化工学报 ›› 2012, Vol. 63 ›› Issue (10): 3262-3268.DOI: 10.3969/j.issn.0438-1157.2012.10.036

• 能源和环境工程 • 上一篇    下一篇

单级好氧脉冲式SBR处理垃圾渗滤液深度脱氮

朱如龙1, 王淑莹1, 李军2, 王凯1, 苗蕾1, 彭永臻1   

  1. 1. 北京工业大学北京市水质科学与水环境恢复工程重点实验室, 北京 100124;
    2. 浙江工业大学建筑工程学院, 浙江 杭州 310014
  • 收稿日期:2012-01-17 修回日期:2012-03-20 出版日期:2012-10-05 发布日期:2012-10-05
  • 通讯作者: 王淑莹
  • 作者简介:王淑莹,朱如龙(1987- ),男,硕士研究生。
  • 基金资助:

    国家自然科学基金项目(50978003)。

Advanced nitrogen removal of landfill leachate in single stage oxic pulsed SBR process

ZHU Rulong1, WANG Shuying1, LI Jun2, WANG Kai1, MIAO Lei1, PENG Yongzhen1   

  1. 1. Key Laboratory of Beijing for Water Quality Science and Water Environmental Recovery Engineering, Beijing University of Technology, Beijing 100124, China;
    2. College of Civil Engineering and Architecture, Zhejiang University of Technology, Hangzhou 310014, Zhejiang, China
  • Received:2012-01-17 Revised:2012-03-20 Online:2012-10-05 Published:2012-10-05
  • Supported by:

    supported by the National Natural Science Foundation of China(50978003).

摘要: 为了考察单级好氧工艺处理垃圾渗滤液的可行性和脱氮性能,采用脉冲进水式SBR工艺处理高氨氮实际垃圾渗滤液。脉冲SBR运行周期共分为4个缺氧段和3个好氧段,采用3次等量进水模式。缺氧4(An4)不投加外碳源,利用微生物内碳源将NO2--N 还原为N2。结果表明,经过4个不同进水TN阶段(118 d)的连续运行,获得了稳定和高效的脱氮性能。在进水COD为733~3971 mg·L-1的条件下,出水COD稳定在298 ~888.15 mg·L-1;在进水TN为299.78~1100.34 mg·L-1的条件下,出水TN稳定在13.89~36.27 mg·L-1。An4的平均理论内源反硝化速率(TDNRm)达到1.53 mg N·h-1·(g MLVSS)-1。运行阶段的单个周期内,An4内源反硝化速率(DNR)分为快(DNR1)和慢(DNR2)两部分。其中阶段2(Ph2)中的一个周期内DNR1可达2.80 mg N·h-1·(g MLVSS)-1。在没有物化预处理和不投加外加碳源的情况下,实现单级好氧系统对垃圾渗滤液的深度脱氮。

关键词: 脉冲进水, 垃圾渗滤液, SBR, 内源反硝化

Abstract: In order to investigate the feasibility and denitrification performance of single stage oxic process,pulsed feeding was employed in sequence batch reactor(SBR)process for treating a real landfill leachate containing much ammonia nitrogen(NH4+-N).Three equal feeds were used in the pulsed SBR process containing four anoxic and three oxic stages.No extra carbon source was demanded in all fourth anoxic stage(An4),and by use of internal carbon source from microorganism NO2--N was deoxidated into nitrogen(N2).The results indicate that the system is of stable and efficient performance of nitrogen removal after the acclimatization of activated sludge,as shown by continuous running of 118 days at 4 various total nitrogen(TN)concentration in influent.When chemical oxygen demand(COD)concentration in influent is a range of 733 mg稬-1 to 3971 mg稬-1,its concentration in effluent can be reduced to between 298 mg稬-1 and 888.15 mg稬-1,while TN concentration can be decreased from 299.78 mg稬-1 to 1100.34 mg稬-1 to between 13.89 mg稬-1 and 36.27 mg稬-1.The mean value of theoretical denitrification rate(TDNRm)by endogenous carbon for An4 is 1.53 mg N穐-1?(g MLVSS)-1.In a single cycle of operating phase,the endogenous denitrification rate(DNR)could be separated into two parts:fast one(DNR1)and slow one(DNR2),the value of DNR1 in a single cycle of phase2(Ph2) could reach 2.80 mg N穐-1?(g MLVSS)-1.Advanced nitrogen removal of landfill leachate can be realized in the single stage oxic process under well-controlled conditions without physicochemical pre-treatment and demand of extra carbon source.

Key words: pulsed feeding, landfill leachate, SBR, endogenous denitrification

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