A liquid-solid fluidized bed reactor was used to carry out sulfate reduction with a mixed culture of sulfate reducing bacteria. The bacteria were immobilized on porous glass beads. Stable fluidized bed operation with these biofilm-coated beads was possible. The low specific gravity of the hydrated b
Selective catalytic reduction by urea in a fluidized-bed reactor
β Scribed by Seon Ah Roh; Soon Hwa Jung; Sang Mun Jeong; Sang Done Kim
- Publisher
- Wiley (John Wiley & Sons)
- Year
- 2003
- Tongue
- English
- Weight
- 159 KB
- Volume
- 78
- Category
- Article
- ISSN
- 0268-2575
- DOI
- 10.1002/jctb.910
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β¦ Synopsis
Abstract
The selective catalytic reduction (SCR) of NO~x~ by urea as a reducing agent was carried out over fresh and sulfated CuO/Ξ³βAl~2~O~3~ catalysts in a fluidizedβbed reactor. The optimum temperature ranges for NO reduction on the fresh and sulfated CuO/Ξ³βAl~2~O~3~ catalysts were 300β350 Β°C and 400β450 Β°C, respectively. NO reduction with the sulfated CuO/Ξ³βAl~2~O~3~ catalyst was somewhat higher than that with the fresh CuO/Ξ³βAl~2~O~3~ catalyst. N~2~O formation increased with increasing reaction temperature. Ammonia (NH~3~) slip increased with increasing gas velocity and decreased with increasing reaction temperature. Copyright Β© 2003 Society of Chemical Industry
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