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dc.contributor.authorChou, SSen_US
dc.contributor.authorHuang, CPen_US
dc.contributor.authorHuang, YHen_US
dc.date.accessioned2014-12-08T15:46:05Z-
dc.date.available2014-12-08T15:46:05Z-
dc.date.issued1999-11-01en_US
dc.identifier.issn0045-6535en_US
dc.identifier.urihttp://dx.doi.org/10.1016/S0045-6535(99)00089-2en_US
dc.identifier.urihttp://hdl.handle.net/11536/30989-
dc.description.abstractThe aim of this study was to investigate the effect of Fe2+ on the catalytic oxidation in the fluidized-bed reactor (FBR) applying supported gamma-FeOOH as the carrier. Processes without Fe2+ addition and with Fe2+ addition (FBR-Fenton method) were performed on the oxidation of benzoic acid (BA) by H2O2. When Fe2+ was not added in the FBR, the high COD removal at low pH was caused by homogeneous catalysis of Fe2+ formed via reductive dissolution of gamma-FeOOH. In the FBR-Fenton process, both mineralization of organics and crystallization of Fe(III) were simultaneously well performed under adequate condition. The reaction mechanism, including the reductive dissolution and crystallization of gamma-FeOOH as well as the oxidation of BA, was proposed based on the experimental results. (C)1999 Elsevier Science Ltd. All rights reserved.en_US
dc.language.isoen_USen_US
dc.subjectcatalysten_US
dc.subjectcrystallizationen_US
dc.subjectfluidized-beden_US
dc.subjecthydrogen peroxideen_US
dc.subjectiron oxideen_US
dc.subjectoxidationen_US
dc.titleEffect of Fe2+ on catalytic oxidation in a fluidized bed reactoren_US
dc.typeArticleen_US
dc.identifier.doi10.1016/S0045-6535(99)00089-2en_US
dc.identifier.journalCHEMOSPHEREen_US
dc.citation.volume39en_US
dc.citation.issue12en_US
dc.citation.spage1997en_US
dc.citation.epage2006en_US
dc.contributor.department環境工程研究所zh_TW
dc.contributor.departmentInstitute of Environmental Engineeringen_US
dc.identifier.wosnumberWOS:000082900100002-
dc.citation.woscount30-
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