Efficiency and stability of hydrogen production from seawater using solid oxide electrolysis cells

2021 ◽  
Vol 300 ◽  
pp. 117439
Author(s):  
Zhao Liu ◽  
Beibei Han ◽  
Zhiyi Lu ◽  
Wanbing Guan ◽  
Yuanyuan Li ◽  
...  
2013 ◽  
Vol 57 (1) ◽  
pp. 3099-3104 ◽  
Author(s):  
K. J. Yoon ◽  
J.-W. Son ◽  
J.-H. Lee ◽  
B.-K. Kim ◽  
H.-J. Je ◽  
...  

2019 ◽  
Vol 10 (1) ◽  
Author(s):  
Hiroyuki Shimada ◽  
Toshiaki Yamaguchi ◽  
Haruo Kishimoto ◽  
Hirofumi Sumi ◽  
Yuki Yamaguchi ◽  
...  

AbstractSolid oxide electrolysis cells can theoretically achieve high energy-conversion efficiency, but current density must be further increased to improve the hydrogen production rate, which is essential to realize widespread application. Here, we report a structure technology for solid oxide electrolysis cells to achieve a current density higher than 3 A cm−2, which exceeds that of state-of-the-art electrolyzers. Bimodal-structured nanocomposite oxygen electrodes are developed where nanometer-scale Sm0.5Sr0.5CoO3−δ and Ce0.8Sm0.2O1.9 are highly dispersed and where submicrometer-scale particles form conductive networks with broad pore channels. Such structure is realized by fabricating the electrode structure from the raw powder material stage using spray pyrolysis. The solid oxide electrolysis cells with the nanocomposite electrodes exhibit high current density in steam electrolysis operation (e.g., at 1.3 V), reaching 3.13 A cm−2 at 750 °C and 4.08 A cm−2 at 800 °C, corresponding to a hydrogen production rate of 1.31 and 1.71 L h−1 cm−2 respectively.


Author(s):  
J. E. O’Brien ◽  
C. M. Stoots ◽  
J. S. Herring ◽  
P. A. Lessing

An experimental study has been completed to assess the hydrogen-production performance of single solid-oxide electrolysis cells operating over a temperature range of 800 to 900°C. The experiments were performed over a range of steam inlet partial pressures (2.3 – 12.2 kPa), carrier gas flow rates (50–200 sccm), and current densities (−0.75 to 0.25 A/cm2) using single electrolyte-supported button cells of scandia-stabilized zirconia. Steam consumption rates associated with electrolysis were measured directly using inlet and outlet dewpoint instrumentation. Cell operating potentials and cell current were varied using a programmable power supply. Values of area-specific resistance and hydrogen production rate are presented as a function of current density. Cell performance is shown to be continuous from the fuel-cell mode to the electrolysis mode of operation. The effects of steam starvation and thermal cycling on cell performance parameters are discussed. Laboratory capabilities are currently being expanded to allow for testing and characterization of multiple-cell electrolysis stacks. Some fundamental differences between the fuel-cell and electrolysis modes of operation have been summarized.


2019 ◽  
Vol 25 (2) ◽  
pp. 1015-1020 ◽  
Author(s):  
Tohru Kato ◽  
Nobutaka Sakaki ◽  
Akira Negishi ◽  
Takeo Honda ◽  
Lan Nguyen ◽  
...  

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