Alumina/silica aerogel with zinc chloride as an alkylation catalyst

The alumina/silica with zinc chloride aerogel alkylation catalyst was obtained using a one step sol-gel synthesis, and subsequent drying with supercritical carbon dioxide. The aerogel catalyst activity was found to be higher compared to the corresponding xerogel catalyst, as a result of the...

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Main Authors: Orlović Aleksandar M., Janaćković Đorđe T., Drmanić Saša, Marinković Zorica, Skala Dejan U.
Format: Article
Language:English
Published: Serbian Chemical Society 2001-01-01
Series:Journal of the Serbian Chemical Society
Subjects:
Online Access:http://www.doiserbia.nb.rs/img/doi/0352-5139/2001/0352-51390110685O.pdf
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author Orlović Aleksandar M.
Janaćković Đorđe T.
Drmanić Saša
Marinković Zorica
Skala Dejan U.
author_facet Orlović Aleksandar M.
Janaćković Đorđe T.
Drmanić Saša
Marinković Zorica
Skala Dejan U.
author_sort Orlović Aleksandar M.
collection DOAJ
description The alumina/silica with zinc chloride aerogel alkylation catalyst was obtained using a one step sol-gel synthesis, and subsequent drying with supercritical carbon dioxide. The aerogel catalyst activity was found to be higher compared to the corresponding xerogel catalyst, as a result of the higher aerogel surface area, total pore volume and favourable pore size distribution. Mixed Al-O-Si bonds were present in both gel catalyst types. Activation by thermal treatment in air was needed prior to catalytic alkylation, due to the presence of residual organic groups on the aerogel surface. The optimal activation temperature was found to be in the range 185-225 ºC, while higher temperatures resulted in the removal of zinc chloride from the surface of the aerogel catalyst with a consequential decrease in the catalytic activity. On varying the zinc chloride content, the catalytic activity of the aerogel catalyst exhibited a maximum. High zinc chloride contents decreased the catalytic activity of the aerogel catalyst as the result of the pores of the catalyst being plugged with this compound, and the separation of the alumina/silica support into Al-rich and Si-rich phases. The surface area, total pore volume, pore size distribution and zinc chloride content had a similar influence on the activity of the aerogel catalyst as was the case of xerogel catalyst and supported zinc chloride catalysts.
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spelling doaj.art-7341fe1b51f44d429d8000cfe04c55fc2022-12-21T23:24:45ZengSerbian Chemical SocietyJournal of the Serbian Chemical Society0352-51391820-74212001-01-01661068569510.2298/JSC0110685O0352-51390110685OAlumina/silica aerogel with zinc chloride as an alkylation catalystOrlović Aleksandar M.0Janaćković Đorđe T.1Drmanić Saša2Marinković Zorica3Skala Dejan U.4Faculty of Technology and Metallurgy, BelgradeFaculty of Technology and Metallurgy, BelgradeFaculty of Technology and Metallurgy, BelgradeCenter for Multidisciplinary Studies, BelgradeFaculty of Technology and Metallurgy, BelgradeThe alumina/silica with zinc chloride aerogel alkylation catalyst was obtained using a one step sol-gel synthesis, and subsequent drying with supercritical carbon dioxide. The aerogel catalyst activity was found to be higher compared to the corresponding xerogel catalyst, as a result of the higher aerogel surface area, total pore volume and favourable pore size distribution. Mixed Al-O-Si bonds were present in both gel catalyst types. Activation by thermal treatment in air was needed prior to catalytic alkylation, due to the presence of residual organic groups on the aerogel surface. The optimal activation temperature was found to be in the range 185-225 ºC, while higher temperatures resulted in the removal of zinc chloride from the surface of the aerogel catalyst with a consequential decrease in the catalytic activity. On varying the zinc chloride content, the catalytic activity of the aerogel catalyst exhibited a maximum. High zinc chloride contents decreased the catalytic activity of the aerogel catalyst as the result of the pores of the catalyst being plugged with this compound, and the separation of the alumina/silica support into Al-rich and Si-rich phases. The surface area, total pore volume, pore size distribution and zinc chloride content had a similar influence on the activity of the aerogel catalyst as was the case of xerogel catalyst and supported zinc chloride catalysts.http://www.doiserbia.nb.rs/img/doi/0352-5139/2001/0352-51390110685O.pdfaerogel catalystfriedel-crafts alkylation catalystsol-gel derived catalyst
spellingShingle Orlović Aleksandar M.
Janaćković Đorđe T.
Drmanić Saša
Marinković Zorica
Skala Dejan U.
Alumina/silica aerogel with zinc chloride as an alkylation catalyst
Journal of the Serbian Chemical Society
aerogel catalyst
friedel-crafts alkylation catalyst
sol-gel derived catalyst
title Alumina/silica aerogel with zinc chloride as an alkylation catalyst
title_full Alumina/silica aerogel with zinc chloride as an alkylation catalyst
title_fullStr Alumina/silica aerogel with zinc chloride as an alkylation catalyst
title_full_unstemmed Alumina/silica aerogel with zinc chloride as an alkylation catalyst
title_short Alumina/silica aerogel with zinc chloride as an alkylation catalyst
title_sort alumina silica aerogel with zinc chloride as an alkylation catalyst
topic aerogel catalyst
friedel-crafts alkylation catalyst
sol-gel derived catalyst
url http://www.doiserbia.nb.rs/img/doi/0352-5139/2001/0352-51390110685O.pdf
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AT janackovicđorđet aluminasilicaaerogelwithzincchlorideasanalkylationcatalyst
AT drmanicsasa aluminasilicaaerogelwithzincchlorideasanalkylationcatalyst
AT marinkoviczorica aluminasilicaaerogelwithzincchlorideasanalkylationcatalyst
AT skaladejanu aluminasilicaaerogelwithzincchlorideasanalkylationcatalyst