JPH04310298A - Biological nitrogen removing unit - Google Patents

Biological nitrogen removing unit

Info

Publication number
JPH04310298A
JPH04310298A JP3073426A JP7342691A JPH04310298A JP H04310298 A JPH04310298 A JP H04310298A JP 3073426 A JP3073426 A JP 3073426A JP 7342691 A JP7342691 A JP 7342691A JP H04310298 A JPH04310298 A JP H04310298A
Authority
JP
Japan
Prior art keywords
region
nitrification
water
treated
cage
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.)
Pending
Application number
JP3073426A
Other languages
Japanese (ja)
Inventor
Akio Toriyama
明夫 鳥山
Ichiro Nakano
一郎 中野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
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 by Kubota Corp filed Critical Kubota Corp
Priority to JP3073426A priority Critical patent/JPH04310298A/en
Publication of JPH04310298A publication Critical patent/JPH04310298A/en
Pending legal-status Critical Current

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Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To facilitate anchoring and withdrawal and to simplify the attachment and detachment of necessary apparatuses by utilizing an existing activated sludge sewage treatment plant to remove not only the org. matter but also nitrogen in water to be treated. CONSTITUTION:A biological nitrogen removing unit is constituted of the cage 1 immersed in an aeration tank 9 and provided with a net 1 having a mesh size smaller than bacteria immobilizing carriers 8 under tension, the partitioning means 4 dividing the cage 1 into a denitrifying region 2 and a nitrating region 3, the submerged stirring device 5 arranged in the denitrifying region 2 of the cage 1 and stirring the water to be treated in the denitrifying region 2, the air diffuser 6 arranged in the nitrating region 3 of the cage 1 to send air into the water to be treated of the nitrating region 3, the nitrated liquid circulating apparatus 7 arranged to the cage 1 to circulate the water to be treated from the nitrating region 3 to the denitrifying region 2 and the bacteria immobilizing carriers 8 charged in the denitrifying region 2 and the nitrating region 3.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、例えば、下廃水などの
中に存在している各種の窒素化合物を不活性な窒素ガス
などに変換して除去する窒素除去装置の装置類をユニッ
ト化した生物学的窒素除去用ユニットに関するものであ
る。
[Industrial Application Field] The present invention is a unitized nitrogen removal device that converts various nitrogen compounds present in sewage water, etc. into inert nitrogen gas, etc. and removes them. The present invention relates to a unit for biological nitrogen removal.

【0002】0002

【従来の技術】図2は、従来の下廃水処理法の一つであ
る活性汚泥法の一例を示す概略図である。この活性汚泥
法は、一般には下廃水などの被処理水のSS分を沈澱分
離する最初沈澱池21と、被処理水にエアーを送り込ん
で曝気する曝気槽22と、汚泥を沈殿分離する最終沈澱
池23とから構成されている。
2. Description of the Related Art FIG. 2 is a schematic diagram showing an example of an activated sludge method, which is one of the conventional sewage water treatment methods. This activated sludge method generally consists of an initial sedimentation tank 21 that settles and separates the SS component of water to be treated such as sewage water, an aeration tank 22 that aerates the water by sending air into the water, and a final sedimentation tank that sediments and separates the sludge. It consists of a pond 23.

【0003】この従来の活性汚泥法では、被処理水中の
沈澱しやすい浮遊物を最初沈澱池21で沈澱・除去して
から連続的に曝気槽22へ導入する。曝気槽22では好
気性微生物を流動状態で浮遊して曝気しながら排水中の
有機物の酸化分解を行なう。ついで曝気槽22の混合液
を連続的に沈澱槽23に導入して活性汚泥を沈降分離し
、処理水を越流させて滅菌後放流する。同時に沈降した
活性汚泥の一部を曝気槽22に返送し、他の一部は余剰
汚泥として脱水等の処理をした後に処分する。
[0003] In this conventional activated sludge method, suspended matter that tends to settle in the water to be treated is first settled and removed in a settling tank 21, and then continuously introduced into an aeration tank 22. In the aeration tank 22, aerobic microorganisms are suspended in a fluid state and organic matter in the wastewater is oxidized and decomposed while being aerated. Next, the mixed liquid in the aeration tank 22 is continuously introduced into the settling tank 23, the activated sludge is separated by sedimentation, and the treated water is overflowed to be sterilized and then discharged. At the same time, a part of the activated sludge that has settled is returned to the aeration tank 22, and the other part is disposed of as surplus sludge after being subjected to dewatering and other treatments.

【0004】0004

【発明が解決しようとする課題】最近、下廃水処理にお
いて富栄養化を防止する見地から窒素の除去が求められ
ている。しかも、従来の活性汚泥法の既設備を窒素の除
去ができる設備に変換して利用できれば費用その他の面
で好ましい。
[Problems to be Solved by the Invention] Recently, there has been a demand for the removal of nitrogen from the viewpoint of preventing eutrophication in wastewater treatment. Moreover, it would be preferable in terms of cost and other aspects if existing equipment for the conventional activated sludge method could be converted into equipment that can remove nitrogen.

【0005】しかし、上記従来の活性汚泥法は有機物を
除去することを目的として設計されたもので、被処理水
中の窒素除去は期待できない。しかも、活性汚泥法の既
設下水処理場を窒素除去施設として利用するためには曝
気槽22を大きくする必要があるが、曝気槽22を拡張
することは用地難等により困難である。
However, the conventional activated sludge method described above was designed for the purpose of removing organic matter, and cannot be expected to remove nitrogen from the water to be treated. Moreover, in order to use an existing sewage treatment plant using the activated sludge method as a nitrogen removal facility, it is necessary to enlarge the aeration tank 22, but expanding the aeration tank 22 is difficult due to land constraints and the like.

【0006】本発明は、上記のような課題を解決するた
めになされたもので、既設の活性汚泥法の下水処理場を
そのまま利用して被処理水中の窒素を除去することがで
き、しかも据付、撤去が容易で、必要な装置類の取り付
け、取り外しが簡単な生物学的窒素除去用ユニットを提
供することを目的としている。
The present invention has been made to solve the above-mentioned problems, and it is possible to remove nitrogen from the water to be treated by using the existing activated sludge method sewage treatment plant as is, and it is easy to install. The object of the present invention is to provide a biological nitrogen removal unit that is easy to remove, and the necessary equipment can be easily installed and removed.

【0007】[0007]

【課題を解決するための手段】本発明は、反応槽内に浸
漬されて窒素除去装置の装置類を取り付けるフレームと
、このフレームを脱窒領域と硝化領域に分割する仕切手
段と、脱窒領域のフレームに設置されて脱窒領域内の被
処理水を攪拌する水中攪拌装置と、硝化領域のフレーム
に設置されて硝化領域内の被処理水にエアーを送り込む
散気装置と、フレームに設置されて硝化領域から脱窒領
域に被処理水を循環させる硝化液循環装置とから構成さ
れている。
[Means for Solving the Problems] The present invention provides a frame that is immersed in a reaction tank to which devices of a nitrogen removal device are attached, partition means that divides the frame into a denitrification region and a nitrification region, and a denitrification region. An underwater agitation device is installed in the frame of the nitrification area to agitate the water to be treated in the denitrification area, an aeration device is installed in the frame of the nitrification area to send air into the water to be treated in the nitrification area, and and a nitrification liquid circulation device that circulates the water to be treated from the nitrification region to the denitrification region.

【0008】本発明は、反応槽内に浸漬されたフレーム
を微生物固定化担体よりも小さい目開きのネットを張着
したケージによって形成し、このケージ内に微生物固定
化担体を投入している。
[0008] In the present invention, a frame immersed in a reaction tank is formed by a cage covered with a net having a mesh size smaller than that of the microorganism immobilized carrier, and the microorganism immobilized carrier is introduced into this cage.

【0009】[0009]

【作用】被処理水が硝化領域に滞留している間に散気装
置からエアーが吹き込まれ硝化が促進され、さらに、硝
化領域の被処理水の一部が硝化液循環装置によって脱窒
領域に循環され脱窒領域において脱窒される。
[Effect] While the water to be treated remains in the nitrification area, air is blown from the air diffuser to promote nitrification, and a part of the water to be treated in the nitrification area is transferred to the denitrification area by the nitrification liquid circulation device. It is circulated and denitrified in the denitrification area.

【0010】微生物固定化担体を硝化領域や脱窒領域に
投入することによって、反応槽当りの微生物濃度が高ま
る結果、硝化速度ないし脱窒速度が高まり、既設の曝気
槽であっても硝化、脱窒を十分行なうことができる。
By introducing a microorganism-immobilized carrier into the nitrification region or denitrification region, the concentration of microorganisms per reaction tank increases, resulting in an increase in the nitrification rate or denitrification rate, and even in the existing aeration tank, nitrification and denitrification It is possible to carry out sufficient nitrification.

【0011】窒素除去に必要な装置類をユニット化する
ことによって、既存の下廃水処理設備に対して容易に据
付、撤去ができる。しかも、簡単に装置類の取り付け、
取り外しができることから修理や補修が容易である。
[0011] By unitizing the equipment necessary for nitrogen removal, it can be easily installed and removed from existing wastewater treatment equipment. Moreover, it is easy to install equipment,
Since it is removable, it is easy to repair and repair.

【0012】0012

【実施例】以下に本発明の生物学的窒素除去装置の一実
施を図1に基づいて説明する。図1は、この発明の一実
施例の生物学的窒素除去用ユニットを活性汚泥法の反応
槽に浸漬した構成図である。この窒素除去用ユニットは
、窒素除去用の装置類を取り付けるケージ1と、このケ
ージ1を脱窒領域2と硝化領域3に分割する仕切手段4
と、脱窒領域2のケージ1に設置されて脱窒領域2内の
被処理水を攪拌する水中攪拌装置5と、硝化領域3のケ
ージ1に設置されて硝化領域3内の被処理水にエアーを
送り込む散気装置6と、ケージ1に設置されて硝化領域
3から脱窒領域2に被処理水を循環させる硝化液循環装
置7と、脱窒領域2および硝化領域3に投入された微生
物固定化担体8とから構成されている。
[Embodiment] An embodiment of the biological nitrogen removal apparatus of the present invention will be described below with reference to FIG. FIG. 1 is a block diagram showing a biological nitrogen removal unit according to an embodiment of the present invention immersed in a reaction tank of an activated sludge method. This nitrogen removal unit includes a cage 1 in which devices for nitrogen removal are attached, and a partition means 4 that divides the cage 1 into a denitrification area 2 and a nitrification area 3.
, an underwater stirring device 5 installed in the cage 1 of the denitrification area 2 to stir the water to be treated in the denitrification area 2, and an underwater stirring device 5 installed in the cage 1 of the nitrification area 3 to stir the water to be treated in the nitrification area 3. An aeration device 6 that sends air, a nitrification liquid circulation device 7 that is installed in the cage 1 and that circulates the water to be treated from the nitrification region 3 to the denitrification region 2, and microorganisms introduced into the denitrification region 2 and the nitrification region 3. It is composed of an immobilization carrier 8.

【0013】ケージ1は、既設曝気槽9に浸漬できる寸
法であって、水中攪拌装置5や散気装置6等を取り付け
るに十分な強度を有する枠体(図示せず)に微生物固定
化担体8の最小寸法の1/4 〜3/4 の目開きのネ
ット1aを被着している。そして、このケージ1は、据
付、撤去が容易なように脱窒領域2と硝化領域3の二つ
の別体の領域のケージ1に分割されている。
The cage 1 has microorganism immobilization carriers 8 in a frame (not shown) that has a size that can be immersed in an existing aeration tank 9 and has sufficient strength to attach an underwater stirring device 5, an aeration device 6, etc. A net 1a with a mesh size of 1/4 to 3/4 of the minimum dimension of the net 1a is attached. The cage 1 is divided into two separate regions, a denitrification region 2 and a nitrification region 3, for ease of installation and removal.

【0014】脱窒領域2と硝化領域3を分ける仕切手段
4は、硝化領域3と接する脱窒領域2のケージ1の側部
に設けられている。この仕切手段4は、下部に硝化領域
3の被処理水が脱窒領域2に逆流しないように設けられ
た仕切壁4Aと、上部に脱窒領域2の被処理水が硝化領
域3側に越流する際、微生物固定化担体8が越流しない
ようにするためのスクリーン4Bとからなり、スクリー
ン4Bは、仕切壁4Aに対して0〜60度の範囲で傾斜
させて取り付けられている。
A partition means 4 for separating the denitrification region 2 and the nitrification region 3 is provided on the side of the cage 1 of the denitrification region 2 which is in contact with the nitrification region 3. This partitioning means 4 has a partition wall 4A provided at the bottom so that the water to be treated in the nitrification region 3 does not flow back into the denitrification region 2, and a partition wall 4A provided at the top to prevent the water to be treated in the denitrification region 2 from flowing back into the nitrification region 3. It consists of a screen 4B to prevent the microorganism immobilized carrier 8 from overflowing during flowing, and the screen 4B is attached to the partition wall 4A at an angle of 0 to 60 degrees.

【0015】なお、硝化領域3側のケージ1の流出口部
分にも前記と同様にスクリーン3Bが設けられ、硝化領
域3の微生物固定化担体8が硝化領域3から越流しない
ように構成されている。但し、脱窒領域2と硝化領域3
のケージ1に設けられたスクリーン4B,3B は、ケ
ージ1全体がネット1aで被覆され、流出口部分のネッ
ト1aがスクリーン4B,3B の役割を果たす場合は
必ずしも必要ではない。
[0015] A screen 3B is also provided at the outlet of the cage 1 on the side of the nitrification region 3 in the same manner as described above, and is configured to prevent the microorganism immobilization carrier 8 in the nitrification region 3 from overflowing from the nitrification region 3. There is. However, denitrification region 2 and nitrification region 3
The screens 4B and 3B provided in the cage 1 are not necessarily necessary when the entire cage 1 is covered with the net 1a and the net 1a at the outlet portion plays the role of the screens 4B and 3B.

【0016】脱窒領域2のケージ1の底部には脱窒領域
2の被処理水を攪拌するための水中攪拌装置5が設けら
れている。他方、硝化領域3のケージ1には被処理水中
にエアーを送り込むための散気装置6が設けられている
。この散気装置6は、既設活性汚泥法の下水処理場に設
置された散気装置(図示せず)とは別の装置であって硝
化領域3のケージ1に取り付けられユニット化されたも
のである。
An underwater stirring device 5 for stirring the water to be treated in the denitrification region 2 is provided at the bottom of the cage 1 in the denitrification region 2 . On the other hand, the cage 1 in the nitrification region 3 is provided with an air diffuser 6 for feeding air into the water to be treated. This air diffuser 6 is a separate device from the air diffuser (not shown) installed in the existing activated sludge method sewage treatment plant, and is installed in the cage 1 of the nitrification area 3 and is unitized. be.

【0017】ただし、既設の散気装置をそのまま利用す
ることにしてもよいが本法のように硝化を図るには既設
散気装置の散気能力が不足していることが多く、本法の
ように新たに散気装置6を付加することが必要なことが
多い。
[0017] However, although it is possible to use the existing aeration equipment as is, the existing aeration equipment often lacks the aeration capacity to achieve nitrification as in this method. In many cases, it is necessary to add a new air diffuser 6.

【0018】硝化領域3の流出口と脱窒領域2の流入口
との間には硝化液循環装置7が設置され、硝化をへた被
処理水が脱窒領域2へ循環するように構成されている。 7Aは、硝化液循環用配管であり、7Bは、硝化液を送
る硝化液循環ポンプである。
A nitrifying liquid circulation device 7 is installed between the outlet of the nitrification zone 3 and the inlet of the denitrification zone 2, and is configured so that the treated water that has undergone nitrification is circulated to the denitrification zone 2. ing. 7A is a nitrified liquid circulation pipe, and 7B is a nitrated liquid circulation pump that sends the nitrated liquid.

【0019】脱窒領域2と硝化領域3のケージ1内には
微生物固定化担体8が多数投入してある。この微生物固
定化担体8は、ポリウレタン、セラミック、活性炭など
の多孔質単体物質によって形成され、この多孔質単体物
質の孔中または表面に脱窒領域2側においては脱窒菌、
硝化領域3側においては硝化菌を担持したものある。
A large number of microorganism immobilization carriers 8 are placed in the cages 1 in the denitrification zone 2 and nitrification zone 3. This microorganism immobilization carrier 8 is formed of a porous single material such as polyurethane, ceramic, activated carbon, etc., and denitrifying bacteria,
On the nitrification region 3 side, there is one carrying nitrifying bacteria.

【0020】上記構成の据付は、ユニット化された窒素
除去用ユニットのうち脱窒領域2のケージ1を曝気槽9
内の上流側に設置し、硝化領域3のケージ1を曝気槽9
内の下流側に設置する。なお、脱窒領域2と硝化領域3
には予め微生物固定化担体8が投入されている。
[0020]In the installation of the above configuration, the cage 1 of the denitrification area 2 of the unitized nitrogen removal unit is placed in the aeration tank 9.
The cage 1 in the nitrification area 3 is placed in the aeration tank 9.
Installed on the downstream side of the In addition, denitrification region 2 and nitrification region 3
A microorganism immobilization carrier 8 is placed in advance.

【0021】以下に上記構成の窒素除去装置の動作を説
明する。まず、原水が脱窒領域2の流入口から導かれ、
脱窒領域2内で一定時間滞留する。滞留している間は水
中攪拌装置5によって絶えず脱窒領域2の被処理水が攪
拌されて微生物固定化担体8と被処理水とが均一に混合
されて窒素除去効率を高める。
The operation of the nitrogen removal apparatus having the above structure will be explained below. First, raw water is led from the inlet of denitrification area 2,
It stays in the denitrification region 2 for a certain period of time. During the retention period, the water to be treated in the denitrification area 2 is constantly stirred by the underwater stirring device 5, and the microorganism immobilization carrier 8 and the water to be treated are uniformly mixed, thereby increasing nitrogen removal efficiency.

【0022】被処理水は、脱窒領域2に一定時間滞留し
た後、仕切壁4A上部から硝化領域3に越流し、一定時
間硝化領域3に滞留する。硝化領域3に滞留している間
に被処理水に散気装置6からエアーが吹き込まれ硝化が
促進される。そして、硝化領域3内の被処理水の一部は
硝化液循環装置7によって脱窒領域2に循環される。こ
のように被処理液が脱窒領域2と硝化領域3とを循環す
るうちに、脱窒領域2では被処理水中の亜硝酸塩や硝酸
塩が微生物固定化担体8に担持された脱窒菌や水中の脱
窒菌によって脱窒され不活性な窒素ガスに変化し、硝化
槽では硝化菌によって被処理水中のアンモニアなどが亜
硝酸塩や硝酸塩に変わり、この循環によって被処理水中
の窒素化合物は除去されていく。
After the water to be treated remains in the denitrification region 2 for a certain period of time, it overflows into the nitrification region 3 from the upper part of the partition wall 4A, and remains in the nitrification region 3 for a certain period of time. While the water remains in the nitrification region 3, air is blown into the water from the aeration device 6 to promote nitrification. A part of the water to be treated in the nitrification region 3 is circulated to the denitrification region 2 by the nitrification liquid circulation device 7. While the liquid to be treated circulates between the denitrification area 2 and the nitrification area 3, in the denitrification area 2, nitrites and nitrates in the water to be treated are absorbed by the denitrifying bacteria carried on the microorganism immobilization carrier 8 and the denitrifying bacteria in the water. It is denitrified by denitrifying bacteria and converted into inert nitrogen gas, and in the nitrification tank, ammonia and other substances in the water to be treated are converted to nitrites and nitrates by nitrifying bacteria, and nitrogen compounds in the water to be treated are removed through this cycle.

【0023】なお、図示していないが脱窒、硝化された
被処理水は、硝化領域3から沈澱池に導かれ、処理水は
沈澱池から越流させて滅菌後放流し、他方沈澱した汚泥
は沈澱池の底部に沈澱する。沈澱した汚泥は汚泥引抜ポ
ンプによって一部は返送汚泥パイプを通って脱窒領域2
の流入口に返送され、残りは余剰汚泥パイプを通って脱
水等の処理をされた後処分される。
Although not shown, denitrified and nitrified water to be treated is led from the nitrification region 3 to a settling tank, and the treated water is overflowed from the settling tank and discharged after sterilization, while the settled sludge is settles at the bottom of the settling basin. A part of the settled sludge is sent to the denitrification area 2 through the return sludge pipe by the sludge extraction pump.
The remaining sludge is sent back to the inlet of the sludge, and the remaining sludge passes through a surplus sludge pipe where it is dehydrated and then disposed of.

【0024】なお、水中攪拌装置5や散気装置6等の修
理や補修を行なう場合は、ケージ1を曝気槽9から引き
上げれば簡単に修理や補修ができ、従来のように反応槽
内の被処理水を抜く必要はない。
When repairing or repairing the underwater agitation device 5 or the aeration device 6, etc., the cage 1 can be easily repaired or repaired by pulling it up from the aeration tank 9, and the inside of the reaction tank can be easily repaired or repaired. There is no need to drain the water to be treated.

【0025】上記実施例では、一つのユニットについて
説明したが、脱窒、硝化を複数段連続的に処理する活性
汚泥法に本ユニットを複数用いてもよいことは言うまで
もない。
Although one unit has been described in the above embodiment, it goes without saying that a plurality of units may be used in an activated sludge method in which denitrification and nitrification are carried out continuously in multiple stages.

【0026】また、生物学的窒素除去用ユニットを脱窒
領域2と硝化領域3のケージ1に分割して構成している
が、本窒素除去用ユニットはこれらのケージ1を一体の
ものとして脱窒領域2と硝化領域3を単に仕切手段4に
よって仕切ったものであってもよい。
[0026]Although the biological nitrogen removal unit is constructed by dividing the cage 1 into the denitrification area 2 and the nitrification area 3, this nitrogen removal unit removes these cages 1 as one unit. The nitrification region 2 and the nitrification region 3 may be simply separated by a partitioning means 4.

【0027】さらに、上記実施例ではケージ1を水中攪
拌装置5や散気装置6等を取り付ける枠体にネット1a
を被覆して構成しているが、水中攪拌装置5や散気装置
6等を取り付ける枠体だけからなるフレームで構成し、
このフレームの脱窒領域2と硝化領域3をスクリーン4
Bを有する仕切手段4によって仕切り、硝化領域3の流
出口にもスクリーン3Bを設けて構成したものであって
もよい。
Furthermore, in the above embodiment, the cage 1 is attached with a net 1a on the frame body to which the underwater stirring device 5, the aeration device 6, etc. are attached.
It consists of a frame consisting only of a frame body to which an underwater stirring device 5, an aeration device 6, etc. are attached,
The denitrification region 2 and nitrification region 3 of this frame are separated by a screen 4.
The nitrification region 3 may be partitioned by a partition means 4 having a nitrification region 3, and a screen 3B may also be provided at the outlet of the nitrification region 3.

【0028】また、上記実施例では脱窒領域2と硝化領
域3には微生物固定化担体8が投入してあるが、必ずし
も両槽1,2 に微生物固定化担体8を投入しなくても
よく、少なくともいずれか一方の槽に投入したものであ
ってもよい。また、脱窒領域2と硝化領域3に全く微生
物固定化担体8を投入しなくてもよい。
Furthermore, in the above embodiment, the microorganism immobilization carrier 8 is placed in the denitrification zone 2 and the nitrification zone 3, but the microorganism immobilization carrier 8 does not necessarily have to be placed in both tanks 1 and 2. , or may be added to at least one of the tanks. Further, it is not necessary to introduce the microorganism immobilization carrier 8 into the denitrification region 2 and the nitrification region 3 at all.

【0029】[0029]

【発明の効果】上記構成のように窒素除去に必要な装置
類をユニット化することによって、既設の活性汚泥法の
下水処理場をそのまま利用することができると共に、既
存の下廃水処理設備に対する据付、撤去が容易である。 しかも簡単に必要な装置類の取り付けや取り外しができ
ることから修理や補修が容易である。
[Effects of the Invention] By unitizing the equipment necessary for nitrogen removal as in the above configuration, existing activated sludge method sewage treatment plants can be used as is, and installation in existing sewage and wastewater treatment equipment is possible. , easy to remove. In addition, repairs and repairs are easy because the necessary equipment can be easily attached and removed.

【0030】また、本発明は、微生物固定化担体を脱窒
領域と硝化領域の少なくとのいずれか一方に投入するこ
とによって、反応槽当りの微生物濃度が高まることによ
って脱窒速度と硝化速度の少なくともいずれか一方が高
まつて反応槽の容積を小さくすることも可能である。
[0030] Furthermore, the present invention improves the denitrification rate and the nitrification rate by increasing the microorganism concentration per reaction tank by introducing a microorganism-immobilized carrier into at least one of the denitrification region and the nitrification region. It is also possible to reduce the volume of the reaction tank by increasing the height of at least one of them.

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

【図1】本発明の生物学的窒素除去用ユニットの一実施
例を曝気槽に浸漬した使用状態図である。
FIG. 1 is a diagram showing a state in which an embodiment of the biological nitrogen removal unit of the present invention is immersed in an aeration tank.

【図2】従来の活性汚泥法の一実施例を示す構成図であ
る。
FIG. 2 is a configuration diagram showing an example of a conventional activated sludge method.

【符号の説明】[Explanation of symbols]

1    ケージ 2    脱窒領域 3    硝化領域 4    仕切手段 5    水中攪拌装置 6    散気装置 7    硝化液循環装置 8    微生物固定化担体 9    曝気槽 1 Cage 2   Denitrification area 3 Nitrification area 4 Partition means 5. Underwater stirring device 6. Air diffuser 7 Nitrification liquid circulation device 8 Microorganism immobilization carrier 9 Aeration tank

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】  反応槽内に浸漬され反応槽から取り出
し可能に設けられたフレームと、このフレームを脱窒領
域と硝化領域に分割する仕切手段と、脱窒領域のフレー
ムに設置されて脱窒領域内の被処理水を攪拌する水中攪
拌装置と、硝化領域のフレームに設置されて硝化領域内
の被処理水にエアーを送り込む散気装置と、フレームに
設置されて硝化領域から脱窒領域に被処理水を循環させ
る硝化液循環装置とから構成された生物学的窒素除去用
ユニット。
1. A frame immersed in a reaction tank and removable from the reaction tank, a partition means for dividing the frame into a denitrification area and a nitrification area, and a partition means installed in the frame of the denitrification area for denitrification. An underwater stirring device that stirs the water to be treated in the area, a diffuser installed in the frame of the nitrification area to send air into the water to be treated in the nitrification area, and a diffuser installed in the frame to move air from the nitrification area to the denitrification area. A biological nitrogen removal unit consisting of a nitrification liquid circulation device that circulates the water to be treated.
【請求項2】  反応槽内に浸漬されたフレームを微生
物固定化担体よりも小さい目開きのネットを張着したケ
ージによって形成し、このケージ内に微生物固定化担体
を投入した請求項1記載の生物学的窒素除去用ユニット
2. The method according to claim 1, wherein the frame immersed in the reaction tank is formed by a cage covered with a net having a mesh size smaller than that of the microorganism-immobilized carrier, and the microorganism-immobilized carrier is introduced into the cage. Unit for biological nitrogen removal.
JP3073426A 1991-04-08 1991-04-08 Biological nitrogen removing unit Pending JPH04310298A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3073426A JPH04310298A (en) 1991-04-08 1991-04-08 Biological nitrogen removing unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3073426A JPH04310298A (en) 1991-04-08 1991-04-08 Biological nitrogen removing unit

Publications (1)

Publication Number Publication Date
JPH04310298A true JPH04310298A (en) 1992-11-02

Family

ID=13517903

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3073426A Pending JPH04310298A (en) 1991-04-08 1991-04-08 Biological nitrogen removing unit

Country Status (1)

Country Link
JP (1) JPH04310298A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996037444A1 (en) * 1995-05-23 1996-11-28 Ebara Corporation Method of aerobically treating wastewater and treatment tank
EP0870427A3 (en) * 1997-04-07 1999-09-08 Hermann Hugel Planting bed for a sewage plant
JP2007319807A (en) * 2006-06-01 2007-12-13 Aqua House Kk Flow carrier biological treatment tank
JP2008029943A (en) * 2006-07-27 2008-02-14 Kanazawa Univ Microorganism carrier and waste water treatment equipment
JP2009028698A (en) * 2007-07-31 2009-02-12 Metawater Co Ltd Reaction tank for sewage treatment
JP2011235287A (en) * 2011-07-20 2011-11-24 Maezawa Ind Inc Wastewater treatment apparatus
JP6854381B1 (en) * 2020-12-21 2021-04-07 三菱重工環境・化学エンジニアリング株式会社 Denitrification tank repair method for human waste treatment facility

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996037444A1 (en) * 1995-05-23 1996-11-28 Ebara Corporation Method of aerobically treating wastewater and treatment tank
US6077424A (en) * 1995-05-23 2000-06-20 Ebara Corporation Method for aerobically treating wastewater and a treatment tank for such method
KR100409056B1 (en) * 1995-05-23 2004-03-22 가부시키 가이샤 에바라 세이사꾸쇼 Aerobic treatment method and treatment tank of sewage
EP0870427A3 (en) * 1997-04-07 1999-09-08 Hermann Hugel Planting bed for a sewage plant
JP2007319807A (en) * 2006-06-01 2007-12-13 Aqua House Kk Flow carrier biological treatment tank
JP2008029943A (en) * 2006-07-27 2008-02-14 Kanazawa Univ Microorganism carrier and waste water treatment equipment
JP2009028698A (en) * 2007-07-31 2009-02-12 Metawater Co Ltd Reaction tank for sewage treatment
JP2011235287A (en) * 2011-07-20 2011-11-24 Maezawa Ind Inc Wastewater treatment apparatus
JP6854381B1 (en) * 2020-12-21 2021-04-07 三菱重工環境・化学エンジニアリング株式会社 Denitrification tank repair method for human waste treatment facility
JP2022097821A (en) * 2020-12-21 2022-07-01 三菱重工環境・化学エンジニアリング株式会社 Denitrification tank repairing method in excreta treatment facility

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