JPH08267079A - Sewage treating device - Google Patents

Sewage treating device

Info

Publication number
JPH08267079A
JPH08267079A JP7024695A JP7024695A JPH08267079A JP H08267079 A JPH08267079 A JP H08267079A JP 7024695 A JP7024695 A JP 7024695A JP 7024695 A JP7024695 A JP 7024695A JP H08267079 A JPH08267079 A JP H08267079A
Authority
JP
Japan
Prior art keywords
tank
sewage
sludge
septic
septic tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
JP7024695A
Other languages
Japanese (ja)
Inventor
Shigeyuki Yamaguchi
重行 山口
Etsuro Fujino
悦郎 藤野
Hideto Shinpo
秀人 新保
Akio Kubota
晃生 窪田
Hideaki Yamada
秀昭 山田
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.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works 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 Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP7024695A priority Critical patent/JPH08267079A/en
Publication of JPH08267079A publication Critical patent/JPH08267079A/en
Withdrawn legal-status Critical Current

Links

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

  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE: To prevent the degradation in the quality of purified water without rapidly increasing the volume of the sewage in a septic tank by providing this septic tank with a filter bed stuck with microorganisms and installing a buffer tank packed with fine wooden pieces to the septic tank at the time of subjecting the sewage to a purification treatment with the microorganisms of this filter bed. CONSTITUTION: The sewage 3 is first supplied to a buffer tank 5 by a supply pipe 6 in the case the purification treatment of the sewage 3 is executed. The supplied sewage 3, then, flows down gradually while oozing to a fine wooden pieces 4 and passing the gaps among the fine wooden pieces 4. This sewage is discharged from a drain port 7 into an anaerobic treating vessel 11. The sewage is anaerobically treated by the effect of the anaerobic bacteria sticking to an anaerobic filter bed 13. The sewage flows from an overflow section 17 into an aerobic treating vessel 12 and is then aerobically treated by the aerobic bacteria sticking to an aerobic filter bed 14 and the air supplied from an air diffusion pipe 15. The purified water subjected to the purification treatment is thereafter flows from a communicating section 24 to a settling tank 23 where sludge is precipitated. The treated water is discharged out of an outflow port 16 through a disinfecting vessel 25.

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、汚水を浄化するための
浄水処理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 water purification device for purifying sewage.

【0002】[0002]

【従来の技術】図8には従来から用いられている汚水処
理装置の一例が示してある。1は合併処理槽などと称さ
れる浄化槽であって、浄化槽1の内部は嫌気性処理槽1
1と好気性処理槽12とに分割されている。嫌気性処理
槽11には嫌気性菌によって形成される生物膜が付着し
た嫌気性濾床13と、汚水3を供給するための供給管6
が設けてある。好気性処理槽12には好気性菌によって
形成される生物膜が付着した好気性濾床14と、好気性
処理槽12内に空気を供給するための散気管15と、浄
化処理された水を浄化槽1外に排出するための流出口1
6が設けてある。
2. Description of the Related Art FIG. 8 shows an example of a conventionally used sewage treatment apparatus. Reference numeral 1 is a septic tank called a combined treatment tank, and the inside of the septic tank 1 is an anaerobic treatment tank 1
1 and an aerobic treatment tank 12. The anaerobic treatment tank 11 has an anaerobic filter bed 13 to which a biofilm formed by anaerobic bacteria is attached, and a supply pipe 6 for supplying the sewage 3.
Is provided. The aerobic treatment tank 12 has an aerobic filter bed 14 to which a biofilm formed by aerobic bacteria is attached, an aeration pipe 15 for supplying air into the aerobic treatment tank 12, and purified water. Outlet 1 for discharging to outside of septic tank 1
6 are provided.

【0003】このような汚水処理装置で汚水3の浄化を
おこなうにあたっては、供給管6から嫌気性処理槽11
に汚水3を供給して汚水3を嫌気性菌で嫌気性処理し、
この後オーバーフロー部17を介して汚水3を好気性処
理槽12に流入させて汚水3を好気性菌で好気性処理
し、この後浄化処理された水を流出口16から排出する
ようにすることができる。
In purifying the sewage 3 with such a sewage treatment apparatus, the anaerobic treatment tank 11 is supplied from the supply pipe 6.
Sewage 3 is supplied to the sewage and sewage 3 is anaerobically treated with anaerobic bacteria,
After that, the sewage 3 is allowed to flow into the aerobic treatment tank 12 through the overflow section 17 to aerobically treat the sewage 3 with aerobic bacteria, and then the purified water is discharged from the outlet 16. You can

【0004】[0004]

【発明が解決しようとする課題】しかし上記従来例で
は、供給管6から流入量の変動が著しい汚水を直接嫌気
性処理槽11に流入させるようにしてあるので、嫌気性
処理槽11に流入する汚水の量が急激に増えると、嫌気
性濾床13に付着した嫌気性菌の生物膜が剥離して流出
することがあり、このため嫌気性処理槽11で十分に汚
水3を嫌気性処理することができず、流出口16から排
出される浄化水の水質が低下する恐れがあった。そこで
供給管6にポンプ等を設けて供給管6から流入量を調節
するようなことが試みられているが、構造が複雑になっ
たりコスト高になったりするという問題があった。
However, in the above-mentioned conventional example, since the sewage having a large fluctuation in the inflow amount is directly introduced into the anaerobic treatment tank 11 from the supply pipe 6, it is introduced into the anaerobic treatment tank 11. When the amount of sewage increases sharply, the biofilm of anaerobic bacteria adhering to the anaerobic filter bed 13 may peel off and flow out. Therefore, the sewage 3 is sufficiently anaerobically treated in the anaerobic treatment tank 11. However, the quality of the purified water discharged from the outflow port 16 may be deteriorated. Therefore, it has been attempted to provide a pump or the like on the supply pipe 6 to adjust the inflow amount from the supply pipe 6, but there has been a problem that the structure becomes complicated and the cost becomes high.

【0005】また上記従来例では、嫌気性処理槽11に
汚水3の嫌気性処理によって発生する汚泥18を一定期
間溜め、その後この汚泥18を取り出して焼却処分など
をおこなうようにしていたので、汚泥18を一定期間溜
めるためのスペースを浄化槽1に確保しなければなら
ず、装置を小型化することができないという問題があっ
た。
Further, in the above-mentioned conventional example, the sludge 18 generated by the anaerobic treatment of the sewage 3 is stored in the anaerobic treatment tank 11 for a certain period of time, and then the sludge 18 is taken out for incineration or the like. A space for accumulating 18 for a certain period has to be secured in the septic tank 1, and there is a problem that the device cannot be downsized.

【0006】本発明は上記の点に鑑みてなされたもので
あり、構造が複雑になったりコスト高になったりするこ
となく浄化水の水質の低下を防止することができると共
に、小型化することができる汚水処理装置を提供するこ
とを目的とするものである。
The present invention has been made in view of the above points, and it is possible to prevent the quality of purified water from deteriorating without complicating the structure and increasing the cost, and to reduce the size. An object of the present invention is to provide a sewage treatment apparatus capable of performing the above.

【0007】[0007]

【課題を解決するための手段】本発明に係る汚水処理装
置は、浄化槽1に微生物を付着させた濾床2を設け、浄
化槽1に汚水3を流入させると共に濾床2の微生物で汚
水を浄化処理するようにした汚水処理装置において、浄
化槽1に木質細片4を充填した緩衝槽5を設け、汚水3
を緩衝槽5に供給するための供給管6を浄化槽1に設け
ると共に汚水3を浄化槽1に排出するための排水口7を
緩衝槽5に形成して成ることを特徴とするものである。
In the sewage treatment apparatus according to the present invention, a septic tank 1 is provided with a filter bed 2 on which microorganisms are adhered, the sewage 3 is introduced into the septic tank 1 and the sewage is purified by the microorganisms on the filter bed 2. In the sewage treatment apparatus adapted to treat, the septic tank 1 is provided with a buffer tank 5 filled with wood chips 4, and the sewage 3
Is provided in the septic tank 1, and a drainage port 7 for discharging the sewage 3 to the septic tank 1 is formed in the buffer tank 5.

【0008】また本発明に係る汚水処理装置は、浄化槽
1に微生物を付着させた濾床2を設け、浄化槽1に汚水
3を流入させると共に濾床2の微生物で汚水3を浄化処
理するようにした汚水処理装置において、浄化槽1の汚
水3の水面よりも上方に木質細片4を充填した濾過槽9
を設け、汚水3の浄化処理によって浄化槽1に発生する
汚泥を濾過槽9に移送するための移送管10を浄化槽1
に設けると共に濾過槽9内の汚泥中の水分を浄化槽1に
排出するための排水口7を濾過槽9に形成して成ること
を特徴とするものである。
Further, in the wastewater treatment apparatus according to the present invention, the septic tank 1 is provided with a filter bed 2 on which microorganisms are adhered, and the wastewater 3 is introduced into the septic tank 1 and the microorganisms in the filter bed 2 purify the wastewater 3. In the treated sewage treatment apparatus, the filtration tank 9 in which the wood strips 4 are filled above the surface of the sewage 3 in the septic tank 1
And a transfer pipe 10 for transferring sludge generated in the septic tank 1 to the filtration tank 9 by the purification treatment of the septic water 3 is installed in the septic tank 1
And the drainage port 7 for discharging the water in the sludge in the filtration tank 9 to the purification tank 1 is formed in the filtration tank 9.

【0009】また本発明に係る汚水処理装置は、浄化槽
1に微生物を付着させた濾床2を設け、浄化槽1に汚水
3を流入させると共に濾床2の微生物で汚水3を浄化処
理するようにした汚水処理装置において、浄化槽1に木
質細片4を充填した汚泥処理槽8を設けると共に木質細
片4に汚水3の浄化処理によって浄化槽1に発生する汚
泥を分解する微生物を寄生させ、汚泥を浄化槽1から汚
泥処理槽8に移送するための移送管10を具備して成る
ことを特徴とする汚水処理装置。
Further, in the wastewater treatment apparatus according to the present invention, the septic tank 1 is provided with the filter bed 2 on which microorganisms are adhered, the wastewater 3 is introduced into the septic tank 1, and the microorganisms in the filter bed 2 are used to purify the wastewater 3. In the sewage treatment apparatus described above, the septic tank 1 is provided with the sludge treatment tank 8 filled with the wood strips 4, and the wood strips 4 are caused to parasitize microorganisms that decompose the sludge generated in the septic tank 1 by the purification treatment of the waste water 3 to remove sludge. A sewage treatment apparatus comprising a transfer pipe 10 for transferring from the septic tank 1 to the sludge treatment tank 8.

【0010】[0010]

【作用】浄化槽1に木質細片4を充填した緩衝槽5を設
け、汚水3を緩衝槽5に供給するための供給管6を浄化
槽1に設けると共に汚水3を浄化槽1に排出するための
排水口7を緩衝槽5に形成したので、緩衝槽5に供給管
6から汚水3を供給すると共に緩衝槽5から排水口7を
通じて浄化槽1に汚水3を供給することによって、緩衝
槽5に供給された汚水3は、木質細片4による通水抵抗
を受けて緩衝槽5内を徐々に流れた後、排水口7から浄
化槽1に排出されることになり、従って供給管6から直
接浄化槽に汚水3を供給するよりも浄化槽1内の汚水3
の量を急激に増加させないようにすることができる。
Function: The septic tank 1 is provided with the buffer tank 5 filled with the wooden strips 4, the supply pipe 6 for supplying the dirty water 3 to the buffer tank 5 is provided in the septic tank 1, and the drainage for discharging the dirty water 3 to the septic tank 1 is provided. Since the mouth 7 is formed in the buffer tank 5, the waste water 3 is supplied to the buffer tank 5 by supplying the waste water 3 from the supply pipe 6 to the buffer tank 5 and the waste water 3 from the buffer tank 5 to the septic tank 1 through the drainage port 7. The sewage 3 which has been subjected to water resistance due to the wood strips 4 gradually flows through the buffer tank 5 and is then discharged from the drainage port 7 to the septic tank 1. Therefore, the sewage 3 is directly supplied from the supply pipe 6 to the septic tank. Sewage 3 in septic tank 1 rather than supplying 3
The amount of can be prevented from increasing rapidly.

【0011】また浄化槽1の汚水3の水面よりも上方に
木質細片4を充填した濾過槽9を設け、汚水3の浄化処
理によって浄化槽1に発生する汚泥を濾過槽9に移送す
るための移送管10を浄化槽1に設けると共に濾過槽9
内の汚泥中の水分を浄化槽1に排出するための排水口7
を濾過槽9に形成したので、汚泥中に含まれる水分を木
質細片4で濾過して濾過槽9に汚泥の固形分を捕捉して
濃縮して減量することができると共に、排水口7から汚
泥中の水分を排出することができる。
Further, a filtration tank 9 filled with wood chips 4 is provided above the surface of the wastewater 3 in the septic tank 1, and the sludge generated in the septic tank 1 by the purification treatment of the wastewater 3 is transferred to the filtration tank 9. The pipe 10 is provided in the septic tank 1 and the filtration tank 9 is provided.
Drainage port 7 for discharging the water in the sludge inside to the septic tank 1
Since it is formed in the filter tank 9, the water contained in the sludge can be filtered by the wood strips 4 to capture the solid content of the sludge in the filter tank 9 to condense and reduce the volume, and also from the drain port 7. Water in sludge can be discharged.

【0012】また浄化槽1に木質細片4を充填した汚泥
処理槽8を設けると共に木質細片4に汚水3の浄化処理
によって浄化槽1に発生する汚泥を分解する微生物を寄
生させ、汚泥を浄化槽1から汚泥処理槽8に移送するた
めの移送管10を具備したので、木質細片4に寄生した
微生物によって汚泥を分解処理して汚泥を減量すること
ができる。
Further, the sludge treatment tank 8 filled with the wood strips 4 is provided in the septic tank 1, and the wood strips 4 are made to parasitize microorganisms which decompose sludge generated in the septic tank 1 by the purifying process of the wastewater 3 to sludge the septic tank 1 Since the transfer pipe 10 for transferring the sludge to the sludge treatment tank 8 is provided, the sludge can be decomposed by the microorganisms parasitic on the wood strips 4 to reduce the sludge.

【0013】[0013]

【実施例】以下本発明を実施例によって詳述する。図1
には本発明の一実施例が示してある。1は合併処理槽な
どと称される浄化槽であって、浄化槽1の内部は仕切り
板21と分割板22によって嫌気性処理槽11と好気性
処理槽12と沈澱槽23に分割されている。嫌気性処理
槽11と好気性処理槽12の各上面には点検口26を設
けてある。嫌気性処理槽11には嫌気性菌によって形成
される生物膜が付着した濾床2としての嫌気性濾床13
と、汚水3を供給するための供給管6と、嫌気性処理槽
11と好気性処理槽12とを連通させるオーバーフロー
部17が設けてある。好気性処理槽12には好気性菌に
よって形成される生物膜が付着した濾床2としての好気
性濾床14と、好気性処理槽12内に空気を供給するた
めの散気管15が設けてある。また好気性処理槽12に
は汚水3の好気性処理で発生する汚泥や沈澱槽23で沈
澱する汚泥を嫌気性処理槽11に搬送するための搬送管
25が設けてある。
EXAMPLES The present invention will be described in detail below with reference to examples. FIG.
Shows an embodiment of the present invention. Reference numeral 1 denotes a septic tank called a combined treatment tank, and the inside of the septic tank 1 is divided by a partition plate 21 and a dividing plate 22 into an anaerobic treatment tank 11, an aerobic treatment tank 12, and a precipitation tank 23. An inspection port 26 is provided on each upper surface of the anaerobic treatment tank 11 and the aerobic treatment tank 12. The anaerobic treatment tank 11 has an anaerobic filter bed 13 as a filter bed 2 to which a biofilm formed by anaerobic bacteria is attached.
A supply pipe 6 for supplying the sewage 3 and an overflow section 17 for connecting the anaerobic treatment tank 11 and the aerobic treatment tank 12 are provided. The aerobic treatment tank 12 is provided with an aerobic filter bed 14 as a filter bed 2 to which a biofilm formed by aerobic bacteria is attached, and an air diffuser pipe 15 for supplying air into the aerobic treatment tank 12. is there. Further, the aerobic treatment tank 12 is provided with a transport pipe 25 for transporting sludge generated in the aerobic treatment of the wastewater 3 and sludge settled in the settling tank 23 to the anaerobic treatment tank 11.

【0014】沈澱槽23は嫌気性処理槽11と好気性処
理槽12で浄化処理された浄化水に含まれる汚泥を沈澱
させるための槽であって、沈澱槽23の下部を連通部2
4として開口させて好気性処理槽12と沈澱槽23を連
通させてある。また沈澱槽23には嫌気性処理槽11と
好気性処理槽12で浄化処理された浄化水を消毒するた
めの消毒槽25と、消毒槽25に接続され浄化処理され
た水を浄化槽1外に排出するための流出口16が設けて
ある。
The settling tank 23 is a tank for precipitating sludge contained in the purified water purified by the anaerobic treatment tank 11 and the aerobic treatment tank 12.
4, the aerobic treatment tank 12 and the precipitation tank 23 are communicated with each other. In the settling tank 23, a disinfection tank 25 for disinfecting the purified water purified by the anaerobic treatment tank 11 and the aerobic treatment tank 12, and water purified by being connected to the disinfection tank 25 to the outside of the purification tank 1. An outlet 16 is provided for discharging.

【0015】嫌気性処理槽11において、槽内の汚水3
の水面と供給管6の間には緩衝槽5が着脱自在に配設し
てある。緩衝槽5は上面が開口し容積が40〜50リッ
トルの箱で形成されるものであり、その側面及び底面に
は多数の排水口7が設けてあると共に緩衝槽5には木質
細片(おがくず)4が充填してある。このように形成さ
れる汚水処理装置で汚水3の浄化処理をおこなうにあた
っては、先ず供給管6より緩衝槽5に汚水3が供給され
る。緩衝槽5に供給された汚水3は木質細片4にしみ込
んだり木質細片4の間隙を通ったりして徐々に流下し、
排水口7から嫌気性処理槽11に排出される。この後汚
水3は嫌気性処理槽11で嫌気性濾床13に付着した嫌
気性菌の作用で嫌気性処理を受けて浄化される。この後
汚水3はオーバーフロー部17からオーバーフローにて
嫌気性処理槽11から好気性処理槽12へと流入する。
そして汚水3は好気性処理槽12で好気性濾床14に付
着した好気性菌と散気管15から汚水3に供給される空
気とで好気性処理(曝気処理)されて浄化される。この
後嫌気性処理槽11と好気性処理槽12で浄化処理され
た浄化水は連通部24から沈澱槽23に流入してここで
汚泥を沈澱させ、消毒槽25を通って流出口16から浄
化槽1外に排出される。
In the anaerobic treatment tank 11, wastewater 3 in the tank
A buffer tank 5 is removably arranged between the water surface of and the supply pipe 6. The buffer tank 5 is formed of a box having an open top surface and a volume of 40 to 50 liters. The buffer tank 5 is provided with a large number of drainage ports 7 on its side surface and bottom surface, and the buffer tank 5 has wood chips (sawdust). ) 4 is filled. In purifying the sewage 3 with the sewage treatment apparatus thus formed, the sewage 3 is first supplied from the supply pipe 6 to the buffer tank 5. The sewage 3 supplied to the buffer tank 5 permeates the wood strips 4 or passes through the gaps between the wood strips 4 and gradually flows down,
It is discharged from the drainage port 7 to the anaerobic treatment tank 11. After this, the sewage 3 is subjected to anaerobic treatment in the anaerobic treatment tank 11 by the action of anaerobic bacteria adhering to the anaerobic filter bed 13 to be purified. After that, the sewage 3 flows from the anaerobic treatment tank 11 into the aerobic treatment tank 12 by overflow from the overflow section 17.
Then, the sewage 3 is purified in the aerobic treatment tank 12 by aerobic treatment (aeration treatment) with aerobic bacteria adhering to the aerobic filter bed 14 and air supplied from the air diffuser 15 to the sewage 3. After that, the purified water purified by the anaerobic treatment tank 11 and the aerobic treatment tank 12 flows into the settling tank 23 from the communicating portion 24 to cause sludge to settle there, passes through the disinfection tank 25, and flows from the outlet 16 to the purification tank. 1 is discharged to the outside.

【0016】上記実施例では供給管6から緩衝槽5に汚
水3を供給したので、汚水3は木質細片4の通水抵抗を
受けてゆっくりと緩衝槽5内を流下して嫌気性処理槽1
1に排出されることになり、供給管6を通過してくる単
位時間当たりの汚水3の量に比べて嫌気性処理槽11に
供給される汚水3の量を小さくすることができ、嫌気性
処理槽11内の汚水3の量が急激に増加しないようにす
ることができる。従って嫌気性濾床13に付着した微生
物膜が剥離して流出しないようにすることができ、また
供給管6からの汚水が嫌気性処理を受けず、オーバーフ
ロー部17から好気性処理槽12へと流れる、所謂短絡
流の発生を防止することができる。
In the above embodiment, the sewage water 3 was supplied from the supply pipe 6 to the buffer tank 5, so that the sewage water 3 slowly passed through the buffer tank 5 due to the resistance of the wood strips 4 to pass through the anaerobic treatment tank. 1
Therefore, the amount of the sewage 3 supplied to the anaerobic treatment tank 11 can be made smaller than the amount of the sewage 3 per unit time passing through the supply pipe 6, and the anaerobic property can be reduced. It is possible to prevent the amount of the dirty water 3 in the processing tank 11 from rapidly increasing. Therefore, the microbial film attached to the anaerobic filter bed 13 can be prevented from separating and flowing out, and the sewage from the supply pipe 6 is not subjected to anaerobic treatment, and the overflow portion 17 is transferred to the aerobic treatment tank 12. It is possible to prevent a so-called short-circuit flow that flows.

【0017】図2には他の実施例が示してある。この実
施例では嫌気性処理槽11において、槽内の汚水3の水
面の上方に濾過槽9が配設してある。濾過槽9は上面が
開口し容積が40〜50リットルの箱で形成されるもの
であり、その側面及び底面には多数の排水口7が設けて
あると共に濾過槽9には木質細片(おがくず)4が充填
してある。
FIG. 2 shows another embodiment. In this embodiment, in the anaerobic treatment tank 11, the filtration tank 9 is arranged above the water surface of the dirty water 3 in the tank. The filtration tank 9 is formed of a box having an upper surface opened and a volume of 40 to 50 liters, and a large number of drainage ports 7 are provided on the side surface and the bottom surface thereof. ) 4 is filled.

【0018】また嫌気性処理槽11には、汚水3の嫌気
性処理で発生する汚泥を濾過槽9にまで搬送する移送管
10としての嫌気性汚泥移送管10aが配設してあっ
て、嫌気性汚泥移送管10aは下端を嫌気性処理槽11
の下部で、上端を濾過槽9の上方でそれぞれ開口させて
ある。また好気性処理槽12には汚水3の好気性処理で
発生する汚泥を濾過槽9にまで搬送する移送管10とし
ての好気性汚泥移送管10bが配設してあって、好気性
汚泥移送管10bは下端を好気性処理槽12の下部で、
上端を濾過槽9の上方でそれぞれ開口させてある。各移
送管10にはエアーリフトなどのポンプが設けてあっ
て、このポンプで汚泥を嫌気性処理槽11や好気性処理
槽12から濾過槽9へと定期的(6か月に1度程度)に
移送するようにしてある。
Further, the anaerobic treatment tank 11 is provided with an anaerobic sludge transfer pipe 10a as a transfer pipe 10 for conveying the sludge generated by the anaerobic treatment of the wastewater 3 to the filtration tank 9. The sludge transfer pipe 10a has an anaerobic treatment tank 11 at the lower end.
And the upper end is opened above the filter tank 9. Further, the aerobic sludge transfer pipe 10b is provided in the aerobic treatment tank 12 as a transfer pipe 10 for transporting sludge generated by the aerobic treatment of the wastewater 3 to the filtration tank 9, and the aerobic sludge transfer pipe is provided. 10b is the lower end of the lower part of the aerobic treatment tank 12,
The upper ends are opened above the filtration tank 9. Each transfer pipe 10 is provided with a pump such as an air lift, and sludge is periodically (about once every 6 months) from the anaerobic treatment tank 11 or the aerobic treatment tank 12 to the filtration tank 9 by this pump. It is transferred to.

【0019】このように形成される汚水処理装置で汚水
3の浄化処理をおこなうにあたっては、供給管6より嫌
気性処理槽11に汚水3が直接供給された後、上記実施
例と同様にして汚水3は嫌気性処理槽11で嫌気性処理
され、好気性処理槽12で好気性処理され、沈澱槽2
3、消毒槽25を通って流出口16から浄化槽1外に流
出される。また汚水処理装置では汚水3を嫌気性処理槽
11で嫌気性処理することによって発生する汚泥を嫌気
性汚泥移送管10aで汲み上げて濾過槽9に排出すると
共に、汚水3を好気性処理槽12で好気性処理すること
によって発生する汚泥を好気性汚泥移送管10bで汲み
上げて濾過槽9に排出するようにしてある。そして汲み
上げられた汚泥は木質細片4で濾過されて汚泥中の固形
分のみが濾過槽9内に残り、汚泥中の水分は排水口7を
通じて嫌気性処理槽11に排出される。
In purifying the sewage 3 with the sewage treatment apparatus thus formed, after the sewage 3 is directly supplied from the supply pipe 6 to the anaerobic treatment tank 11, the sewage is treated in the same manner as in the above embodiment. 3 is anaerobically treated in the anaerobic treatment tank 11, and aerobically treated in the aerobic treatment tank 12, and the precipitation tank 2
3. Outflow from the outlet 16 through the disinfection tank 25 to the outside of the septic tank 1. In the sewage treatment apparatus, sludge generated by anaerobic treatment of the sewage 3 in the anaerobic treatment tank 11 is pumped up by the anaerobic sludge transfer pipe 10a and discharged into the filtration tank 9, and the sewage 3 is treated in the aerobic treatment tank 12 by the aerobic treatment tank 12. Sludge generated by the aerobic treatment is pumped up by the aerobic sludge transfer pipe 10b and discharged to the filtration tank 9. The sludge pumped up is filtered by the wood strips 4, only the solid content in the sludge remains in the filtration tank 9, and the water content in the sludge is discharged to the anaerobic treatment tank 11 through the drainage port 7.

【0020】上記実施例では嫌気性処理槽11で発生す
る汚泥を嫌気性汚泥移送管10aで汲み上げて濾過槽9
に排出すると共に汚水3を好気性処理槽12で発生する
汚泥を好気性汚泥移送管10bで汲み上げては濾過槽9
に排出するようにしたので、汚泥に90wt%以上含ま
れる水分を木質細片4で濾過することによって、汚泥の
脱水、濃縮を簡単におこなうことができ、従って嫌気性
処理槽11や好気性処理槽12に汚泥を溜めておくスペ
ースを確保する必要がなくなる。また濾過槽9で濃縮さ
れた汚泥は一定期間(6か月程度)でコンポスト化され
て堆肥としても利用することができる。尚、木質細片4
に微生物を寄生させて濾過槽9に残った固形分を微生物
で水とガスにまで分解処理するようにしてもよい。
In the above-described embodiment, the sludge generated in the anaerobic treatment tank 11 is pumped up by the anaerobic sludge transfer pipe 10a to be filtered in the filtration tank 9.
The sludge generated in the aerobic treatment tank 12 is pumped up by the aerobic sludge transfer pipe 10b and the filtration tank 9 is discharged.
The sludge can be dehydrated and concentrated easily by filtering the water contained in the sludge in an amount of 90 wt% or more with the wood strips 4, so that the anaerobic treatment tank 11 and the aerobic treatment can be performed. It is not necessary to secure a space for storing sludge in the tank 12. The sludge concentrated in the filtration tank 9 can be composted in a certain period (about 6 months) and used as compost. In addition, wood strip 4
Alternatively, the solid content remaining in the filtration tank 9 may be decomposed into water and gas by the microorganisms.

【0021】図3には本発明のさらに他の実施例が示し
てある。この実施例では上記実施例の緩衝槽5と濾過槽
9の両方の機能を持つ木質細片充填槽30が槽内の汚水
3の水面と供給管6の間に設けてあり、木質細片充填槽
30には木質細片(おがくず)4が充填してある。また
嫌気性処理槽11と好気性処理槽12には上記実施例と
同様な嫌気性汚泥移送管10aと好気性汚泥移送管10
bをそれぞれ設けてある。
FIG. 3 shows another embodiment of the present invention. In this embodiment, a wood debris filling tank 30 having both the functions of the buffer tank 5 and the filtration tank 9 of the above embodiment is provided between the water surface of the sewage 3 in the tank and the supply pipe 6 to fill the wood debris. The tank 30 is filled with wood chips (sawdust) 4. Further, in the anaerobic treatment tank 11 and the aerobic treatment tank 12, the same anaerobic sludge transfer pipe 10a and aerobic sludge transfer pipe 10 as in the above-described embodiment are used.
b are provided respectively.

【0022】この実施例では木質細片充填槽30で上記
緩衝槽5と濾過槽9の両方の働きをおこなわせることが
できる。図4には本発明のさらに他の実施例が示してあ
る。この実施例では図2に示す実施例の濾過槽9に、回
転軸31の周囲に複数枚の攪拌刃32を設けて形成され
る攪拌装置20を回転自在に設けて形成してあると共に
木質細片4に汚泥を分解処理する微生物を寄生させて形
成してある。このものでは攪拌装置20を用いて木質細
片4と汚泥と混合攪拌して両者の接触を高めることがで
きると共に混合物への空気の取り入れを十分に行うこと
ができ、汚泥の分解処理を効率を高めることができる。
In this embodiment, the wood debris filling tank 30 can function as both the buffer tank 5 and the filtration tank 9. FIG. 4 shows still another embodiment of the present invention. In this embodiment, a stirring device 20 formed by providing a plurality of stirring blades 32 around a rotating shaft 31 is rotatably provided in the filtration tank 9 of the embodiment shown in FIG. The piece 4 is formed by allowing a microorganism that decomposes sludge to parasitize. In this one, the agitator 20 can be used to mix and stir the wood chips 4 and the sludge to enhance the contact between them, and at the same time, the air can be sufficiently taken into the mixture, so that the sludge can be decomposed efficiently. Can be increased.

【0023】図5にはさらに他の実施例が示してある。
この実施例では浄化槽1に隣接させて汚泥処理槽8を設
けて形成してある。図6に示すように浄化槽1は上面が
開口し、内部には外面に多数の孔を設けた散気管15が
配設してあって、散気管15よりも上側を好気性菌で形
成される生物膜が付着した好気性濾床14を設けた好気
性処理槽12として形成してあり、また散気管15より
も下側を嫌気性処理槽11として形成してある。この散
気管15は接続管48を介してエアーブロワー等で形成
されるポンプ47と接続してある。23は分割板22に
よって好気性処理槽12と仕切られて形成される沈澱槽
であって、沈澱槽23の底部は連通部24で嫌気性処理
槽11に連通させてある。50はエアーリフト等で形成
されるポンプであって、移送管10の途中に設けてあ
り、移送管10の下端は嫌気性処理槽11の下部で開口
させてある。
FIG. 5 shows still another embodiment.
In this embodiment, a sludge treatment tank 8 is formed adjacent to the septic tank 1. As shown in FIG. 6, the septic tank 1 has an upper surface opened, and an air diffuser 15 having a large number of holes on the outer surface is disposed inside, and the upper side of the air diffuser 15 is formed of aerobic bacteria. It is formed as an aerobic treatment tank 12 provided with an aerobic filter bed 14 to which a biofilm is attached, and below the diffuser pipe 15 is formed as an anaerobic treatment tank 11. The air diffuser 15 is connected to a pump 47 formed of an air blower or the like via a connecting pipe 48. Reference numeral 23 is a precipitation tank formed by being divided from the aerobic treatment tank 12 by a dividing plate 22, and the bottom of the precipitation tank 23 is communicated with the anaerobic treatment tank 11 by a communication portion 24. A pump 50 formed by an air lift or the like is provided in the middle of the transfer pipe 10, and the lower end of the transfer pipe 10 is opened at the lower part of the anaerobic treatment tank 11.

【0024】このような浄化槽1で汚水3の浄化処理を
おこなうにあたっては、先ず浄化槽1の上面開口から矢
印イで示すように汚水3を供給する。次にポンプ47を
作動させて接続管48を介して散気管15に空気を送
り、散気管15から好気性処理槽12中の汚水3に気泡
状の空気を放出する。ここで汚水3は好気性濾床14に
付着する好気性菌と散気管15から供給される空気とで
曝気処理される。次に曝気処理された汚水3は嫌気性処
理槽11に流入して、ここで汚水は嫌気性処理され、汚
泥が分解処理される。その後汚水3は沈澱槽23に流入
して汚水3中に含まれる汚泥を沈澱させ、上澄み液を矢
印ロで示すように浄化槽1外に排出される。尚、汚水3
を好気性処理槽12と嫌気性処理槽11で往復させるよ
うにしてもよく、このことで汚水3を繰り返し好気性処
理したり嫌気性処理したりすることができる。
In purifying the sewage 3 in the septic tank 1, the sewage 3 is first supplied from the top opening of the septic tank 1 as shown by the arrow a. Next, the pump 47 is operated to send air to the air diffuser pipe 15 via the connecting pipe 48, and bubble air is discharged from the air diffuser pipe 15 to the dirty water 3 in the aerobic treatment tank 12. Here, the sewage 3 is aerated with aerobic bacteria adhering to the aerobic filter bed 14 and the air supplied from the air diffuser 15. Next, the aeration-treated wastewater 3 flows into the anaerobic treatment tank 11, where the wastewater is anaerobically treated and sludge is decomposed. After that, the sewage 3 flows into the settling tank 23 to precipitate the sludge contained in the sewage 3, and the supernatant liquid is discharged to the outside of the septic tank 1 as shown by the arrow B. In addition, dirty water 3
May be made to reciprocate between the aerobic treatment tank 12 and the anaerobic treatment tank 11, whereby the sewage 3 can be repeatedly subjected to aerobic treatment or anaerobic treatment.

【0025】上記のように汚水3の嫌気性処理と好気性
処理及び沈澱槽23での汚泥の沈澱をおこなうと、嫌気
性処理槽11に重いSS成分や濾床14から剥離する生
物膜が汚泥18として沈澱するが、この汚泥18はポン
プ50を作動させて移送管10を通して汲み上げられ
る。そして汲み上げられた汚泥18は生ごみ処理装置や
汚泥処理槽8へと送られて分解処理される。
When the anaerobic treatment and the aerobic treatment of the sewage 3 and the sludge settling in the settling tank 23 are performed as described above, heavy SS components in the anaerobic treatment tank 11 and biofilms peeled from the filter bed 14 are sludge. The sludge 18 precipitates as 18, but the sludge 18 is pumped through the transfer pipe 10 by operating the pump 50. Then, the sludge 18 pumped up is sent to the garbage treatment device or the sludge treatment tank 8 and decomposed.

【0026】従来よりおこなわれている汚水の好気性処
理方法では、浄化処理効率が高い反面、汚泥(余剰汚
泥)の発生量が多く、汚泥の管理、処理、処分が大きな
問題となっていた。また従来よりおこなわれている汚水
の嫌気性処理方法では、動力費が少なく、固形の有機物
の可溶化、汚泥の発生量が少ないなどの利点があるが、
反面、反応速度が遅い、悪臭が発生する等の問題があっ
た。さらに従来では嫌気性処理された汚水中に含まれる
アンモニア性窒素を好気性処理して亜硝酸性窒素や硝酸
性窒素に酸化し、さらに好気性処理槽の脱窒素菌でN2
にまで分解することがおこなわれているが、これをおこ
なうためには嫌気性処理槽で処理された汚水を再び好気
性処理槽に返送しなければならず、返送管等が必要とな
ったり、或いは一つの反応槽で上記工程をおこなおうと
すれば、間欠曝気運転が必要であり、制御機構が複雑に
なるという問題があった。
In the conventional aerobic treatment method of sewage, although the purification efficiency is high, the amount of sludge (excess sludge) is large, and the management, treatment and disposal of sludge have become major problems. In addition, the conventional anaerobic treatment method for wastewater has advantages such as low power cost, solubilization of solid organic matter, and small amount of sludge generation.
On the other hand, there were problems such as a slow reaction rate and generation of a foul odor. Further, conventionally, the ammonia nitrogen contained in the anaerobic-treated wastewater is aerobically treated to be oxidized to nitrite nitrogen or nitrate nitrogen, and further N 2 is deoxidized by the denitrifying bacteria in the aerobic treatment tank.
However, in order to do this, the sewage treated in the anaerobic treatment tank must be returned to the aerobic treatment tank again, and a return pipe is required. Alternatively, if the above process is carried out in one reaction tank, there is a problem that intermittent aeration operation is required and the control mechanism becomes complicated.

【0027】しかし本実施例の浄化槽1では、一つの浄
化槽1に好気性処理槽12と嫌気性処理槽11を混在さ
せてあるので、汚水3に好気性処理と嫌気性処理の両方
をおこなうことができ、汚泥の発生を少なくすることが
できると共に、好気性処理の後に嫌気性処理をおこなう
ことによって汚水3に脱窒素反応を施すことができ、汚
水3中の窒素除去を容易に行うことができる。また汚水
を返送するための返送管等が必要でなくなり、また間欠
曝気運転が必要でなくなって制御機構が複雑になるとい
うこともない。尚、図7に示すようにこの浄化槽1は二
基並設して用いてもよい。
However, in the septic tank 1 of the present embodiment, the aerobic treatment tank 12 and the anaerobic treatment tank 11 are mixed in one septic tank 1, so that both the aerobic treatment and the anaerobic treatment should be performed on the wastewater 3. It is possible to reduce the generation of sludge, and by performing anaerobic treatment after aerobic treatment, the sewage 3 can be subjected to a denitrification reaction, and nitrogen in the sewage 3 can be easily removed. it can. In addition, there is no need for a return pipe or the like for returning sewage, and there is no need for intermittent aeration operation and the control mechanism is not complicated. As shown in FIG. 7, two septic tanks 1 may be installed side by side.

【0028】本実施例では上記浄化槽1の側方に汚泥処
理槽8が設けてある。汚泥処理槽8には木質細片4が充
填されていると共に回転軸31の周囲に複数枚の攪拌翌
32を設けた攪拌装置20が配設してある。攪拌装置2
0はその下に配設されるモーター40で回転駆動され
る。即ちモーター40の回転軸に設けた主動プーリー4
3と、攪拌装置20の回転軸31に設けた従動プーリー
42とをベルト41で連結し、モーター43の駆動を主
動プーリー43と従動プーリー42と、ベルト41を介
して伝えるようにしてある。44はファンであって排気
口46から汚泥の処理で発生するガスを放出するように
してある。
In this embodiment, a sludge treatment tank 8 is provided beside the septic tank 1. The sludge treatment tank 8 is filled with the wood strips 4, and a stirring device 20 having a plurality of stirring stages 32 provided around the rotating shaft 31 is disposed. Stirrer 2
0 is rotationally driven by a motor 40 arranged below it. That is, the driving pulley 4 provided on the rotation shaft of the motor 40
3 and a driven pulley 42 provided on the rotary shaft 31 of the stirring device 20 are connected by a belt 41, and the drive of the motor 43 is transmitted via the driven pulley 43, the driven pulley 42, and the belt 41. Reference numeral 44 denotes a fan, which discharges gas generated by sludge treatment from an exhaust port 46.

【0029】この実施例では浄化槽1で発生する汚泥1
8をポンプ50で汲み上げて移送管10で汚泥処理槽8
に搬送するようにしてある。そして汚泥18は木質細片
4に寄生する微生物でガスと水とに分解処理させるもの
である。このように本実施例では、木質細片4に寄生し
た微生物によって汚泥を分解処理して汚泥18を減量す
ることができ、浄化槽1に汚泥を溜めるためのスペース
を確保する必要がなくなって小型化することができるも
のである。また汚泥を自己完結的に処理して汚泥処理槽
8外に出さないようにすることができる。
In this embodiment, sludge 1 generated in the septic tank 1
8 is pumped up by the pump 50 and the sludge treatment tank 8 is transferred by the transfer pipe 10.
It is designed to be transported to. The sludge 18 is decomposed into gas and water by microorganisms parasitic on the wood chips 4. As described above, in the present embodiment, the sludge can be decomposed by the microorganisms parasitic on the wood chips 4 to reduce the amount of the sludge 18, and it is not necessary to secure a space for accumulating the sludge in the septic tank 1 and the size can be reduced. Is what you can do. Further, it is possible to treat the sludge in a self-contained manner so as not to be discharged outside the sludge treatment tank 8.

【0030】[0030]

【発明の効果】上記のように本発明は、浄化槽に木質細
片を充填した緩衝槽を設け、汚水を緩衝槽に供給するた
めの供給管を浄化槽に設けると共に汚水を浄化槽に排出
するための排水口を緩衝槽に形成したので、緩衝槽に供
給管から汚水を供給すると共に緩衝槽から排水口を通じ
て浄化槽に汚水を供給することによって、緩衝槽に供給
された汚水は、木質細片による通水抵抗を受けて緩衝槽
内を徐々に流れた後、排水口から浄化槽に排出されるこ
とになり、従って供給管から直接浄化槽に汚水を供給す
るよりも浄化槽内の汚水の量を急激に増加させないよう
にすることができ、構造が複雑になったりコスト高にな
ったりすることなく浄化水の水質の低下を防止すること
ができるものである。
As described above, according to the present invention, the septic tank is provided with the buffer tank filled with the wood chips, the supply pipe for supplying the waste water to the buffer tank is provided in the septic tank, and the waste water is discharged to the septic tank. Since the drainage port was formed in the buffer tank, by supplying the wastewater from the supply pipe to the buffer tank and supplying the wastewater from the buffer tank to the septic tank through the drainage port, the wastewater supplied to the buffer tank is passed by the wood strips. After gradually flowing in the buffer tank due to water resistance, it will be discharged to the septic tank from the drain port, so the amount of wastewater in the septic tank will increase rapidly compared to directly supplying wastewater to the septic tank from the supply pipe. It is possible to prevent the deterioration of the quality of the purified water without complicating the structure and increasing the cost.

【0031】また浄化槽の汚水の水面よりも上方に木質
細片を充填した濾過槽を設け、汚水の浄化処理によって
浄化槽に発生する汚泥を濾過槽に移送するための移送管
を浄化槽に設けると共に濾過槽内の汚泥中の水分を浄化
槽に排出するための排水口を濾過槽に形成したので、汚
泥中に含まれる水分を木質細片で濾過することができ、
汚泥を濃縮して減量することができ、浄化槽に汚泥を溜
めるためのスペースを確保する必要がなくなって小型化
することができるものである。
Further, a filter tank filled with wood chips is provided above the surface of the wastewater in the septic tank, and a transfer pipe for transferring sludge generated in the septic tank to the filter tank by the purification treatment of the wastewater is provided in the septic tank and filtered. Since the drainage port for discharging the water in the sludge in the tank to the septic tank is formed in the filter tank, the water contained in the sludge can be filtered with wood strips,
The sludge can be concentrated and reduced in volume, and it is not necessary to secure a space for accumulating the sludge in the septic tank, and the size can be reduced.

【0032】また浄化槽に木質細片を充填した汚泥処理
槽を設けると共に木質細片に汚水の浄化処理によって浄
化槽に発生する汚泥を分解する微生物を寄生させ、汚泥
を浄化槽から汚泥処理槽に移送するための移送管を具備
したので、木質細片に寄生した微生物によって汚泥を分
解処理して汚泥を減量することができ、浄化槽に汚泥を
溜めるためのスペースを確保する必要がなくなって小型
化することができるものである。
Further, a sludge treatment tank filled with wood debris is provided in the septic tank, and the wood debris is transferred from the septic tank to the sludge treatment tank by causing the microorganisms that decompose the sludge generated in the septic tank by the purification treatment of the waste water to parasitize. Since it is equipped with a transfer pipe for reducing the amount of sludge by decomposing sludge with microorganisms parasitic on wood chips, it is not necessary to secure a space for accumulating sludge in the septic tank and downsizing. Is something that can be done.

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

【図1】本発明の一実施例を示す断面図である。FIG. 1 is a sectional view showing an embodiment of the present invention.

【図2】同上の他の実施例を示す断面図である。FIG. 2 is a sectional view showing another embodiment of the above.

【図3】(a)は同上のさらに他の実施例を示す側面断
面図、(b)は上面断面図である。
3A is a side sectional view showing still another embodiment of the same, and FIG. 3B is a top sectional view.

【図4】同上のさらに他の実施例を示す断面図である。FIG. 4 is a sectional view showing still another embodiment of the above.

【図5】同上のさらに他の実施例を示す断面図である。FIG. 5 is a sectional view showing still another embodiment of the above.

【図6】同上の図5に用いる浄化槽を示す断面図であ
る。
FIG. 6 is a cross-sectional view showing the septic tank used in FIG. 5 above.

【図7】同上の浄化槽の他の実施例を示す断面図であ
る。
FIG. 7 is a cross-sectional view showing another embodiment of the above septic tank.

【図8】従来例を示す断面図である。FIG. 8 is a sectional view showing a conventional example.

【符号の説明】[Explanation of symbols]

1 浄化槽 2 濾床 3 汚水 4 木質細片 5 緩衝槽 6 供給管 7 排水口 8 汚泥処理槽 9 濾過槽 10 移送管 1 Septic tank 2 Filter bed 3 Sewage 4 Wood debris 5 Buffer tank 6 Supply pipe 7 Drainage port 8 Sludge treatment tank 9 Filtration tank 10 Transfer pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 窪田 晃生 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 山田 秀昭 大阪府門真市大字門真1048番地松下電工株 式会社内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Akio Kubota 1048, Kadoma, Kadoma, Osaka Prefecture Matsushita Electric Works Co., Ltd. (72) Hideaki Yamada, 1048, Kadoma, Kadoma City, Osaka Matsushita Electric Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 浄化槽に微生物を付着させた濾床を設
け、浄化槽に汚水を流入させると共に濾床の微生物で汚
水を浄化処理するようにした汚水処理装置において、浄
化槽に木質細片を充填した緩衝槽を設け、汚水を緩衝槽
に供給するための供給管を浄化槽に設けると共に汚水を
浄化槽に排出するための排水口を緩衝槽に形成して成る
ことを特徴とする汚水処理装置。
1. A sewage treatment apparatus in which a septic tank is provided with a filter bed to which microorganisms are attached, and sewage is introduced into the septic tank and sewage is purified by the microorganisms of the filter bed. The septic tank is filled with wood chips. A sewage treatment apparatus comprising a buffer tank, a supply pipe for supplying sewage to the buffer tank, and a drainage port for discharging sewage into the buffer tank.
【請求項2】 浄化槽に微生物を付着させた濾床を設
け、浄化槽に汚水を流入させると共に濾床の微生物で汚
水を浄化処理するようにした汚水処理装置において、浄
化槽の汚水の水面よりも上方に木質細片を充填した濾過
槽を設け、汚水の浄化処理によって浄化槽に発生する汚
泥を濾過槽に移送するための移送管を浄化槽に設けると
共に濾過槽内の汚泥中の水分を浄化槽に排出するための
排水口を濾過槽に形成して成ることを特徴とする汚水処
理装置。
2. A sewage treatment apparatus in which a septic tank is provided with a filter bed to which microorganisms are adhered, and sewage is made to flow into the septic tank, and sewage is purified by the microorganisms of the filter bed. A filter tank filled with wood chips is installed in the filter tank, and a transfer pipe for transferring sludge generated in the filter tank to the filter tank is installed in the filter tank, and water in the filter tank is discharged to the filter tank. A sewage treatment device, characterized in that a drainage port for forming the same is formed in a filtration tank.
【請求項3】 浄化槽に微生物を付着させた濾床を設
け、浄化槽に汚水を流入させると共に濾床の微生物で汚
水を浄化処理するようにした汚水処理装置において、浄
化槽に木質細片を充填した汚泥処理槽を設けると共に木
質細片に汚水の浄化処理によって浄化槽に発生する汚泥
を分解する微生物を寄生させ、汚泥を浄化槽から汚泥処
理槽に移送するための移送管を具備して成ることを特徴
とする汚水処理装置。
3. A sewage treatment apparatus in which a septic tank is provided with a filter bed on which microorganisms are adhered, and sewage is introduced into the septic tank, and sewage is purified by the microorganisms of the filter bed. A sludge treatment tank is provided, and a wood pipe is provided with a transfer pipe for causing microorganisms that decompose sludge generated in the septic tank by the purification treatment of the wastewater to parasitize and transfer the sludge from the septic tank to the sludge treatment tank. Sewage treatment equipment to be.
JP7024695A 1995-03-28 1995-03-28 Sewage treating device Withdrawn JPH08267079A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7024695A JPH08267079A (en) 1995-03-28 1995-03-28 Sewage treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7024695A JPH08267079A (en) 1995-03-28 1995-03-28 Sewage treating device

Publications (1)

Publication Number Publication Date
JPH08267079A true JPH08267079A (en) 1996-10-15

Family

ID=13426025

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7024695A Withdrawn JPH08267079A (en) 1995-03-28 1995-03-28 Sewage treating device

Country Status (1)

Country Link
JP (1) JPH08267079A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109748463A (en) * 2019-03-06 2019-05-14 国合海伦环境技术(宜兴)有限公司 A kind of drawing and pulling type cover board purification tank having both lavatory and sanitary sewage disposal function
CN111762887A (en) * 2020-05-25 2020-10-13 宏升塑胶(杭州)有限公司 Rural domestic sewage treatment system
CN115784491A (en) * 2022-11-02 2023-03-14 河北能先环保科技有限公司 Treatment method of high-viscosity sewage

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109748463A (en) * 2019-03-06 2019-05-14 国合海伦环境技术(宜兴)有限公司 A kind of drawing and pulling type cover board purification tank having both lavatory and sanitary sewage disposal function
CN109748463B (en) * 2019-03-06 2023-10-17 国合海伦环境技术(宜兴)有限公司 Drawing type cover plate purifying tank with functions of toilet and domestic sewage treatment
CN111762887A (en) * 2020-05-25 2020-10-13 宏升塑胶(杭州)有限公司 Rural domestic sewage treatment system
CN111762887B (en) * 2020-05-25 2023-02-14 宏升塑胶(杭州)有限公司 Rural area domestic sewage treatment system
CN115784491A (en) * 2022-11-02 2023-03-14 河北能先环保科技有限公司 Treatment method of high-viscosity sewage
CN115784491B (en) * 2022-11-02 2024-02-13 河北能先环保科技有限公司 Treatment method of high-viscosity sewage

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