JPH0217677Y2 - - Google Patents

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Publication number
JPH0217677Y2
JPH0217677Y2 JP14282485U JP14282485U JPH0217677Y2 JP H0217677 Y2 JPH0217677 Y2 JP H0217677Y2 JP 14282485 U JP14282485 U JP 14282485U JP 14282485 U JP14282485 U JP 14282485U JP H0217677 Y2 JPH0217677 Y2 JP H0217677Y2
Authority
JP
Japan
Prior art keywords
tank
anaerobic
aerobic
communication path
aerobic tank
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
Application number
JP14282485U
Other languages
Japanese (ja)
Other versions
JPS6250800U (en
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to JP14282485U priority Critical patent/JPH0217677Y2/ja
Publication of JPS6250800U publication Critical patent/JPS6250800U/ja
Application granted granted Critical
Publication of JPH0217677Y2 publication Critical patent/JPH0217677Y2/ja
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、下水、産業廃水その他の有機性廃水
を生物学的に浄化処理するための廃水処理装置に
関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a wastewater treatment device for biologically purifying sewage, industrial wastewater, and other organic wastewater.

〔従来の技術〕[Conventional technology]

従来、有機性廃水の生物学的処理法としては、
嫌気条件下で嫌気性微生物を働かせて分解浄化を
行う嫌気性処理法と、酸素の溶存下で好気性微生
物を働かせて分解浄化を行う好気性処理法とに大
別される。
Traditionally, biological treatment methods for organic wastewater include:
It is broadly divided into anaerobic treatment methods, which perform decomposition and purification by using anaerobic microorganisms under anaerobic conditions, and aerobic treatment methods, which perform decomposition and purification by using aerobic microorganisms under dissolved oxygen.

これらのうち、嫌気性処理法は、エネルギー消
費量及び汚泥の発生量が少なく、省エネルギー型
であるという利点であるものの、浄化効率には限
度があるところから、その二次処理として好気性
処理法による浄化の仕上げを行うといつた嫌気性
処理と好気性処理を組み合わせた方法が採用され
るようになつてきた。
Among these, anaerobic treatment has the advantage of being energy-saving with low energy consumption and sludge generation, but its purification efficiency is limited, so aerobic treatment is recommended as a secondary treatment. Methods that combine anaerobic and aerobic treatments have come to be used to complete the purification process.

〔考案が解決しようとする問題点〕[Problem that the invention attempts to solve]

このような嫌気性処理と好気性処理を組み合わ
せた方法においては、嫌気性処理後の流出液は当
然のことながら嫌気性状態になつており、これを
そのまま好気性処理すると多量の酸素を消費する
ことになり、好気性処理のために供給すべき酸素
量も大量を必要としていた。
In such a method that combines anaerobic treatment and aerobic treatment, the effluent after anaerobic treatment is naturally in an anaerobic state, and if it is directly treated aerobically, a large amount of oxygen will be consumed. Consequently, a large amount of oxygen was required to be supplied for aerobic treatment.

〔問題点を解決するための手段〕[Means for solving problems]

本考案は、上記問題点を解決するものであつ
て、従来、好気槽で酸素溶解に利用されたのちそ
のまま大気中へ放散されていた排気中の残留酸素
を有効利用し、嫌気槽流出液を好気槽への流入前
に好気的状態にし、好気槽での酸素消費量を節減
することのできる嫌気性処理と好気性処理とを組
み合わせた装置、即ち、廃水流入部と流出部を設
けた嫌気槽を上部に、散気装置、排気口及び処理
水流出部を設けた好気槽を下部に配設し、前記嫌
気槽の流出部と前記好気槽とを連通路にて連通す
ると共に、該連通路に前記好気槽の排気口を連結
して連通路内で流下する液と排気とを向流接触せ
しめるようにした廃水処理装置を提供するもので
ある。
The present invention solves the above-mentioned problems by effectively utilizing the residual oxygen in the exhaust gas, which was conventionally used to dissolve oxygen in the aerobic tank and then dissipated into the atmosphere. A device that combines anaerobic treatment and aerobic treatment, which can bring wastewater into an aerobic state before flowing into an aerobic tank and reduce oxygen consumption in the aerobic tank, i.e., an inlet and an outlet of wastewater. An anaerobic tank equipped with an air diffuser, an exhaust port, and a treated water outflow section is installed at the bottom, and an aerobic tank equipped with an aeration device, an exhaust port, and a treated water outflow section is installed at the bottom, and the outflow section of the anaerobic tank and the aerobic tank are connected through a communication path. The present invention provides a wastewater treatment device in which the exhaust port of the aerobic tank is connected to the communication path so that the liquid flowing down in the communication path and the exhaust gas are brought into countercurrent contact with each other.

〔実施例〕〔Example〕

本考案の実施例を図面を参照しながら説明する
と、1は嫌気槽で廃水流入管2と流出口3が設け
られ、4は好気槽で、槽内下部に空気その他の酸
素含有気体の散気装置5が、また上部には排気口
6及び処理水流出管7が設けられている。そし
て、嫌気槽1は好気槽4より上方に配設され、嫌
気槽1の流出口3と好気槽4とは連通路8で連通
され、この連通路8を経て嫌気槽からの流出液が
好気槽4内に自然流下するようになつている。さ
らに、連通路8には好気槽4の排気口6が連結さ
れ、連通路8内で流下する液と排気とが向流接触
し、流下液中に排気中の酸素を溶解させるように
なつている。したがつて、連通路8中の流下液と
排気との向流接触部には、図示例のような棚9を
多数配設した棚段式、その他の公知の多孔板式、
カスケード式、充填床式等のガス吸収促進機構を
配備することが好ましい。
An embodiment of the present invention will be described with reference to the drawings. 1 is an anaerobic tank provided with a wastewater inlet pipe 2 and an outlet 3; 4 is an aerobic tank in which air or other oxygen-containing gas is diffused in the lower part of the tank; An air device 5 is provided, and an exhaust port 6 and a treated water outflow pipe 7 are provided at the top. The anaerobic tank 1 is arranged above the aerobic tank 4, and the outflow port 3 of the anaerobic tank 1 and the aerobic tank 4 are communicated through a communication path 8, and the effluent from the anaerobic tank is passed through the communication path 8. is designed to naturally flow down into the aerobic tank 4. Further, the exhaust port 6 of the aerobic tank 4 is connected to the communication path 8, so that the liquid flowing down in the communication path 8 and the exhaust gas come into countercurrent contact, and the oxygen in the exhaust gas is dissolved in the flowing liquid. ing. Therefore, the countercurrent contact portion between the flowing liquid and the exhaust gas in the communication path 8 may be a shelf type in which a large number of shelves 9 are arranged as shown in the illustrated example, or other known perforated plate type.
It is preferable to provide a gas absorption promotion mechanism such as a cascade type or a packed bed type.

また、連通路8の頂部には、大気に開口させた
大気放散口10が設けられ、この大気放散口10
は嫌気槽1で発生するガスを排出するための嫌気
槽ガス調整装置11とも連なつている。
Further, at the top of the communication path 8, an atmosphere release port 10 that opens to the atmosphere is provided.
is also connected to an anaerobic tank gas adjustment device 11 for discharging gas generated in the anaerobic tank 1.

図中、12は好気槽4と連通路8との連通口を
示す。
In the figure, 12 indicates a communication port between the aerobic tank 4 and the communication path 8.

なお、嫌気槽1と好気槽4とは、前述の上下の
関係位置を保つていれば、互いに離して配設する
ことができるが、図示例のように、嫌気槽1と好
気槽4とを上下に立体的に連設すれば、コンパク
トになり、敷地面積も少なくてすむから、好まし
い配設例である。
Note that the anaerobic tank 1 and the aerobic tank 4 can be placed apart from each other as long as the above-mentioned vertical relationship is maintained. If these are arranged vertically in a three-dimensional manner, it will be more compact and require less site area, so this is a preferable example of arrangement.

さらにまた、嫌気槽1と好気槽4内には、それ
ぞれ槽内の汚泥濃度を高めると同時に接触効率を
高めるべく、公知の天然或いは合成の各種充填材
13を充填するとよく、また嫌気槽1では槽下部
に廃水流入管2を、槽上部に流出口3を設け、好
気槽4では槽下部に連通路8との連通口12を設
けるのが好ましい。
Furthermore, the anaerobic tank 1 and the aerobic tank 4 are preferably filled with various known natural or synthetic fillers 13 in order to increase the sludge concentration in the tank and at the same time to increase the contact efficiency. In this case, it is preferable to provide a wastewater inflow pipe 2 in the lower part of the tank and an outlet 3 in the upper part of the tank, and in the aerobic tank 4, provide a communication port 12 with the communication passage 8 in the lower part of the tank.

しかして、処理すべき原廃水は、廃水流入管2
から嫌気槽1内に導入され、汚泥濃度を高くした
槽内で廃水は十分に汚泥と接触しながら一次的に
嫌気性処理を受ける。嫌気槽1で一次処理された
液は、流出口3から連通路8へ流出し、連通路8
内を流下して連通口12から好気槽4内に流入す
るが、一方、好気槽4にて散気装置5から散気さ
れ利用された空気その他の酸素含有気体の排気が
排気口6から連通路8内へ流入、上昇し、流下す
る液と向流接触しながら排気中に残留する酸素に
よつて流下液中に溶存酸素が与えられ、好気的状
態の液となつて連通口12を経て好気槽4に流入
し、散気装置5から散気される酸素含有気体によ
つて二次処理としての好気性処理が行われる。
Therefore, the raw wastewater to be treated is transferred to the wastewater inflow pipe 2.
The wastewater is introduced into the anaerobic tank 1, and undergoes primary anaerobic treatment while fully contacting the sludge in the tank with a high sludge concentration. The liquid that has been primarily treated in the anaerobic tank 1 flows out from the outlet 3 to the communication path 8.
On the other hand, the air and other oxygen-containing gases that have been diffused and used by the aeration device 5 in the aerobic tank 4 are exhausted through the exhaust port 6. Flows into the communication passage 8, rises, and comes into countercurrent contact with the flowing liquid, and the oxygen remaining in the exhaust gas gives dissolved oxygen to the flowing liquid, turning it into an aerobic liquid and passing through the communication port. The oxygen-containing gas flows into the aerobic tank 4 via the aerobic tank 12 and is diffused from the aeration device 5 to perform aerobic treatment as a secondary treatment.

このように、嫌気槽1から好気槽4へ流入する
嫌気性処理液は、その途中で好気槽4の排気によ
つて好気的状態となるから、好気槽4における酸
素消費量は少なくなり、好気槽4へ供給される酸
素含有体の量は節減される。
In this way, the anaerobic treatment liquid flowing from the anaerobic tank 1 to the aerobic tank 4 becomes aerobic due to the exhaust air from the aerobic tank 4, so the oxygen consumption in the aerobic tank 4 is This reduces the amount of oxygen-containing material supplied to the aerobic tank 4.

かくて、好気槽4にて二次処理された処理水
は、処理水流出管7から槽外へ流出し、図示しな
い沈殿槽で固液分離し、塩素滅菌後放流される一
方、連通路8内で再利用された排気は大気放散口
10より大気中に放散され、また、嫌気槽1で発
生したガスも適宜嫌気槽ガス調整装置11を経由
して大気放散口10から大気中に放散される。
Thus, the treated water that has been subjected to secondary treatment in the aerobic tank 4 flows out of the tank from the treated water outflow pipe 7, undergoes solid-liquid separation in a settling tank (not shown), is sterilized with chlorine, and is then discharged. The exhaust gas reused in the anaerobic tank 8 is released into the atmosphere from the air release port 10, and the gas generated in the anaerobic tank 1 is also appropriately released into the atmosphere from the air release port 10 via the anaerobic tank gas adjustment device 11. be done.

〔考案の効果〕[Effect of idea]

以上述べたように、本考案は嫌気槽と好気槽を
合理的に連通配設したことによつて、嫌気槽流出
液が好気槽へ流入する前に好気槽の排気を有効利
用して好気的状態となり、二次処理たる好気性処
理を効率よく行うことができると共に、好気性処
理のために供給される酸素量を極めて節減するこ
とができる。
As described above, the present invention effectively utilizes the exhaust air from the aerobic tank before the anaerobic tank effluent flows into the aerobic tank by rationally arranging the anaerobic tank and aerobic tank in communication. This makes it possible to efficiently perform aerobic treatment as a secondary treatment, and to significantly reduce the amount of oxygen supplied for aerobic treatment.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本考案の一実施例を示す断面図である。 1……嫌気槽、2……廃水流入管、3……流出
口、4……好気槽、5……散気装置、6………排
気口、7……処理水流出管、8……連通路、9…
…棚、10……大気放散口、11……嫌気槽ガス
調整装置、12……連通口、13……充填材。
The drawing is a sectional view showing an embodiment of the present invention. 1...Anaerobic tank, 2...Wastewater inflow pipe, 3...Outlet, 4...Aerobic tank, 5...Aeration device, 6...Exhaust port, 7...Treated water outflow pipe, 8... ...Communication path, 9...
...Shelf, 10...Atmospheric release port, 11...Anaerobic tank gas adjustment device, 12...Communication port, 13...Filling material.

Claims (1)

【実用新案登録請求の範囲】 1 廃水流入部と流出部を設けた嫌気槽を上部
に、散気装置、排気口及び処理水流出部を設け
た好気槽を下部に配設し、前記嫌気槽の流出部
と前記好気槽とを連通路にて連通すると共に、
該連通路に前記好気槽の排気口を連結して連通
路内で流下する液と排気とを向流接触せしめる
ことを特徴とする廃水処理装置。 2 前記連通路内の液と排気との向流接触部にガ
ス吸収促進機構を配備したものである実用新案
登録請求の範囲第1項記載の廃水処理装置。 3 前記嫌気槽と好気槽とを上下に立体的に連設
したものである実用新案登録請求の範囲第1項
又は第2項記載の廃水処理装置。 4 前記嫌気槽及び好気槽内に充填材を充填した
ものである実用新案登録請求の範囲第1〜3項
のいずれか一つの項記載の廃水処理装置。 5 前記嫌気槽内下部に前記廃水流入部を、上部
に前記流出部を設け、前記好気槽内下部に前記
連通路との連通部を設けたものである実用新案
登録請求の範囲第1〜4項のいずれか一つの項
記載の廃水処理装置。
[Scope of Claim for Utility Model Registration] 1. An anaerobic tank provided with a wastewater inlet and an outlet is provided in the upper part, an aerobic tank provided with an aeration device, an exhaust port, and a treated water outlet is provided in the lower part, and the anaerobic Communicating the outflow part of the tank and the aerobic tank through a communication path,
A wastewater treatment device characterized in that an exhaust port of the aerobic tank is connected to the communication path so that the liquid flowing down in the communication path and the exhaust gas are brought into countercurrent contact. 2. The wastewater treatment device according to claim 1, wherein a gas absorption promoting mechanism is provided at a countercurrent contact portion between the liquid and the exhaust gas in the communication path. 3. The wastewater treatment apparatus according to claim 1 or 2, which is a system in which the anaerobic tank and the aerobic tank are arranged vertically in series. 4. The wastewater treatment device according to any one of claims 1 to 3, wherein the anaerobic tank and the aerobic tank are filled with a filler. 5 Utility model registration claims 1 to 5, wherein the wastewater inflow part is provided in the lower part of the anaerobic tank, the outflow part is provided in the upper part, and the communication part with the communication path is provided in the lower part of the aerobic tank. The wastewater treatment device according to any one of Item 4.
JP14282485U 1985-09-20 1985-09-20 Expired JPH0217677Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14282485U JPH0217677Y2 (en) 1985-09-20 1985-09-20

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14282485U JPH0217677Y2 (en) 1985-09-20 1985-09-20

Publications (2)

Publication Number Publication Date
JPS6250800U JPS6250800U (en) 1987-03-30
JPH0217677Y2 true JPH0217677Y2 (en) 1990-05-17

Family

ID=31051919

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14282485U Expired JPH0217677Y2 (en) 1985-09-20 1985-09-20

Country Status (1)

Country Link
JP (1) JPH0217677Y2 (en)

Also Published As

Publication number Publication date
JPS6250800U (en) 1987-03-30

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