[1]王玉敏,邵先涛,周家中,等.BFM工艺用于山东某污水厂提标改造[J].中国给水排水,2025,41(12):97-102.
　WANGYu-min,SHAOXian-tao,ZHOU Jia-zhong,et al.Application of BFM Process in the Upgrading and Reconstruction of a WWTP in Shandong Province[J].China Water & Wastewater,2025,41(12):97-102.
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BFM工艺用于山东某污水厂提标改造

中国给水排水[ISSN:1000-4062/CN:12-1073/TU] 卷: 第41卷 期数: 2025年第12期 页码: 97-102 栏目: 出版日期: 2025-06-17
Title:
Application of BFM Process in the Upgrading and Reconstruction of a WWTP in Shandong Province
作者:
王玉敏1， 邵先涛2， 周家中3， 苗在上4， 孙玉国4， 吴迪3
（1.临朐县住房和城乡建设局，山东 潍坊 262619；2.青岛西海岸新区工业和信息化局，山东 青岛 266555；3.青岛思普润水处理股份有限公司，山东 青岛 266510；4.青岛西海岸新区水务发展中心，山东 青岛 266500）
Author(s):
WANG　Yu-min1， SHAO　Xian-tao2， ZHOU Jia-zhong3， MIAO　Zai-shang4， SUN　Yu-guo4， WU　Di3
（1. Linqu County Bureau of Housing and Urban?Rural Development， Weifang 262619， China； 2. Bureau of Industry and Information Technology of Qingdao West Coast New Area， Qingdao 266555， China； 3. Qingdao SPRING Water Treatment Co. Ltd.， Qingdao 266510， China； 4. Qingdao West Coast New Area Water Affairs Development Center， Qingdao 266500， China）
关键词:
提标改造;  生物膜;  流化床生物膜反应器;  深度处理
Keywords:
upgrading and reconstruction;  biofilm;  MBBR;  advanced treatment
摘要:
山东某污水厂处理规模为6×104 m3/d，采用新增污水处理工艺单元的方式进行地表水准Ⅳ类提标改造。采用基于生物膜法的BFM并集成活性炭吸附的技术路线。提标改造处理单元占地面积为0.03 m2/（m3·d-1），BFM生物池好氧区和缺氧区悬浮载体填充率分别达到55%和50%。稳定运行期间，BFM实际进水水质波动较大，在进水COD、NH3-N、TN、TP、SS分别为16.72~37.34、0.22~4.19、9.70~14.15、0.03~0.42、6.79~9.54 mg/L的条件下，出水相应指标可稳定降至16.59~21.89、0.03~0.13、7.15~9.04、0.02~0.10、3.24~6.51 mg/L。高通量测序结果显示，生物膜在低基质条件下实现了功能菌的高效富集，好氧区硝化菌和缺氧区反硝化菌的相对丰度分别达到7.77%和16.5%。BFM工艺具有集约、高效、稳定的优势，对类似污水厂的提标改造具有借鉴作用。
Abstract:
A wastewater treatment plant (WWTP) in Shandong Province has a treatment capacity of 6×104 m3/d, adopting the method of adding new wastewater treatment process units for the upgrading of class Ⅳ standard. The process adopts the technical route of BFM based on biofilm method and integrated activated carbon adsorption unit. The area occupied by the upgrading and reconstruction processing unit is 0.03 m2/(m3·d-1), and the filling rates of the aerobic and anaerobic zones in the BFM biological tank reached to 55% and 50%, respectively. During stable operation, the actual influent of BFM fluctuates greatly. Under the conditions of influent COD, NH3-N, TN, TP, and SS being 16.72-37.34 mg/L, 0.22-4.19 mg/L, 9.70-14.15 mg/L, 0.03-0.42, and 6.79-9.54 mg/L, respectively, after BFM treatment, it can be stably reduced to 16.59-21.89 mg/L, 0.03-0.13 mg/L, 7.15-9.04 mg/L, 0.02-0.10 mg/L, and 3.24-6.51 mg/L. High-throughput sequencing results showed that the biofilm achieved efficient enrichment of functional bacteria under low substrate conditions, with relative abundances of aerobic nitrifying bacteria and anaerobic denitrifying bacteria reaching 7.77% and 16.5%, respectively. The BFM process has the advantages of intensification, efficiency, and stability, which can serve as a reference for upgrading and reconstruction similar sewage treatment plants.

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更新日期/Last Update: 2025-06-17