The role of CuSn alloy in the co-electrolysis of CO2 and H2O through an intermediate temperature solid oxide electrolyser

Abstract A novel cermet based on CuSn-CGO is synthesized and used as a coating layer in the cathode of a conventional Solid Oxide Electrolyser for the co-electrolysis of H2O and CO2. Electrochemical experiments are carried out in the temperature range 525–600 °C by feeding reagents with a stoichiometry of 2:1 with respect to the operating current density (i.e. 150 mA cm−2). Outlet gas is analysed under OCV and operating conditions. The results are discussed in comparison with the theoretical values achievable under equilibrium. A stable electrochemical behaviour is observed in the studied temperature range. Although the performance of cell is affected by activation constraints in the temperature range 525–550 °C, minimal differences are observed with regard to the reduction kinetics of H2O and CO2. The analytical treatment of gas analysis data reveals that the coated layer promotes an increase of methane produced through the simultaneous reduction of H2O and CO2.

[1]  F. Graf,et al.  Renewable Power-to-Gas: A technological and economic review , 2016 .

[2]  S. Jensen,et al.  Hydrogen and synthetic fuel production from renewable energy sources , 2007 .

[3]  F. Tietz,et al.  Degradation phenomena in a solid oxide electrolysis cell after 9000 h of operation , 2013 .

[4]  K. Lackner,et al.  Sustainable hydrocarbon fuels by recycling CO2 and H2O with renewable or nuclear energy , 2011 .

[5]  S. Ebbesen,et al.  Co-electrolysis of CO2 and H2O in solid oxide cells: Performance and durability , 2011 .

[6]  Yong Wang,et al.  Composite ceramic cathode La0.9Ca0.1Fe0.9Nb0.1O3-δ/Sc0.2Zr0.8O2−δ towards efficient carbon dioxide electrolysis in zirconia-based high temperature electrolyser , 2017 .

[7]  V. Antonucci,et al.  New insights on the co-electrolysis of CO2 and H2O through a solid oxide electrolyser operating at intermediate temperatures , 2019, Electrochimica Acta.

[8]  David Popp,et al.  Energy, the Environment, and Technological Change , 2009 .

[9]  Chung‐Jen Tseng,et al.  Redox-reversible perovskite ferrite cathode for high temperature solid oxide steam electrolyser , 2017 .

[10]  Scott A. Barnett,et al.  A perspective on low-temperature solid oxide fuel cells , 2016 .

[11]  A. B. Gallo,et al.  Energy storage in the energy transition context: A technology review , 2016 .

[12]  M. Laguna-Bercero Recent advances in high temperature electrolysis using solid oxide fuel cells: A review , 2012 .

[13]  Joongmyeon Bae,et al.  Electrochemical performance of solid oxide electrolysis cell electrodes under high-temperature coele , 2011 .

[14]  Paul J. A. Kenis,et al.  Electrochemical conversion of CO2 to useful chemicals: current status, remaining challenges, and future opportunities , 2013 .

[15]  Peter Lund,et al.  Review of energy system flexibility measures to enable high levels of variable renewable electricity , 2015 .

[16]  Brian Vad Mathiesen,et al.  Smart Energy Systems for coherent 100% renewable energy and transport solutions , 2015 .

[17]  Peter Newell,et al.  Climate capitalism: global warming and the transformation of the global economy , 2011 .

[18]  A. Aricò,et al.  Investigation of Ni-based alloy/CGO electro-catalysts as protective layer for a solid oxide fuel cell anode fed with ethanol , 2015, Journal of Applied Electrochemistry.

[19]  T. Nejat Veziroglu,et al.  “Green” path from fossil-based to hydrogen economy: An overview of carbon-neutral technologies , 2008 .

[20]  A. Aricò,et al.  Nickel–Copper/Gadolinium‐Doped Ceria (CGO) Composite Electrocatalyst as a Protective Layer for a Solid‐Oxide Fuel Cell Anode Fed with Ethanol , 2014 .

[21]  H. Flandorfer,et al.  The Cu–Sn phase diagram, Part I: New experimental results , 2013, Intermetallics.

[22]  Hans Flandorfer,et al.  The Cu–Sn phase diagram part II: New thermodynamic assessment , 2013 .

[23]  Xiufu Sun,et al.  Durability of high performance Ni-yttria stabilized zirconia supported solid oxide electrolysis cells at high current density , 2014 .

[24]  M. Zahid,et al.  Long Term Testing of Short Stacks with Solid Oxide Cells for Water Electrolysis , 2011 .

[25]  N. Brandon,et al.  Hydrogen production through steam electrolysis: Model-based steady state performance of a cathode-supported intermediate temperature solid oxide electrolysis cell , 2007 .

[26]  A. Owen,et al.  Renewable energy: Externality costs as market barriers , 2006 .

[27]  A. Aricò,et al.  Ni-Cu based catalysts prepared by two different methods and their catalytic activity toward the ATR of methane , 2015 .

[28]  V. Antonucci,et al.  Production of syngas by solid oxide electrolysis: A case study , 2017 .