The solid oxide electrolyser (SOE) is an electrochemical membrane reactor based upon oxygen ion conducting ceramic electrolyte which can efficiently produce syn-gas (mixture of H2 and CO) as a feedstock for synthesis of liquid fuels. SOEs can be thermally integrated to liquid fuel synthesis reactors which boosts the overall efficiency of the system with heat input from an exothermic fuel synthesis reaction used in the SOE. The total synthesis and transport efficiencies of such integrated system can be above 75 % with cost in the range of US$ 0.8 to 0.9 per litre of the fuel using well established existing fuel transportation infrastructure.[iv]
Traditionally, yttria stabilised zirconia (YSZ) electrolytes are used in SOE with Ni-YSZ cermet electrodes for splitting of CO2 and H2O on cathode side (negative electrode) and a perovskite La0.80Sr0.20MnO3 (LSM) is used to facilitate oxygen evolution reaction on the anode side (positive electrode). While Ni-YSZ electrodes have demonstrated excellent compatibility with YSZ electrolytes and sufficient catalytic activity as a fuel cell electrode, its application in solid oxide electrolyser typically requires additional external supply of hydrogen as a reducing gas along with steam and CO2 mixtures. Further, redox and thermal stability of Ni-YSZ cathodes could be of a concern considering intermittent nature of renewable energy sources. Thus, alternative electrodes such as ceramic perovskites and ceramic-Ag composites are under development as an alternative to Ni-YSZ cathode.
In this presentation, an overview of the development work at CSIRO (Australia) and Ben Gurion University at Negev (Israel) would be presented along with the experimental data on the electrochemical performance of various ceramic and composite cathodes. Some of these newly developed cathodes have demonstrated excellent electrochemical performance with an operating voltage close to 1.25 V providing current densities up to 350 mA/cm2 in robust and scalable electrolyte supported cells, with 80% CO2-H2O conversion to syngas in a single pass at 800° C for over 500 h of operation. The presentation will also compare the energy efficiencies of the cells with different cathodes based upon the product energy content. The advantages/disadvantages of using alternative electrodes would be also elaborated based upon initial assessment.
References:
[i] REN21 Renewables Global Status Report, 2017.
[ii] Final Report: Hydrogen Storage System Cost Analysis, Strategic Analysis Inc for US DOE, September 2016.
[iii] Global Greenhouse Gas Emissions Data, US EPA, January 2010.
[iv] Syngas Production By Coelectrolysis of CO2/H2O: The Basis for a Renewable Energy Cycle, Energy Fuels, 23 (6), pp 3089–3096, DOI: 10.1021/ef900111f, 2010.