JPS5815038B2 - Sewage treatment equipment - Google Patents
Sewage treatment equipmentInfo
- Publication number
- JPS5815038B2 JPS5815038B2 JP55020962A JP2096280A JPS5815038B2 JP S5815038 B2 JPS5815038 B2 JP S5815038B2 JP 55020962 A JP55020962 A JP 55020962A JP 2096280 A JP2096280 A JP 2096280A JP S5815038 B2 JPS5815038 B2 JP S5815038B2
- Authority
- JP
- Japan
- Prior art keywords
- anaerobic
- tank
- treatment
- aerobic
- treatment chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Description
【発明の詳細な説明】
この発明は、回転生物接触法にもとづいて汚水を処理す
る装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for treating wastewater based on a rotary biological contact method.
回転生物接触法による汚水処理は、単位容積当りの微生
物保持量が多いために処理能力が大きく、また回転動力
だけで嫌気性処理も好気性処理も行えるなどの利点を有
している。Wastewater treatment using the rotary biological contact method has the advantage that it has a large treatment capacity because it holds a large amount of microorganisms per unit volume, and that both anaerobic and aerobic treatments can be performed using only rotary power.
この発明は、上記のような回転生物接触法の利点を活用
して、汚水中に含まれている有機物の低分子化、有機物
の除去および脱窒を効率よく行うことが可能な汚水処理
装置を提供することを目的としている。This invention utilizes the advantages of the rotary biological contact method as described above to provide a wastewater treatment device that can efficiently reduce the molecular weight of organic matter contained in wastewater, remove organic matter, and denitrify it. is intended to provide.
つぎにこの発明の一実施例について図面を参照して説明
する。Next, an embodiment of the present invention will be described with reference to the drawings.
第1図に示す汚水処理装置は、相互に隣接して配置され
た2つの槽1および2を有する。The sewage treatment apparatus shown in FIG. 1 has two tanks 1 and 2 arranged adjacent to each other.
一方の槽1は密閉形のもので、その内部は隔壁によって
3つの嫌気性処理室1a、1b。One tank 1 is of a closed type, and inside thereof there are three anaerobic treatment chambers 1a and 1b separated by partition walls.
1cに分割され、各室内に回転接触体3が配置されてい
る。It is divided into 1c, and a rotating contact body 3 is arranged in each chamber.
この回転接触体3は、各嫌気性処理室la、1b、Ic
内の液面下で第1図の矢印方向に回転するように、図示
しない駆動源に接続されている。This rotary contact body 3 includes each anaerobic treatment chamber la, 1b, and Ic.
It is connected to a drive source (not shown) so as to rotate in the direction of the arrow in FIG. 1 below the liquid level inside.
また他方の槽2は、隔壁によって分離された3つの好気
性処理室2 a t 2 b 、2 cを形成した開放
形のもので、各好気性処理室2ay2by20内には、
周面の一部が空気中に露出した状態で、図示しない駆動
源からの動力を受けて矢印方向に回転する回転接触体4
が設けられている。The other tank 2 is an open type having three aerobic treatment chambers 2 a t 2 b and 2 c separated by a partition wall, and each aerobic treatment chamber 2 a y 2 by 20 includes:
A rotating contact body 4 that rotates in the direction of the arrow while receiving power from a drive source (not shown) with a part of its peripheral surface exposed in the air.
is provided.
各嫌気性処理室1a、1b、1cおよび各好気性処理室
2a、2b、’2cの平面的な配置と、各室間での液体
の移動を第2図のフローシートに示す。The planar arrangement of each anaerobic treatment chamber 1a, 1b, 1c and each aerobic treatment chamber 2a, 2b, '2c and the movement of liquid between each chamber are shown in the flow sheet of FIG.
処理すべき流入汚水は、まず嫌気性処理室1a内に導入
され、ここで汚水中の有機物の低分子化が行われたのち
、オーバーフローで好気性処理室2aに流入する。The inflowing wastewater to be treated is first introduced into the anaerobic treatment chamber 1a, where the organic matter in the wastewater is reduced in molecular weight, and then flows into the aerobic treatment chamber 2a as an overflow.
この好気性処理室2a内では、好気性条件下で有機物の
除去が行われ、ついで隣接する好気性処理室2bに移行
し、ここで硝化作用を受けたのち、嫌気性処理室1bを
経てさらに嫌気性処理室1cに流入する。In this aerobic treatment chamber 2a, organic matter is removed under aerobic conditions, and then transferred to the adjacent aerobic treatment chamber 2b, where it undergoes nitrification, and then continues through the anaerobic treatment chamber 1b. It flows into the anaerobic treatment chamber 1c.
この嫌気性処理室1bおよび1cは、供給された液体に
対して嫌気性条件のもとで脱窒処理を行う。The anaerobic processing chambers 1b and 1c perform denitrification processing on the supplied liquid under anaerobic conditions.
ここで、嫌気性処理室1aで低分子化された汚水の一部
を嫌気性処理室1bおよび1cに流入させ、上記脱窒処
理に必要な水素供与体として、嫌気性処理室1a内の液
体に含まれている低分子化された有機物を利用すること
ができ、この目的のために、ポンプを有する糸路(図示
せず)が設けられている。Here, part of the wastewater that has been reduced in molecular weight in the anaerobic treatment chamber 1a is flowed into the anaerobic treatment chambers 1b and 1c, and the liquid in the anaerobic treatment chamber 1a is used as a hydrogen donor necessary for the denitrification treatment. It is possible to make use of the low-molecular-weight organic substances contained in the fibers, and for this purpose a thread path (not shown) with a pump is provided.
また嫌気性処理室1cで脱窒処理を受けた液体は、オー
バーフローで好気性処理室2Cに移行し、ここで再ばつ
気を受けたのちに沈澱池5に送られる3そして各嫌気性
処理槽1a、1b、Icおよび各好気性処理槽2 a
、2b t 2 c内での生物学的処理は、主に各々の
内部で回転する回転接触体3゜4の表面に付着した生物
膜中の微生物の作用で行われる。In addition, the liquid that has undergone denitrification treatment in the anaerobic treatment chamber 1c overflows and moves to the aerobic treatment chamber 2C, where it is aerated again and then sent to the sedimentation tank 5 and then to each anaerobic treatment tank. 1a, 1b, Ic and each aerobic treatment tank 2a
, 2b t 2 c is carried out mainly by the action of microorganisms in biofilms attached to the surfaces of the rotating contact bodies 3 and 4 rotating inside each of them.
沈澱池5は、好気性処理室2cから受入れた液体中に含
まれている汚泥を沈澱させるためのもので、沈澱した汚
泥は余剰汚泥として排出され、上澄液は処理水として流
出する。The settling tank 5 is for settling the sludge contained in the liquid received from the aerobic treatment chamber 2c, and the settled sludge is discharged as surplus sludge, and the supernatant liquid flows out as treated water.
また処理水の一部は、好気性処理室2bに返送される。A part of the treated water is also returned to the aerobic treatment chamber 2b.
あるいは処理水を返送する代りに、好気性処理室2cを
出た液体の一部を返送してもよい。Alternatively, instead of returning the treated water, a portion of the liquid that has left the aerobic treatment chamber 2c may be returned.
すなわち第1図および第2図に示した汚水処理装置は、
嫌気性処理室1a、1b、1cおよび好気性処理室2a
、2b 、2cにおいて、各室内で回転する回転接触
体3,4表面の生物層に含まれている微生物の作用によ
って、第3図に示したような生物学的処理を行う。In other words, the sewage treatment equipment shown in Figures 1 and 2 is
Anaerobic treatment chambers 1a, 1b, 1c and aerobic treatment chamber 2a
, 2b and 2c, biological treatment as shown in FIG. 3 is performed by the action of microorganisms contained in the biological layer on the surfaces of the rotary contact bodies 3 and 4 rotating in each chamber.
このように第1段階で流入水中の基質を低分子化させて
いるので、その後の処理で有機物の除去が効率よく行わ
れる。Since the substrate in the inflow water is reduced in molecular weight in the first step, organic matter can be efficiently removed in subsequent treatments.
また有機物の除去に続いて脱窒も行われるので、さらに
高度な処理が達成される。Moreover, since denitrification is also performed following the removal of organic matter, a more advanced treatment can be achieved.
そしてこれらの生物学的処理は、回転生物接触法にした
がって行われるので、各嫌気性処理室において、各々の
内部に収容された液体の溶存酸素の多少の存在によって
脱窒等の処理が阻害されることはなく、また生物膜の微
生物保持量が多いことから、汚泥返送の必要がない。Since these biological treatments are carried out according to the rotary biological contact method, denitrification and other treatments are inhibited by the presence of some dissolved oxygen in the liquid contained in each anaerobic treatment chamber. Since the amount of microorganisms retained in the biofilm is large, there is no need to return the sludge.
さらに嫌気性処理室が形成される槽1と、好気性処理室
が形成される槽2とを隣接して設け、各種1,2にそれ
ぞれ別個に回転接触体3,4を設けたので、撹拌機は不
要となり、また配管が著るしく簡略になるなどの効果が
得られ、小規模処理場に適したコンパクトな構成が可能
であり、動力源としてのエネルギ消費量も少なくてすむ
。Furthermore, tank 1 in which an anaerobic treatment chamber is formed and tank 2 in which an aerobic treatment chamber is formed are provided adjacent to each other, and rotary contact bodies 3 and 4 are provided separately for each type 1 and 2, so that stirring This eliminates the need for a machine, significantly simplifies piping, and enables a compact configuration suitable for small-scale treatment plants, and consumes less energy as a power source.
なお上記の実施例では、2段階での脱窒処理を行うため
に2つの嫌気性処理室2b、2cを設けたが、流入汚水
の性質などに応じてその一方を省略することもまた3つ
以上することも可能である。In the above embodiment, two anaerobic treatment chambers 2b and 2c were provided to perform denitrification treatment in two stages, but one of them may be omitted depending on the nature of the inflowing wastewater. It is also possible to do the above.
また有機物除去および硝化を同一の室で行うように、好
気性処理室2aおよび2bを単一の室とすることができ
、再ばつ気のための好気性処理室2cを省略できる場合
もあるAlso, the aerobic treatment chambers 2a and 2b can be made into a single chamber so that organic matter removal and nitrification are carried out in the same chamber, and the aerobic treatment chamber 2c for re-aeration can sometimes be omitted.
第1図はこの発明の一実施例による汚水処理装置の斜視
図、第2図は同装置内での流体の流れを平面的に示す説
明図、第3図は同装置における生物学的処理の工程を示
すフローシートである。
1.2・・・・・・槽、1 a t 1 b 、1 c
・・・・・・嫌気性処理室、2a、2b、2c・・・・
・・好気的処理室、3゜4・・・・・・回転接触体、5
・・・・・・沈澱池。FIG. 1 is a perspective view of a sewage treatment device according to an embodiment of the present invention, FIG. 2 is an explanatory diagram showing a fluid flow in the device in plan, and FIG. 3 is a diagram showing biological treatment in the device. This is a flow sheet showing the process. 1.2...tank, 1 a t 1 b, 1 c
...Anaerobic treatment room, 2a, 2b, 2c...
...Aerobic treatment chamber, 3゜4...Rotating contact body, 5
...Sedimentation pond.
Claims (1)
槽内に位置する第1の回転接触体と、第1の槽に隣接し
、内部に少なくとも一つの好気性処理室を構成する第2
の槽と、上記好気性処理室内に位置する第2の回転接触
体と、上記第1の回転接触体により撹拌される上記嫌気
性処理室の一つに流入汚水を導入して基質の低分子化を
行わせ、ついで上記好気性処理室に導いて有機物除去お
よび硝化を行わせ、さらに上記嫌気性処理室の他の一つ
に導いて脱窒を行わせると共に上記低分子化工程からの
汚水の一部を上記脱窒工程へ流入させる液体移動手段と
を備えた汚水処理装置。1. A first tank forming a plurality of anaerobic processing chambers, a first rotating contact body located in each anaerobic tank, and at least one aerobic processing chamber adjacent to the first tank. Second to do
The inflow wastewater is introduced into one of the anaerobic treatment chambers, which is agitated by the tank, the second rotary contact body located in the aerobic treatment chamber, and the first rotary contact body, and the low molecular weight substrate is removed. The sewage from the low molecular weight process is then led to the aerobic treatment chamber for organic matter removal and nitrification, and then to another of the anaerobic treatment chambers for denitrification. A sewage treatment device comprising a liquid transfer means for causing a part of the liquid to flow into the denitrification process.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55020962A JPS5815038B2 (en) | 1980-02-21 | 1980-02-21 | Sewage treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55020962A JPS5815038B2 (en) | 1980-02-21 | 1980-02-21 | Sewage treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56118789A JPS56118789A (en) | 1981-09-17 |
JPS5815038B2 true JPS5815038B2 (en) | 1983-03-23 |
Family
ID=12041791
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP55020962A Expired JPS5815038B2 (en) | 1980-02-21 | 1980-02-21 | Sewage treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5815038B2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4324614A1 (en) * | 1993-07-22 | 1995-01-26 | Agfa Gevaert Ag | Monomers with cyclic carbonate groups |
KR19990073490A (en) * | 1999-07-13 | 1999-10-05 | 이영호 | Wastewater Treatment Apparatus and Method Using Rotating Biofilm Contact Tube Reactor |
KR100444908B1 (en) * | 2002-04-19 | 2004-08-21 | 한상근 | Waste water treatment apparatus using biological rotating disc apparatus |
KR100483305B1 (en) * | 2002-05-17 | 2005-04-15 | 한라산업개발 주식회사 | Biological Nutrient Removal Device Using Rotating Biological Contactor Package system |
KR100551914B1 (en) * | 2005-09-16 | 2006-02-16 | 대호산업 주식회사 | Dmr:(dai-ho microbe revolution) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS51128157A (en) * | 1975-04-16 | 1976-11-08 | Air Prod & Chem | Method of removing polluted matter containing bod nitrogen from waste water |
JPS52137156A (en) * | 1976-05-11 | 1977-11-16 | Sumitomo Const | Sewage treating apparatus by rotary disc |
-
1980
- 1980-02-21 JP JP55020962A patent/JPS5815038B2/en not_active Expired
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS51128157A (en) * | 1975-04-16 | 1976-11-08 | Air Prod & Chem | Method of removing polluted matter containing bod nitrogen from waste water |
JPS52137156A (en) * | 1976-05-11 | 1977-11-16 | Sumitomo Const | Sewage treating apparatus by rotary disc |
Also Published As
Publication number | Publication date |
---|---|
JPS56118789A (en) | 1981-09-17 |
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