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Comparative test results showed the proposed design surpasses performance of both parallel and interdigitated flow field design at operation current density of 0.7 A cm−2 or higher.
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It is found that the parallel and interdigitated flow channels are easily flooded under certain conditions.
In this study a flow field capable of switching between parallel and interdigitated configurations was designed and tested.
This study compares the cold-start performance between a parallel and interdigitated flow-field PEMFCs at various current densities.
This work will provide the cell designers with a quick guide to optimize the design parameters of the parallel and interdigitated flow field.
Parallel and interdigitated flow fields are two common types of PEMFC designs that have benefits and draw backs depending upon operating conditions.
This study investigates the effects of the relative humidity (RH) of the reactants on the cell performance and local transport phenomena in proton exchange membrane fuel cells with parallel and interdigitated flow fields.
Transient characteristics of proton exchange membrane (PEM) fuel cells with parallel and interdigitated flow fields upon changes in voltage load were investigated by applying a three-dimensional, two-phase model.
Three-dimensional models of proton exchange membrane fuel cells (PEMFCs) with parallel and interdigitated flow channel designs were developed including the effects of liquid water formation on the reactant gas transport.
A 3D numerical model was developed to explore the effects of the cathode flow channel configuration on the local transport phenomena and cell performance for parallel and interdigitated flow fields in proton exchange membrane (PEM) fuel cells.
A partially-parallel architecture, which comprises properties of both parallel and serial architectures, is also discussed.
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