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- W2376762347 abstract "A three-phase, fluidized-bed photocatalytic reactor for immobilized TiO2 catalyst was designed, the parameters of the reactor were preliminarily studied, while the performance of it in the treatment of phenol-containing wastewater, the factors affecting the catalytic reaction and the extent of the affection were analyzed. Compared with fixed bed, the fluidized-bed reactor showed a better result of treatment. It made the catalyst and the phenol-containing wastewater in sufficient contact with each other and provided sufficient amount of oxygen, so that large-area, effective contact of light, solid catalyst and solution with one another was realized, the mass transfer efficiency was improved, and the photocatalytic reaction rate speeded up. When the pH value was 9.6, the amount of catalyst used was 50 g, the air flow was 500 L/h and the liquid flow was 8.0 L/h, the treatment capacity of the fluidized-bed reactor in one operating cycle(12 h) was 19.5 mg/g, while the treatment capacity of fixed-bed reactor was 14.4 mg/g. The treatment capacity of fluidized bed is 35.4% higher than that of fixed bed. The removal rate of phenol was 99.8%." @default.
- W2376762347 created "2016-06-24" @default.
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- W2376762347 date "2004-01-01" @default.
- W2376762347 modified "2023-09-28" @default.
- W2376762347 title "A Study of Parameters of Photocatalytic Oxidizing Fluidized Bed" @default.
- W2376762347 hasPublicationYear "2004" @default.
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