2004
DOI: 10.1016/j.jpowsour.2003.11.011
|View full text |Cite
|
Sign up to set email alerts
|

Materials and design development for bipolar/end plates in fuel cells

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
2
1

Citation Types

1
89
0
1

Year Published

2009
2009
2019
2019

Publication Types

Select...
6
2

Relationship

0
8

Authors

Journals

citations
Cited by 189 publications
(91 citation statements)
references
References 8 publications
1
89
0
1
Order By: Relevance
“…Similar simulations were conducted, with the vertical length of the simulated domain H changed from 0.1 mm to 1.0 mm, and the time step Δt 1.0 x 10 -8 s. Here, the maximum pore diameter becomes about 0.3 mm and this simulates liquid water behavior in a porous separator without channels, like that recently proposed as an alternative to cells with gas flow channels [17,18]. The results in Figs.…”
Section: Liquid Water Behavior In a Porous Mediummentioning
confidence: 63%
See 1 more Smart Citation
“…Similar simulations were conducted, with the vertical length of the simulated domain H changed from 0.1 mm to 1.0 mm, and the time step Δt 1.0 x 10 -8 s. Here, the maximum pore diameter becomes about 0.3 mm and this simulates liquid water behavior in a porous separator without channels, like that recently proposed as an alternative to cells with gas flow channels [17,18]. The results in Figs.…”
Section: Liquid Water Behavior In a Porous Mediummentioning
confidence: 63%
“…The porous separator has recently been proposed as an alternative to cells with gas flow channels, and the structure without channels is expected to enable a realization of uniform reaction over the active area of the membrane electrode assembly [17,18]. Fig.…”
Section: Liquid Water and Air Flow Behavior In A Porous Separator Witmentioning
confidence: 99%
“…This can lead to large concentration gradients across the GDL and mass transfer limitations because of the small channel dimensions, laminar gas flow and the inherent slow molecular diffusion process. It is also noted that permeability reduction with the conventional machined channel design is not possible beyond a particular value (around 10 -8 m 2 ), due to difficulty in machining thin cross-section channels [5] and increased velocity and pressure drop issues [40].…”
Section: Discussionmentioning
confidence: 99%
“…The flow plate is a vital component of a PEM fuel cell and can constitute to 80% of the weight and 30% of the total cost in a fuel cell stack [5]. It supplies fuel and oxidant to reactive sites, collects produced current, removes reaction products, manages water through the cell and provides mechanical support for the cells in a stack [6].…”
Section: Introductionmentioning
confidence: 99%
“…The authors have observed phenomena related to water production behavior inside a cell, analyzed the effects on the current and temperature distributions across the reaction area [8], and reported the specific phenomena in the flow of condensed water and gas using cells with serpentine and straight channels [9]. Different from the channel and land configurations, porous flow fields have been proposed as an alternative to conventional flow channels, and a structure without channels is expected to enable realization of uniform reaction over the active area of the membrane electrode assembly [10]. Recently, performance and mass transport of a single cell with open metallic element flow field architecture have been investigated at ultra-high current densities under low humidity conditions [11].…”
Section: Introductionmentioning
confidence: 99%