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Method and device for the removal of nitrogen from nitrogen-containing and organic compounds containing wastewater

机译:从含氮和有机化合物废水中脱氮的方法和装置

摘要

1432667 Activated sludge process SOUTH AFRICAN INVENTIONS DEVELOPMENT CORP 16 July 1973 [4 Aug 1972] 33817/73 Heading C1C A 4- or 5-stage activated sludge process for removing nitrogen (and possibly phosphates) from organic waste water (e.g. sewage) comprises: (1) mixing the influent water with recycled liquor from stage 2 and recycled sludge from stage 5 and applying anaerobic or slightly aerobic conditions, preferably at a pH of at least 6À2 to effect bacterial denitrification; (2) aerating the product from stage 1 (optionally in admixture with further sludge recycled from stage 5) to effect bacterial nitrification; (3) subjecting the product from stage 2 (optionally in admixture with a carbon source, e.g. methanol) to anaerobic or slightly aerobic conditions to effect bacterial denitrification; (4) optionally aerating the product from stage 3 with the possible result of nitrification and/or phosphate precipitation; and (5) separating the product from stage 3 or 4 into activated sludge and clarified effluent. At any stage of the process, the liquor or sludge may be treated with time, alum, aluminate or iron slats to effect phosphate removal. Fig. 3 shows stages 1-5 of the above process being effected in zones 14.3, 16.3, 18.3, 20.3 and 22.3 respectively, where zones 16.3 and 20.3 are concentric endless annular channels through which the liquor is propelled by the rotation of surface aeration discs 44; and zones 14.3 and 18.3 have stirrers 36.3. Fig. 4 (not shown) is similar to Fig. 3 but with three central zones and only one annular channel. Fig. 5 (not shown) shows stages 1-4 being effected in adjoining rectangular tanks (with surface or submerged aeration for stages 2 and 4) and a separate -circular clarifier for stage 5. Fig. 2 (not shown) is a diagrammatic flow sheet.
机译:1432667活性污泥法南非发明开发公司1973年7月16日[1972年8月4日]标题C1C一种用于除去有机废水(例如污水)中的氮(可能是磷酸盐)的4或5级活性污泥法,包括: (1)将进水与第2阶段的回收液和第5阶段的回收污泥混合,并应用厌氧或略需氧的条件,最好在至少6至2的pH值下进行细菌反硝化; (2)给第1阶段的产品充气(可选地与从第5阶段回收的其他污泥混合)以实现细菌硝化作用; (3)使第2阶段的产品(可选地与碳源,例如甲醇混合)经受厌氧或略有氧的条件,以实现细菌的反硝化作用; (4)可选地对阶段3的产品进行充气,以产生硝化和/或磷酸盐沉淀的可能结果; (5)将第3或第4阶段的产物分离为活性污泥和澄清的废水。在该方法的任何阶段,可以用时间,明矾,铝酸盐或铁板条处理液体或污泥以除去磷酸盐。图3示出了上述方法的步骤1-5分别在区域14.3、16.3、18.3、20.3和22.3中进行,其中区域16.3和20.3是同心的环形环形通道,通过表面曝气盘的旋转推动液体通过该环形通道。 44;区域14.3和18.3具有搅拌器36.3。图4(未示出)类似于图3,但是具有三个中心区域和仅一个环形通道。图5(未示出)示出了在邻接的矩形罐(对于第二和第四阶段具有表面或浸入式曝气)中进行的第一至第四阶段,以及用于第五阶段的单独的圆形澄清器。图2(未示出)是示意图流程图。

著录项

  • 公开/公告号DE2339557B2

    专利类型

  • 公开/公告日1976-09-30

    原文格式PDF

  • 申请/专利权人

    申请/专利号DE19732339557

  • 发明设计人

    申请日1973-08-02

  • 分类号C02C1/17;

  • 国家 DE

  • 入库时间 2022-08-23 02:07:19

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