Abstract
Literature data on the promotional role of under-rib convection for polymer electrolyte membrane fuel cells (PEMFCs) fueled by hydrogen and methanol are structured and analyzed, with the aim of providing a guide to improve fuel cell performance through the optimization of flow-field interaction. Data are presented for both physical and electrochemical performance showing reactant mass transport, electrochemical reaction, water behavior, and power density enhanced by under-rib convection. Performance improvement studies ranging from single cell to stack are presented for measuring the performance of real operating conditions and large-scale setups. The flow-field optimization techniques by under-rib convection are derived from the collected data over a wide range of experiments and modeling studies with a variety of components including both single cell and stack arrangements. Numerical models for PEMFCs are presented with an emphasis on mass transfer and electrochemical reaction inside the fuel cell. The models are primarily used here as a tool in the parametric analysis of significant design features and to permit the design of the experiment. Enhanced flow-field design that utilizes the promotional role of under-rib convection can contribute to commercializing PEMFCs.
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Abbreviations
- \(\Delta p_{\text{tot}}\) :
-
Total pressure drop
- z max :
-
Total length of the path
- K ch :
-
Channel permeability derived from the Hagen–Poiseuille equation
- \(\Delta c_{\text{tot}}\) :
-
Total concentration loss
- q rib :
-
Under-rib convection flowrate
- K gdl :
-
Flow permeability of the GDL
- \(\overline{{\dot{v}}}_{\text{spec}}\) :
-
Mean specific volume flow
- \(\dot{V}\) :
-
Inlet volume flow
- \(\dot{V}_{\text{local}}^{\text{meander}}\) :
-
Integral of the local volume flow (l/h)
- \(\overline{{\dot{v}}}_{\text{spec}}^{\text{meander}}\) :
-
Specific volume flow in the meander channel
- \(\overline{{\dot{v}}}_{\text{spec}}^{\text{diff}}\) :
-
Total specific flow through the diffusion layer
- P cell :
-
Cell output power density
- W P :
-
Pressure drop loss
- AFC:
-
Alkaline fuel cell
- BOP:
-
Balance of plant
- CFD:
-
Computational fluid dynamic
- CL:
-
Catalyst layer
- DMFC:
-
Direct methanol fuel cell
- EIS:
-
Electrochemical impedance spectroscopy
- GDL:
-
Gas diffusion layer
- GFF:
-
Grid flow-field
- MCFC:
-
Molten carbonate fuel cell
- MEA:
-
Membrane electrolyte assembly
- MFF:
-
Original design mixed parallel and serpentine
- MPL:
-
Microporous gas diffusion layer
- MSFF:
-
Multi-serpentine
- OCV:
-
Open-circuit voltages, E0
- ORR:
-
Oxygen reduction reaction
- PAFC:
-
Phosphoric acid fuel cell
- PEMFC:
-
Polymer electrolyte membrane fuel cell
- PFF:
-
Parallel flow-field
- PTFE:
-
Polytetrafluoroethylene
- SFF:
-
Single serpentine
- SSFF:
-
Single serpentine flow-field
- SOFC:
-
Solid oxide fuel cell
- VOF:
-
Volume of fluid
- q tot :
-
Total flow rate
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Kim, HM., Nguyen, V.D. (2017). Electrochemical Promotional Role of Under-Rib Convection-Based Flow-Field in Polymer Electrolyte Membrane Fuel Cells. In: Inamuddin, D., Mohammad, A., Asiri, A. (eds) Organic-Inorganic Composite Polymer Electrolyte Membranes. Springer, Cham. https://doi.org/10.1007/978-3-319-52739-0_10
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DOI: https://doi.org/10.1007/978-3-319-52739-0_10
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