Combined thermal characteristics analysis of steam reforming and combustion for 5 kW domestic PEMFC system
- Authors
- Jo, Taehyun; Koo, Bonchan; Lee, Yonghan; Kim, Dowook; Lee, Dohyung
- Issue Date
- Aug-2018
- Publisher
- PERGAMON-ELSEVIER SCIENCE LTD
- Keywords
- Steam reformer; Polymer electrolyte fuel cell; Natural gas; Combustion; Fuel distribution ratio
- Citation
- INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, v.43, no.31, pp 14226 - 14237
- Pages
- 12
- Indexed
- SCI
SCIE
SCOPUS
- Journal Title
- INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
- Volume
- 43
- Number
- 31
- Start Page
- 14226
- End Page
- 14237
- URI
- https://scholarworks.bwise.kr/erica/handle/2021.sw.erica/5708
- DOI
- 10.1016/j.ijhydene.2018.05.159
- ISSN
- 0360-3199
1879-3487
- Abstract
- A natural gas-based steam reformer for a domestic polymer electrolyte membrane fuel cell (PEMFC) system is thermodynamically analyzed with a special focus on the heat supply mechanism, which is critical to the endothermic steam reforming process. The interdependence of the reforming and combustion processes is evaluated through a characteristic study of heat transfer from the heat source to the reforming zone. Premixed combustion patterns may be affected by the inclusion of controlling means such as a metal fiber screen or burner placement. In this study, we attempted to enhance reforming performances of a reformer embedded in a 5 kW in-house PEMFC through modification of the combustion pattern by varying the type and placement of the burner and other operating conditions. Reforming input conditions such as steam-carbon ratio (SCR) and fuel distribution ratio (FDR) are also analyzed to quantify the overall performance such as thermal efficiency and fuel conversion rate. In our experiments involving three types of combustors cylindrical metal fiber burner, flat type metal fiber burner and nozzle-mixing burner the operating conditions are set so that the SCR and FDR are in the range 3.0-4.0 and 0.4-0.7, respectively. It is found that the cylindrical metal fiber burner at an appropriate location could improve thermal efficiency up to 79% by 10%, compared to other devices. This maximum thermal efficiency output is obtained with 0.63 FDR, which eventually yields 99% hydrogen conversion rate when using a cylindrical metal fiber burner, while the other burners produce 95% conversion. These outputs substantiate that the overall efficiency is strongly affected by an appropriate control for uniform temperature distribution on the catalyst layer. (C) 2018 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
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