DC Field | Value | Language |
---|---|---|
dc.contributor.author | Irfan, Muhammad F. | ko |
dc.contributor.author | Kim, Sang Done | ko |
dc.contributor.author | Usman, Muhammad R. | ko |
dc.date.accessioned | 2013-03-08T22:53:04Z | - |
dc.date.available | 2013-03-08T22:53:04Z | - |
dc.date.created | 2012-02-06 | - |
dc.date.created | 2012-02-06 | - |
dc.date.issued | 2009-09 | - |
dc.identifier.citation | INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, v.48, no.17, pp.7959 - 7964 | - |
dc.identifier.issn | 0888-5885 | - |
dc.identifier.uri | http://hdl.handle.net/10203/94571 | - |
dc.description.abstract | The NO reduction over CuO/gamma-Al2O3 catalyst in a bubbling fluidized bed reactor has been determined on the basis of the two-phase model at the maximum conversion temperature of 300 degrees C. This temperature is critical as it deals maximum conversion, NH3 adsorption/desorption, and NH3 oxidation, which also takes place above this temperature and hence causes a decrease of NO reduction. The effects of superficial gas velocity (u(g)), [NH3]/[NO] molar ratio, and the static bed height (h(s)) on the reduction efficiency of NO over CuO/gamma-Al2O3 as a bed material in a fluidized bed reactor with variation of reaction temperatures (rate constant, k(r)) have been determined, and a model has been developed for the NO removal process in a bubbling fluidized bed using the two-phase theory. The results are compared with the Simulation results obtained through the Maple and MATLAB simulation tools. | - |
dc.language | English | - |
dc.publisher | Amer Chemical Soc | - |
dc.subject | ON-ALUMINA CATALYSTS | - |
dc.subject | SELECTIVE REDUCTION | - |
dc.subject | NITRIC-OXIDE | - |
dc.subject | NH3 | - |
dc.subject | AMMONIA | - |
dc.subject | CONVERSION | - |
dc.subject | COPPER | - |
dc.subject | REACTIVITY | - |
dc.subject | ADSORPTION | - |
dc.subject | OXIDATION | - |
dc.title | Modeling of NO Removal over CuO/gamma-Al2O3 Catalyst in a Bubbling Fluidized Bed Reactor | - |
dc.type | Article | - |
dc.identifier.wosid | 000269197400014 | - |
dc.identifier.scopusid | 2-s2.0-69949126513 | - |
dc.type.rims | ART | - |
dc.citation.volume | 48 | - |
dc.citation.issue | 17 | - |
dc.citation.beginningpage | 7959 | - |
dc.citation.endingpage | 7964 | - |
dc.citation.publicationname | INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH | - |
dc.identifier.doi | 10.1021/ie8018214 | - |
dc.contributor.localauthor | Kim, Sang Done | - |
dc.contributor.nonIdAuthor | Usman, Muhammad R. | - |
dc.type.journalArticle | Article | - |
dc.subject.keywordPlus | ON-ALUMINA CATALYSTS | - |
dc.subject.keywordPlus | SELECTIVE REDUCTION | - |
dc.subject.keywordPlus | NITRIC-OXIDE | - |
dc.subject.keywordPlus | NH3 | - |
dc.subject.keywordPlus | AMMONIA | - |
dc.subject.keywordPlus | CONVERSION | - |
dc.subject.keywordPlus | COPPER | - |
dc.subject.keywordPlus | REACTIVITY | - |
dc.subject.keywordPlus | ADSORPTION | - |
dc.subject.keywordPlus | OXIDATION | - |
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