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作者:

Li, Dong (Li, Dong.) (学者:李冬) | Cao, Ruihua (Cao, Ruihua.) | Yang, Hang (Yang, Hang.) | Cheng, Shuo (Cheng, Shuo.) | Zeng, Huiping (Zeng, Huiping.) | Zhang, Jie (Zhang, Jie.) (学者:张杰)

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摘要:

The effluent manganese (Mn) and ammonia nitrogen (NH3-N) concentration were found excessive when the low-temperature (5-7.8) groundwater containing high NH3-N, iron (Fe) and Mn contents (NH3-N>3.0 mg/L, Total Fe>12 mg/L, Fe2+>8.0 mg/L, Mn2+>3.0 mg/L) was purified by 'one-stage aeration combined with one-stage filtration' process. To improve the purification efficiency, the start-up of 'two-stage aeration combined with two-stage filtration' purification process and the oxidation-removal active sites (ORAS) of Fe, Mn and NH3-N were investigated. Two-stage bio-purification process successfully started after 133 days and the start-up period was mainly related to the Mn content. The results showed that the removal capacity of NH3-N and Mn was 29.66 g/(m2·h) and 27.08 g/(m2·h) respectively, and the water yield was a double of one-stage bio-purification process. According to the ORAS, Fe was removed to trace levels in the 0-50 cm section of the primary filter column, and the NH3-N was removed by 55.23% and 44.10% respectively in the 0-135 cm segment of the primary filter column and 0-50 cm segment of the secondary filter column. There were significant removal classification between Mn and NH3-N during the oxidation-removal process. The activity of Mn-oxidizing bacteria (MnOB) was significantly inhibited by NH3-N in concentration greater than 2.25 mg/L. The removal ratio and ORAS of Mn in both filter columns were affected by the concentration of NH3-N in raw water as well as the filtration rate. After a successful start-up, the Mn was removed by 5.53% and 89.34% respectively in the primary and secondary filter columns. © 2018, Editorial Board of Journal of Harbin Institute of Technology. All right reserved.

关键词:

Ammonia Boron compounds Effluents Groundwater Iron Iron compounds Manganese removal (water treatment) Nitrogen Nitrogen removal Oxidation Purification Reactor startup Temperature Water aeration Water filtration

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 ] [Cao, Ruihua]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering(Beijing University of Technology), Beijing; 100124, China
  • [ 3 ] [Yang, Hang]State Key Laboratory of Urban Water Resource and Environment(Harbin Institute of Technology), Harbin; 150090, China
  • [ 4 ] [Cheng, Shuo]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering(Beijing University of Technology), Beijing; 100124, China
  • [ 5 ] [Zeng, Huiping]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering(Beijing University of Technology), Beijing; 100124, China
  • [ 6 ] [Zhang, Jie]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering(Beijing University of Technology), Beijing; 100124, China
  • [ 7 ] [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: 2018

期: 2

卷: 50

页码: 8-18

被引次数:

WoS核心集被引频次: 0

SCOPUS被引频次: 3

ESI高被引论文在榜: 0 展开所有

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