| 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 |
| LI Dong,ZHAO Shixun,WANG Junan,GUAN Hongwei,ZHU Jinfeng,ZHANG Jie.Operation of lab-scale SAD process in wastewater treatment plant[J].Journal of Harbin Institute of Technology,2018,50(10):194.DOI:10.11918/j.issn.0367-6234.201705156 |
|
| 本文已被：浏览 1659次 下载 831次 |
码上扫一扫！ |
|
|
| 污水处理厂SAD工艺小试运行研究 |
|
李冬1,赵世勋1,王俊安2,关宏伟1,朱金凤1,张杰1,3
|
|
(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)
|
|
| 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.
|
| 关键词: 生活污水 厌氧氨氧化 反硝化 滤柱 生物膜 |
| DOI：10.11918/j.issn.0367-6234.201705156 |
| 分类号:X523 |
| 文献标识码:A |
| 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 |
|
LI Dong1,ZHAO Shixun1,WANG Junan2,GUAN Hongwei1,ZHU Jinfeng1,ZHANG Jie1,3
|
|
(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)
|
| 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.
|
| Key words: sewage Anammox denitrification filter biomembrane |
