Temperature-Programmed Reduction of Metal-Contaminated Fluid Catalytic Cracking (fcc) Catalysts
| dc.contributor.author | Bayraktar, Oğuz | |
| dc.contributor.author | Kugler, Edwin L. | |
| dc.coverage.doi | 10.1016/j.apcata.2003.10.013 | |
| dc.date.accessioned | 2016-07-11T12:55:01Z | |
| dc.date.available | 2016-07-11T12:55:01Z | |
| dc.date.issued | 2004 | |
| dc.description.abstract | A temperature-programmed reduction study of equilibrium fluid catalytic cracking (FCC) catalysts has shown three hydrogen-consumption peaks associated with contaminanted metals. A low-temperature peak, located near 510°C, is produced by the reduction of several components in the catalyst. Highly-dispersed vanadium contributes to this peak. A high-temperature peak, located near 800°C, is produced by reduction of nickel aluminate or nickel silicate compounds. A linear relationship exists between the area of the high-temperature peak and nickel concentration on equilibrium catalysts. An intermediate-temperature peak, located near 690°C, appears to be related to some form of vanadium compound. The intermediate-temperature peak does not occur on low-vanadium-concentration equilibrium catalysts, but is observed at higher vanadium-contamination levels. The presence of the 690°C peak was found by deconvoluting hydrogen-consumption data. The existence of this intermediate-temperature peak was proven by external reduction of highly-contaminated equilibrium catalyst at 500 and 700°C. External reduction at 500°C removes the low-temperature peak from the temperature-programmed reduction (TPR) spectrum. External reduction at 700°C removes both the low-temperature and intermediate-temperature peaks from the TPR spectrum. The difference in spectrum between calcined and 700°C reduced samples shows a clear spectrum with only the low and intermediate-temperature peaks present. | en_US |
| dc.identifier.citation | Bayraktar, O., and Kugler, E. L. (2004). Temperature-programmed reduction of metal-contaminated fluid catalytic cracking (FCC) catalysts. Applied Catalysis A: General, 260(1), 125-132. doi:10.1016/j.apcata.2003.10.013 | en_US |
| dc.identifier.doi | 10.1016/j.apcata.2003.10.013 | en_US |
| dc.identifier.doi | 10.1016/j.apcata.2003.10.013 | |
| dc.identifier.issn | 0926-860X | |
| dc.identifier.scopus | 2-s2.0-1542316834 | |
| dc.identifier.uri | http://doi.org/10.1016/j.apcata.2003.10.013 | |
| dc.identifier.uri | https://hdl.handle.net/11147/1879 | |
| dc.language.iso | en | en_US |
| dc.publisher | Elsevier Ltd. | en_US |
| dc.relation.ispartof | Applied Catalysis A: General | en_US |
| dc.rights | info:eu-repo/semantics/openAccess | en_US |
| dc.subject | Catalysts | en_US |
| dc.subject | Pretreatment | en_US |
| dc.subject | Temperature-programmed reduction | en_US |
| dc.subject | Fluidized catalytic cracking catalysts | en_US |
| dc.subject | Nickel | en_US |
| dc.subject | Vanadium | en_US |
| dc.title | Temperature-Programmed Reduction of Metal-Contaminated Fluid Catalytic Cracking (fcc) Catalysts | en_US |
| dc.type | Article | en_US |
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| gdc.author.institutional | Bayraktar, Oğuz | |
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| gdc.description.department | İzmir Institute of Technology. Chemical Engineering | en_US |
| gdc.description.endpage | 132 | en_US |
| gdc.description.issue | 1 | en_US |
| gdc.description.publicationcategory | Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı | en_US |
| gdc.description.scopusquality | Q2 | |
| gdc.description.startpage | 125 | en_US |
| gdc.description.volume | 260 | en_US |
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| gdc.oaire.keywords | Fluidized catalytic cracking catalysts | |
| gdc.oaire.keywords | Catalysts | |
| gdc.oaire.keywords | Nickel | |
| gdc.oaire.keywords | Vanadium | |
| gdc.oaire.keywords | Temperature-programmed reduction | |
| gdc.oaire.keywords | Pretreatment | |
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