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作者:

Li, Dong (Li, Dong.) (学者:李冬) | Guo, Yuezhou (Guo, Yuezhou.) | Lao, Huimei (Lao, Huimei.) | Cao, Meizhong (Cao, Meizhong.) | Zhang, Jie (Zhang, Jie.) (学者:张杰)

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摘要:

In order to assess the impact of different carbon/nitrogen (C/N) on anoxic/aerobic sequencing batch reactor (SBR) nitrosation system, the C/N was adjusted to 0, 2/3, 1, 4/3, 2, 3, 6 at room temperature (18-20). The results showed that the activated sludge system with the influent chemical oxygen demand (COD) loading and ammonia loading of 0.2 and 0.3 kg/(m3•d) successfully achieved nitritation only after 24 d. It needed more time to achieve nitritation with no COD in influent. When the C/N was less than 6, the system maintained good nitritation performance with the nitrosation rate of over 90%. When the C/N was 6, the nitrosation rate dropped to 70%. When the C/N was 4/3, the heterotrophic bacteria used the influent COD for denitrification adequately, the total nitrogen removal efficiency reached 49.8%, and the COD removal efficiency remained above 80%. Because the sludge system lacked the carbon source, the total nitrogen removal efficiency increased with the increase of the C/N when it was less than 4/3. When the C/N was 4/3 to 2, the COD and total nitrogen removal efficiencies almost remained unchanged. When the C/N was 2 to 6, due to the reduction of influent ammonia loading, the removal efficiencies of COD and total nitrogen showed a downward trend. At the end of operation (154 d), COD and total nitrogen removal efficiencies were 64.8% and 18%, respectively. When the C/N increased due to an increase in COD, the proteins (PN) tended to increase gradually, and polysaccharides (PS) almost did not change, while the decrease in ammonia caused an increase in the C/N, PN and PS decreased, but the value of PN/PS increased. © 2019, Editorial Board of Journal of Harbin Institute of Technology. All right reserved.

关键词:

Activated sludge process Ammonia Batch reactors Carbon Chemical oxygen demand Chemical reactions Efficiency Loading Nitrogen removal

作者机构:

  • [ 1 ] [Li, Dong]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing; 100124, China
  • [ 2 ] [Guo, Yuezhou]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing; 100124, China
  • [ 3 ] [Lao, Huimei]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing; 100124, China
  • [ 4 ] [Cao, Meizhong]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing; 100124, China
  • [ 5 ] [Zhang, Jie]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing; 100124, China
  • [ 6 ] [Zhang, Jie]State Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology, Harbin; 150090, China

通讯作者信息:

  • 李冬

    [li, dong]key laboratory of beijing for water quality science and water environment recovery engineering, beijing university of technology, beijing; 100124, china

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来源 :

Journal of Harbin Institute of Technology

ISSN: 0367-6234

年份: 2019

期: 2

卷: 51

页码: 1-7

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