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Microchannels were patterned on the metal sheets and fabricated to make unit reactors such as vaporizer, heat exchanger, reformer and catalytic combustor. Three types of patterned sheets were prepared to construct a base structure. The aspect ratio of microchannels can be regulated by changing the number of microchannel sheets. Catalyst was deposited inside the microchannel of a reformer unit. Catalytic combustor provided heat for the endothermic reaction of methanol reforming and the vaporization of liquid fuel. An integrated microchannel reformer was fabricated by connecting unit reactors including vaporizer, heat exchanger, reformer and catalytic combustor. The dimensions of an integrated reformer were 50x40x30 mm respectively. The performance of the integrated microchannel reformer was investigated at various operating conditions. The developed fuel processor generates hydrogen for power output of 14 Wt.

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Abstract

1. Introduction

2. Experimental

3. Results and discussion

4. Conclusion

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UCI(KEPA) : I410-ECN-0101-2009-563-018203697