Heat transfer enhancement in methanol steam reforming for a fuel cell
Citation
S. Nagano et al., Heat transfer enhancement in methanol steam reforming for a fuel cell, ENERG CONV, 42(15-17), 2001, pp. 1817-1829
Categorie Soggetti
Environmental Engineering & Energy
Journal title
ENERGY CONVERSION AND MANAGEMENT
SICI code
0196-8904(200110/11)42:15-17<1817:HTEIMS>2.0.ZU;2-
Abstract
The catalytic methanol steam reforming reaction was investigated by numeric
al simulation and experiments. Methanol conversion ratio as well as carbon
monoxide (CO), which poisons a typical polymer electrolyte fuel cell, incre
ases in a tablet catalyst when temperature is elevated. There is a trade-of
f relationship between methanol conversion ratio and CO concentration. It w
as found that the reforming reaction is controlled by heat transfer at larg
e methanol flow rate, where the trade-off relationship shifts to lower meth
anol conversion ratio and higher CO concentration.
To improve the trade-off relationship, internal corrugated metal heater and
external catalytic combustion heater were applied to enhance the heat tran
sfer. Optimal cell density for the internal corrugated metal heater, which
was about 9 x 10(5) cell/m(2), was closely related with reaction parameters
such as velocity, cell density, geometric surface area and hydraulic diame
ter. The catalytic combustion heater is larger than the internal corrugated
metal heater in size. Both high methanol conversion ratio and low CO conce
ntration were accomplished by heat transfer enhancement with the two techni
ques at large methanol flow rate. (C) 2001 Elsevier Science Ltd. All rights
reserved.