Abstract
The ferric oxide catalyst was prepared by the dipping-calcination method using γ-Al2O3 as a carrier and the microwave-induced oxidation process was developed to treat phenol in water. The effects of operating conditions on the catalyst activity, the using life of the catalyst, and the reaction kinetics were studied. α-Fe2O3 was loaded on the surface of γ-Al2O3 and the content of α-Fe2O3 in the catalyst was 3.71%. Under the optimal treatment conditions of phenol concentration of 100 mg/L, microwave power of 400 w, irradiation time of 5 min, catalyst amount of 60 g/L, H2O2 concentration of 600 mg/L and pH > 4, a phenol removal rate of 97.98% was obtained. The catalyst could be reused > 20 times remaining a phenol removal rate of 96.34%.
| Original language | English |
|---|---|
| Pages (from-to) | 597-601 |
| Number of pages | 5 |
| Journal | Chinese Journal of Catalysis |
| Volume | 26 |
| Issue number | 7 |
| State | Published - 2005 |
Keywords
- Alumina
- Ferric oxide
- Hydrogen peroxide
- Microwave-induced oxidation process
- Phenol
- Supported catalyst
- Wastewater treatment
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