Catalytic wet air oxidation of gasoline oxygenates (ETBE and TAME) were carried out using Rh/g-Al 2 O 3 , Rh/g-Al 2 O 3 -CeO 2 catalysts in a Parr reactor at 100, 120 and 150 8C using oxygen as oxidant source at 10 bar of pressure. Aqueous solutions of ETBE and TAME were prepared using the quantitie
Highly stable Fe/γ-Al2O3 catalyst for catalytic wet peroxide oxidation
✍ Scribed by Patricia Bautista; Angel F. Mohedano; Jose A. Casas; Juan A. Zazo; Juan J. Rodriguez
- Publisher
- Wiley (John Wiley & Sons)
- Year
- 2010
- Tongue
- English
- Weight
- 190 KB
- Volume
- 86
- Category
- Article
- ISSN
- 0268-2575
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✦ Synopsis
Abstract
BACKGROUND: A highly stable Fe/γ‐Al~2~O~3~ catalyst for catalytic wet peroxide oxidation has been studied using phenol as target pollutant. The catalyst was prepared by incipient wetness impregnation of γ‐Al~2~O~3~ with an aqueous solution of Fe(NO~3~)~3~· 9H~2~O. The influence of pH, temperature, catalyst and H~2~O~2~ doses, as well as the initial phenol concentration has been analyzed.
RESULTS: The reaction temperature and initial pH significantly affect both phenol conversion and total organic carbon removal. Working at 50 °C, an initial pH of 3, 100 mg L^−1^ of phenol, a dose of H~2~O~2~ corresponding to the stoichiometric amount and 1250 mg L^−1^ of catalyst, complete phenol conversion and a total organic carbon removal efficiency close to 80% were achieved. When the initial phenol concentration was increased to 1500 mg L^−1^, a decreased efficiency in total organic carbon removal was observed with increased leaching of iron that can be related to a higher concentration of oxalic acid, as by‐product from catalytic wet peroxide oxidation of phenol.
CONCLUSION: A laboratory synthesized γ‐Al~2~O~3~ supported Fe has shown potential application in catalytic wet peroxide oxidation of phenolic wastewaters. The catalyst showed remarkable stability in long‐term continuous experiments with limited Fe leaching, < 3% of the initial loading. Copyright © 2010 Society of Chemical Industry
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## Abstract A large variety of catalytic systems have been studied for the catalytic wet air oxidation of phenolic solutions. Most of them show good activity, but serious stability problems. In this contribution, stability studies were performed over CuO/Al~2~O~3~ conventional (CNT) and polytetrafl