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Author:

Zhang, J. (Zhang, J..) (Scholars:张菁) | Zhang, Y. (Zhang, Y..) (Scholars:张勇) | Li, D. (Li, D..) (Scholars:李冬) | Liang, Y. (Liang, Y..) | Guan, H. (Guan, H..) | Zhao, S. (Zhao, S..)

Indexed by:

Scopus PKU CSCD

Abstract:

To compare the effect of two different operational modes on partial nitrification (PN), two-stage continuous stirred-tank reactors (CSTR) 1# (anoxic-oxic) and 2# (controlling DO and HRT) were constructed and operated at room temperature (18-22 ℃). Start-up time, stability, aeration consumption, sludge settling ability, as well as the adaptability to the decreasing of ammonia nitrogen concentration were investigated. PN in 1# and 2# were accomplished in 26 d and 41 d, respectively. When the effluent of an anaerobic/oxic (A/O) process for phosphorous removing (containing ammonia nitrogen 35-43 mg/L) was used as influent, PN was stable both under 1# and 2# condition, however, aeration consumption could be reduced by about 20% in 2#. When the ammonia nitrogen decreasing from 43 to 27 mg/L, PN in 1# would be unstable and the rates of PN decreased to 67.39%. For comparison, PN in 2# could be maintained stable with an ammonia removal rate of >88%. Settleability of sludge was good both in 1# and 2#. Rapid start-up could be achieved through controlling DO and HRT, and a stable and efficient PN could be maintained through anoxic-oxic. © 2016, Editorial Board of Journal of Harbin Institute of Technology. All right reserved.

Keyword:

Anoxic-oxic; Continuous stirred-tank reactor (CSTR); Dissolved oxygen (DO); Domestic wastewater; Hydraulic retention time (HRT); Partial nitrification

Author Community:

  • [ 1 ] [Zhang, J.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing, 100124, China
  • [ 2 ] [Zhang, J.]State Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology, Harbin, 150090, China
  • [ 3 ] [Zhang, Y.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing, 100124, China
  • [ 4 ] [Li, D.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing, 100124, China
  • [ 5 ] [Liang, Y.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing, 100124, China
  • [ 6 ] [Guan, H.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing, 100124, China
  • [ 7 ] [Zhao, S.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing, 100124, China

Reprint Author's Address:

  • 李冬

    [Li, D.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of TechnologyChina

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Source :

Journal of Harbin Institute of Technology

ISSN: 0367-6234

Year: 2016

Issue: 8

Volume: 48

Page: 11-16

Cited Count:

WoS CC Cited Count:

SCOPUS Cited Count: 3

ESI Highly Cited Papers on the List: 0 Unfold All

WanFang Cited Count:

Chinese Cited Count:

30 Days PV: 0

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