2004
DOI: 10.1016/j.jpowsour.2003.11.089
|View full text |Cite
|
Sign up to set email alerts
|

CFD simulation tool for solid oxide fuel cells

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

1
70
2
1

Year Published

2006
2006
2017
2017

Publication Types

Select...
8
2

Relationship

1
9

Authors

Journals

citations
Cited by 96 publications
(74 citation statements)
references
References 5 publications
1
70
2
1
Order By: Relevance
“…Numerous SOFC models considering the intricate interdependency among ionic and electronic conduction, gas transport phenomena, and electrochemical processes have been reported in the literatures for pure hydrogen, syngas or methane [10][11][12][13][14][15][16][17][18][19][20]. Hecht et al [21] further reported a multi-step heterogeneous elementary reaction mechanism for CH 4 reforming using Ni as catalyst.…”
Section: Dcfcmentioning
confidence: 99%
“…Numerous SOFC models considering the intricate interdependency among ionic and electronic conduction, gas transport phenomena, and electrochemical processes have been reported in the literatures for pure hydrogen, syngas or methane [10][11][12][13][14][15][16][17][18][19][20]. Hecht et al [21] further reported a multi-step heterogeneous elementary reaction mechanism for CH 4 reforming using Ni as catalyst.…”
Section: Dcfcmentioning
confidence: 99%
“…The gas inlet pressure was 13 psi, which can be converted to a gas velocity of 289 m·s ¹1 with an initial gas temperature of 278.15 K. The cooling air inlet velocity was 300 m·s ¹1 with a constant temperature of 278.15 K, and the sample temperature was initially set to be 523.15 K. Using the volume-weighted mixing law for individual heat capacities, the heat capacity of the mixture can be determined. 25 …”
Section: Numerical Detailsmentioning
confidence: 99%
“…The gas inlet pressure was 13 psi and it was converted to the velocity of 289 m/s with initial gas temperature of 278.15 K. The cooling air inlet velocity was 300 m/s with constant temperature of 278.15 K and the sample temperature was initially 523.15 K. Using the volume weighted mixing law of individual heat capacities, the heat capacity of the mixture is calculated. 22,23) For the combustion model, we used the chemical reaction formulae of 2C 2 H 2 + 5O 2 ! 4CO 2 + 2H 2 O and the global reaction.…”
Section: Numerical Detailsmentioning
confidence: 99%