Physicochemical and Catalytic Properties of Vanadia/Titania Catalysts. IV. Catalytic Oxidation of -Xylene
Titania samples were prepared by precipitation at pH 3.0 (to provide ‘T a ’ samples) or at pH 9.0 (to provide ‘T b ’ samples). These materials were then impregnated with NH 4 VO 3 to obtain vanadia/titania catalysts of different V 2 O 5 content. These V 2 O 5 /TiO 2 samples were subsequently calcine...
| Main Authors: | , , , |
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| Format: | Article |
| Language: | English |
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SAGE Publishing
2002-11-01
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| Series: | Adsorption Science & Technology |
| Online Access: | https://doi.org/10.1260/02636170260555787 |
| _version_ | 1826910860888506368 |
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| author | Th. El-Nabarawy M.N. Alaya S.A. Sayed Ahmed A.M. Youssef |
| author_facet | Th. El-Nabarawy M.N. Alaya S.A. Sayed Ahmed A.M. Youssef |
| author_sort | Th. El-Nabarawy |
| collection | DOAJ |
| description | Titania samples were prepared by precipitation at pH 3.0 (to provide ‘T a ’ samples) or at pH 9.0 (to provide ‘T b ’ samples). These materials were then impregnated with NH 4 VO 3 to obtain vanadia/titania catalysts of different V 2 O 5 content. These V 2 O 5 /TiO 2 samples were subsequently calcined at 400°C or 600°C to obtain two series. The oxidation of o -xylene was undertaken at 250°C, 300°C or 350°C using a conventional flow apparatus at atmospheric pressure. The reaction products were detected and separated via a gas chromatograph fitted with a flame ionization detector. The chemical composition of the catalyst, the calcination temperature, the reaction mixture employed and the reaction temperature were among the variables considered. Catalysts calcined at 400°C were more active than those calcined at 600°C, thereby indicating that anatase was the proper titania phase for supporting oxidation catalysts. Titania samples precipitated at pH 3.0 were more effective as a support for vanadia than those precipitated at pH 9.0 despite the fact that they possessed lower surface areas. This demonstrated that surface area was not a determining factor in catalyst performance. The conversion of o -xylene to phthalic anhydride increased with increasing vanadia content in the catalysts employed and with increasing reaction temperature. Surface acidity was one factor amongst others contributing to the catalytic activity. It is thought that acid sites enhance the reduction of V 5+ to lower oxidation states to provide the active oxidation sites. Mechanisms for the partial oxidation of o -xylene were advanced and explained. |
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| format | Article |
| id | doaj.art-662d36e1a1c94b38b970e10b74f8faac |
| institution | Directory Open Access Journal |
| issn | 0263-6174 2048-4038 |
| language | English |
| last_indexed | 2025-02-17T10:07:06Z |
| publishDate | 2002-11-01 |
| publisher | SAGE Publishing |
| record_format | Article |
| series | Adsorption Science & Technology |
| spelling | doaj.art-662d36e1a1c94b38b970e10b74f8faac2025-01-02T02:59:03ZengSAGE PublishingAdsorption Science & Technology0263-61742048-40382002-11-012010.1260/02636170260555787Physicochemical and Catalytic Properties of Vanadia/Titania Catalysts. IV. Catalytic Oxidation of -XyleneTh. El-Nabarawy0M.N. Alaya1S.A. Sayed Ahmed2A.M. Youssef3 Laboratory of Surface Chemistry and Catalysis, National Research Centre, Dokki, Cairo, Egypt Faculty of Science, University of Aleppo, Aleppo, Syria Laboratory of Surface Chemistry and Catalysis, National Research Centre, Dokki, Cairo, Egypt Chemistry Department, Faculty of Science, Mansoura University, Mansoura, EgyptTitania samples were prepared by precipitation at pH 3.0 (to provide ‘T a ’ samples) or at pH 9.0 (to provide ‘T b ’ samples). These materials were then impregnated with NH 4 VO 3 to obtain vanadia/titania catalysts of different V 2 O 5 content. These V 2 O 5 /TiO 2 samples were subsequently calcined at 400°C or 600°C to obtain two series. The oxidation of o -xylene was undertaken at 250°C, 300°C or 350°C using a conventional flow apparatus at atmospheric pressure. The reaction products were detected and separated via a gas chromatograph fitted with a flame ionization detector. The chemical composition of the catalyst, the calcination temperature, the reaction mixture employed and the reaction temperature were among the variables considered. Catalysts calcined at 400°C were more active than those calcined at 600°C, thereby indicating that anatase was the proper titania phase for supporting oxidation catalysts. Titania samples precipitated at pH 3.0 were more effective as a support for vanadia than those precipitated at pH 9.0 despite the fact that they possessed lower surface areas. This demonstrated that surface area was not a determining factor in catalyst performance. The conversion of o -xylene to phthalic anhydride increased with increasing vanadia content in the catalysts employed and with increasing reaction temperature. Surface acidity was one factor amongst others contributing to the catalytic activity. It is thought that acid sites enhance the reduction of V 5+ to lower oxidation states to provide the active oxidation sites. Mechanisms for the partial oxidation of o -xylene were advanced and explained.https://doi.org/10.1260/02636170260555787 |
| spellingShingle | Th. El-Nabarawy M.N. Alaya S.A. Sayed Ahmed A.M. Youssef Physicochemical and Catalytic Properties of Vanadia/Titania Catalysts. IV. Catalytic Oxidation of -Xylene Adsorption Science & Technology |
| title | Physicochemical and Catalytic Properties of Vanadia/Titania Catalysts. IV. Catalytic Oxidation of -Xylene |
| title_full | Physicochemical and Catalytic Properties of Vanadia/Titania Catalysts. IV. Catalytic Oxidation of -Xylene |
| title_fullStr | Physicochemical and Catalytic Properties of Vanadia/Titania Catalysts. IV. Catalytic Oxidation of -Xylene |
| title_full_unstemmed | Physicochemical and Catalytic Properties of Vanadia/Titania Catalysts. IV. Catalytic Oxidation of -Xylene |
| title_short | Physicochemical and Catalytic Properties of Vanadia/Titania Catalysts. IV. Catalytic Oxidation of -Xylene |
| title_sort | physicochemical and catalytic properties of vanadia titania catalysts iv catalytic oxidation of xylene |
| url | https://doi.org/10.1260/02636170260555787 |
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