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Effects of Cell Temperature and Reactant Humidification on Anion Exchange Membrane Fuel Cells
The performance of an anion exchange membrane fuel cell (AEMFC) under various operating conditions, including cell temperature and humidification of inlet gases, was systematically investigated in this study. The experimental results indicate that the power density of an AEMFC is susceptible to the...
Autores principales: | , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
MDPI
2019
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6650884/ https://www.ncbi.nlm.nih.gov/pubmed/31247928 http://dx.doi.org/10.3390/ma12132048 |
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author | Truong, Van Men Duong, Ngoc Bich Wang, Chih-Liang Yang, Hsiharng |
author_facet | Truong, Van Men Duong, Ngoc Bich Wang, Chih-Liang Yang, Hsiharng |
author_sort | Truong, Van Men |
collection | PubMed |
description | The performance of an anion exchange membrane fuel cell (AEMFC) under various operating conditions, including cell temperature and humidification of inlet gases, was systematically investigated in this study. The experimental results indicate that the power density of an AEMFC is susceptible to the cell temperature and inlet gas humidification. A high performance AEMFC can be achieved by elevating the cell operating temperature along with the optimization of the gas feed dew points at the anode and cathode. As excess inlet gas humidification at the anode is supplied, the flooding is less severe at a higher cell temperature because the water transport in the gas diffusion substrate by evaporation is more effective upon operation at a higher cell temperature. The cell performance is slightly affected when the humidification at the anode is inadequate, owing to dehydration of the membrane, especially at a higher cell temperature. Furthermore, the cell performance in conditions of under-humidification or over-humidification at the cathode is greatly reduced at the different cell temperatures tested due to the dehydration of the anion exchange membrane and the water shortage or oxygen mass transport limitations, respectively, for the oxygen reduction reaction. In addition, back diffusion could partly support the water demand at the cathode once a water concentration gradient between the anode and cathode is formed. These results, in which sophisticated water management was achieved, can provide useful information regarding the development of high-performance AEMFC systems. |
format | Online Article Text |
id | pubmed-6650884 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2019 |
publisher | MDPI |
record_format | MEDLINE/PubMed |
spelling | pubmed-66508842019-08-07 Effects of Cell Temperature and Reactant Humidification on Anion Exchange Membrane Fuel Cells Truong, Van Men Duong, Ngoc Bich Wang, Chih-Liang Yang, Hsiharng Materials (Basel) Article The performance of an anion exchange membrane fuel cell (AEMFC) under various operating conditions, including cell temperature and humidification of inlet gases, was systematically investigated in this study. The experimental results indicate that the power density of an AEMFC is susceptible to the cell temperature and inlet gas humidification. A high performance AEMFC can be achieved by elevating the cell operating temperature along with the optimization of the gas feed dew points at the anode and cathode. As excess inlet gas humidification at the anode is supplied, the flooding is less severe at a higher cell temperature because the water transport in the gas diffusion substrate by evaporation is more effective upon operation at a higher cell temperature. The cell performance is slightly affected when the humidification at the anode is inadequate, owing to dehydration of the membrane, especially at a higher cell temperature. Furthermore, the cell performance in conditions of under-humidification or over-humidification at the cathode is greatly reduced at the different cell temperatures tested due to the dehydration of the anion exchange membrane and the water shortage or oxygen mass transport limitations, respectively, for the oxygen reduction reaction. In addition, back diffusion could partly support the water demand at the cathode once a water concentration gradient between the anode and cathode is formed. These results, in which sophisticated water management was achieved, can provide useful information regarding the development of high-performance AEMFC systems. MDPI 2019-06-26 /pmc/articles/PMC6650884/ /pubmed/31247928 http://dx.doi.org/10.3390/ma12132048 Text en © 2019 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (http://creativecommons.org/licenses/by/4.0/). |
spellingShingle | Article Truong, Van Men Duong, Ngoc Bich Wang, Chih-Liang Yang, Hsiharng Effects of Cell Temperature and Reactant Humidification on Anion Exchange Membrane Fuel Cells |
title | Effects of Cell Temperature and Reactant Humidification on Anion Exchange Membrane Fuel Cells |
title_full | Effects of Cell Temperature and Reactant Humidification on Anion Exchange Membrane Fuel Cells |
title_fullStr | Effects of Cell Temperature and Reactant Humidification on Anion Exchange Membrane Fuel Cells |
title_full_unstemmed | Effects of Cell Temperature and Reactant Humidification on Anion Exchange Membrane Fuel Cells |
title_short | Effects of Cell Temperature and Reactant Humidification on Anion Exchange Membrane Fuel Cells |
title_sort | effects of cell temperature and reactant humidification on anion exchange membrane fuel cells |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6650884/ https://www.ncbi.nlm.nih.gov/pubmed/31247928 http://dx.doi.org/10.3390/ma12132048 |
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