2006
DOI: 10.1016/j.jpowsour.2006.03.044
|View full text |Cite
|
Sign up to set email alerts
|

Dynamic modeling of proton exchange membrane fuel cell using non-integer derivatives

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1
1

Citation Types

0
46
0

Year Published

2009
2009
2023
2023

Publication Types

Select...
9

Relationship

1
8

Authors

Journals

citations
Cited by 70 publications
(46 citation statements)
references
References 18 publications
0
46
0
Order By: Relevance
“…By substituting Equation (19) for Equations (29) and (31) and using variable heat resistance (R t ), the equivalence of which is determined by the heat transfer coefficient inverse (H t ), the equation for the FC operating temperature is obtained:…”
Section: Final Configuration Of the Thermal Modelmentioning
confidence: 99%
“…By substituting Equation (19) for Equations (29) and (31) and using variable heat resistance (R t ), the equivalence of which is determined by the heat transfer coefficient inverse (H t ), the equation for the FC operating temperature is obtained:…”
Section: Final Configuration Of the Thermal Modelmentioning
confidence: 99%
“…7. Both electrodes (anode and cathode) are presented with Randles models and are connected in series with the internal resistance R m linked to the membrane [26,27]. In Fig.…”
Section: Poor Water Managementmentioning
confidence: 99%
“…The physical model used to obtain the following governing equation for PEMFC responses is based on a previous d.c. and a.c. model [20]. In the absence of mass transport limitation, the electrochemical reaction is simply represented by an equivalent electrical circuit of parallel RC cells.…”
Section: Experimental Set-up and Modellingmentioning
confidence: 99%