ZHOUJia-zhong,HANWen-jie,SONGPing-zhou,et al.BFM Process Design and Operation Analysis of an Intensive WWTP in North China[J].China Water & Wastewater,2023,39(18):126-132.
华北某集约型污水厂BFM工艺设计与运行分析
- Title:
- BFM Process Design and Operation Analysis of an Intensive WWTP in North China
- Keywords:
- suspended carrier; biofilm; magnetic loading precipitation; BFM; emergency treatment; rainy season overflow; prefabricated
- 摘要:
- 华北某新建处理规模为2×104 m3/d的污水处理设施,面临占地受限、进水水质复杂(含工业废水)、出水水质要求高(需达到地表水准Ⅴ类标准)、需在4个月内通水达标等难题。采用BFM为核心工艺,即纯膜MBBR工艺(B段)与改良磁加载沉淀工艺(M段),同时采用模块化设计,80 d完成了设计施工,20 d实现了通水达标。工艺流程为预处理+BFM+臭氧氧化+转盘滤池,B段总HRT仅为10 h,不设二沉池;M段设计表面负荷为11.57 m3/(m2·h);除预处理采用土建形式,其余均采用模块方式,可以缩短建设周期。全厂出水COD、氨氮、TN、TP、SS分别为(21.86±3.26)、(0.44±0.24)、(10.19±1.37)、(0.09±0.03)、(4.77±0.89) mg/L,出水水质稳定达到地表水准Ⅴ类标准。当BFM出水COD>30 mg/L时开启臭氧氧化装置。智水优控信息控制平台的加载,提高了污水厂的综合运营管理水平,实现了26%的节能降耗。本项目经营成本为0.98元/m3。
- Abstract:
- The treatment capacity of a new WWTP in north China is 2×104 m3/d, which faced with many problems, such as limited land occupation, complex quality of influent containing industrial wastewater, high effluent quality to reach level quasi-V standard for surface water within four months. BFM was adopted as core process, which consists of pure moving bed biofilm reactor, MBBR in section B and improved magnetic coagulation precipitation process in section process M. At the same time, the modular design was adopted. The design and construction were completed in 80 days, and the water supply reached the standard in 20 days. The process flow is pretreatment, BFM, ozone oxidation, and rotary filter. The HRT of section B without secondary sedimentation tank is 10 h. The design surface load of section M is 11.57 m3/(m2·h). Except that the pre?processing adopts civil construction, the rest sections are modular, which shortens the construction period. The effluent of COD, NH4+-N, TN, TP and SS are (21.86±3.26), (0.44±0.24), (10.19±1.37), (0.09±0.03) and (4.77±0.89) mg/L respectively. The effluent quality could stably superior to the design effluent criteria of level quasi-V. When the COD of BFM effleunt exceeds 30 mg/L, the ozone oxidation device will be started. The loading of artificial intelligence system improves the comprehensive operation and management level of WWTP, and saves 26% of energy and consumption. The operating cost of this project is 0.98 yuan/m3.
相似文献/References:
[1]郭莉芳,朱宇峰,滕良方,等.MBBR用于南方某污水厂强化脱氮效果分析[J].中国给水排水,2020,36(7):101.
[2]周家中,吴迪,郑临奥.纯膜MBBR工艺在国内外的工程应用[J].中国给水排水,2020,36(22):37.
ZHOU Jia-zhong,WU Di,ZHENG Lin-ao.Engineering Application of Pure MBBR Process at Home and Abroad[J].China Water & Wastewater,2020,36(18):37.
[3]张晓霞,熊仁久,周家中,等.浙江某工业废水处理厂升级改造运行效果解析[J].中国给水排水,2021,37(5):37.
ZHANG Xiao-xia,XIONG Ren-jiu,ZHOU Jia-zhong,et al.Analysis on Upgrading and Retrofitting Effect of an Industrial Wastewater Treatment Plant in Zhejiang[J].China Water & Wastewater,2021,37(18):37.
[4]杨平,周家中,管勇杰,等.基于MBBR的AAO和Bardenpho工艺改造效果对比[J].中国给水排水,2021,37(7):11.
YANG Ping,ZHOU Jia-zhong,GUAN Yong-jie,et al.Comparison of AAO and Bardenpho Processes Transformation Effect Based on MBBR[J].China Water & Wastewater,2021,37(18):11.
[5]陈如勇,张晓霞,周家中,等.MSBR改为三级A/O-MBBR连续流工艺的应用效果[J].中国给水排水,2021,37(14):108.
CHEN Ru-yong,ZHANG Xiao-xia,ZHOU Jia-zhong,et al.Practical Application Effect of Retrofitted MSBR into Three-stage A/O-MBBR Continuous Flow Process[J].China Water & Wastewater,2021,37(18):108.
[6]刘妍,余军,杨忠启,等.微污染水处理厂纯膜MBBR工艺改造工程设计[J].中国给水排水,2022,38(6):107.
LIUYan,YUJun,YANGZhong-qi,et al.Design of Pure MBBR Process Retrofitting Project for a Micro-polluted Water Treatment Plant[J].China Water & Wastewater,2022,38(18):107.
[7]李志超,肖宁,林蔓,等.MBBR耦合MBR用于东北某低温高排放标准污水厂[J].中国给水排水,2022,38(14):77.
LIZhi-chao,XIAONing,LINMan,et al.Application of MBBR Coupled with MBR Process in a Stringent Discharge Standard Wastewater Treatment Plant in Northeast China at Low Temperature[J].China Water & Wastewater,2022,38(18):77.
[8]王帆,李军,艾胜书,等.HRT对多级A/O耦合流离生化工艺低温脱氮的影响[J].中国给水排水,2022,38(17):74.
WANGFan,LIJun,AISheng-shu,et al.Effect of Hydraulic Retention Time on Multistage A/O Coupled with Flow-separated Biochemical Process for Nitrogen Removal from Wastewater at Low Temperature[J].China Water & Wastewater,2022,38(18):74.
[9]丁鑫,李祥,毕贞,等.厌氧/好氧交替生物膜工艺利用原水中碳源回收磷[J].中国给水排水,2023,39(5):1.
DINGXin,LIXiang,BIZhen,et al.Recovery of Phosphorus by Anaerobic/Aerobic Alternative Biofilm Process Using Organic Carbon from Raw Wastewater[J].China Water & Wastewater,2023,39(18):1.
[10]许航,刘伯男,王月婷,等.备用水源原水管道水质及生物膜群落结构变化[J].中国给水排水,2023,39(5):38.
XUHang,LIUBo-nan,WANGYue-ting,et al.Changes of Water Quality and Biofilm Community Composition in Raw Water Pipeline of Emergency Water Source[J].China Water & Wastewater,2023,39(18):38.