污水处理厂SAD工艺小试运行研究
CSTR:
作者:
作者单位:

(1.水质科学与水环境恢复工程北京市重点实验室(北京工业大学),北京 100124; 2.北京桑德环保集团技术研发中心,北京 101102; 3.城市水资源与水环境国家重点实验室(哈尔滨工业大学),哈尔滨 150090)

作者简介:

李冬(1976—),女,教授,博士生导师; 张杰(1938—),男,博士生导师,中国工程院院士

通讯作者:

中图分类号:

X523

基金项目:

国家自然科学基金优秀青年科学基金(51222807)


Operation of lab-scale SAD process in wastewater treatment plant
Author:
Affiliation:

(1.Key Laboratory of Beijing Water Quality Science & Water Environment Recovery Engineering(Beijing University of Technology), Beijing 100124, China; 2.Technology Research and Development Center, Beijing Sander Environmental Group, Beijing 101102, China; 3.State Key Laboratory of Urban Water Resource and Environment(Harbin Institute of Technology), Harbin 150090, China)

Fund Project:

  • 摘要
  • |
  • 图/表
  • |
  • 访问统计
  • |
  • 参考文献
  • |
  • 相似文献
  • |
  • 引证文献
  • |
  • 资源附件
  • |
  • 文章评论
    摘要:

    为提高反应器的氮素去除率,在市政污水处理厂进行同步厌氧氨氧化反硝化(SAD)工艺小试.以A/O除磷和亚硝化工艺处理后的生活污水为基质,启动厌氧氨氧化滤柱.反应器启动成功后,基质中投加有机碳源促进反硝化菌生长,启动SAD工艺,研究碳源质量浓度对SAD工艺的影响.由于葡萄糖对厌氧氨氧化菌抑制作用较小,成本较低,作为SAD工艺的有机碳源.结果表明:常温条件下,进水分别投加10,20和30 mg/L Glu,SAD工艺耦合效果良好,平均出水总氮质量浓度为9.16,8.10和6.41 mg/L.相较于厌氧氨氧化工艺,SAD工艺出水总氮质量浓度降低了16%~42%,常温条件下取得了良好的运行效果.冬季水温为10~12 ℃,基质中投加30 mg/L Glu,SAD工艺稳定性受到破坏并向反硝化工艺转变,出水氨氮质量浓度由0.5 mg/L增长至6.2 mg/L.水温对SAD工艺有较大影响,低温条件下SAD工艺中厌氧氨氧化菌与反硝化菌的竞争中占据劣势,工艺稳定性受到破坏.将基质Glu质量浓度降低到20 mg/L,出水总氮质量浓度为6.5~8.5 mg/L,冬季SAD工艺出水氨氮和总氮质量浓度满足北京市地方标准的A类排放标准.

    Abstract:

    Lab-scale simultaneously anaerobic ammonia oxidation and denitrification (SAD) process was operated in Municipal Waste Water Treatment Plant (WWTP). Sewage treated by A/O and nitrification process was served as substance to start up anaerobic ammonia oxidation filter reactor. Adding organic carbon-source to influent was served as substance to start up SAD filter reactor after successful start-up of Anammox reactor. Glucose was selected as organic carbon-source because it is harmless and inexpensive. The result show that SAD process performed well with 10, 20, and 30 mg/L Glucose added to effluent sewage at ambient temperature and average total nitrogen concentration of effluent was 9.16, 8.10, and 6.41 mg/L. Compared with Anammox process, SAD process performed better and total nitrogen concentration in effluent decreased 16-42 percents. Stability of SAD process was destroyed and SAD process turned to denitrification process when 30 mg/L Glucose was added in influent sewage in winter. Ammonia in effluent increased from 0.5 mg/L to 6.2 mg/L. The results indicate that temperature has superior effect on SAD process. The total nitrogen concentration in effluent varied from 6.5 to 8.5 mg/L when concentration of Glucose decreased to 20 mg/L. In winter, the effluent of SAD process reached the 1A level of integrated discharge standard of water pollutants applied in Beijing City.

    参考文献
    相似文献
    引证文献
引用本文

李冬,赵世勋,王俊安,关宏伟,朱金凤,张杰.污水处理厂SAD工艺小试运行研究[J].哈尔滨工业大学学报,2018,50(10):194. DOI:10.11918/j. issn.0367-6234.201705156

复制
相关视频

分享
文章指标
  • 点击次数:
  • 下载次数:
  • HTML阅读次数:
  • 引用次数:
历史
  • 收稿日期:2017-05-27
  • 最后修改日期:
  • 录用日期:
  • 在线发布日期: 2018-10-16
  • 出版日期:
文章二维码