gd Co-Doped Ceria PrxGd0.1Ce0.9-xO1.95-δcitations
- 2017Chemical and Electrochemical Properties of La0.58Sr0.4Fe0.8Co0.2O3-δ (LSCF) Thin Films upon Oxygen Reduction and Evolution Reactions
- 2017Oxygen transport properties of tubular Ce0.9Gd0.1O1.95-La0.6Sr0.4FeO3−d composite asymmetric oxygen permeation membranes supported on magnesium oxidecitations
- 2016Relaxation of stresses during reduction of anode supported SOFCs
- 2016High Temperature and Pressure Alkaline Electrochemical Reactor for Conversion of Power to Chemicals
- 2016Evolution of the electrochemical interface in high-temperature fuel cells and electrolyserscitations
- 2016Design and optimization of porous ceramic supports for asymmetric ceria-based oxygen transport membranescitations
- 2016Design and optimization of porous ceramic supports for asymmetric ceria-based oxygen transport membranescitations
- 2016New Hypothesis for SOFC Ceramic Oxygen Electrode Mechanismscitations
- 2016High Temperature Alkaline Electrolysis Cells with Metal Foam Based Gas Diffusion Electrodescitations
- 2015Size of oxide vacancies in fluorite and perovskite structured oxidescitations
- 2015Need for In Operando Characterization of Electrochemical Interface Features
- 2015Kinetics of CO/CO 2 and H 2 /H 2 O reactions at Ni-based and ceria-based solid-oxide-cell electrodescitations
- 2014Composite Fe - BaCe0.2Zr0.6Y0.2O2.9 Anodes for Proton Conductor Fuel Cellscitations
- 2014Composite Fe - BaCe 0.2 Zr 0.6 Y 0.2 O 2.9 Anodes for Proton Conductor Fuel Cellscitations
- 2014Power to fuel using electrolysis and CO2 capture
- 2014TOF-SIMS characterization of impurity enrichment and redistribution in solid oxide electrolysis cells during operationcitations
- 2014High performance and highly durable infiltrated cathodes using Pr-modified Ce0.9Gd0.1O1.95 backbone
- 2014High performance and highly durable infiltrated cathodes using Pr-modified Ce 0.9 Gd 0.1 O 1.95 backbone
- 2013Defect chemistry, thermomechanical and transport properties of (RE2−xSrx)0.98(Fe0.8Co0.2)1−yMgyO4−δ (RE = La, Pr)citations
- 2013Pressurized HxCyOz Cells at ca. 250 °C: Potential and Challenges
- 2013Infiltration of ionic-, electronic- and mixed-conducting nano particles into La0.75Sr0.25MnO3–Y0.16Zr0.84O2 cathodes – A comparative study of performance enhancement and stability at different temperaturescitations
- 2013High temperature and pressure alkaline electrolysis
- 2013Alkaline electrolysis cell at high temperature and pressure of 250 °C and 42 barcitations
- 2013Pressurized H x C y O z Cells at ca. 250 °C: Potential and Challenges
- 2013Defect chemistry, thermomechanical and transport properties of (RE 2 - x Sr x ) 0.98 (Fe 0.8 Co 0.2 ) 1 - y Mg y O 4 - δ (RE = La, Pr)citations
- 2013Infiltration of ionic-, electronic- and mixed-conducting nano particles into La 0.75 Sr 0.25 MnO 3 –Y 0.16 Zr 0.84 O 2 cathodes – A comparative study of performance enhancement and stability at different temperaturescitations
- 2012Characterization of impregnated GDC nano structures and their functionality in LSM based cathodescitations
- 2011Evaluation of thin film ceria membranes for syngas membrane reactors—Preparation, characterization and testingcitations
- 2010Oxygen Nonstoichiometry and Defect Chemistry Modeling of Ce0.8Pr0.2O2-deltacitations
- 2010Defect Chemistry and Thermomechanical Properties of Ce0.8PrxTb0.2-xO2-deltacitations
Places of action
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document
Pressurized HxCyOz Cells at ca. 250 °C: Potential and Challenges
Abstract
The increasing need for easy and affordable storage of intermittent renewable energy has encouraged us to explore the possibilities of pressurized electrolysis and fuel cells operating in the temperature range of 200 – 300 °C and pressure from a few bar up to 50 bar and above. Most electrochemical rate limiting processes are strongly thermal activated. Also, increased pressure may increase the electrode reaction rates. High pressure means increase energy density in gaseous products. Furthermore, as hydrocarbons, alcohols or ethers - in common denoted HxCyOz - are very convenient fuels, we have focus on cells that may have a potential of forming or using HxCyOz in electrolysis or fuel cell mode, respectively. Examples of HxCyOz are hydrogen with (x,y,z) = (2,0,0), carbon monoxide with (x,y,z) = (0,1,1),methane with (x,y,z) = (4,1,0),gasoline with approximately (x,y,z) = (18,8,0), methanol with (x,y,z) = (4,1,1), and dimethyl ether (DME) with (x,y,z) = (6,2,1). The temperature about 200 – 300 °C is of particular interest because if the direct electrochemical reduction products from electrolysis of H2O and CO2 mixtures are H2 and CO (syngas) then this temperature together with increased pressure makes it potentially possible to convert the syngas into HxCyOz inside the cathode compartment using suitable catalysts, because such conditions are very similar to the commercial catalysis technology used by chemical industry.<br/>A brief review of some literature behind this strategic thinking is given, followed by examples of results from our own laboratory. So far the concept of high temperature and pressure electrolysis has proven successful on small scale using button cell with KOH(aq.) electrolyte immobilized in a porous ceramic layer. Also cells using immobilized K2CO3(aq.), CsH2PO4 solid acid, and BaZr1-u-vCeuYvO3-δ proton conducting electrolytes have been constructed and tested. Reduction of CO2 seems significantly more difficult than reduction of H2O. This and many other challenges appear from our work. <br/>The apparent challenges and the potential benefits that make it worthwhile to overcome the challenges are discussed and some main arguments in favor of continuing this strategy are presented.