2013
DOI: 10.1002/ceat.201100295
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Optimization of Catalyst Loading for Porous Copper Fiber Sintered Felts Used in Methanol Steam Reforming Microreactors

Abstract: A novel porous copper fiber sintered felt (PCFSF) has been used as catalyst support to construct a methanol steam reforming microreactor for hydrogen production. The Cu/Zn/Al/Zr catalyst was loaded on the PCFSF by means of a two-layer impregnation method. The ultrasonic water bath vibration method was employed to investigate the effect of porosity, catalyst loading, and sintering temperature on the loading performance of PCFSFs. The effective catalyst loading, being limited by porosity and pore size, was >92% … Show more

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Cited by 17 publications
(2 citation statements)
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“…Wang et al [7] designed a new MSR system by combing MSR and CO selective methanation modules to produce hydrogen with low CO concentration. Zhou et al [8] adopted a novel copper fiber as catalyst support to improve hydrogen production in a microreactor. Chougule and Sonde [9] did both modeling and experimental investigations on a novel compact packed bed reactor for MSR to determine the effects of several important operation conditions on hydrogen production.…”
Section: Introductionmentioning
confidence: 99%
“…Wang et al [7] designed a new MSR system by combing MSR and CO selective methanation modules to produce hydrogen with low CO concentration. Zhou et al [8] adopted a novel copper fiber as catalyst support to improve hydrogen production in a microreactor. Chougule and Sonde [9] did both modeling and experimental investigations on a novel compact packed bed reactor for MSR to determine the effects of several important operation conditions on hydrogen production.…”
Section: Introductionmentioning
confidence: 99%
“…Three grid trays were used in the evaporation chamber to increase the amount of water vaporization and the flow uniformity. A mixture of methanol and distilled water (mole ratio of 1:1.3) was pumped into the evaporation chamber through the inlet tube with an injection pump [28]. After the mixture evaporated in the evaporation chamber, the reformate gas reacted in the presence of the catalyst in the reaction chamber at a temperature range of 200℃ to 400℃ which was controlled by the heating cartridges.…”
Section: Introductionmentioning
confidence: 99%