Performance comparison of the mass transfer models with internal reforming for solid oxide fuel cell anodes

2012 ◽  
Vol 55 (15-16) ◽  
pp. 3933-3945 ◽  
Author(s):  
Shuping Wang ◽  
William M. Worek ◽  
W.J. Minkowycz
2005 ◽  
Vol 127 (1) ◽  
pp. 86-90 ◽  
Author(s):  
Eric A. Liese ◽  
Randall S. Gemmen

Solid Oxide Fuel Cell (SOFC) developers are presently considering both internal and external reforming fuel cell designs. Generally, the endothermic reforming reaction and excess air through the cathode provide the cooling needed to remove waste heat from the fuel cell. Current information suggests that external reforming fuel cells will require a flow rate twice the amount necessary for internal reforming fuel cells. The increased airflow could negatively impact system performance. This paper compares the performance among various external reforming hybrid configurations and an internal reforming hybrid configuration. A system configuration that uses the reformer to cool a cathode recycle stream is introduced, and a system that uses interstage external reforming is proposed. Results show that the thermodynamic performance of these proposed concepts are an improvement over a base-concept external approach, and can be better than an internal reforming hybrid system, depending on the fuel cell cooling requirements.


2011 ◽  
Vol 196 (6) ◽  
pp. 3089-3094 ◽  
Author(s):  
David M. Bierschenk ◽  
Elizabeth Potter-Nelson ◽  
Cathleen Hoel ◽  
Yougui Liao ◽  
Laurence Marks ◽  
...  

2009 ◽  
Vol 193 (2) ◽  
pp. 706-712 ◽  
Author(s):  
Daniel Storjohann ◽  
James Daggett ◽  
Neal P. Sullivan ◽  
Huayang Zhu ◽  
Robert J. Kee ◽  
...  

2021 ◽  
Vol 35 (18) ◽  
pp. 15084-15093
Author(s):  
Md Raziun Bin Mamtaz ◽  
Zheng Wang ◽  
Alessio Belotti ◽  
Emanuele Quattrocchi ◽  
Jing Yu ◽  
...  

2005 ◽  
Vol 2 (2) ◽  
pp. 136-140 ◽  
Author(s):  
Eric S. Greene ◽  
Maria G. Medeiros ◽  
Wilson K. S. Chiu

A one-dimensional model of chemical and mass transport phenomena in the porous anode of a solid-oxide fuel cell, in which there is internal reforming of methane, is presented. Macroscopically averaged porous electrode theory is used to model the mass transfer that occurs in the anode. Linear kinetics at a constant temperature are used to model the reforming and shift reactions. Correlations based on the Damkohler number are created to relate anode structural parameters and thickness to a nondimensional electrochemical conversion rate and cell voltage. It is shown how these can be applied in order to assist the design of an anode.


2019 ◽  
Vol 131 ◽  
pp. 1032-1051 ◽  
Author(s):  
Maciej Chalusiak ◽  
Michal Wrobel ◽  
Marcin Mozdzierz ◽  
Katarzyna Berent ◽  
Janusz S. Szmyd ◽  
...  

Fuel Cells ◽  
2016 ◽  
Vol 16 (2) ◽  
pp. 219-234 ◽  
Author(s):  
G. B. Johnson ◽  
P. Hjalmarsson ◽  
K. Norrman ◽  
U. S. Ozkan ◽  
A. Hagen

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