Performance Evaluation of a Catalytic Flat Plate Fuel Reformer for Hydrogen-rich Reformate

被引:0
作者
Das, Susanta K. [1 ]
Berry, K. Joel
机构
[1] Kettering Univ, Dept Mech Engn, 1700 West Third Ave, Flint, MI 48504 USA
来源
PROCEEDINGS OF THE ASME 11TH FUEL CELL SCIENCE, ENGINEERING, AND TECHNOLOGY CONFERENCE, 2013 | 2014年
关键词
SYNTHESIS GAS; METHANE; REACTOR;
D O I
暂无
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A two-dimensional computational fluid dynamics (CFD) model is used for reforming methane with the help of catalytic combustion and refonnation in a catalytic flat plate reformer. The two-dimensional approach makes the computational model more realistic by eliminating the uncertainties introduced by heat and mass transfer coefficients used in one-dimensional models. It also increased its capability to capture the effect of design parameters such as catalyst thickness, reaction rates, inlet temperature and velocity, and channel height has on producing high purity reformate gas. In order to carry out parametric studies related to various design parameters, in our present work, we simulate the entire flat plate reformer domain by considering full electro-kinetics that provide guidance for the practical implementation of such design. We chose different designs and operating conditions in such a way which makes possible to build a catalytic flat plate fuel reformer prototype. Based on the CFD results obtained in this study, we built a first generation catalytic flat plate fuel reformer prototype using the optimized design parameters. The performance of the fuel reformer prototype is tested with a 5-cell high temperature PEM fuel cell stack.
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页数:8
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