2011
DOI: 10.1002/9781118144527.ch10
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Effect of Fuel Impurity on Structural Integrity of Ni‐YSZ Anode of SOFCs

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Cited by 2 publications
(2 citation statements)
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“…Efforts to lower the degradation rates further (to ∼0.5%/1000 h) while achieving longer (5000 h and beyond) endurance periods are part of the technology development. Initial work is in progress to identify the SOFC tolerance limits to contaminants present in the coal syngas. To achieve an initial target for SOFC module life of 40000 h, a sulfur specification of 30 ppbv has been assumed for this analysis. However, this specification is subject to change as additional insights to the SOFC anode contaminant analysis are gained.…”
Section: Igfc Power Plant System Developmentmentioning
confidence: 99%
“…Efforts to lower the degradation rates further (to ∼0.5%/1000 h) while achieving longer (5000 h and beyond) endurance periods are part of the technology development. Initial work is in progress to identify the SOFC tolerance limits to contaminants present in the coal syngas. To achieve an initial target for SOFC module life of 40000 h, a sulfur specification of 30 ppbv has been assumed for this analysis. However, this specification is subject to change as additional insights to the SOFC anode contaminant analysis are gained.…”
Section: Igfc Power Plant System Developmentmentioning
confidence: 99%
“…[8][9][10][11] Therefore, a system of coupling a gasifier producing bio-syngas and SOFCs has been suggested by many authors with their simulation works, [12][13][14][15] tested with simulated syngas [16][17][18][19][20] and with actual bio-syngas. [21][22][23] A system using actual bio-syngas needs an additional reformer for cleaning the bio-syngas because it includes impurities such as tars, [16][17][18][19][20] sulfur, [24][25][26] and phosphorus 27,28 causing significant mechanical and electrochemical degradation. This additional reformer makes the system more complex and expensive.…”
mentioning
confidence: 99%