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作者:

Zhang, Jie (Zhang, Jie.) (学者:张杰) | Cheng, Shuo (Cheng, Shuo.) | Li, Dong (Li, Dong.) (学者:李冬) | Lü, Yufeng (Lü, Yufeng.) | Cao, Ruihua (Cao, Ruihua.) | Wang, Yanju (Wang, Yanju.)

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摘要:

To optimize the initiation of continuous flow CANON process, the research compared startup course and nitrogen removal performance under distinct NLR in room temperature ((25±1)) between two sets of AUSB reactors, one of which was middle-setting aeration (1#), and the other was bottom-setting aeration (2#). The results showed that 1#, 2# successfully started CANON process treating domestic wastewater with relatively low ammonium concentration (90 mg/L) in 55 d and 70 d respectively. In the progress of increasing nitrogen loading rate gradually, both of them gained the highest nitrogen removal rate, which was 0.280 kg/(m3·d) for 1#, and 0.256 kg/(m3·d) for 2# under the condition of HRT=6 h. In later operation, 1# maintained efficient nitrogen removal status whose eigenvalue (Δρ(TN)/Δρ(NO3--N)) remained around 7.83, however, eigenvalue of 2# decreased to 7.49 after 125 d operation owing to the activity of NOB strengthened. The middle-setting aerated AUSB accomplished a higher total nitrogen removal rate which was 74.98% through the combination with simultaneous nitritation-Anammox (SNA) and alternate nitritation-Anammox (ANA) double pathways, which was ascribed to the enhancement of AOB and AnAOB activity and the effective suppression on NOB. Middle-setting aerated AUSB could shorten starting period of continuous flow CANON process, and furthermore realize long-term stable autotrophic nitrogen removal. © 2018, Editorial Board of Journal of Harbin Institute of Technology. All right reserved.

关键词:

Eigenvalues and eigenfunctions Nitrogen removal Wastewater treatment Ammonia

作者机构:

  • [ 1 ] [Zhang, Jie]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering(Beijing University of Technology), Beijing; 100124, China
  • [ 2 ] [Zhang, Jie]State Key Laboratory of Urban Water Resource and Environment(Harbin Institute of Technology), Harbin; 150090, China
  • [ 3 ] [Cheng, Shuo]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering(Beijing University of Technology), Beijing; 100124, China
  • [ 4 ] [Li, Dong]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering(Beijing University of Technology), Beijing; 100124, China
  • [ 5 ] [Lü, Yufeng]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering(Beijing University of Technology), Beijing; 100124, China
  • [ 6 ] [Cao, Ruihua]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering(Beijing University of Technology), Beijing; 100124, China
  • [ 7 ] [Wang, Yanju]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering(Beijing University of Technology), Beijing; 100124, 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: 2018

期: 2

卷: 50

页码: 1-7

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SCOPUS被引频次: 1

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