scholarly journals Tailoring cations in a perovskite cathode for proton-conducting solid oxide fuel cells with high performance

2019 ◽  
Vol 7 (36) ◽  
pp. 20624-20632 ◽  
Author(s):  
Xi Xu ◽  
Huiqiang Wang ◽  
Marco Fronzi ◽  
Xianfen Wang ◽  
Lei Bi ◽  
...  

Tailoring cathode materials with cations enables an improved hydration ability and proton migration, leading to a high fuel cell performance.

Author(s):  
Kang Wang ◽  
Pingying Zeng ◽  
Jeongmin Ahn

This work presents the performance of YSZ-SDC multilayered anode-supported solid oxide fuel cell (AS-SOFC). The anode-supported SOFC showed an extraordinary fuel cell performance of ∼1.57 W/cm2 by wet spraying a SDC layer onto YSZ layer. It was found that the fuel cell performance varied with the sintering temperature of fuel cell. At the high sintering temperatures, the reactions between YSZ and SDC have a significant effect on the fuel cell performance.


RSC Advances ◽  
2021 ◽  
Vol 11 (1) ◽  
pp. 7-14
Author(s):  
Cheng Cheng Wang ◽  
Mortaza Gholizadeh ◽  
Bingxue Hou ◽  
Xincan Fan

Strontium segregation in a La0.6Sr0.4Co0.2Fe0.8O3−δ (LSCF) electrode reacts with Cr and S in a solid oxide fuel cell (SOFC), which can cause cell performance deterioration.


Author(s):  
Zongping Shao ◽  
Jennifer Mederos ◽  
Chan Kwak ◽  
Sossina M. Haile

The compound Bi2V0.9Cu0.1O5.35, a typical Aurivillius-type fast oxygen ion conductor, was evaluated as a possible cathode material for single-chamber solid-oxide fuel cells operated under mixed propane and oxygen. The material was found to be structurally stable under various C3H8+O2 environments over a wide temperature range and furthermore displayed low catalytic activity for propane oxidation. However, at temperatures above 650°C, detrimental reactions between the cathode and the ceria electrolyte occurred, producing low conductivity interfacial phases. At these high temperatures the cathode additionally underwent extensive sintering and loss of porosity and, thus, stable fuel cell operation was limited to furnace temperatures of <600°C. Even under such conditions, however, the partial oxidation occurring at the anode (a ceria nickel cermet) resulted in cell temperatures as much as 70–110°C higher than the gas-phase temperature. This explains the sharp decrease in fuel cell performance with time during operation at a furnace temperature of 586°C. Under optimized conditions, a peak power density of ∼60 mW/cm2 was obtained, which does not compete with recent values obtained from higher activity cathodes. Thus, the poor electrochemical activity of Bi2V0.9Cu0.1O5.35, combined with its chemical instability at higher temperatures, discourages further consideration of this material as a cathode in single-chamber fuel cells.


2017 ◽  
Vol 5 (48) ◽  
pp. 25641-25651 ◽  
Author(s):  
Zhihong Du ◽  
Chunlin Yan ◽  
Hailei Zhao ◽  
Yang Zhang ◽  
Chunyang Yang ◽  
...  

Y1−xCaxBaCo2O5+δ double perovskites exhibit good structural stability and excellent cell performance, making them a promising cathode for IT-SOFCs.


Author(s):  
William J. Sembler ◽  
Sunil Kumar

A typical single-cell fuel cell is capable of producing less than 1 V of direct current. Therefore, to produce the voltages required in most industrial applications, many individual fuel cells must typically be stacked together and connected electrically in series. Computational fluid dynamics (CFD) can be helpful to predict fuel-cell performance before a cell is actually built and tested. However, to perform a CFD simulation using a three-dimensional model of an entire fuel-cell stack can require a considerable amount of time and multiprocessor computing capability that may not be available to the designer. To eliminate the need to model an entire multicell assembly, a study was conducted to determine the incremental effect on fuel-cell performance of adding individual solid-oxide fuel cells (SOFCs) to a CFD model of a multicell stack. As part of this process, a series of simulations was conducted to establish a CFD-nodal density that would not only produce reasonably accurate results but could also be used to create and analyze the relatively large models of the multicell stacks. Full three-dimensional CFD models were then created of a single-cell SOFC and of SOFC stacks containing two, three, four, five, and six cells. Values of the voltages produced when operating with various current densities, together with temperature distributions, were generated for each of these CFD models. By comparing the results from each of the simulations, adjustment factors were developed to permit single-cell CFD results to be modified to estimate the performance of stacks containing multiple fuel cells. The use of these factors could enable fuel-cell designers to predict multicell stack performance using a CFD model of only a single cell.


2020 ◽  
Vol 478 ◽  
pp. 228763 ◽  
Author(s):  
Fangfang Wang ◽  
Haruo Kishimoto ◽  
Tomohiro Ishiyama ◽  
Katherine Develos-Bagarinao ◽  
Katsuhiko Yamaji ◽  
...  

Author(s):  
Kang Wang ◽  
Pingying Zeng ◽  
Jeongmin Ahn

This work presents the performance of the flame fuel cell based on the anode-supported solid oxide fuel cell (AS-SOFC) with a methane flame, which serves not only as a fuel reformer but also as a heat source to sustain the fuel cell operation. The anode-supported SOFC showed an extraordinary fuel cell performance of 475 mW/cm2 by using a methane flame. The fuel cell performance was determined by fuel cell temperature and fuel concentration which varied with the equivalent ratio and methane flow rate.


Author(s):  
Kang Wang ◽  
Pingying Zeng ◽  
James Schwartz ◽  
Jeongmin Ahn

This work presents the performance of the flame fuel cell based on the anode-supported solid oxide fuel cell (AS-SOFC) with a methane flame, which serves not only as a fuel reformer but also as a heat source to sustain the fuel cell operation. The anode-supported SOFC showed an extraordinary fuel cell performance of 475 mW.cm−2 by using a methane flame. The fuel cell performance was determined by fuel cell temperature and fuel concentration which varied with the equivalent ratio and methane flow rate.


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