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AEROBIC NITRATING DENITRIFICATION PROCESS

机译:好氧硝化脱氮工艺

摘要

PURPOSE: To simplify a process constitution, the operation facilitate and also efficiently perform nitrating/denitrification of sewage by placing alternately an aerobic stage and an anaerobic stage in multistage at the time of aerobically nitrating/denitrifying biologically an org. sewage containing a reducing type sulfur. ;CONSTITUTION: At first, waste water 1 is introduced into a hydrogen fermentation tank 2, where org. matters are decomposed at the time of treating a sulfur and ammonia-containing waste water such as night soil. Then, a fermented nitrated liq. 21 is introduced into an aerobic tank 3, and also a hydrogen sulfide 11 obtained by washing and desulfuring 10 a generated gas 9 is introduced into a selection tank 4 to control a concn. of total reducing type sulfur in the fermented nitrated liq. At this time, a tank in which aerobic tank/selection tank are made to be one unit are arranged in multi-stages (3, 5)/(4, 6) at an aerobic nitrating denitrification process. In the last selection tank 6, is a mixed gas 13 of a gaseous hydrogen and a gaseous CO2 is introduced by using a blower 14. Then, an efluent from the last selection tank 6 is introduced into a solid-liq. separation process 7 and this denitrifed water is discharged to outside, and also a concentrated fungus body is returned to the aerobic tank 3 as a return sludge 19.;COPYRIGHT: (C)1996,JPO
机译:目的:为简化工艺结构,在有机地对有机物进行需氧硝化/反硝化时,通过在多级中交替设置好氧阶段和厌氧阶段,从而简化了污水的硝化/反硝化操作。含还原型硫的污水。 ;组成:首先,将废水1引入到氢气发酵罐2中,该发酵罐位于org。在处理诸如夜土壤之类的含硫和氨的废水时,这些物质会分解。然后,发酵硝化液。将图21所示的气体引入需氧槽3中,并且还将通过洗涤和脱硫10获得的硫化氢11将生成的气体9引入选择槽4中以控制浓度。发酵硝化液中总还原型硫的含量此时,在好氧硝化反硝化工序中,将好氧槽/选择槽作为一个单元的槽以多级(3、5)/(4、6)排列。在最后选择箱6中,通过鼓风机14将气态氢和气态CO 2 的混合气体13引入。然后,将来自最后选择箱6的流出物引入到第一选择箱6中。固体液分离过程7,该反硝化的水被排放到外部,并且浓缩的菌体也作为回流污泥19返回到好氧池3中。版权所有:(C)1996,JPO

著录项

  • 公开/公告号JPH08168796A

    专利类型

  • 公开/公告日1996-07-02

    原文格式PDF

  • 申请/专利权人 EBARA CORP;EBARA RES CO LTD;

    申请/专利号JP19940333555

  • 发明设计人 TOYA TAISUKE;

    申请日1994-12-16

  • 分类号C02F3/34;C02F3/30;

  • 国家 JP

  • 入库时间 2022-08-22 04:01:14

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