Adsorption and heterogeneous advanced oxidation of phenolic contaminants using Fe loaded mesoporous SBA-15 and H2O2
| dc.contributor.author | Shukla, Pradeep | |
| dc.contributor.author | Wang, Shaobin | |
| dc.contributor.author | Sun, Hongqi | |
| dc.contributor.author | Ang, Ming | |
| dc.contributor.author | Tade, Moses | |
| dc.date.accessioned | 2017-01-30T12:50:43Z | |
| dc.date.available | 2017-01-30T12:50:43Z | |
| dc.date.created | 2015-03-03T20:16:44Z | |
| dc.date.issued | 2010 | |
| dc.identifier.citation | Shukla, P. and Wang, S. and Sun, H. and Ang, M. and Tade, M. 2010. Adsorption and heterogeneous advanced oxidation of phenolic contaminants using Fe loaded mesoporous SBA-15 and H2O2. Chemical Engineering Journal. 164 (1): pp. 255-260. | |
| dc.identifier.uri | http://hdl.handle.net/20.500.11937/25891 | |
| dc.identifier.doi | 10.1016/j.cej.2010.08.061 | |
| dc.description.abstract |
Mesoporous silica, SBA-15, supported Fe/SBA-15 catalysts were prepared by impregnation and tested for adsorption and heterogeneous advanced oxidation of 2,4-dichlorophenol (DCP) in aqueous solution using H2O2. Characterisation indicated that Fe impregnation did not change the porous structure of SBA-15. Fe/SBA-15 exhibits moderate DCP adsorption, however, Fe/SBA-15 is effective for DCP oxidation under H2O2. The catalytic activity depends on Fe loading, H2O2 concentration, DCP concentration and solution pH. Fe/SBA-15 can achieve 100% DCP conversion and 60% TOC removal at the conditions of 100 ppm DCP, 0.05 g 10%wt Fe/SBA-15, and 1000 ppm H2O2. This catalyst also shows stable performance with low Fe leaching. | |
| dc.publisher | Elsevier BV | |
| dc.title | Adsorption and heterogeneous advanced oxidation of phenolic contaminants using Fe loaded mesoporous SBA-15 and H2O2 | |
| dc.type | Journal Article | |
| dcterms.source.volume | 164 | |
| dcterms.source.startPage | 255 | |
| dcterms.source.endPage | 260 | |
| dcterms.source.issn | 13858947 | |
| dcterms.source.title | Chemical Engineering Journal | |
| curtin.department | Department of Chemical Engineering | |
| curtin.accessStatus | Fulltext not available |