JPH07116692A - Treating device for nitrification and denitrification of sewage - Google Patents
Treating device for nitrification and denitrification of sewageInfo
- Publication number
- JPH07116692A JPH07116692A JP5291555A JP29155593A JPH07116692A JP H07116692 A JPH07116692 A JP H07116692A JP 5291555 A JP5291555 A JP 5291555A JP 29155593 A JP29155593 A JP 29155593A JP H07116692 A JPH07116692 A JP H07116692A
- Authority
- JP
- Japan
- Prior art keywords
- nitrification
- sludge
- anaerobic
- carrier
- denitrification
- 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.)
- Granted
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
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、汚水の硝化脱窒素処理
装置に係り、特に硝化菌をゲル粒子などに固定化した担
体を使用する汚水の生物学的硝化脱窒素装置に関するも
のである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for treating nitrification and denitrification of sewage, and more particularly to a biological nitrification and denitrification apparatus for sewage using a carrier in which nitrifying bacteria are immobilized on gel particles.
【0002】[0002]
【従来の技術】硝化菌固定化担体を用いた硝化処理装置
としては、従来、例えば特公昭5−46279号公報に
記載の技術が知られている。この技術は、生物反応槽
と、硝化細菌を担持した担体を収納し散気装置を有する
硝化槽ユニットとから成り、前記生物反応槽には、前記
硝化ユニットが単数或いは複数配置され、生物反応槽内
の被処理液を硝化槽ユニットに循環流通させ硝化処理す
る装置である。2. Description of the Related Art As a nitrification treatment apparatus using a nitrifying bacterium-immobilized carrier, the technology described in, for example, Japanese Patent Publication No. 46279/1993 is known. This technique comprises a bioreaction tank and a nitrification tank unit having a diffusing device for accommodating a carrier supporting nitrifying bacteria, and the bioreaction tank is provided with one or more nitrification units. It is an apparatus for circulating and circulating the liquid to be treated in a nitrification tank unit.
【0003】しかし、上記装置には次のような問題点が
ある。 担体の流出を阻止するためのスクリーンを通過させ
るという方法で硝化液を脱窒素部へ循環させているの
で、スクリーン通過装置が多くなり、それに比例してス
クリーン所要面積が増加してしまう。 硝化ユニットの各々の被処理液流出部に、これに連
なる水路を付設して、脱窒素部と最終沈殿池へと液を導
入しなければならないので、水路が長く、かつ構造が複
雑である。 脱窒素部への硝化液の循環を行うために、硝化部に
設けた散気装置によるエアリフト効果を利用するので、
所要の循環量を得るために、散気量が過大になり易い。
しかも、スクリーンを通して、硝化液を循環させなけれ
ばならないので、スクリーンの通水抵抗によって硝化液
循環量が減少し易くなってしまう。However, the above device has the following problems. Since the nitrification solution is circulated to the denitrification section by a method of passing the carrier through a screen to prevent the carrier from flowing out, the number of screen passing devices increases and the required screen area increases in proportion thereto. Since a water channel connecting to the treated liquid outflow portion of each nitrification unit must be attached to introduce the liquid into the denitrification portion and the final settling tank, the water channel is long and the structure is complicated. In order to circulate the nitrification liquid to the denitrification section, the air lift effect by the air diffuser provided in the nitrification section is used,
To obtain the required circulation amount, the air diffused amount tends to be excessive.
In addition, since the nitrifying solution must be circulated through the screen, the amount of circulation of the nitrifying solution tends to decrease due to the water flow resistance of the screen.
【0004】[0004]
【発明が解決しようとする課題】本発明は、上記技術の
問題点をすべて解消でき、簡単な装置で効率的に硝化脱
窒素処理できる新規な汚水の硝化脱窒素処理装置を提供
することを課題とする。SUMMARY OF THE INVENTION It is an object of the present invention to provide a novel nitrification denitrification treatment apparatus for wastewater, which can solve all the problems of the above technology and can efficiently perform nitrification denitrification treatment with a simple apparatus. And
【0005】[0005]
【課題を解決するための手段】上記課題を解決するため
に、本発明では、嫌気部と硝化部とを有した活性汚泥式
処理装置と、該処理装置から流出する汚泥を分離する汚
泥分離装置を有する汚水の硝化脱窒素処理装置におい
て、前記活性汚泥式処理装置は、下端に導通口を有する
隔壁を介して嫌気部と硝化部とを有する処理ユニットが
複数直列に配置され、該各処理ユニットの硝化部には、
硝化菌を固定化した浮遊担体と、含酸素気体を導入する
散気手段と、前記担体の処理ユニット外への流出を防止
する手段を有する流出口とが配備されると共に、前記各
処理ユニットの嫌気部には、原水を分配供給する手段を
有し、また、最初の処理ユニットの嫌気部には前記汚泥
分離装置からの分離汚泥を返送する手段を有することと
したものである。In order to solve the above problems, according to the present invention, an activated sludge type treatment apparatus having an anaerobic section and a nitrification section, and a sludge separation apparatus for separating sludge flowing out from the treatment apparatus. In the nitrification / denitrification treatment apparatus for sewage, the activated sludge type treatment apparatus has a plurality of treatment units having an anaerobic section and a nitrification section arranged in series via a partition wall having a conduction port at a lower end thereof, and each of the treatment units. The nitrification part of
A floating carrier on which nitrifying bacteria are immobilized, an air diffuser for introducing an oxygen-containing gas, and an outlet having a means for preventing the carrier from flowing out of the processing unit are provided, and each of the processing units is provided. The anaerobic part has means for distributing and supplying raw water, and the anaerobic part of the first treatment unit has means for returning the separated sludge from the sludge separating device.
【0006】また、前記処理ユニットにおいて、最後の
処理ユニットには隔壁の上部水面下にも開口を設けるの
がよい。本発明に用いる汚泥分離装置は、沈殿槽でも膜
分離装置でも良い。また、担体の流出防止手段は、種々
のスクリーン等を用いることができる。散気装置は生物
担体を破損しない程度のものを用いることが必要であ
る。In the above processing unit, it is preferable that the last processing unit has an opening below the water surface above the partition wall. The sludge separation device used in the present invention may be a sedimentation tank or a membrane separation device. Various screens and the like can be used as the carrier outflow preventing means. It is necessary to use an air diffuser that does not damage the biological carrier.
【0007】なお、本発明においては、上記した嫌気部
と硝化部を有する処理ユニットが複数配置されればよい
から、例えば、上記した硝化部に相当する部分を活性汚
泥槽内に配置し、或いは元々上下回流式の曝気槽であれ
ば1槽おきに曝気を停止し、原水流入部を各々に設ける
だけで処理ユニットが形成でき、既設の活性汚泥施設の
曝気槽を容易に、硝化担体を用いた生物学的硝化脱窒素
装置に変更できる。In the present invention, since a plurality of treatment units having the above-mentioned anaerobic part and nitrification part may be arranged, for example, a part corresponding to the above-mentioned nitrification part is arranged in the activated sludge tank, or Originally, if it is a vertical circulation type aeration tank, aeration can be stopped every other tank, and a treatment unit can be formed by simply providing a raw water inflow section for each, and an aeration tank of an existing activated sludge facility can be easily used with a nitrification carrier. The biological nitrification and denitrification equipment that was used can be replaced.
【0008】[0008]
【実施例】以下、本発明を実施例により具体的に説明す
るが、本発明はこれに限定されるものではない。 実施例1 図1は、本発明の汚水の硝化脱窒素処理装置の代表的な
例を示す全体構成図である。EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited thereto. Example 1 FIG. 1 is an overall configuration diagram showing a typical example of the wastewater nitrification denitrification treatment apparatus of the present invention.
【0009】図1において、1は活性汚泥槽であり、D
1 〜D4 は嫌気部、N1 〜N4 は硝化部である。2は散
気装置、3は攪拌ポンプである。a、bは隔壁であり、
4は下水などの汚水(原水)の流入管、4−1〜4−4
は汚水をD1 〜D4 の各々に分注する管路である。5は
スクリーンであり、N1 〜N4 内に収納され、懸濁流動
している担体の流出を阻止し、浮遊状の活性汚泥は通過
させる。従って、担体は硝化部内に留まり、後続するD
槽には移動できないようになっている。In FIG. 1, 1 is an activated sludge tank, and D
1 to D 4 are anaerobic parts, and N 1 to N 4 are nitrification parts. 2 is an air diffuser and 3 is a stirring pump. a and b are partition walls,
4 is an inflow pipe for sewage (raw water) such as sewage, 4-1 to 4-4
Is a pipe for dispensing sewage into each of D 1 to D 4 . Reference numeral 5 denotes a screen, which is housed in N 1 to N 4 and prevents the carrier flowing in suspension from flowing out, and allows floating activated sludge to pass through. Therefore, the carrier remains in the nitrification zone and the subsequent D
It cannot be moved to the tank.
【0010】6は硝化脱窒素反応を受けた液の流出部で
あり、7は沈殿池、8は清澄処理水、9は沈殿汚泥であ
る。沈殿池7では浮遊状の活性汚泥が沈降分離され、沈
殿汚泥9は返送汚泥管10からD1 槽にリサイクルされ
る。12は汚泥返送ポンプである。また11は余剰汚泥
引抜管である。しかして、以下に本発明の作用原理を説
明する。硝化槽N1 〜N4 には、ポリエチレングリコー
ル(PEG)ゲル、ポリビニルアルコール(PVA)ゲ
ルなどのゲル、又は粒状スポンジなどの浮遊可能な軽量
担体に硝化菌を固定化した生物担体が収納されている。Reference numeral 6 is an outflow portion of the liquid which has undergone the nitrification denitrification reaction, 7 is a sedimentation tank, 8 is clarified treated water, and 9 is sedimentation sludge. In the settling basin 7, floating activated sludge is settled and separated, and the settling sludge 9 is recycled from the return sludge pipe 10 to the D 1 tank. 12 is a sludge return pump. Further, 11 is a surplus sludge drawing pipe. The principle of operation of the present invention will be described below. The nitrification tanks N 1 to N 4 contain a biological carrier in which nitrifying bacteria are immobilized on a floatable lightweight carrier such as a polyethylene glycol (PEG) gel, polyvinyl alcohol (PVA) gel, or a granular sponge. There is.
【0011】また、D1 〜D4 には担体に固定化されて
いない浮遊微生物、即ち活性汚泥が懸濁している。攪拌
ポンプ3によって活性汚泥の浮遊微生物が汚水と効率よ
く接触するようになっている。硝化担体には、散気装置
2から供給される酸素含有ガスによって酸素が与えられ
る。また、散気ガスの上昇運動によって硝化担体がN1
〜N4 槽内で懸濁流動する。しかして、下水などの汚水
は、嫌気部Dに流入し、前段の硝化部から流入してくる
NOx −Nが浮遊状の脱窒素菌によって、汚水中のBO
D成分を水素供与体としてN2 ガスに還元除去される。Further, suspended microorganisms which are not immobilized on the carrier, that is, activated sludge, are suspended in D 1 to D 4 . The agitation pump 3 enables the floating microorganisms of the activated sludge to efficiently contact the wastewater. Oxygen is given to the nitrification carrier by the oxygen-containing gas supplied from the diffuser 2. In addition, the nitrification carrier is converted into N 1 by the rising motion of the diffused gas.
~ Suspended in N 4 tank. Thus, sewage, such as sewage, anaerobic section flows into D, by denitrifying bacteria NO x -N coming flows from the preceding nitrification unit is suspended form, BO in wastewater
The D component is reduced to N 2 gas by using it as a hydrogen donor.
【0012】なお、嫌気部D1 には、硝化部N4 で生成
したNOx −Nが返送汚泥とともに流入してくる。次
に、硝化部Nにおいては、原汚水中に含まれるNH4 −
Nが硝化担体の硝化作用によってNOx −N(主にNO
3 −Nの型になる)に酸化される。浮遊微生物も一部、
硝化作用を進行できる。硝化部Nから後続する嫌気部D
にはNOx −Nを含んだ液と浮遊微生物が流出されてゆ
き、硝化担体はスクリーン5によって流出が阻止され
る。The NO x -N produced in the nitrification section N 4 flows into the anaerobic section D 1 together with the returned sludge. Next, in the nitrification section N, NH 4 − contained in the raw wastewater is
N is NO x -N by nitrification nitrification carrier (mainly NO
3- N type). Some floating microorganisms,
Nitrification can proceed. Anaerobic part D following the nitrification part N
The liquid containing NO x -N and the floating microorganisms flow out to the nitric acid carrier, and the nitrification carrier is prevented from flowing out by the screen 5.
【0013】もし、このスクリーン5が設けられていな
いと、硝化部N1 〜N4 内の硝化担体が水の流れにのっ
て移動し、硝化部N4 内に集まってしまうという大きな
トラブルを招く。しかして、硝化部N4 からの流出スラ
リーは沈殿池7において沈降分離され、清澄上澄水8と
沈殿汚泥9に分離される。なお、嫌気部D4 と硝化部N
4 を区画する隔壁の上部の水面下には開口部Aを設けて
おくのが好ましく、こうすることによって硝化部N4 で
生成したNOx −Nが嫌気部D4 に循環され、脱窒素さ
れる。この場合は開口部Aを通って、硝化担体が嫌気部
D4 に流入するが特に問題はない。If the screen 5 is not provided, the nitrification carrier in the nitrification sections N 1 to N 4 will move along with the flow of water and will collect in the nitrification section N 4 . Invite. Then, the outflow slurry from the nitrification section N 4 is settled and separated in the settling tank 7, and is separated into the clear supernatant water 8 and the settling sludge 9. The anaerobic part D 4 and the nitrification part N
It is preferable to provide an opening A below the water surface above the partition wall that divides 4 so that NO x -N generated in the nitrification section N 4 is circulated to the anaerobic section D 4 and denitrified. It In this case, the nitrification carrier flows into the anaerobic part D 4 through the opening A, but there is no particular problem.
【0014】[0014]
【発明の効果】本発明によれば、次のような効果を奏す
ることができる。 装置構成が著しくシンプルなので、設計施工が容易
である。 硝化ユニットN1 〜N4 の各々に水路を付設する必
要が全くないので、構造が簡略化される。 硝化部の液をエアリフトによって嫌気槽に強制的に
リサイクルさせる必要がないので、硝化部N1 〜N4 に
設ける散気装置への供給空気量が少なくてすむ。 簡単な改造だけで従来の活性汚泥式処理槽を硝化脱
窒素装置に転用できる。According to the present invention, the following effects can be obtained. Since the device configuration is extremely simple, design and construction is easy. Since it is not necessary to attach a water channel to each of the nitrification units N 1 to N 4 , the structure is simplified. Since it is not necessary to forcibly recycle the liquid in the nitrification section to the anaerobic tank by the air lift, the amount of air supplied to the air diffusers provided in the nitrification sections N 1 to N 4 can be small. The conventional activated sludge type treatment tank can be converted to a nitrification and denitrification device with a simple modification.
【図1】本発明の硝化脱窒素処理装置の一例を示す全体
構成図。FIG. 1 is an overall configuration diagram showing an example of a nitrification denitrification treatment apparatus of the present invention.
1:活性汚泥槽、2:散気装置、3:攪拌ポンプ、4:
原水流入管、4−1〜4−4:原水分注管、5:スクリ
ーン、6:液流出部、7:沈殿池、8:清澄処理水、
9:沈殿汚泥、10:返送汚泥、11:余剰汚泥、1
2:ポンプ、a、b:隔壁、D1 〜D4 :嫌気部、N1
〜N4 :硝化部、A:開口部1: Activated sludge tank, 2: Air diffuser, 3: Stirring pump, 4:
Raw water inflow pipe, 4-1 to 4-4: Raw water injection pipe, 5: Screen, 6: Liquid outflow part, 7: Sedimentation tank, 8: Clarified treated water,
9: Settled sludge, 10: Returned sludge, 11: Excess sludge, 1
2: pump, a, b: partition wall, D 1 to D 4 : anaerobic part, N 1
~ N 4 : Nitrification part, A: Opening part
Claims (2)
理装置と、該処理装置から流出する汚泥を分離する汚泥
分離装置を有する汚水の硝化脱窒素処理装置において、
前記活性汚泥式処理装置は、下端に導通口を有する隔壁
を介して嫌気部と硝化部とを有する処理ユニットが複数
直列に配置され、該各処理ユニットの硝化部には、硝化
菌を固定化した浮遊担体と、含酸素気体を導入する散気
手段と、前記担体の処理ユニット外への流出を防止する
手段を有する流出口とが配備されると共に、前記各処理
ユニットの嫌気部には、原水を分配供給する手段を有
し、また、最初の処理ユニットの嫌気部には前記汚泥分
離装置からの分離汚泥を返送する手段を有することを特
徴とする汚泥の硝化脱窒素処理装置。1. A nitrification denitrification treatment apparatus for wastewater comprising an activated sludge type treatment apparatus having an anaerobic section and a nitrification section, and a sludge separation apparatus for separating sludge flowing out from the treatment apparatus,
In the activated sludge type treatment device, a plurality of treatment units having an anaerobic part and a nitrification part are arranged in series via a partition wall having a conduction port at the lower end, and nitrifying bacteria are immobilized in the nitrification part of each treatment unit. The floating carrier, an air diffusing means for introducing an oxygen-containing gas, and an outlet having a means for preventing the carrier from flowing out of the processing unit are provided, and the anaerobic part of each processing unit, An apparatus for nitrifying and denitrifying sludge, comprising means for distributing and supplying raw water, and means for returning the separated sludge from the sludge separating apparatus to the anaerobic part of the first treatment unit.
ユニットには隔壁の上部水面下にも開口を設けたことを
特徴とする請求項1記載の汚水の硝化脱窒素処理装置。2. The nitrification denitrification treatment apparatus of sewage according to claim 1, wherein in the last treatment unit, an opening is provided below the upper water surface of the partition wall in the last treatment unit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29155593A JP3373015B2 (en) | 1993-10-28 | 1993-10-28 | Wastewater nitrification denitrification treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29155593A JP3373015B2 (en) | 1993-10-28 | 1993-10-28 | Wastewater nitrification denitrification treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07116692A true JPH07116692A (en) | 1995-05-09 |
JP3373015B2 JP3373015B2 (en) | 2003-02-04 |
Family
ID=17770437
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP29155593A Expired - Lifetime JP3373015B2 (en) | 1993-10-28 | 1993-10-28 | Wastewater nitrification denitrification treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3373015B2 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003047989A (en) * | 2001-08-06 | 2003-02-18 | Nisshin Steel Co Ltd | Denitrification method and apparatus |
KR100419030B1 (en) * | 2001-12-18 | 2004-02-21 | 대림산업 주식회사 | Advanced sludge reaeration process without first clarifier and internal recycling for nutrient removal |
US7166220B2 (en) * | 2001-11-22 | 2007-01-23 | Ebara Corporation | Systems and methods for organic wastewater treatment |
JP2010155184A (en) * | 2008-12-26 | 2010-07-15 | Nishihara Environment Technology Inc | Support feeding type biological reaction apparatus |
JP2013049013A (en) * | 2011-08-31 | 2013-03-14 | Nishihara Environment Co Ltd | Wastewater treating apparatus and wastewater treating method |
WO2021102484A1 (en) * | 2019-11-21 | 2021-05-27 | Organo (Vietnam) Co., Ltd. | Biological treatment apparatus, carrier capturing device for biological treatment apparatus, water treatment method and method of modifying biological treatment apparatus |
CN114667270A (en) * | 2019-11-21 | 2022-06-24 | 奥加诺株式会社 | Biological treatment apparatus, carrier capturing apparatus for biological treatment apparatus, water treatment method, and modification method for biological treatment apparatus |
-
1993
- 1993-10-28 JP JP29155593A patent/JP3373015B2/en not_active Expired - Lifetime
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003047989A (en) * | 2001-08-06 | 2003-02-18 | Nisshin Steel Co Ltd | Denitrification method and apparatus |
US7166220B2 (en) * | 2001-11-22 | 2007-01-23 | Ebara Corporation | Systems and methods for organic wastewater treatment |
KR100419030B1 (en) * | 2001-12-18 | 2004-02-21 | 대림산업 주식회사 | Advanced sludge reaeration process without first clarifier and internal recycling for nutrient removal |
JP2010155184A (en) * | 2008-12-26 | 2010-07-15 | Nishihara Environment Technology Inc | Support feeding type biological reaction apparatus |
JP2013049013A (en) * | 2011-08-31 | 2013-03-14 | Nishihara Environment Co Ltd | Wastewater treating apparatus and wastewater treating method |
WO2021102484A1 (en) * | 2019-11-21 | 2021-05-27 | Organo (Vietnam) Co., Ltd. | Biological treatment apparatus, carrier capturing device for biological treatment apparatus, water treatment method and method of modifying biological treatment apparatus |
CN114667270A (en) * | 2019-11-21 | 2022-06-24 | 奥加诺株式会社 | Biological treatment apparatus, carrier capturing apparatus for biological treatment apparatus, water treatment method, and modification method for biological treatment apparatus |
JP2022549249A (en) * | 2019-11-21 | 2022-11-24 | オルガノ株式会社 | Biological treatment device, carrier capture device for biological treatment device, water treatment method, and modification method for biological treatment device |
Also Published As
Publication number | Publication date |
---|---|
JP3373015B2 (en) | 2003-02-04 |
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