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作者:

Wang, Xiaolian (Wang, Xiaolian.) | Wang, Shuying (Wang, Shuying.) (学者:王淑莹) | Ma, Yong (Ma, Yong.) | Peng, Yongzhen (Peng, Yongzhen.) (学者:彭永臻)

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摘要:

A pilot-scale nutrient removal activated sludge system, based on the A2O configuration, was used to treat brewery wastewater. In the experiment, the existence of denitrifying phosphorus removing bacteria (DPB) and the contribution of DPB to phosphorus removal was observed. The tests showed the average total amount of anoxic P uptake accounted for 70% of the total amount of P uptake of the system at steady state, oxygen requirement could be decreased significantly (about 25%). Denitrifying phosphate removal resolved the competition for organic substrates between Poly-P organisms and denitrifiers under lower organic loading. Effluent total-P concentration could achieve less than 0.30 mg·L-1 and average effluent total-N was less than 10 mg·L-1. It is clearly demonstrated that the phosphorus uptake almost stopped in an over-aerated system, the released phosphorus could not be taken up fully again. Consequently, incomplete phosphorus uptake led to temporary reduction of biological phosphorous removal efficiency. It took about the time of one sludge age to eliminate that disturbance.

关键词:

Bacteria Chemical industry Effluents Nitrogen removal Phosphorus Removal Wastewater treatment

作者机构:

  • [ 1 ] [Wang, Xiaolian]School of Environmental and Energy Engineering, Beijing University of Technology, Beijing 100022, China
  • [ 2 ] [Wang, Shuying]School of Environmental and Energy Engineering, Beijing University of Technology, Beijing 100022, China
  • [ 3 ] [Ma, Yong]School of Municipal and Environmental Engineering, Harbin Institute of Technology, Harbin 150090, China
  • [ 4 ] [Peng, Yongzhen]School of Environmental and Energy Engineering, Beijing University of Technology, Beijing 100022, China

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来源 :

Journal of Chemical Industry and Engineering (China)

ISSN: 0438-1157

年份: 2005

期: 8

卷: 56

页码: 1565-1570

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