A schematic representation of the p

A schematic representation of the phosphorus-removing apparatus of Japanese Unexamined Laid Open Patent Application Hll-188383 is shown in FIG. 5, where the raw water 31 is introduced into the anaerobic tank 33 o f the biological phosphorous-removal activated sludge treatment process 32 along with return sludge 38 from the settling tank 35 and ozone-oxidized sludge 49 which is discharged from the ozone oxidation tank 48, and BOD elimination and absorption of phosphorus by the phosphorus-removing bacteria are carried out in the anaerobic tank 33 and the aerobic tank 34 which is connected thereto in the process 32. Some of the sludge in the same process is sent to the settling tank 35 and the supernatant w ater in the settling tank 35 is taken out as treated water 36, and most of the settled sludge 37 which has settled out is recycled to the anaerobic tank 33 as the returned sludge 38.
A part of the sludge is divided off from the aforementioned settled sludge 37 and is poured into the sludge anaerobic tank 40 as the branched or divided sludge 39 and phosphorus is released from the phosphorus-containing sludge on being left to stand here under anaerobic conditions. The sludge in the sludge anaerobic tank 40 is then subjected to solid/liquid separation by means of a membrane separating tank 41, and then the separated sludge 43 obtained by solid/liquid separation is introduced into an ozone-oxidation tank 48 and subjected to oxidative degradation with ozone, and soluble organic material is dissolved out. The ozone-oxidized sludge 49 produced in this ozone- oxidation tank 48 is returned to the anaerobic tank 33 of the biological phosphorous removal activated sludge treatment process 32 and then flows into the aerobic tank 34, and the ozone-oxidized sludge 49 (o f which the biodegradability by microorganisms has been improved) is degraded to carbon dioxide gas and water microbiologically.

結果 (中文) 1:

日本混混噩噩奠定了开放专利应用 Hll-188383 磷去除装置示意图如图 5 所示，在原水 31 引入厌氧池 33 o f 生物磷去除活性污泥处理工艺 32 和污泥回流从沉淀池 35 38 和臭氧氧化污泥排出臭氧氧化池 48 49和 33 厌氧池和好氧池 34 32 过程中及其连接进行生化需氧量消除和磷去除细菌对磷的吸收。一些在同一过程中污泥送到沉降罐 35 和上清液吸沉淀柜 35 中的作为处理的水 36 和大部分的固定的污泥 37 落定是再生厌氧池 33 作为返回污泥 38。污泥的一部分分为从上述固定的污泥 37 和作为分枝或分裂的 39 污泥污泥厌氧池 40 倒入磷释放从含磷污泥上被留在厌氧条件下站在这里。在污泥厌氧池 40 污泥然后遭受固/液分离膜分离罐 41，然后固液分离所得的分离的污泥 43 是引入臭氧氧化池 48 遭受氧化降解和臭氧，和可溶性有机物质溶出。在这个臭氧氧化池 48 产生的臭氧氧化淤泥 49 返回到生物厌氧池 33 磷活性炭去除污泥处理工艺 32，然后流入 34，好氧池和臭氧氧化污泥 49 (o f 它的生物降解能力的微生物已改善) 微生物降解对气体中的二氧化碳和水。

結果 (中文) 3:

对磷的去除日本混混噩噩的公开专利申请hll-188383装置示意图如图5所示，31是在厌氧池中引入33的生物除磷活性污泥处理工艺32以及从沉淀池35和臭氧氧化污泥49这是从臭氧氧化池排出48，由磷菌BOD去除和吸收磷的厌氧池、好氧池33进行34，连接过程中32。一些过程中的污泥送至沉淀池35、上清水沉淀池中35是作为处理水36，其中大部分已解决的37个已解决的污泥回收利用厌氧池33作为回流污泥38。污泥的一部分被分为从上述的沉降污泥37和被倾倒入污泥厌氧池40作为分支或分为39和磷是释放从磷的污泥中被留下站在这里，在厌氧条件下。将污泥厌氧池中的污泥进行固液分离，采用分离式41、膜分离的方法，将固体/液体分离的分离污泥43引入到一个臭氧氧化池48中，并通过臭氧氧化降解，溶解性有机物溶解。臭氧氧化污泥49本臭氧产生氧化槽48返回到厌氧池33的生物除磷活性污泥处理工艺32然后流入好氧池34，和臭氧氧化污泥49（O F的可生物降解的微生物进行了改进）是降解为二氧化碳和水微生物学。