JPH1024299A - Aerobic treatment of organic sewage and device therefor - Google Patents

Aerobic treatment of organic sewage and device therefor

Info

Publication number
JPH1024299A
JPH1024299A JP20116396A JP20116396A JPH1024299A JP H1024299 A JPH1024299 A JP H1024299A JP 20116396 A JP20116396 A JP 20116396A JP 20116396 A JP20116396 A JP 20116396A JP H1024299 A JPH1024299 A JP H1024299A
Authority
JP
Japan
Prior art keywords
tank
water
carrier
treated
aerobic treatment
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
JP20116396A
Other languages
Japanese (ja)
Inventor
Kiyohide Idogawa
清秀 伊戸川
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.)
CLEAN TEC KK
Original Assignee
CLEAN TEC KK
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 CLEAN TEC KK filed Critical CLEAN TEC KK
Priority to JP20116396A priority Critical patent/JPH1024299A/en
Priority to KR1019970003736A priority patent/KR980009141A/en
Publication of JPH1024299A publication Critical patent/JPH1024299A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/10Packings; Fillings; Grids
    • C02F3/101Arranged-type packing, e.g. stacks, arrays
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/06Aerobic processes using submerged filters
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F2003/001Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms
    • 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

  • Life Sciences & Earth Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for treating org. sewage with the aerobic decomposition capacity enhanced by practically eliminating the wear of a carrier, charging the whole amt. of the necessary carrier at the start of operation, incubating a microorganism in the carrier bed while passing water through the device and repeatedly passing the water through the carrier bed. SOLUTION: Org. sewage is introduced into an aerobic treating tank 1. A reticular body 2 for blocking the passage of a carrier 3 is horizontally fitted in the tank 1 in a single stage or in multiple stages to vertically divide the inside of the tank 1 into several compartments. The floatable microorganism immobilizing carrier 3 is packed in each compartment, the water to be treated is passed through the carrier 3 bed in each compartment, air is diffused by a blower 5 from the bottom of the tank 1, the water is circulated in the tank 1 by a circulating pump 7, and the water is purified.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は下水などの各種有機
性汚水を極めて合理的な処理方法及び装置により生物学
的に高度に浄化処理する有機性汚水の処理方法及びその
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 a method and an apparatus for treating organic sewage such as sewage, which is highly biologically purified by a very rational treatment method and apparatus.

【0002】[0002]

【従来の技術】従来、有機ポリマー化合物からなる粒状
物を微生物固定化担体(以下担体と称する)として利用
し、汚水を浄化するには処理槽内に容積の5〜70%相
応量の担体を浸漬投入し、処理槽内を散気・回流を行
い、当該担体を自由に移動させ被処理水を接触させる流
動床によっている。
2. Description of the Related Art Conventionally, a granular material comprising an organic polymer compound has been used as a carrier for immobilizing microorganisms (hereinafter referred to as a carrier). To purify sewage, a carrier having an amount corresponding to 5 to 70% of the volume in a treatment tank is required. It is immersed and charged, diffuses and circulates in the treatment tank, and the carrier is freely moved to make contact with the water to be treated.

【0003】[0003]

【発明が解決しようとする課題】従来の流動床で有機性
汚水を浄化する場合は、被処理水と共に担体を回流する
ため大きな動力を必要とすると共に、回流時に担体は処
理槽壁に摺擦され摩耗が激しく耐久性に欠ける問題があ
った。又、担体の投入初期は微生物の増殖がなく比重が
小さく水面近くに浮上し旋回が起きないので、担体に微
生物を予め付着させる馴養のための培養槽を必要とし
た。又、担体の投入量は微生物の繁殖と相関し最大70
%の投入を行うには約6ケ月程度の少量ずつの投入作業
が必要であり、手間がかかると共に、この間は処理能力
に限度がある。
In the case of purifying organic wastewater with a conventional fluidized bed, a large power is required to circulate the carrier together with the water to be treated, and the carrier rubs against the wall of the treatment tank during the circulation. There was a problem that wear was severe and durability was lacking. In addition, at the initial stage of loading of the carrier, there is no growth of microorganisms, the specific gravity is small, the surface floats near the water surface, and no swirling occurs. In addition, the input amount of the carrier correlates with the growth of
In order to input the%, it is necessary to perform an input operation in small amounts of about six months, which is troublesome, and the processing capacity is limited during this time.

【0004】上記点より本発明は担体の摩耗が殆どない
と共に、運転開始時に必要な担体の全量を装入し、通水
運転を行いつつ担体層の微生物培養を行い担体層を繰り
返し通過することにより好気分解能力を早急に発揮でき
るようにした有機性汚水の処理方法及びその装置を提供
しようとするものである。
[0004] In view of the above, the present invention is characterized in that there is almost no wear of the carrier, the entire amount of the carrier required at the start of the operation is charged, and the microorganisms are cultivated in the carrier layer and the water is repeatedly passed through the carrier layer while running the water. Accordingly, it is an object of the present invention to provide a method and an apparatus for treating organic sewage, in which aerobic decomposition capacity can be promptly exerted.

【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
本発明方法は、有機性汚水を好気処理槽内に導入し、槽
内に担体の通過を阻止する網状体を単段又は多段に水平
に横設して槽内を上下方向に数室に区画し、各室に浮上
性を有する微生物固定化担体を充填し、被処理水を各室
の担体層を通過させると同時に槽の底部より散気を行
い、被処理水を槽内で循環し浄化処理を行うことを特徴
とするものである。
According to the present invention, there is provided a method for introducing organic wastewater into an aerobic treatment tank, wherein a network for preventing the carrier from passing through the tank is provided in a single stage or in multiple stages. Horizontally laid horizontally, the inside of the tank is divided into several chambers in the vertical direction, each chamber is filled with a buoyant microorganism-immobilized carrier, and the water to be treated passes through the carrier layer in each chamber, and at the same time the bottom of the tank. It is characterized by performing more aeration and purifying by circulating the water to be treated in the tank.

【0006】又、本発明方法は、有機性汚水を横方向に
数槽に仕切られた好気処理槽内に導入し、各槽内に担体
の通過を阻止する網状体を単段又は多段に水平に横設し
て、各槽内を上下方向に数室に区画し、各室に浮上性を
有する微生物固定化担体を充填し、被処理水を各室の担
体層を通過させると同時に各槽の底部より散気を行い被
処理水を各槽内で循環し、最前部の槽より最後部の槽へ
被処理水を順次移流し浄化処理を行うことを特徴とする
ものである。又、本発明方法は、請求項2記載の有機性
汚水の好気処理方法の好気処理槽の最後部の槽より被処
理水の一部を最前部の槽へ返送し、浄化処理を繰り返す
ことを特徴とするものである。
In the method of the present invention, the organic wastewater is introduced laterally into aerobic treatment tanks divided into several tanks, and a mesh for preventing the passage of carriers is provided in each tank in a single stage or in multiple stages. Horizontally, each tank is divided into several chambers in the vertical direction, each chamber is filled with a buoyant microorganism-immobilized carrier, and water to be treated is passed through the carrier layer of each chamber at the same time. It is characterized in that air is diffused from the bottom of the tank, the water to be treated is circulated in each tank, and the water to be treated is sequentially transferred from the foremost tank to the last tank to perform a purification treatment. In the method of the present invention, part of the water to be treated is returned from the last tank of the aerobic treatment tank to the forefront tank in the aerobic treatment method for organic wastewater according to claim 2, and the purification treatment is repeated. It is characterized by the following.

【0007】又、本発明方法は、有機性汚水を横方向に
数槽に仕切られた好気処理槽内に導入し、各槽内に担体
の通過を阻止する網状体を単段又は多段に水平に横設し
て各槽内を上下方向に数室に区画し、各室に浮上性を有
する微生物固定化担体を充填し、被処理水を各室の担体
層を通過させると同時に各槽の底部より散気を行い、最
前部の槽より最後部の槽へ被処理水を順次移流し最後部
の槽より被処理水の一部を最前部の槽へ返送し、浄化処
理を繰り返すことを特徴とするものである。
In the method of the present invention, the organic wastewater is introduced into an aerobic treatment tank divided into several tanks in a horizontal direction, and a mesh body for preventing passage of a carrier is provided in each tank in a single stage or in multiple stages. Horizontally laid horizontally, each tank is divided into several chambers in the vertical direction, each chamber is filled with a buoyant microorganism-immobilized carrier, and water to be treated passes through the carrier layer of each chamber, and each tank is simultaneously filled. Aeration from the bottom of the tank, sequentially transfer the water to be treated from the foremost tank to the last tank, return a portion of the to-be-treated water from the last tank to the forefront tank, and repeat the purification process. It is characterized by the following.

【0008】又、本発明装置は、好気処理槽内が単段又
は多段に水平に横設された担体の通過を阻止する網状体
で上下方向に数室に区画され、各室内に浮上性を有する
微生物固定化担体が充填されると共に、槽の底部に散気
装置が設置され、且つ槽内に槽内で被処理水を循環する
循環装置が設置されていることを特徴とするものであ
る。
In the apparatus of the present invention, the inside of the aerobic treatment tank is divided into several chambers in a vertical direction by a net-like body that blocks the passage of carriers horizontally arranged in a single stage or in multiple stages. A microorganism-immobilized carrier having the same is filled, an air diffuser is installed at the bottom of the tank, and a circulating device for circulating the water to be treated in the tank is installed in the tank. is there.

【0009】又、本発明装置は、好気処理槽が仕切り壁
で横方向に数槽に仕切られ、各槽内が単段又は多段に水
平に横設された担体の通過を阻止する網状体で上下方向
に数室に区画され、各室内に浮上性を有する微生物固定
化担体が充填されると共に、各槽の底部に散気装置が設
置され、且つ各槽内に各槽内で被処理水を循環する循環
装置が設置され前記仕切り壁に後続の槽への被処理水の
移流部が設けられていることを特徴とするものである。
又、本発明装置は、請求項6記載の有機性汚水の好気処
理装置の好気処理槽の最後部の槽に、最後部の槽の被処
理水の一部を最前部の槽へ返送する返送手段が設けられ
ていることを特徴とするものである。
In the apparatus of the present invention, the aerobic treatment tank is divided into several tanks in a horizontal direction by a partition wall, and the inside of each tank is a net-like body for preventing passage of a carrier horizontally laid in a single stage or in multiple stages. The chamber is vertically divided into several chambers, each chamber is filled with a buoyant microorganism-immobilizing carrier, an air diffuser is installed at the bottom of each tank, and each tank is treated in each tank. A circulating device for circulating water is provided, and the partition wall is provided with an advancing section for the water to be treated to a subsequent tank.
Further, the apparatus of the present invention returns a part of the water to be treated in the last tank to the last tank of the aerobic treatment tank of the aerobic treatment apparatus for organic wastewater according to claim 6 to the front tank. A return means is provided.

【0010】又、本発明装置は、好気処理槽が仕切り壁
で横方向に数槽に仕切られ、各槽内が単段又は多段に水
平に横設された担体の通過を阻止する網状体で上下方向
に数室に区画されると共に、各室内に浮上性を有する微
生物固定化担体が充填され、各槽の底部に散気装置が設
置されると共に、前記仕切り壁に後続の槽への被処理水
の移流部が設けられ、最後部の槽に被処理水の一部を最
前部の槽へ返送する返送手段が設けられていることを特
徴とするものである。
[0010] In the apparatus of the present invention, the aerobic treatment tank may be divided into several tanks by a partition wall in a horizontal direction, and the inside of each tank may be a single-stage or multi-stage horizontally-arranged carrier for preventing passage of carriers. The chamber is vertically divided into several chambers, and each chamber is filled with a buoyant microorganism-immobilizing carrier, and a diffuser is installed at the bottom of each tank, and the partition wall is connected to a subsequent tank. An advection section for the water to be treated is provided, and a return means for returning a part of the water to be treated to the frontmost tank is provided in the last tank.

【0011】依って、請求項1及び請求項5の本発明は
好気処理槽内の担体が担体の通過を阻止する網状体で区
画されているため、各室に担体層が形成される。担体は
浮揚状態であるが上下の網状体の区画内にあり移動がな
い。又、槽内で被処理水が循環するため有機不純物を好
気分解する担体層を数回通過するので、担体内外の微生
物の接触回数が増え浄化が促進される。網状体及び担体
は、散気及び被処理水の流れで目詰まりが防止される。
According to the first and fifth aspects of the present invention, since the carrier in the aerobic treatment tank is divided by a mesh for preventing passage of the carrier, a carrier layer is formed in each chamber. The carrier is in a floating state, but does not move in the upper and lower mesh sections. Further, since the water to be treated circulates in the tank, it passes through the carrier layer that aerobically decomposes organic impurities several times, so that the number of times of contact of microorganisms inside and outside the carrier increases, and purification is promoted. The mesh and the carrier are prevented from being clogged by aeration and the flow of the water to be treated.

【0012】又、請求項2及び請求項6の本発明は大き
な処理能力を必要とする大型の好気処理槽等に使用さ
れ、好気処理槽が横方向に数槽に仕切られているもの
で、仕切られた各槽内は前記請求項1及び請求項5の発
明と同様の機能を有し、最前部の槽より最後部の槽へ被
処理水を順次移流して担体層での微生物の接触回数をよ
り多くして処理能力を大にしている。
Further, the present invention according to claims 2 and 6 is used for a large aerobic treatment tank or the like which requires a large processing capacity, and the aerobic treatment tank is divided into several tanks in a lateral direction. The inside of each partitioned tank has the same function as that of the first and fifth aspects of the present invention, and the water to be treated is sequentially transferred from the foremost tank to the last tank so that the microorganisms in the carrier layer are transferred. The number of contacts is increased to increase the processing capacity.

【0013】又、請求項3及び請求項7の本発明は請求
項2及び請求項6の発明と同様の機能を有するが好気処
理槽が数槽に仕切られている場合、各槽で循環を受けた
被処理水が最後部の槽で循環を受けた後、被処理水の一
部が最前部の槽へ再び返送され繰り返し浄化処理を受け
るので、好気分解をより効率よく行うことができる。
The present invention according to claims 3 and 7 has the same function as the inventions according to claims 2 and 6, but when the aerobic treatment tank is divided into several tanks, the circulation is performed in each tank. After the water to be treated is circulated in the last tank, a part of the water to be treated is returned to the foremost tank and subjected to repeated purification treatment, so that aerobic decomposition can be performed more efficiently. it can.

【0014】又、請求項4及び請求項8の本発明は好気
処理槽内の担体が担体の通過を阻止する網状体で区画さ
れているため、各室に担体層が形成され、担体は浮揚状
態であるが上下の網状体の区画内にあり移動がない。
又、網状体及び担体は散気及び被処理水の流れで目詰ま
りが防止されるのは同様であるが、各槽の有機不純物を
好気分解する担体層を通過した後最後部の被処理水の一
部が最前部の槽へ再び返送され繰り返し浄化処理を受け
るので、各槽内で被処理水を循環させるものと同様好気
分解を効率よく行うことができる。
Further, in the present invention according to claims 4 and 8, the carrier in the aerobic treatment tank is divided by a mesh that blocks the passage of the carrier, so that a carrier layer is formed in each chamber, and the carrier is It is in a floating state but within the upper and lower mesh sections and does not move.
Similarly, the mesh body and the carrier are prevented from being clogged by aeration and flow of the water to be treated, but after passing through the carrier layer that aerobicly decomposes the organic impurities in each tank, the final portion of the material to be treated is treated. Since a part of the water is returned to the forefront tank again and repeatedly subjected to the purification treatment, aerobic decomposition can be performed efficiently as in the case of circulating the water to be treated in each tank.

【0015】[0015]

【発明の実施の形態】以下、本発明の一実施の形態を図
面に基づき説明する。図1は請求項1及び請求項5の発
明の一実施の形態を示す構成図、図2は請求項2、3及
び請求項6、7の発明の一実施の形態を示す構成図、図
3は請求項4及び請求項8の発明の一実施の形態を示す
構成図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a block diagram showing one embodiment of the first and fifth aspects of the present invention, FIG. 2 is a block diagram showing one embodiment of the second and third aspects of the present invention, and FIGS. FIG. 7 is a configuration diagram showing one embodiment of the inventions of claims 4 and 8.

【0016】而して、図1に於いて図中1は好気処理槽
であり、好気処理槽1内に水平に網状体2が横設され
て、上部室1A中央部室1B、下部室1Cに区画されて
いる。図面では三段に区画されているが単段又は多段の
室に区画することもできる。
In FIG. 1, reference numeral 1 denotes an aerobic treatment tank, and a net 2 is horizontally disposed in the aerobic treatment tank 1 so that an upper chamber 1A, a central chamber 1B, and a lower chamber 1 1C. Although it is divided into three stages in the drawing, it can be divided into a single-stage or a multi-stage room.

【0017】上部室1Aと中央部室1B及び下部室1C
内には被処理水中に含まれる有機不純物を好気分解する
好気性微生物が担持された浮上性を有する担体3が緩や
かに多数充填された担体層が形成されている。前記網状
体2の網目は担体3の通過を阻止する大きさに形成され
ており、担体3は室内より出ることはない。
Upper chamber 1A, central chamber 1B and lower chamber 1C
Inside, a carrier layer is formed, which is slowly filled with a large number of buoyant carriers 3 carrying aerobic microorganisms that aerobically decompose organic impurities contained in the water to be treated. The mesh of the mesh body 2 is formed in a size that prevents the passage of the carrier 3, and the carrier 3 does not exit from the room.

【0018】担体3は浮上性を有する粒状体であれば特
に素材は制限されないが、有機ポリマー化合物の発泡体
又は加工品等公知のものを使用できるが、中でも素材自
体に適度な弾性と強度とを有する素材が好ましく、特に
ウレタン樹脂等が好ましい。例えば主原料であるポリオ
ールの高分子鎖がエーテル結合からなる軟質ポリウレタ
ンフォーム等の弾性多孔性粒状物を、ウレタン樹脂等の
プラスチックを連通気泡を造る発泡法で発泡して作製し
て、所望の形状サイズに切断して使用する。そのサイズ
は10〜30mmであり、その形状は角形、球状その他
種々の形状がとれるが、角形が好ましい。エーテル系の
軟質ポリウレタンフォームを使用すれば、加水分解を受
け難く耐久性も十分有すると共に、内面及び外面の気孔
が互いに連通しているので、微生物は担体の内部に入り
込むため培養が容易で、被処理水や空気流によって微生
物が剥離しない。
The material of the carrier 3 is not particularly limited as long as it is a particulate material having a floating property. Known materials such as a foamed or processed product of an organic polymer compound can be used. Are preferable, and urethane resin is particularly preferable. For example, an elastic porous granular material such as a flexible polyurethane foam in which a polymer chain of a polyol as a main raw material is formed of an ether bond is produced by foaming a plastic such as a urethane resin by a foaming method for forming open cells to obtain a desired shape. Cut to size and use. Its size is 10 to 30 mm, and its shape can be square, spherical or various other shapes, but square is preferred. If an ether-based flexible polyurethane foam is used, it is resistant to hydrolysis and has sufficient durability.In addition, since the pores on the inner surface and the outer surface communicate with each other, microorganisms enter the inside of the carrier, so that cultivation is easy, and Microorganisms do not exfoliate due to treated water or air flow.

【0019】4は好気処理槽1の底部に設けた散気管で
あり、好気処理槽1外に設けた送風機5より送気管6を
経て空気又は純粋な酸素が槽内に供給され散気管4、送
風機5、送気管6で散気装置を構成している。7は好気
処理槽1の底部に設けた循環ポンプであり、循環ポンプ
7に循環パイプ8が連結され、循環パイプ8の先端は水
面上に突出して下方に屈曲され、被処理水が槽内で循環
できる循環装置を構成している。9は汚水供給管、10
は好気処理槽1に後続する沈澱槽であり、仕切り壁11
の底部に好気処理槽1よりの好気処理済水の移流口12
が設けられている。13は沈澱槽10に設けた処理済水
の排水管である。
Reference numeral 4 denotes an air diffuser provided at the bottom of the aerobic treatment tank 1, and air or pure oxygen is supplied into the tank from a blower 5 provided outside the aerobic treatment tank 1 via an air supply pipe 6. 4, a blower 5, and an air pipe 6 constitute an air diffuser. Reference numeral 7 denotes a circulation pump provided at the bottom of the aerobic treatment tank 1. A circulation pipe 8 is connected to the circulation pump 7, and the tip of the circulation pipe 8 projects above the water surface and is bent downward, so that the water to be treated is supplied into the tank. The circulating device that can circulate is constituted. 9 is a sewage supply pipe, 10
Reference numeral denotes a sedimentation tank following the aerobic treatment tank 1, and a partition wall 11.
Of the aerobic treated water from the aerobic treatment tank 1 at the bottom of
Is provided. Reference numeral 13 denotes a drainage pipe of the treated water provided in the sedimentation tank 10.

【0020】次に図2に於いて、図1と相当する箇所に
はそれと同一符号を付してある。図面は好気処理槽1が
横方向に三槽に仕切られているが、設置規模により任意
数の槽に仕切ることができる。仕切られた各槽内は前記
好気処理槽1と同様の網状体2による担体3層、循環ポ
ンプ7及び散気管4、送風機5、送気管6より成る散気
装置を有する構成であるが、最後部の槽内の底部に設け
た循環ポンプ7に連結する循環パイプ8と分岐して最前
部の槽内の上部へ返送する返送管14が設けられ、最後
部の槽より被処理水の一部が最前部の槽内の上部へ返送
可能となっている。
Next, in FIG. 2, portions corresponding to those in FIG. 1 are denoted by the same reference numerals. In the drawing, the aerobic treatment tank 1 is divided into three tanks in the horizontal direction, but it can be divided into an arbitrary number of tanks depending on the installation scale. Each partitioned tank has a structure including a carrier 3 layer made of a mesh body 2 similar to the aerobic treatment tank 1, a circulation pump 7, an air diffuser 4, a blower 5, and an air diffuser including an air pipe 6. A circulating pipe 8 connected to a circulating pump 7 provided at the bottom of the last tank is provided with a return pipe 14 for branching and returning to the upper part of the foremost tank. Part can be returned to the upper part in the forefront tank.

【0021】図面では最後部の槽の循環ポンプ7と循環
パイプ8が返送用の循環ポンプと返送管14とを共通に
しているが、勿論別々に設置できることは当然である。
15は最後部の槽の循環パイプ8及び返送管13に設け
たバルブである。そして、各槽の境界には仕切り壁16
の中央に四方を壁で仕切られた被処理水の流路17が設
けられ、流路17は下部に前部の槽の底部に通じる移流
口18が設けられ、上部は後続の槽の上部に開口19し
ている垂直に上方へ延長した煙突状に形成された移流部
が構成され各槽への被処理水は下向流となっている。移
流部はかかる構成に限定されるものではなく、単に各槽
の仕切り壁の上部より溢流水が流入するようにしてもよ
い。
In the drawing, the circulation pump 7 and the circulation pipe 8 in the last tank share the circulation pump for return and the return pipe 14, but they can of course be installed separately.
Reference numeral 15 denotes a valve provided in the circulation pipe 8 and the return pipe 13 of the last tank. A partition wall 16 is provided at the boundary of each tank.
In the center of the tank, there is provided a flow path 17 of the water to be treated, which is partitioned on all sides by walls. A vertically extending upwardly extending chimney-shaped advection section having an opening 19 is formed, and the water to be treated to each tank flows downward. The advection section is not limited to such a configuration, and the overflow water may simply flow from above the partition wall of each tank.

【0022】最後部の槽と沈澱室10との境界は仕切り
壁11の底部に移流口12が形成されていることは前同
様である。
The boundary between the last tank and the sedimentation chamber 10 is the same as before in that the advection port 12 is formed at the bottom of the partition wall 11.

【0023】次に図3に於いて、図1及び図2と相当す
る箇所にはそれと同一符号を付してある。図面は好気処
理槽1が横方向に三槽に仕切られているが、設置規模に
より任意数の槽に仕切ることができる。仕切られた各槽
内は前記好気処理槽1と同様の網状体2による担体3層
及び散気管4、送風機5、送気管6より成る散気装置を
有するが、各槽に循環装置は設置されていない。そし
て、最後部の槽に被処理水の一部を最前部の槽へ返送す
る循環ポンプ7及び返送管20から成る返送手段が設け
られている。又、各槽の境界には図2と同様の移流部が
構成されている。
Next, in FIG. 3, portions corresponding to those in FIGS. 1 and 2 are denoted by the same reference numerals. In the drawing, the aerobic treatment tank 1 is divided into three tanks in the horizontal direction, but it can be divided into an arbitrary number of tanks depending on the installation scale. Each partitioned tank has a carrier 3 layer made of the same net 2 as the aerobic treatment tank 1 and an air diffuser including an air diffuser 4, a blower 5, and an air blower 6, and a circulation device is installed in each tank. It has not been. Then, a return means including a circulation pump 7 and a return pipe 20 for returning a part of the water to be treated to the frontmost tank is provided in the last tank. An advection section similar to that shown in FIG. 2 is formed at the boundary between the tanks.

【0024】[0024]

【発明の効果】本発明に依れば、担体は浮揚状態である
が、上下の網状体の区画内にあり、被処理水のみが担体
間を通過するため回流による担体の摩耗がなく、耐久性
を有する。そして、網状体を多段として担体を分けてい
るため担体の有する浮力及び重量によって網状体が破損
することがなく安全である。又、担体を回流しないので
好気処理槽への初期の投入に際し、微生物の増殖がなく
ても馴養の必要がないと共に、担体の投入量も好気処理
槽容積の30〜80%の容積分に相応する量となり、好
気分解能力が格段に向上できる。又、被処理水は担体層
を繰り返し通過するため効率よく好気処理を受けること
ができるものである。
According to the present invention, although the carrier is in a floating state, the carrier is in the upper and lower meshes, and only the water to be treated passes between the carriers, so that the carrier is not worn due to circulating flow, and the carrier is durable. Has the property. Since the carrier is divided into multiple stages of the net, the net is not damaged by the buoyancy and weight of the carrier, so that the net is safe. Also, since the carrier is not circulated, the initial loading into the aerobic treatment tank does not require acclimation even if there is no growth of microorganisms, and the amount of the carrier is 30 to 80% of the volume of the aerobic treatment tank. And the aerobic decomposition capacity can be significantly improved. Moreover, since the water to be treated repeatedly passes through the carrier layer, it can be efficiently subjected to aerobic treatment.

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

【図1】本発明の一実施の形態を示す構成図である。FIG. 1 is a configuration diagram showing an embodiment of the present invention.

【図2】本発明の一実施の形態を示す構成図である。FIG. 2 is a configuration diagram showing an embodiment of the present invention.

【図3】本発明の一実施の形態を示す構成図である。FIG. 3 is a configuration diagram showing one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 好気処理槽 1A 好気処理槽の上部室 1B 好気処理槽の中央部室 1C 好気処理槽の下部室 2 網状体 3 担体 4 散気管 5 送風機 6 送気管 7 循環ポンプ 8 循環パイプ 9 汚水供給管 10 沈澱槽 11 仕切り壁 12 移流口 13 排水管 14 返送管 15 バルブ 16 仕切り壁 17 流路 18 移流口 19 開口 20 返送管 DESCRIPTION OF SYMBOLS 1 Aerobic treatment tank 1A Upper chamber of aerobic treatment tank 1B Central room of aerobic treatment tank 1C Lower chamber of aerobic treatment tank 2 Net-like body 3 Carrier 4 Air diffuser 5 Blower 6 Air supply pipe 7 Circulation pump 8 Circulation pipe 9 Sewage Supply pipe 10 Precipitation tank 11 Partition wall 12 Outflow port 13 Drain pipe 14 Return pipe 15 Valve 16 Partition wall 17 Flow path 18 Transfer port 19 Opening 20 Return pipe

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 有機性汚水を好気処理槽内に導入し、槽
内に担体の通過を阻止する網状体を単段又は多段に水平
に横設して槽内を上下方向に数室に区画し、各室に浮上
性を有する微生物固定化担体を充填し、被処理水を各室
の担体層を通過させると同時に槽の底部より散気を行
い、被処理水を槽内で循環し浄化処理を行うことを特徴
とする有機性汚水の好気処理方法。
1. An organic wastewater is introduced into an aerobic treatment tank, and a mesh body for preventing passage of a carrier is horizontally laid in a single stage or a multistage in the tank, and the inside of the tank is vertically divided into several chambers. Separate and fill each chamber with a buoyant microorganism-immobilizing carrier, allow the water to be treated to pass through the carrier layer in each chamber, and simultaneously diffuse air from the bottom of the tank, and circulate the water to be treated in the tank. An aerobic treatment method for organic wastewater, comprising performing a purification treatment.
【請求項2】 有機性汚水を横方向に数槽に仕切られた
好気処理槽内に導入し、各槽内に担体の通過を阻止する
網状体を単段又は多段に水平に横設して、各槽内を上下
方向に数室に区画し、各室に浮上性を有する微生物固定
化担体を充填し、被処理水を各室の担体層を通過させる
と同時に各槽の底部より散気を行い被処理水を各槽内で
循環し、最前部の槽より最後部の槽へ被処理水を順次移
流し浄化処理を行うことを特徴とする有機性汚水の好気
処理方法。
2. An organic wastewater is introduced laterally into aerobic treatment tanks divided into several tanks, and a mesh body for preventing passage of a carrier is horizontally provided in each tank in a single stage or in multiple stages. Each tank is vertically divided into several chambers, each chamber is filled with a buoyant microorganism-immobilized carrier, and water to be treated is passed through the carrier layer of each chamber and simultaneously scattered from the bottom of each tank. An aerobic treatment method for organic wastewater, wherein air is circulated and water to be treated is circulated in each tank, and the water to be treated is sequentially transferred from the foremost tank to the last tank for purification treatment.
【請求項3】 請求項2記載の有機性汚水の好気処理方
法の好気処理槽の最後部の槽より被処理水の一部を最前
部の槽へ返送し、浄化処理を繰り返すことを特徴とする
請求項2記載の有機性汚水の好気処理方法。
3. An aerobic treatment method for organic wastewater according to claim 2, wherein a part of the water to be treated is returned to the forefront tank from the last tank of the aerobic treatment tank, and the purification treatment is repeated. The method for aerobic treatment of organic wastewater according to claim 2, characterized in that:
【請求項4】 有機性汚水を横方向に数槽に仕切られた
好気処理槽内に導入し、各槽内に担体の通過を阻止する
網状体を単段又は多段に水平に横設して各槽内を上下方
向に数室に区画し、各室に浮上性を有する微生物固定化
担体を充填し、被処理水を各室の担体層を通過させると
同時に各槽の底部より散気を行い、最前部の槽より最後
部の槽へ被処理水を順次移流し最後部の槽より被処理水
の一部を最前部の槽へ返送し、浄化処理を繰り返すこと
を特徴とする有機性汚水の好気処理方法。
4. An organic wastewater is introduced laterally into an aerobic treatment tank divided into several tanks, and a mesh body for preventing passage of a carrier is horizontally laid in each tank in a single stage or in multiple stages. Each tank is vertically divided into several chambers, each chamber is filled with a floating microorganism-immobilized carrier, and the water to be treated is passed through the carrier layer of each chamber and diffused from the bottom of each tank at the same time. Organic water characterized by repeating the purification process by sequentially transferring treated water from the foremost tank to the last tank, returning a portion of the to-be-treated water from the last tank to the foremost tank, and repeating the purification process. Aerobic treatment method for sewage.
【請求項5】 好気処理槽内が単段又は多段に水平に横
設された担体の通過を阻止する網状体で上下方向に数室
に区画され、各室内に浮上性を有する微生物固定化担体
が充填されると共に、槽の底部に散気装置が設置され、
且つ槽内に槽内で被処理水を循環する循環装置が設置さ
れていることを特徴とする有機性汚水の好気処理装置。
5. The aerobic treatment tank is vertically divided into several chambers in a single-stage or multi-stage net-like structure that blocks the passage of carriers horizontally disposed thereon, and immobilizes microorganisms having a floating property in each room. While the carrier is filled, an air diffuser is installed at the bottom of the tank,
An aerobic treatment device for organic sewage, wherein a circulation device for circulating water to be treated in the tank is installed in the tank.
【請求項6】 好気処理槽が仕切り壁で横方向に数槽に
仕切られ、各槽内が単段又は多段に水平に横設された担
体の通過を阻止する網状体で上下方向に数室に区画さ
れ、各室内に浮上性を有する微生物固定化担体が充填さ
れると共に、各槽の底部に散気装置が設置され、且つ各
槽内に各槽内で被処理水を循環する循環装置が設置され
前記仕切り壁に後続の槽への被処理水の移流部が設けら
れていることを特徴とする有機性汚水の好気処理装置。
6. An aerobic treatment tank is divided into several tanks in a horizontal direction by a partition wall, and inside each tank is a net-like body for preventing passage of a carrier horizontally laid in a single stage or in multiple stages. Each chamber is filled with a buoyant microorganism-immobilizing carrier in each chamber, a diffuser is installed at the bottom of each tank, and the water to be treated is circulated in each tank in each tank. An aerobic treatment apparatus for organic sewage, wherein an apparatus is installed and an advection section for treated water to a subsequent tank is provided on the partition wall.
【請求項7】 請求項6記載の有機性汚水の好気処理装
置の好気処理槽の最後部の槽に、最後部の槽の被処理水
の一部を最前部の槽へ返送する返送手段が設けられてい
ることを特徴とする請求項6記載の有機性汚水の好気処
理装置。
7. A return for returning a part of the water to be treated in the last tank to the last tank of the aerobic treatment tank of the aerobic treatment apparatus for organic sewage according to claim 6. The aerobic treatment apparatus for organic sewage according to claim 6, wherein means is provided.
【請求項8】 好気処理槽が仕切り壁で横方向に数槽に
仕切られ、各槽内が単段又は多段に水平に横設された担
体の通過を阻止する網状体で上下方向に数室に区画され
ると共に、各室内に浮上性を有する微生物固定化担体が
充填され、各槽の底部に散気装置が設置されると共に、
前記仕切り壁に後続の槽への被処理水の移流部が設けら
れ、最後部の槽に被処理水の一部を最前部の槽へ返送す
る返送手段が設けられていることを特徴とする有機性汚
水の好気処理装置。
8. The aerobic treatment tank is divided into several tanks in a horizontal direction by a partition wall, and each tank has a mesh in a vertical direction by a mesh body for preventing passage of a carrier horizontally arranged in a single stage or a multistage. While being partitioned into chambers, each chamber is filled with a floating microorganism-immobilized carrier, and an air diffuser is installed at the bottom of each tank,
The partition wall is provided with an advancing section for the water to be treated to a subsequent tank, and the last tank is provided with a return means for returning a part of the water to be treated to the front tank. Aerobic treatment equipment for organic sewage.
JP20116396A 1996-07-10 1996-07-10 Aerobic treatment of organic sewage and device therefor Pending JPH1024299A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP20116396A JPH1024299A (en) 1996-07-10 1996-07-10 Aerobic treatment of organic sewage and device therefor
KR1019970003736A KR980009141A (en) 1996-07-10 1997-02-06 Aerobic treatment method of organic sewage and its apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20116396A JPH1024299A (en) 1996-07-10 1996-07-10 Aerobic treatment of organic sewage and device therefor

Publications (1)

Publication Number Publication Date
JPH1024299A true JPH1024299A (en) 1998-01-27

Family

ID=16436423

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20116396A Pending JPH1024299A (en) 1996-07-10 1996-07-10 Aerobic treatment of organic sewage and device therefor

Country Status (2)

Country Link
JP (1) JPH1024299A (en)
KR (1) KR980009141A (en)

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Publication number Priority date Publication date Assignee Title
JP2001205288A (en) * 2000-01-28 2001-07-31 Takeda Chem Ind Ltd Carrier for water treatment, its production method, and apparatus for water treatment
JP4514874B2 (en) * 2000-01-28 2010-07-28 日本エンバイロケミカルズ株式会社 Water treatment carrier, method for producing water treatment carrier and water treatment device
JP2002113482A (en) * 2000-10-10 2002-04-16 Clean Tec Kk Wastewater treatment apparatus and contact material used therein
JP2013091034A (en) * 2011-10-26 2013-05-16 Tohzai Chemical Industry Co Ltd Apparatus for treating organic wastewater
WO2016132881A1 (en) * 2015-02-16 2016-08-25 栗田工業株式会社 Biological treatment tank, method for operating same and method for treating organic wastewater
JP2016153118A (en) * 2015-02-16 2016-08-25 栗田工業株式会社 Biological treatment tank, method for operating the tank, and method for treating organic waste water
CN108569780A (en) * 2018-04-04 2018-09-25 西安建筑科技大学 A kind of cutting bio-contact oxidation reinforcing of bubble is pumped up water aeration water correction device
CN108569780B (en) * 2018-04-04 2023-08-29 西安建筑科技大学 Bubble cutting biological contact oxidation strengthening water pumping aeration water quality improvement device

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