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Highly selective oxidation of benzyl alcohol over Pt-sulphated zirconia supported on SBA-15 catalyst by using a high-pressure fixed bed reactor
Pt/SO4/ZrO2-SBA-15 catalyst for highly selective oxidation of benzyl alcohol to benzaldehyde. [Display omitted] An active platinum loaded sulphated zirconia supported SBA-15 catalyst (Pt/SO4/ZrO2-SBA-15) was synthesized and characterized using scanning electron microscope, transmission electron micr...
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Published in: | Polyhedron 2018-11, Vol.155, p.390-397 |
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Main Authors: | , , , , , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | Pt/SO4/ZrO2-SBA-15 catalyst for highly selective oxidation of benzyl alcohol to benzaldehyde.
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An active platinum loaded sulphated zirconia supported SBA-15 catalyst (Pt/SO4/ZrO2-SBA-15) was synthesized and characterized using scanning electron microscope, transmission electron microscope, N2adsorption-desorptionisotherms. The different percentage level (10, 20 and 30 wt.%) of ZrO2 was loaded on SBA-15 by precipitation of zirconium oxychloride, calcined and sulfated with H2SO4. The sulphated zirconia supported SBA-15 catalyst were loaded with 0.5 wt.% of Pt and characterized by different characterization technique. The Pt-loaded catalysts were evaluated to the selective oxidation of benzyl alcohol to benzaldehyde by the continuous-flow reactor system. Also, the bulk sample of SO4-ZrO2 and Pt-SO4-ZrO2 was prepared for the comparison purposes. The supported catalysts, even at the lowest loading of 10% ZrO2were more active than unsupported SO4-ZrO2. The catalyst containing 20% of ZrO2 was most active for the selective oxidation of benzyl alcohol; the highest activity was obtained over this catalyst at a lower temperature (90 °C). The Pt/SZ-SBA-15 catalyst showed very high catalytic activity and selectivity to benzyl alcohol oxidation. Besides, the long-term stability of the Pt/SZ-SBA-15 catalyst was excellent and there is no loss in catalytic activity or selectivity occurred during the time of continuous operation. |
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ISSN: | 0277-5387 |
DOI: | 10.1016/j.poly.2018.08.053 |