JPS6257697A - Waste water treatment device - Google Patents

Waste water treatment device

Info

Publication number
JPS6257697A
JPS6257697A JP60195208A JP19520885A JPS6257697A JP S6257697 A JPS6257697 A JP S6257697A JP 60195208 A JP60195208 A JP 60195208A JP 19520885 A JP19520885 A JP 19520885A JP S6257697 A JPS6257697 A JP S6257697A
Authority
JP
Japan
Prior art keywords
tank
anaerobic
treatment
batch
water
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
JP60195208A
Other languages
Japanese (ja)
Inventor
Yoshiaki Arai
喜明 新井
Masao Fujio
藤生 昌男
Keisuke Iwabori
岩堀 恵祐
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.)
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Electric Manufacturing Co Ltd
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 Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Electric Manufacturing Co Ltd
Priority to JP60195208A priority Critical patent/JPS6257697A/en
Publication of JPS6257697A publication Critical patent/JPS6257697A/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
    • C02F3/06Aerobic processes using submerged filters
    • 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

Abstract

PURPOSE:To permit the efficient and inexpensive treatment of high-contg. waste water with a waste water treatment device for dung, etc. by partitioning a hermetic tank to provide an anaerobic tank for an anaerobic treatment and a batch tank for making an aerobic treatment of the anaerobically treated water to said device. CONSTITUTION:The inside of the hermetic tank body 24 is partitioned to provide the anaerobic tank 3 for the anaerobic treatment and the batch tank 7 for making the aerobic treatment of the anaerobically treated water treated in the tank 3. Plural sheets of baffle plates 14-16 are provided toward the upper and lower sides in the tank 3 and filter media 4 for capturing the anaerobic bacteria are disposed in the mid-way of the water flow passages formed by the baffle plates. The filter media 8 are disposed in the tank 7 and an air diffusion pipe 9 is disposed to an air feed pipe 21 introduced into said tank from the outside thereof. More specifically, the high-conc. waste water is efficiently treated at a low cost by ingeniously combining the anaerobic treatment and the aerobic treatment and making use of the respective advantages thereof.

Description

【発明の詳細な説明】 人、産業上の利用分野 本発明は例えば家畜ふん尿等のuト水処理装はに関する
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a system for treating water such as livestock manure.

B1発明の概要 本発明は家畜ふん尿等の排水処理装置において密閉形成
される一つのタンク内を仕切って排水流入側から順に嫌
気性処理用の嫌気槽と、嫌気槽で処理さrt九九嫌気処
理水の好気性処理を行なう回分槽1に設けたことにより
、嫌気性処理と好気性処理をうまく組合せてそれ七nの
利点が生かさ′n1安いコストで高#に度廃水を効率よ
く処理することがで自るようにし九ものである。
B1 Overview of the Invention The present invention is a system for treating wastewater such as livestock manure, etc., in which the inside of one tank that is sealed is partitioned and the wastewater is treated in an anaerobic tank for anaerobic treatment and an anaerobic tank in order from the inflow side.RT99 Anaerobic treatment By installing it in the batch tank 1 that performs aerobic treatment of water, anaerobic treatment and aerobic treatment can be skillfully combined to take advantage of seven advantages. 1. Efficient treatment of high frequency wastewater at low cost. There are nine things you can do to help yourself.

C6従来の技術 家畜ふん尿処塩について、従来は堆肥として農地へ還元
していたが、永畜肱業の規模拡大に伴ない、家畜ふん尿
の諷に比して還元すベキ農地が乏しく、このためそのま
ま河川に放流し、水貝汚濁ノ原囚となっている。この水
質汚濁を防止するために、現在種々の汚水処理技術が開
発され、かつ既に実施さnているが、その中心的技術は
活性汚泥処理方式である。
C6 Conventional technology Regarding the treatment of livestock manure, salt has traditionally been returned to farmland as compost, but as the scale of permanent livestock farming has expanded, there has been less farmland to return salt compared to livestock manure. They are simply released into rivers, becoming a source of water mollusc pollution. In order to prevent this water pollution, various sewage treatment techniques are currently being developed and are already being implemented, the central technology of which is the activated sludge treatment method.

D1発明が解決しようとする問題点 活性汚泥地理方式は廃水に空気を吹込み、微生物を繁殖
させて処理するのであるが、この方式には次の欠点があ
る。■処理施設に要する建設費用は極めて巨額なものと
なっておシ、こnが経済的に大きな負担となっている。
D1 Problems to be Solved by the Invention The activated sludge geological method treats wastewater by blowing air into it and propagating microorganisms, but this method has the following drawbacks. ■The construction costs required for treatment facilities are extremely large, and this is a huge economic burden.

■廃水処理に要する動力量が増加していると共に、要求
される処理の高度化に伴って処理に要する薬品が増加し
ている。■処理に伴って発生する余剰汚泥処理に多くの
施設、人員、費用を必要とする。■大量の希釈水が必要
である。■一定の処理機能を維持するために技術者の常
駐管理が不可欠であシ、投下資本効率の点からも畜産関
連の処理施設向きではない。
■The amount of power required for wastewater treatment is increasing, and the amount of chemicals required for treatment is increasing as the treatment becomes more sophisticated. ■Many facilities, personnel, and costs are required to treat excess sludge generated during treatment. ■A large amount of dilution water is required. ■Resident management by engineers is essential to maintain a certain level of processing function, and it is not suitable for livestock-related processing facilities from the standpoint of invested capital efficiency.

■汚泥の沈降分離が不要となり 沈設檀から流出するバ
ルキング現象を防止するのが難しく、流入した汚水中の
汚濁やV機負が汚泥となって流出する結果となる。
■ Sedimentation and separation of sludge is no longer necessary, making it difficult to prevent the bulking phenomenon that flows out from the sedimentation dam, resulting in the pollution and V-organisms in the inflowing sewage becoming sludge and flowing out.

このようなことから活性汚泥処理方式の種々の変法、改
良が加えられているが、一般的傾向として施設は複雑化
し、m待管理技術が難しくなると同時に多額のエネルギ
ー費用を要する処理法となシ、大きな負担となっている
For this reason, various modifications and improvements have been made to the activated sludge treatment method, but the general trend is that the facilities have become more complex, the management technology has become more difficult, and at the same time the treatment method requires a large amount of energy costs. Yes, it is a huge burden.

本発明は上述の如′a活性汚泥方式の欠点1′4決し九
高A展廃水の生物学的処略裟titt−提供することを
目的とする。
The object of the present invention is to provide a biological treatment method for wastewater that overcomes the drawbacks of the above-mentioned activated sludge system.

E8問題点金牌決する九め0手段 本発明に係る排水処理装置は、密閉式のタンク本体内を
仕切ることによって排水中に含まれる曳岬ψt#L除去
する嫌気性処理用の嫌気槽と、嫌気槽で処理された嫌気
性処理水の好気性処理を行なう回分槽を設け、前記嫌気
槽内には上下方向に向けて複数枚の邪魔板を設けると共
に、邪魔板によって形成される通水路の途中に濾材上配
設し、又回分槽内には濾材と、槽外から導入し上空気送
入管に散気管を配設してなることを特徴とする。
E8 Problem 9th 0 means to decide the gold tile The wastewater treatment device according to the present invention includes an anaerobic tank for anaerobic treatment that removes ψt#L contained in wastewater by partitioning the inside of a closed tank body, and an anaerobic A batch tank is provided to perform aerobic treatment of anaerobically treated water treated in the tank, and a plurality of baffle plates are provided in the vertical direction in the anaerobic tank, and a water passageway formed by the baffle plates is provided with a plurality of baffle plates in the middle. It is characterized in that it is arranged on a filter medium in the batch tank, and the filter medium is introduced into the batch tank from outside the tank, and an aeration pipe is arranged in the upper air feed pipe.

F、実施例 以下本発明を第1図に示す実施例にもとづいて説明する
F. EXAMPLE The present invention will be explained below based on the example shown in FIG.

第1−は全体として密閉さf’L7をタンク形状の排水
処理装置で69、コ弘はそのタンク本体であもタンク本
体コ参内は複数の仕切壁コ0.コ!によって仕切ってあ
シ、3は仕切壁λよとタンク壁とによって形成さnた嫌
気槽、7は仕切壁コ0とタンク壁とによって形成された
回分槽 よけ前記仕蔦 切接20とコ!とによって嫌気槽Jと回分N7との間に
形成さnた一時fA整槽である。
The first one is a tank-shaped wastewater treatment device that is completely sealed f'L7. Ko! 3 is an anaerobic tank formed by the partition wall λ and the tank wall, and 7 is a batch tank formed by the partition wall λ and the tank wall. ! This is a temporary fA tank formed between anaerobic tank J and batch N7.

さらに説明すると、嫌気槽3内において、タンク本体2
μの上下壁から複数枚の邪魔板14A、/!。
To explain further, in the anaerobic tank 3, the tank body 2
Multiple baffle plates 14A from the upper and lower walls of μ, /! .

16が突出して設けてあり、こnにょシ嫌気槽3内にジ
グザグに通水路が形成さnlかっ通水路の途中に位置す
べく邪魔板/44とl!の間に濾材弘を配設している。
16 is provided protrudingly, and a zigzag water passage is formed in the anaerobic tank 3. A baffle plate /44 and l! are provided to be located in the middle of the water passage. A filter medium is placed between them.

濾材弘は嫌気性細菌が捕捉できる材料であればスポンジ
、貝殻、ガラスピーズ等でもよい。また、/3は嫌気性
処理水移流管で、この移流管13を介して嫌気槽3と一
時調整槽!が連通される。
The filter material may be a sponge, shell, glass peas, etc. as long as it is a material that can trap anaerobic bacteria. Also, /3 is an anaerobic treated water transfer pipe, which connects the anaerobic tank 3 and the temporary adjustment tank via this transfer pipe 13! is communicated.

一時調整槽tと回分槽7とは回分ポンプ4とその両端に
設けた通水バイプコぶ、−7t−介して連通している。
The temporary adjustment tank t and the batch tank 7 communicate with each other via the batch pump 4 and water-flowing pipe knobs -7t- provided at both ends of the batch pump 4.

回分槽7内には、タンク本体−lの両側板(紙面の表裏
方向)に取付は九邪魔板itと仕切壁コOとの間に濾材
tが設けであると共にタンク外よシ回分槽7内に空気送
入管コlt−導入してあって、その先端に散気管りを設
けである。
Inside the batch tank 7, a filter material t is installed between the baffle plate IT and the partition wall KO, which is attached to both sides of the tank body (in the direction of the front and back of the page). An air supply pipe is introduced into the interior, and an aeration pipe is provided at the tip of the pipe.

この散気管デは回分槽7の下部に設けてあ)、これから
出た気泡は図中矢印の方向に濾材t’z通過して循環し
、かつ回分槽7のタンク壁上部に設けた空気排出孔2λ
から外方に排出される。さらにコ3は回分槽7の側のタ
ンク壁に設けた排水パイプ、10は排水パイプコJt−
開閉する電磁弁、17は回分槽7内において排水パイプ
JJO内端に近接して設けた邪魔板である。
This air diffuser pipe is installed at the bottom of the batch tank 7), and the air bubbles released from it circulate through the filter material t'z in the direction of the arrow in the figure, and are also circulated through the air discharge pipe installed at the upper part of the tank wall of the batch tank 7. Hole 2λ
is discharged outward from the Further, 3 is a drainage pipe installed on the tank wall on the side of the batch tank 7, and 10 is a drainage pipe.
A solenoid valve 17 that opens and closes is a baffle plate provided in the batch tank 7 close to the inner end of the drain pipe JJO.

さらに、//は排水パイプJJt−介して回分槽7から
の上澄水を流出させる回分処理水槽で、その内部には邪
魔板/lt−配設しである。12は排水口で、これから
回分処理水を排出する。なお、嫌気槽Jと調整1i91
jの上部からはパルプJt、コを有するパイプコタとJ
Ot−導出し、これの先端を発生メタンガス取出しパイ
プ31に接続している。またλは流入水ポンプである。
Further, // is a batch treatment water tank from which supernatant water flows out from the batch tank 7 through a drainage pipe JJt, and a baffle plate /lt is provided inside the tank. 12 is a drain port from which batch-treated water is discharged. In addition, anaerobic tank J and adjustment 1i91
From the top of j, there is a pulp Jt, a pipe with a
The tip of this is connected to the generated methane gas extraction pipe 31. Further, λ is an inflow water pump.

つぎに本発明の詳細な説明する。Next, the present invention will be explained in detail.

まず、畜舎等よシ排出される高濃度廃水の流入水lは流
入水ポンプコによシ嫌気槽Jに流入される。流入水Iは
嫌気槽J内において、邪魔板/ 4(。
First, inflow water l of highly concentrated wastewater discharged from livestock barns, etc. is flowed into an anaerobic tank J by an inflow water pump. The inflow water I is placed in the anaerobic tank J with baffle plates/4 (.

is、itの作用によ9図に矢印で示す流れとなる。こ
の流れによシ流入水lと嫌気槽J内の嫌気性細菌とが反
応しゃすくなシ、流れの途中において濾材lによシ嫌気
性細菌が捕捉される。ま念\鎌気性細菌が濾材参に捕捉
されることによシ鎌気[7外へ流出することが妨げる。
The action of is and it results in the flow shown by the arrow in FIG. This flow prevents the inflow water l from reacting with the anaerobic bacteria in the anaerobic tank J, and the anaerobic bacteria are captured by the filter medium l in the middle of the flow. Remember, sickling bacteria are captured by the filter media, preventing them from flowing out.

こnらのことによシ嫌気性処理効果が大きくなる。These things increase the effect of anaerobic treatment.

しかして1濾材参を通過し之嫌気性処理水は移流管i、
iによシ調整槽!に貯留さルる。貯留された鎌気性処理
水は、回分ポンプ遥によシ回分N7に流入され、この一
つの槽で01気、沈澱、υ導出の三工程を繰返すことに
よシ、好気性処理される。
The anaerobically treated water passes through the filter medium 1, and the anaerobically treated water passes through the advection pipe i,
Iyoshi adjustment tank! It is stored in The stored sickle-treated water is fed into batch N7 by a batch pump, and is subjected to aerobic treatment by repeating the three steps of 01 air, precipitation, and υ derivation in this one tank.

点線の矢印は曝気による水の流れを示す。図から分るよ
うに濾材lに捕捉さnている微生物により好気性処理の
効果が増える。さらに、排水の際に上澄水に浮遊残渣が
多く混入していると、電磁弁10が晶るので、沈澱工程
の時に、1!出弁10の配管付近に浮きかすが残らない
ように前述の邪魔板/7を付けたのである。このように
して好気性処理された回分処理水は、回分処理水槽/l
より外部へ排出される。また、嫌気槽Jと調整槽!で発
生するメタンガスはメタンガス取出しパイプjlを介し
て図示していない貯溜槽へ溜められて燃料。
Dotted arrows indicate water flow due to aeration. As can be seen from the figure, the microorganisms trapped in the filter media increase the effectiveness of the aerobic treatment. Furthermore, if a large amount of floating residue is mixed into the supernatant water during drainage, the solenoid valve 10 will crystallize, so that 1! The aforementioned baffle plate 7 was attached to prevent floating debris from remaining near the outlet valve 10 piping. The batch treated water that has been aerobically treated in this way is stored in a batch treated water tank/l.
is discharged to the outside. Also, anaerobic tank J and adjustment tank! The methane gas generated is stored in a storage tank (not shown) via a methane gas extraction pipe and used as fuel.

発電等に使用される。Used for power generation, etc.

G0発明の効果 以上の通9でありまして、本発明によると次の効果があ
る。■嫌気性処理と好気性処理を組合せたことによ択 
施設面積が小さくてすみ、建設費用が安くてすむ。■す
なわち、厳気性処理は動力のまったくいらない処理方法
でらシ、また、回分式活性汚泥法も、従来の活性汚泥法
よシ動力費用のかからない方式であるからこの従来方式
に比べて大巾に動力費用の削減ができる。■嫌気性処理
、回分式活性汚泥法ともに、汚泥の発生率は低く、余剰
汚泥の発生は少くなる。■希釈水は不要となる。■装置
の保守には嫌気槽では濾材の洗浄と処理程度であシ、回
分槽の運転は、自動運転であるので、簡単な保守で良く
なる。0回分式活性汚泥法においては、汚泥の沈降性は
良く、バルキング現象もない、などの゛効果がある。
G0 Effects of the Invention As stated above, the present invention has the following effects. ■Selectable by combining anaerobic treatment and aerobic treatment
The facility requires a small area and construction costs are low. ■In other words, the strict air treatment is a treatment method that does not require any power, and the batch activated sludge method also requires less power than the conventional activated sludge method, so it is much more efficient than the conventional method. Power costs can be reduced. ■In both anaerobic treatment and batch activated sludge methods, the sludge generation rate is low, and the generation of excess sludge is reduced. ■Dilution water is not required. ■In the case of an anaerobic tank, equipment maintenance is limited to cleaning and processing of the filter media; however, since the operation of the batch tank is automatic, simple maintenance is required. The zero-batch activated sludge method has the following effects: sludge has good settling properties and there is no bulking phenomenon.

面説明図である。FIG.

3・・・嫌気槽、φ、r・・・濾材、7・・・回分槽、
ナ・・・散気管、/ 4c、 / j 、 / 6−・
・邪魔板、−〇、コt・・・仕切壁1,21・・・空気
送入管、コ参・・・タンク本化率 ° I M 1に聞
3... Anaerobic tank, φ, r... Filter medium, 7... Batch tank,
N... air diffuser, / 4c, / j, / 6-.
・Baffle plate, -〇, Kot... Partition walls 1, 21... Air supply pipe, Ko... Tank conversion rate ° I M 1

Claims (1)

【特許請求の範囲】[Claims] 密閉式のタンク本体内を仕切ることによつて嫌気性処理
用の嫌気槽と、嫌気槽で処理された嫌気性処理水の好気
性処理を行なう回分槽を設け、前記嫌気槽内には上下方
向に向けて複数枚の邪魔板を設けると共に、邪魔板によ
つて形成される通水路の途中に嫌気性細菌捕捉用の濾材
を配設し、回分槽内には濾材と、槽外から導入した空気
送入管に散気管を配設してなることを特徴とする排水処
理装置。
An anaerobic tank for anaerobic treatment and a batch tank for aerobic treatment of the anaerobic treated water treated in the anaerobic tank are provided by partitioning the inside of the closed tank body, and the anaerobic tank has a vertical direction. In addition to installing multiple baffle plates toward the water, a filter medium for capturing anaerobic bacteria was placed in the middle of the water passage formed by the baffle plates, and a filter medium was installed inside the batch tank and a filter medium was introduced from outside the tank. A wastewater treatment device characterized by having an air diffuser installed in an air supply pipe.
JP60195208A 1985-09-04 1985-09-04 Waste water treatment device Pending JPS6257697A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60195208A JPS6257697A (en) 1985-09-04 1985-09-04 Waste water treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60195208A JPS6257697A (en) 1985-09-04 1985-09-04 Waste water treatment device

Publications (1)

Publication Number Publication Date
JPS6257697A true JPS6257697A (en) 1987-03-13

Family

ID=16337253

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60195208A Pending JPS6257697A (en) 1985-09-04 1985-09-04 Waste water treatment device

Country Status (1)

Country Link
JP (1) JPS6257697A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02218497A (en) * 1989-02-17 1990-08-31 Ishikawajima Harima Heavy Ind Co Ltd Treatment of waste water
JPH0383698U (en) * 1989-12-08 1991-08-26
JPH03119498U (en) * 1990-03-15 1991-12-10
JPH04102699U (en) * 1991-02-15 1992-09-04 株式会社イナツクス Aeration tank
US5281335A (en) * 1989-07-28 1994-01-25 Eberhard Kuhn Process, installation and reactor for biological treatment of waste water
WO2007115464A1 (en) * 2006-04-11 2007-10-18 Feng Zhao An apparatus for anaerobic treating wastewater
CN100375724C (en) * 2006-05-31 2008-03-19 清华大学 Baffle-board reactor and method for treating sewage by using it

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5711275A (en) * 1980-06-18 1982-01-20 Toray Industries Production of extremely fine fiber containing cloth
JPS58128195A (en) * 1982-01-25 1983-07-30 Kubota Ltd Septic tank of hardly disposable sewage of night soil
JPS6019097A (en) * 1983-07-14 1985-01-31 Kubota Ltd Sewage treating apparatus

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5711275A (en) * 1980-06-18 1982-01-20 Toray Industries Production of extremely fine fiber containing cloth
JPS58128195A (en) * 1982-01-25 1983-07-30 Kubota Ltd Septic tank of hardly disposable sewage of night soil
JPS6019097A (en) * 1983-07-14 1985-01-31 Kubota Ltd Sewage treating apparatus

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02218497A (en) * 1989-02-17 1990-08-31 Ishikawajima Harima Heavy Ind Co Ltd Treatment of waste water
US5281335A (en) * 1989-07-28 1994-01-25 Eberhard Kuhn Process, installation and reactor for biological treatment of waste water
JPH0383698U (en) * 1989-12-08 1991-08-26
JPH03119498U (en) * 1990-03-15 1991-12-10
JPH04102699U (en) * 1991-02-15 1992-09-04 株式会社イナツクス Aeration tank
WO2007115464A1 (en) * 2006-04-11 2007-10-18 Feng Zhao An apparatus for anaerobic treating wastewater
CN100375724C (en) * 2006-05-31 2008-03-19 清华大学 Baffle-board reactor and method for treating sewage by using it

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