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High strength BOD, N, P and low product sludge in piggery waste water treatment by rotating biological contactors
High strength BOD, N, P and low product sludge in piggery waste water treatment by rotating biological contactors
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机译:旋转生物接触器处理猪场废水中的高强度BOD,N,P和低产物污泥
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摘要
PURPOSE: A method for simultaneously eliminating highly concentrated organic material, nitrogen and phosphorous using a biological contact process is provided. CONSTITUTION: The method comprises the steps of treating wastewater in anaerobic zone(58) by operating a set of rotating discs(57), each disc being formed by combining a plurality of segments and being arranged in such a way that water courses of each disc is on the same lines at circumferences of the discs, while the rotating disc set(57) is completely submerged in the wastewater, treating the outflow of the wastewater in anoxic zone(56) by operating a set of rotating discs while the rotating disc set is completely submerged under the wastewater for eliminating organic material and nitrification, and treating the outflow of anoxic zone in an aeration zone(60) by partially submerging rotating disc set(61) in water to be treated, wherein BOD of inflow of the anaerobic zone(58) and the anoxic zone(56) is less than 5 to 120g/m¬2/day, water flow rate is less than 0.1 to 10L/m¬2/day, hydraulic retention time is greater than 2 to 20 hours, NH3-N is less than 0.1 to 10g/m¬2/day, NO3-N is less than 2 to 30g/m¬2/day, alkalinity is 20-100mg/L, CMEOH/N ratio is greater than 2.5, and pH is in a range of 5 to 9.5, and wherein treated water of the anoxic zone is returned to the anaerobic zone(58) by its 0.5 to 20 times, and outflow of a sedimentation tank is returned to the anaerobic zone(58) and the anoxic zone(56) by its 0.1 to 10 times, respectively.
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机译:目的:提供了一种使用生物接触工艺同时去除高浓度有机物质,氮和磷的方法。组成:该方法包括以下步骤:通过操作一组旋转圆盘(57)处理厌氧区(58)中的废水,每个圆盘是通过组合多个段形成的,其排列方式应使每个圆盘的水流向旋转盘组(57)完全浸没在废水中,通过操作一组旋转盘来处理缺氧区(56)中废水的流出完全浸没在废水中以消除有机物质和硝化作用,并通过将转盘组(61)部分浸没在待处理水中来处理曝气区(60)中缺氧区的流出,其中BOD流入厌氧区(58)和缺氧区(56)小于5至120g / m 2 /天,水流量小于0.1至10 L / m 2 /天,水力停留时间大于2至20小时, NH3-N少于0.1至10g /m¬2/天,NO3-N少于小于2至30g / m 2 /天,碱度为20-100mg / L,CMEOH / N比大于2.5,且pH在5至9.5的范围内,并且其中将缺氧区的处理后的水返回至厌氧区(58)的0.5至20倍,沉淀池的流出分别返回厌氧区(58)和缺氧区(56)的0.1至10倍。
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