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dc.contributor.authorDivins, N.J.
dc.contributor.authorLópez, E.
dc.contributor.authorLlorca, J.
dc.contributor.authorVega, Didac
dc.contributor.authorRodríguez Martínez, Ángel
dc.contributor.authorGonzález de Rivera, F.
dc.contributor.authorAngurell, I.
dc.contributor.authorSeco, M.
dc.contributor.authorRossell, O.
dc.contributor.otherUniversitat Politècnica de Catalunya. Departament d'Enginyeria Electrònica
dc.date.accessioned2013-09-12T17:06:33Z
dc.date.created2013
dc.date.issued2013
dc.identifier.citationDivins, N. [et al.]. Macroporous silicon microreactor for the preferential oxidation of CO. A: Spanish Conference on Electron Devices. "Proceedings of the 2013 Spanish Conference on Electron Devices: CDE 2013: February 12-14, 2013: Valladolid, Spain". Valladolid: Institute of Electrical and Electronics Engineers (IEEE), 2013, p. 1-4.
dc.identifier.isbn978-1-4673-4666-5
dc.identifier.urihttp://hdl.handle.net/2117/20128
dc.description.abstractA macroporous silicon micromonolith containing ca. 40,000 regular channels of 3.3 μm in diameter per square millimeter has been successfully functionalized with an Au/TiO2 catalyst for CO preferential oxidation (CO-PrOx) in the presence of hydrogen. The functionalization of the silicon microchannels has been accomplished by growing a SiO2 layer on the channel walls, followed by exchange with a titanium alkoxyde precursor and decomposition into TiO2 and, finally, by anchoring carbosilanethiol dendron protected pre-formed Au nanoparticles. Catalytically active centers at the Au-TiO2 interface have been obtained by thermal activation. With this method, an excellent homogeneity and adherence of the catalytic layer over the microchannels of the macroporous silicon micromonolith has been obtained, which has been tested for CO-PrOx at 363-433 K and λ=2 under H2/CO=0-20 (molar). The macroporous silicon micromonolith converts ca. 3 NmL of CO per minute and mL of micro reactor at 433 K under H2/CO=20, suggesting that it could be particularly effective for hydrogen purification in low-temperature microfuel cells for portable applications.
dc.format.extent4 p.
dc.language.isoeng
dc.publisherInstitute of Electrical and Electronics Engineers (IEEE)
dc.rightsAttribution-NonCommercial-NoDerivs 3.0 Spain
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es/
dc.subjectÀrees temàtiques de la UPC::Enginyeria química
dc.subject.lcshPorous silicon
dc.subject.lcshHydrogen
dc.subject.otherCarbon compounds
dc.subject.otherCatalysts
dc.subject.otherElemental semiconductors
dc.subject.otherFuel cells
dc.subject.otherGold
dc.subject.otherMicroreactors
dc.subject.otherNanoparticles
dc.subject.otherOxidation
dc.subject.otherPorous semiconductors
dc.subject.otherPyrolysis
dc.subject.otherSilicon
dc.subject.otherTitanium compounds
dc.titleMacroporous silicon microreactor for the preferential oxidation of CO
dc.typeConference report
dc.subject.lemacSilici porós
dc.subject.lemacHidrogen
dc.contributor.groupUniversitat Politècnica de Catalunya. MNT - Grup de Recerca en Micro i Nanotecnologies
dc.identifier.doi10.1109/CDE.2013.6481362
dc.description.peerreviewedPeer Reviewed
dc.relation.publisherversionhttp://ieeexplore.ieee.org/xpls/abs_all.jsp?arnumber=6481362
dc.rights.accessRestricted access - publisher's policy
local.identifier.drac12736236
dc.description.versionPostprint (published version)
dc.date.lift10000-01-01
local.citation.authorDivins, N.; López, E.; Llorca, J.; Vega, D.; Rodriguez, A.; González de Rivera, F.; Angurell, I.; Seco, M.; Rossell, O.
local.citation.contributorSpanish Conference on Electron Devices
local.citation.pubplaceValladolid
local.citation.publicationNameProceedings of the 2013 Spanish Conference on Electron Devices: CDE 2013: February 12-14, 2013: Valladolid, Spain
local.citation.startingPage1
local.citation.endingPage4


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