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间歇曝气连续流反应器同步硝化反硝化除磷
引用本文:赵智超,黄剑明,李健,张为堂,张力航,吴雪晴,陈永志.间歇曝气连续流反应器同步硝化反硝化除磷[J].环境科学,2019,40(2):799-807.
作者姓名:赵智超  黄剑明  李健  张为堂  张力航  吴雪晴  陈永志
作者单位:兰州交通大学环境与市政工程学院,兰州,730070;北控水务(中国)投资有限公司,北京,100124
基金项目:国家自然科学基金项目(51668033);甘肃省高等学校特色专业-环境工程(101004);兰州交通大学大学生创新实验项目(2018110)
摘    要:采用连续流反应器处理生活污水,保持厌氧段格室为3格,将缺氧段格室从2格减少至0格,好氧段格室由5格逐渐增加至7格,Run1时对好氧段格室采用连续曝气,Run2~Run4时采用间歇曝气.曝/停比分别为:40 min/20 min、40 min/30min、40 min/40 min,硝化液回流比从150%逐渐减少至0%. Run4时,平均进水COD、NH+4-N、TN、PO_4~(3-)-P浓度分别为259. 34、60. 26、64. 42、6. 10 mg·L-1,出水COD、NH+4-N、TN、PO_4~(3-)-P分别为26. 40、1. 03、5. 84、0. 30 mg·L-1.反应器对氮素的去除量从Run1时的192. 30 mg·h-1逐渐增加至Run4时的244. 00 mg·h-1,相应地去除率从65. 40%逐渐增大至95. 30%;从Run1~Run4,反硝化聚磷菌和聚磷菌的活性分别从36. 05%和38. 20%增大至140. 50%和133. 40%;通过间歇曝气在连续流反应器中实现了同步硝化反硝化除磷脱氮,为污水处理厂提标改造提供参考.

关 键 词:连续流反应器  间歇曝气  反硝化聚磷菌  同步硝化反硝化除磷  生活污水
收稿时间:2018/7/13 0:00:00
修稿时间:2018/8/14 0:00:00

Simultaneous Nitrification and Denitrifying Phosphorus Removal in Continuous Flow Reactor with Intermittent Aeration
ZHAO Zhi-chao,HUANG Jian-ming,LI Jian,ZHANG Wei-tang,ZHANG Li-hang,WU Xue-qing and CHEN Yong-zhi.Simultaneous Nitrification and Denitrifying Phosphorus Removal in Continuous Flow Reactor with Intermittent Aeration[J].Chinese Journal of Environmental Science,2019,40(2):799-807.
Authors:ZHAO Zhi-chao  HUANG Jian-ming  LI Jian  ZHANG Wei-tang  ZHANG Li-hang  WU Xue-qing and CHEN Yong-zhi
Institution:School of Environmental and Municipal Engineering, Lanzhou Jiaotong University, Lanzhou 730070, China,School of Environmental and Municipal Engineering, Lanzhou Jiaotong University, Lanzhou 730070, China,School of Environmental and Municipal Engineering, Lanzhou Jiaotong University, Lanzhou 730070, China,Beijing Enterprises Water Group(China) Investment Limited, Beijing 100124, China,School of Environmental and Municipal Engineering, Lanzhou Jiaotong University, Lanzhou 730070, China,School of Environmental and Municipal Engineering, Lanzhou Jiaotong University, Lanzhou 730070, China and School of Environmental and Municipal Engineering, Lanzhou Jiaotong University, Lanzhou 730070, China
Abstract:A continuous flow reactor (TCFR) with 10 compartments was used to treat domestic sewage. The anaerobic compartments of TCFR were kept at 3. The anoxic compartments of TCFR were reduced from 2 to 0. Therefore, the aerobic compartments of TCFR were increased gradually from 5 to 7. The aerobic compartments were set to continual aeration in Run1 and intermittent aeration from Run2 to Run4. The aeration/non-aeration ratios were 40 min/20 min,40 min/30 min, and 40 min/40 min, respectively. The nitrification liquid reflux ratios were reduced gradually from 150% to 0%. When the average influent concentrations of COD, NH4+-N, TN, and PO43--P were 259.34, 60.26, 64.42, and 6.10 mg·L-1, respectively, the corresponding effluent concentrations were 26.40, 1.03, 5.84, and 0.3 mg·L-1, respectively in Run4. The nitrogen removal amounts increased gradually from 192.30 mg·h-1 in Run1 to 244.00 mg·h-1 in Run4, and the corresponding removal rates increased from 65.40% to 95.30%. The activity of denitrifying phosphorus accumulating organisms (DPAOs) and phosphorus accumulating organisms (PAOs) increased from 36.05% and 38.20% in Run1 to 140.50% and 133.40% in Run4, respectively. Simultaneous nitrification and denitrifying phosphorus removal was achieved in TCFR by adopting intermittent aeration, which provided a reference for the reformation of sewage treatment plants.
Keywords:continuous flow reactor  intermittent aeration  denitrifying phosphorus accumulating organisms(DPAOs)  simultaneous nitrification and denitrifying phosphorus removal  domestic sewage
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