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A/O-MBR工艺处理校园生活污水中水回用工程的设计与运行
引用本文:李菲菲,张衍,陈吕军,李荧,李伟,李建国,赵满成,吕启元. A/O-MBR工艺处理校园生活污水中水回用工程的设计与运行[J]. 环境污染治理技术与设备, 2013, 0(10): 4015-4020
作者姓名:李菲菲  张衍  陈吕军  李荧  李伟  李建国  赵满成  吕启元
作者单位:[1]清华大学环境学院,北京100084 [2]浙江清华长三角研究院生态环境研究所浙江省水质科学与技术重点实验室,嘉兴314050 [3]浙江双益环保科技发展有限公司,嘉兴314000 [4]清华大学修缮校园管理中心,北京100084
摘    要:针对Et处理量为1500m3的高校中水处理设施,论述了缺氧/好氧-MBR(A/O—MBR)处理工艺运行特性,完成了长效监测及经济性评价。系统MBR池污泥浓度(MLSS)控制在8~12g/L,缺氧池和好氧池水力停留时间(HRT)分别为3h和7h,污泥回流比为200%~300%。当进水COD、总氮、氨氮平均浓度分别为481.3、75.1和65.8mg/L时,出水COD、总氮、氨氮平均浓度分别为16.5、13.4和0.7mg/L,平均去除率分别为96.4%、81.9%和99.0%。在进行化学除磷的情况下,出水总磷的平均浓度为0.8mg/L,平均去除率86.5%。出水水质优于《城市污水再生利用城市杂用水水质》(GB/T18920—2002)中的相应水质指标要求。经济性分析结果显示,该中水站的电耗为0.58kWh/m3。

关 键 词:中水回用  校园生活污水  MBR

Design and operation of an A/O-MBR process for campus sewage treatment and reclamation
Affiliation:Li Feifei, Zhang Yan, Chen Lujun, Li Ying, Li Wei, Li Jianguo, Zhao Mancheng, Lu Qiyuan ( 1. School of Environment, Tsinghua University, Beijing 100084, China; 2. Department of Environmental Technology and Ecology,Yangtze Delta Region Institute of Tsinghua University, Zhejiang, Key Laboratory for Water Science and Technology of Zhejiang Province, Jiaxing 314050, China; 3. Envirtecs Water and Wastewater Technology Company, Jiaxing 314000, China 4. Management Center of Campus Repairs, Tsinghua University, Beijing 100084, China)
Abstract:An A/O-MBR process with the capacity of 1 500 m3/d was employed aiming at the reclamation of sewage in a university, and the water quality monitoring and economic analysis were conducted in the long- term operation. The MLSS of the MBR was maintained between 8 g/L to 12 g/L. The HRT of the anoxie tank and the aerobic tank was 3 h and 7 h, respectively, and the sludge return ratio was 200% -300%. When the average influent concentration of COD, total nitrogen and ammonia nitrogen were 481.3,75.1 and 65.8 mg/L, respectively, the average effluent concentration of COD, total nitrogen and ammonia nitrogen were 16.5,13.4 and 0. 7 mg/L, and the corresponding removal efficiency were 96.4% , 81.9% and 99.0% , respectively. The chemical phosphorus removal was achieved with the PAC coagulation, the effluent concentration of total phos- phorus was 0.8 mg/L and the average removal efficiency was 86.5%. The water quality is better than that of the National Water Quality Standard for Urban Miscellaneous Water Consumption (GB/T 18920-2002). The eco- nomic analysis showed that the electicity cost of the systerm is 0.58 kWh/m3.
Keywords:water reuse  college sewage  MBR
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