A perspective on hydrogen production via high temperature steam electrolysis

High temperature (700–900 °C) steam electrolysis (HTSE) based on solid oxide electrolysis cells (SOECs) has been valued as an efficient and clean path for large scale hydrogen production with nearly zero carbon emissions, compared with the traditional paths of steammethane reforming or coal gasification. The main advantage of HTSE is that energy demand for electrolysis reaction of H2O at gaseous state is less than that for liquid state. Thermodynamically, the electricity for water splitting is reduced by 15%–25% at elevated high temperature. HTSE also serves as a solution to the energy storage problems associated with non-electric application of nuclear power and the supply-and-demand conflictions of renewable energy like wind, hydro and solar power (Figure 1) [1]. A total thermal efficiency above 50% was calculated for large scale HTSE system for hydrogen production using the heat from nuclear reactors or solar. Table 1 compares the features of different hydrogen production paths by electrolysis [2,3]. SOECs, in principle, are reversely operated SOFCs (solid oxide fuel cells), sharing similar material libraries and stack configurations [4,5]. The overall electrolysis reaction is expressed in Eq. (1). The concept was first proposed by Donitz and Erdle [6] in the 1980s as part of the “HotElly” project. However, it did not receive enough attention until 2004, when the energy crisis exacerbated and oil price increased significantly. Hydrogen production based on HTSE has been acknowledged as an important function of GEN IV

[1]  W. Dönitz,et al.  High-temperature electrolysis of water vapor—status of development and perspectives for application , 1985 .

[2]  Carl M. Stoots,et al.  HIGH-TEMPERATURE ELECTROLYSIS FOR HYDROGEN PRODUCTION FROM NUCLEAR ENERGY , 2005 .

[3]  U. Stimming,et al.  Recent anode advances in solid oxide fuel cells , 2007 .

[4]  Liu Mingyi,et al.  Thermodynamic analysis of the efficiency of high-temperature steam electrolysis system for hydrogen production , 2008 .

[5]  Chunwen Sun,et al.  Cathode materials for solid oxide fuel cells: a review , 2010 .

[6]  J. O’Brien,et al.  High-temperature electrolysis for large-scale hydrogen and syngas production from nuclear energy: summary of system simulation and economic analyses , 2010 .

[7]  Dongke Zhang,et al.  Recent progress in alkaline water electrolysis for hydrogen production and applications , 2010 .

[8]  G. Tsekouras,et al.  Step-change in high temperature steam electrolysis performance of perovskite oxide cathodes with exsolution of B-site dopants , 2013 .

[9]  Jian‐Qiang Wang,et al.  Syngas production by high temperature steam/CO2 coelectrolysis using solid oxide electrolysis cells. , 2015, Faraday discussions.

[10]  M. Romero,et al.  Part load operation of a solid oxide electrolysis system for integration with renewable energy sources , 2015 .

[11]  James E. O'Brien,et al.  Experimental design, operation, and results of a 4 kW high temperature steam electrolysis experiment , 2015 .

[12]  S. Jensen,et al.  Eliminating degradation in solid oxide electrochemical cells by reversible operation. , 2015, Nature Materials.

[13]  M. Mogensen,et al.  Ni/YSZ electrodes structures optimized for increased electrolysis performance and durability , 2016 .