WANGJing,YANGYi,BAIWen-long,et al.Application of Multi-stage A/O and Ozonation Combined Process for Upgrading and Reconstruction of a Wastewater Treatment Plant to Class Quasi-Ⅲ Standard for Surface Water[J].China Water & Wastewater,2025,41(6):83-88.
多级A/O+臭氧氧化工艺用于污水厂准Ⅲ类水提标改造
- Title:
- Application of Multi-stage A/O and Ozonation Combined Process for Upgrading and Reconstruction of a Wastewater Treatment Plant to Class Quasi-Ⅲ Standard for Surface Water
- Keywords:
- wastewater treatment plant; upgrading and reconstruction; ozonation; class quasi-Ⅲ standard for surface water
- 摘要:
- 鄂尔多斯市某污水处理厂原设计规模为6.0×104 m3/d,主体工艺采用氧化沟+二沉池+混凝沉淀池+砂滤池,设计出水水质执行《城镇污水处理厂污染物排放标准》(GB 18918—2002)的一级A标准。由于污水厂出水的受纳水体下游为水源地,需对现状污水处理工艺进行提标改造,使出水水质达到地表水准Ⅲ类标准。为此,根据污水厂实际处理水量,将设计规模调整为4.5×104 m3/d,将现状氧化沟工艺改造为多级A/O(A/A/O/A/O)运行模式,并在一级好氧池投加填料,强化处理能力的同时提高冬季抗冲击负荷能力,另外新建臭氧接触池进行深度处理。改造后,系统的抗冲击负荷能力增强,出水水质稳定,出水COD、NH3-N、TP平均浓度分别为12.8、0.14、0.08 mg/L,优于地表水Ⅲ类标准;出水TN平均浓度为9.4 mg/L,满足再生水回用和尾水排放要求。
- Abstract:
- The original design scale of a wastewater treatment plant (WWTP) in Ordos City is 6.0×104 m?/d. The primary treatment process incorporates oxidation ditch, followed by secondary sedimentation tank, coagulation sedimentation tank, and sand filter. The effluent quality is designed to meet first level A criteria specified in Discharge Standard of Pollutants for Municipal Wastewater Treatment Plant (GB 18918-2002). Given that the receiving water body downstream of the WWTP serves as the drinking water source, it is imperative to upgrade the existing wastewater treatment process to ensure that the effluent quality meets the class quasi-Ⅲ standard specified in Environmental Quality Standards for Surface Water (GB 3838-2002). In accordance with the actual treatment capacity of the WWTP, the design capacity scale was adjusted to 4.5×104 m3/d. The existing oxidation ditch process was modified to the multi-stage A/O (A/A/O/A/O) system, and fillers were introduced into the primary-aeration tank to enhance treatment efficiency and improve resistance to shock loads in winter. Additionally, a new ozone contact tank was constructed for advanced treatment. Following the reconstruction, the system’s resistance to shock loads was significantly enhanced and the effluent quality was stable. The average concentrations of COD, NH3-N and TP in the effluent were 12.8 mg/L, 0.14 mg/L, and 0.08 mg/L, respectively, all of which were lower than the class Ⅲ limits specified in the surface water standard. Additionally, the average concentration of TN in the effluent was 9.4 mg/L, satisfying the requirements for both reclaimed water reuse and tailwater discharge.
相似文献/References:
[1]王 亮.马来西亚Pantai地埋式污水厂环网供配电结构设计[J].中国给水排水,2018,34(22):63.
WANG Liang.Power Supply and Distribution Structure Design of Ring Network for Pantai Underground Wastewater Treatment Plantin Malaysia[J].China Water & Wastewater,2018,34(6):63.
[2]侯晓庆,邓 磊,高海英,等.MBR工艺在神定河污水处理厂升级改造工程中的应用[J].中国给水排水,2018,34(22):66.
HOU Xiao-qing,DENG Lei,GAO Hai-ying,et al.Application of MBR Process in the Upgrading and Reconstruction Project of Shending River WastewaterTreatment Plant[J].China Water & Wastewater,2018,34(6):66.
[3]邱明海.北京市垡头污水处理厂改扩建工程设计技术方案[J].中国给水排水,2018,34(20):13.
QIU Ming hai.Reconstruction and Expansion Design Technical Plan of Beijing Fatou Wastewater Treatment Plant[J].China Water & Wastewater,2018,34(6):13.
[4]郝二成,郭毅,刘伟岩,等.基于数学模拟的污水厂运行分析——建模与体检[J].中国给水排水,2020,36(15):23.
HAO Er-cheng,GUO Yi,LIU Wei-yan,et al.Operation Analysis of Wastewater Treatment Plant Based on Mathematical Simulation: Modeling and Examination[J].China Water & Wastewater,2020,36(6):23.
[5]张月,王阳,张宏伟,等.阳泉市污水处理二期工程BARDENPHO工艺设计和运行[J].中国给水排水,2020,36(16):64.
ZHANG Yue,WANG Yang,ZHANG Hong-wei,et al.Design and Operation of BARDENPHO Process in Phase Ⅱ Project of Yangquan Wastewater Treatment Plant[J].China Water & Wastewater,2020,36(6):64.
[6]祝新军,蔡芝斌,姚斌,等.绍兴污水处理厂气浮设备的优化改造[J].中国给水排水,2020,36(16):101.
ZHU Xin-jun,CAI Zhi-bin,YAO Bin,et al.Optimization and Modification of Air Floatation Equipment in Shaoxing Wastewater Treatment Plant[J].China Water & Wastewater,2020,36(6):101.
[7]王文明,杨淇椋,蔡依廷,等.MSBR工艺在高排放标准污水处理厂的应用[J].中国给水排水,2020,36(16):111.
WANG Wen-ming,YANG Qi-liang,CAI Yi-ting,et al.Application of MSBR Process in Wastewater Treatment Plant with Stringent Discharge Standard[J].China Water & Wastewater,2020,36(6):111.
[8]郝二成,郭毅,刘伟岩,等.基于数学模拟的污水厂运行分析——控制与优化[J].中国给水排水,2020,36(17):23.
HAO Er-cheng,GUO Yi,LIU Wei-yan,et al.Operation Analysis of Wastewater Treatment Plant Based on Mathematical Simulation: Control and Optimization[J].China Water & Wastewater,2020,36(6):23.
[9]王阳,张月,王晓康,等.高排放标准下的改良AAO+深度处理工程案例[J].中国给水排水,2020,36(18):56.
WANG Yang,ZHANG Yue,WANG Xiao-kang,et al.Project Case of Modified AAO and Advanced Treatment Process under High Emission Standards[J].China Water & Wastewater,2020,36(6):56.
[10]郑枫,慕杨,孙逊.MBR工艺用于山东省某污水处理厂扩建工程[J].中国给水排水,2020,36(18):81.
ZHENG Feng,MU Yang,SUN Xun.MBR Process Used in Expansion Project of a Sewage Treatment Plant in Shandong Province[J].China Water & Wastewater,2020,36(6):81.
[11]伍波,叶昌明,王小林,等.上向流反硝化深床滤池用于污水厂提标改造[J].中国给水排水,2022,38(4):103.
WUBo,YEChang-ming,WANGXiao-lin,et al.Application of Upflow DDBF in Upgrading and Reconstruction of a WWTP[J].China Water & Wastewater,2022,38(6):103.
[12]戴杨叶,张大鹏,伍林芳,等.某污水处理厂提标工程中的氧化沟改造实践[J].中国给水排水,2022,38(24):92.
DAIYang-ye,ZHANGDa-peng,WULin-fang,et al.Reconstruction Practice of Oxidation Ditch in a WWTP Upgrading Project[J].China Water & Wastewater,2022,38(6):92.
[13]杨淇椋,宋凤鸣,古伟,等.反硝化生物滤池+高效气浮工艺用于准Ⅳ类提标改造[J].中国给水排水,2023,39(12):125.
YANGQi-liang,SONGFeng-ming,GUWei,et al.Application of Denitrifying Biofilter and High-efficiency Air Floatation in Upgrading of a WWTP for Quasi-Ⅳ Standard[J].China Water & Wastewater,2023,39(6):125.
[14]李双菊,程瑞丰,柳佳然,等.后置反硝化滤池和活性炭接触池的提标工程设计[J].中国给水排水,2024,40(18):96.
LIShuang-ju,CHENGRui-feng,LIUJia-ran,et al.Upgrading Engineering Design of Post-denitrification Filter and Activated Carbon Contact Tank[J].China Water & Wastewater,2024,40(6):96.