Mathematical Modeling of Polymer Exchange Membrane Fuel Cells

Fuel cells are predicted to be the power delivery devices of the future. They have many advantages such as the wide fuel selection, high energy density, high efficiency and an inherent safety which explains the immense interest in this power source. The need for advanced designs has been limited by...

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Main Author: Spiegel, Colleen
Format: Others
Published: Scholar Commons 2008
Subjects:
Online Access:https://scholarcommons.usf.edu/etd/510
https://scholarcommons.usf.edu/cgi/viewcontent.cgi?article=1509&context=etd
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spelling ndltd-USF-oai-scholarcommons.usf.edu-etd-15092019-10-04T05:18:43Z Mathematical Modeling of Polymer Exchange Membrane Fuel Cells Spiegel, Colleen Fuel cells are predicted to be the power delivery devices of the future. They have many advantages such as the wide fuel selection, high energy density, high efficiency and an inherent safety which explains the immense interest in this power source. The need for advanced designs has been limited by the lack of understanding of the transport processes inside the fuel cell stack. The reactant gases undergo many processes in a fuel cell that cannot be observed. Some of these processes include convective and diffusional mass transport through various types of materials, phase change and chemical reaction. In order to optimize these variables, an accurate mathematical model can provide a valuable tool to gain insight into the processes that are occurring. The goal of this dissertation is to develop a mathematical model for polymer electrolyte-based fuel cells to help contribute to a better understanding of fuel cell mass, heat and charge transport phenomena, to ultimately design more efficient fuel cells. The model is a two-phase, transient mathematical model created with MATLAB. The model was created by using each fuel cell layer as a control volume. In addition, each fuel cell layer was further divided into the number of nodes that the user inputs into the model. Transient heat and mass transfer equations were created for each node. The catalyst layers were modeled using porous electrode equations and the Butler-Volmer equation. The membrane model used Fick's law of diffusion and a set of empirical relations for water uptake and conductivity. Additional work performed for this dissertation includes a mathematical model for predicting bolt torque, and the design and fabrication of four fuel cell stacks ranging in size from macro to micro scale for model validation. The work performed in this dissertation will help improve the designs of polymer electrolyte fuel cells, and other polymer membrane-based fuel cells (such as direct methanol fuel cells) in the future. 2008-11-04T08:00:00Z text application/pdf https://scholarcommons.usf.edu/etd/510 https://scholarcommons.usf.edu/cgi/viewcontent.cgi?article=1509&context=etd default Graduate Theses and Dissertations Scholar Commons PEM fuel cell Flow field Thermal model Microchannels American Studies Arts and Humanities
collection NDLTD
format Others
sources NDLTD
topic PEM fuel cell
Flow field
Thermal model
Microchannels
American Studies
Arts and Humanities
spellingShingle PEM fuel cell
Flow field
Thermal model
Microchannels
American Studies
Arts and Humanities
Spiegel, Colleen
Mathematical Modeling of Polymer Exchange Membrane Fuel Cells
description Fuel cells are predicted to be the power delivery devices of the future. They have many advantages such as the wide fuel selection, high energy density, high efficiency and an inherent safety which explains the immense interest in this power source. The need for advanced designs has been limited by the lack of understanding of the transport processes inside the fuel cell stack. The reactant gases undergo many processes in a fuel cell that cannot be observed. Some of these processes include convective and diffusional mass transport through various types of materials, phase change and chemical reaction. In order to optimize these variables, an accurate mathematical model can provide a valuable tool to gain insight into the processes that are occurring. The goal of this dissertation is to develop a mathematical model for polymer electrolyte-based fuel cells to help contribute to a better understanding of fuel cell mass, heat and charge transport phenomena, to ultimately design more efficient fuel cells. The model is a two-phase, transient mathematical model created with MATLAB. The model was created by using each fuel cell layer as a control volume. In addition, each fuel cell layer was further divided into the number of nodes that the user inputs into the model. Transient heat and mass transfer equations were created for each node. The catalyst layers were modeled using porous electrode equations and the Butler-Volmer equation. The membrane model used Fick's law of diffusion and a set of empirical relations for water uptake and conductivity. Additional work performed for this dissertation includes a mathematical model for predicting bolt torque, and the design and fabrication of four fuel cell stacks ranging in size from macro to micro scale for model validation. The work performed in this dissertation will help improve the designs of polymer electrolyte fuel cells, and other polymer membrane-based fuel cells (such as direct methanol fuel cells) in the future.
author Spiegel, Colleen
author_facet Spiegel, Colleen
author_sort Spiegel, Colleen
title Mathematical Modeling of Polymer Exchange Membrane Fuel Cells
title_short Mathematical Modeling of Polymer Exchange Membrane Fuel Cells
title_full Mathematical Modeling of Polymer Exchange Membrane Fuel Cells
title_fullStr Mathematical Modeling of Polymer Exchange Membrane Fuel Cells
title_full_unstemmed Mathematical Modeling of Polymer Exchange Membrane Fuel Cells
title_sort mathematical modeling of polymer exchange membrane fuel cells
publisher Scholar Commons
publishDate 2008
url https://scholarcommons.usf.edu/etd/510
https://scholarcommons.usf.edu/cgi/viewcontent.cgi?article=1509&context=etd
work_keys_str_mv AT spiegelcolleen mathematicalmodelingofpolymerexchangemembranefuelcells
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