首页|MBR+臭氧催化氧化处理工业废水的设计优化及存在问题分析

MBR+臭氧催化氧化处理工业废水的设计优化及存在问题分析

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针对苏南某工业废水处理厂现状出水难以达到《太湖地区城镇污水处理厂及重点工业行业主要水污染物排放限值》(DB 32/1072-2018)排放标准的问题,提出了膜生物反应器(MBR)+臭氧催化氧化的改造思路。原改良式序列间歇反应器(MSBR)工艺改造为AAO-MBR工艺,原絮凝沉淀池改造为臭氧催化氧化池,着重分析了臭氧催化氧化单元中催化剂污染及清洗措施等因素对CODCr 去除率的影响。结果表明:MBR+臭氧催化氧化作为化工废水提标改造技术路线,占地少,运行效果稳定,出水水质可稳定达标,但臭氧催化氧化单元受催化剂污染等因素影响较大,需加强预处理及清洗措施;工程新增投资为1 596 元/m3,新增运行成本为 0。73 元/m3,具有较好的经济效益。
Design Optimization and Analysis on Problems of MBR+ Catalytic Ozonation Process for Industrial Wastewater Treatment
In view of the problem that the current effluent of an industrial wastewater treatment plant(WWTP)in southern Jiangsu is difficult to meet the discharge standards of Discharge Standard of Main Water Pollutants for Municipal Wastewater Treatment Plant&Key Industries of Taihu Area(DB 32/1072-2018),the design idea of MBR+catalytic ozonation is proposed.The original MSBR process is transformed into AAO-MBR process,and the original flocculation sedimentation tank is transformed into catalytic ozonation tank.The influence of factors such as catalyst pollution and cleaning measures in the catalytic ozonation unit on the CODCr removal rate are analyzed emphatically.Results shows that,as a technical route for industrial wastewater upgrading and reconstruction,the MBR+catalytic ozonation occupies less land,has a stable operation effect,and the effluent quality can reach the standard stably.However,the catalytic ozonation is greatly affected by catalyst pollution and other factors,pretreatment and cleaning measures need to be strengthened.The project additional investment is 1 596 yuan/m3,and the additional operation cost is 0.73 yuan/m3,which has good economic benefits.

catalytic ozonationmembrane bio-reactor(MBR)industrial wastewaterupgrading and reconstructioncatalyst contamination

王国庆、吴念鹏、张雯、李新涛、张思强、张帆

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北京碧水源科技股份有限公司,北京 102206

奥赛科膜科技<天津>有限公司,天津 301800

北京市密云区水务局西田各庄水务站,北京 101509

臭氧催化氧化 膜生物反应器(MBR) 工业废水 提标改造 催化剂污染

2024

净水技术
上海市净水技术学会,上海市城乡建设和交通委员会科学技术委员会办公室

净水技术

CSTPCD
影响因子:0.643
ISSN:1009-0177
年,卷(期):2024.43(1)
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