LIYi-long,BAOYu,DIWen-zheng,et al.Design of Step-feed Multi-stage AO+MBR Process under High Discharge Standard[J].China Water & Wastewater,2022,38(4):76-81.
高排放标准下分段进水多级AO+MBR工艺的设计
- Title:
- Design of Step-feed Multi-stage AO+MBR Process under High Discharge Standard
- Keywords:
- step-feed multi-stage AO; MBR; reclaimed water plant; high discharge standard; ozone catalytic oxidation
- 摘要:
- 北京某再生水厂原设计规模4.5×104 m3/d,需迁址新建,并扩容至一期设计规模6.5×104 m3/d,总规模10×104 m3/d。出水标准由《城镇污水处理厂污染物排放标准》(GB 18918—2002)中的一级A标准,提高至北京地标《城镇污水处理厂水污染物排放标准》(DB 11/890—2012)中的A标准(准Ⅲ类标准)。通过污染物指标分析和工艺方案比选,确定采用预处理+分段进水多级AO+MBR+臭氧催化氧化工艺,实际试运行出水水质稳定达标。采用分段进水多级AO方式,灵活分配进水碳源,强化内源反硝化加强TN去除效果,实际运行在进水超标的工况下通过投加外部碳源使出水TN保持在10 mg/L以下。另外,生物池和膜池膜组件采用精确曝气和脉冲曝气系统,试运行期间有效节约能耗约10%。
- Abstract:
- The original design scale of a reclaimed water plant in Beijing is 4.5×104 m3/d. The plant was newly built in other place and expanded to the design scale of 6.5×104 m3/d in the phase Ⅰ project (the total scale is 10×104 m3/d), and the discharge standard was upgraded from the first level A criteria specified in Discharge Standard of Pollutants for Municipal Wastewater Treatment Plant (GB 18918-2002) to level A criteria (quasi?class Ⅲ standard) specified in a local standard of Beijing Discharge Standard of Water Pollutants for Municipal Wastewater Treatment Plants (DB 11/890-2012). Through analysis of the pollutant indicators and comparison of the process scheme, the process of pretreatment, step-feed multi-stage AO process, MBR and ozone catalytic oxidation was selected. The trial operation indicated that the effluent quality stably met the discharge standard. The step?feed multi?stage AO process flexibly allocated the carbon sources in the influent and improved the endogenous denitrification to enhance TN removal performance. When the influent quality exceeded the standard in actual operation, TN in the effluent still remained below 10 mg/L by adding external carbon source. In addition, precise aeration and pulse aeration systems were applied to the biological tank and membrane tank, which effectively saved energy consumption by approximately 10% during trial operation.
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