TY - GEN
T1 - Development of the integrated hydrogen production system using micro-structured devices
AU - Byun, Y. C.
AU - Kwon, Y.
AU - Choe, J.
AU - Song, K. H.
PY - 2005
Y1 - 2005
N2 - An integrated fuel processor, which produces hydrogen for fuel cell from aqueous methanol solution, has been developed by employing wall-coated microchannel catalytic reactors for steam reforming and preferential oxidation reaction. The developed fuel processor can produce the amount of hydrogen equivalent to a few hundred watts of electricity, when supplied to a fuel cell. We fabricated methanol fuel processor consists of a catalytic combustor, heat exchangers, evaporators, a reformer, and a PrOx(preferential oxidation) reactor. CuO/ZnO/Al2O3 catalyst was used for reforming and Pt/Al2O3 catalyst was used for both preferential oxidation and catalytic combustion. Besides the reformer and the PrOx reactor, the whole system also required three micro-structured evaporators. The main evaporator for the reformer feed vaporization was integrated with the catalytic combustor, and the heat recuperated from combustor vent gas is used to vaporize the methanol feed for two additional evaporators. The integrated system was operated consistently with methanol conversion of over 99.0 mol% at 300 °C, and the carbon monoxide concentration under 20 ppm in the final product flow.
AB - An integrated fuel processor, which produces hydrogen for fuel cell from aqueous methanol solution, has been developed by employing wall-coated microchannel catalytic reactors for steam reforming and preferential oxidation reaction. The developed fuel processor can produce the amount of hydrogen equivalent to a few hundred watts of electricity, when supplied to a fuel cell. We fabricated methanol fuel processor consists of a catalytic combustor, heat exchangers, evaporators, a reformer, and a PrOx(preferential oxidation) reactor. CuO/ZnO/Al2O3 catalyst was used for reforming and Pt/Al2O3 catalyst was used for both preferential oxidation and catalytic combustion. Besides the reformer and the PrOx reactor, the whole system also required three micro-structured evaporators. The main evaporator for the reformer feed vaporization was integrated with the catalytic combustor, and the heat recuperated from combustor vent gas is used to vaporize the methanol feed for two additional evaporators. The integrated system was operated consistently with methanol conversion of over 99.0 mol% at 300 °C, and the carbon monoxide concentration under 20 ppm in the final product flow.
UR - http://www.scopus.com/inward/record.url?scp=22444446702&partnerID=8YFLogxK
M3 - Conference contribution
AN - SCOPUS:22444446702
SN - 0816909849
T3 - 2005 AIChE Spring National Meeting, Conference Proceedings
SP - 2733
EP - 2737
BT - 2005 AIChE Spring National Meeting, Conference Proceedings
T2 - 2005 AIChE Spring National Meeting
Y2 - 10 April 2005 through 14 April 2005
ER -