DC Field | Value | Language |
---|---|---|
dc.contributor.author | Jeong, SM | ko |
dc.contributor.author | Kim, Sang Done | ko |
dc.date.accessioned | 2008-05-22T10:08:37Z | - |
dc.date.available | 2008-05-22T10:08:37Z | - |
dc.date.created | 2012-02-06 | - |
dc.date.created | 2012-02-06 | - |
dc.date.issued | 2000-06 | - |
dc.identifier.citation | INDUSTRIAL ENGINEERING CHEMISTRY RESEARCH, v.39, no.6, pp.1911 - 1916 | - |
dc.identifier.issn | 0888-5885 | - |
dc.identifier.uri | http://hdl.handle.net/10203/4676 | - |
dc.description.abstract | Selective reduction of NO and the simultaneous removal SO2/NO by CuO/gamma-Al2O3\ sorbent/catalyst were carried out in a fluidized-bed reactor. The optimum temperature ranges for NO reduction over the fresh and sulfated CuO/gamma-Al2O3 catalyst are found to be 250-300 and 300-450 degrees C, respectively. The NO removal efficiency with the sulfated catalyst is somewhat higher than that with the fresh catalyst. The amount of optimum Cu/S is found to be 1.5 in the simultaneous removal of SO2/NO. The optimum temperature range for the simultaneous removal of SO2/NO by CuO/gamma-Al2O3 sorbent/catalyst in the reactor is 350-400 degrees C based on the SO2 and NO removal efficiencies (> 90%) and N2O formation (< 10% of NO in feed). | - |
dc.description.sponsorship | Ministry of Science and Technology, Korea, and the alumina support from Alcoa Co., Pittsburgh, PA | en |
dc.language | English | - |
dc.language.iso | en_US | en |
dc.publisher | AMER CHEMICAL SOC | - |
dc.subject | SELECTIVE CATALYTIC REDUCTION | - |
dc.subject | FLUE-GAS | - |
dc.subject | SORBENT | - |
dc.subject | COPPER | - |
dc.subject | SIMULATION | - |
dc.subject | SULFATION | - |
dc.subject | OXIDE | - |
dc.subject | NH3 | - |
dc.title | Removal of NOx and SO2 by CuO/gamma-Al2O3 sorbent/catalyst in a fluidized-bed reactor | - |
dc.type | Article | - |
dc.identifier.wosid | 000087568600040 | - |
dc.type.rims | ART | - |
dc.citation.volume | 39 | - |
dc.citation.issue | 6 | - |
dc.citation.beginningpage | 1911 | - |
dc.citation.endingpage | 1916 | - |
dc.citation.publicationname | INDUSTRIAL ENGINEERING CHEMISTRY RESEARCH | - |
dc.identifier.doi | 10.1021/ie990482r | - |
dc.embargo.liftdate | 9999-12-31 | - |
dc.embargo.terms | 9999-12-31 | - |
dc.contributor.localauthor | Kim, Sang Done | - |
dc.contributor.nonIdAuthor | Jeong, SM | - |
dc.type.journalArticle | Article | - |
dc.subject.keywordPlus | SELECTIVE CATALYTIC REDUCTION | - |
dc.subject.keywordPlus | FLUE-GAS | - |
dc.subject.keywordPlus | SORBENT | - |
dc.subject.keywordPlus | COPPER | - |
dc.subject.keywordPlus | SIMULATION | - |
dc.subject.keywordPlus | SULFATION | - |
dc.subject.keywordPlus | OXIDE | - |
dc.subject.keywordPlus | NH3 | - |
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