Kinetics of the catalytic air oxidation
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J. Skrzypek; M. Grzesik; M. Galantowicz; J. SoliΕski
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Article
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1985
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Elsevier Science
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English
β 836 KB
The gas-phase oxidation of o-xylene over a commercial V205-Ti02 catalyst was studied in tied bed non-isothermal reactor. The experiments were carried out at initial o-xylene concentrations which differed greatly from each other. The following reaction network was suggested.