JPH09136096A - Purification tank - Google Patents

Purification tank

Info

Publication number
JPH09136096A
JPH09136096A JP29505795A JP29505795A JPH09136096A JP H09136096 A JPH09136096 A JP H09136096A JP 29505795 A JP29505795 A JP 29505795A JP 29505795 A JP29505795 A JP 29505795A JP H09136096 A JPH09136096 A JP H09136096A
Authority
JP
Japan
Prior art keywords
tank
storage tank
sludge
water
sludge storage
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP29505795A
Other languages
Japanese (ja)
Other versions
JP3271882B2 (en
Inventor
Hachiro Sato
八郎 佐藤
Yoshito Kitai
良人 北井
Masanobu Iwahashi
正修 岩橋
Kazuyuki Honda
和之 本田
Katsumi Hamada
勝己 浜田
Shinichi Furuse
真一 古瀬
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP29505795A priority Critical patent/JP3271882B2/en
Publication of JPH09136096A publication Critical patent/JPH09136096A/en
Application granted granted Critical
Publication of JP3271882B2 publication Critical patent/JP3271882B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Abstract

PROBLEM TO BE SOLVED: To make extraction operation possible after sludge being concentrated to a high concentration by a method in which a filtrate transfer pipe is installed in another tank adjacent to a sludge storage tank from the sludge storage tank to install in parallel with a filter membrane apparatus. SOLUTION: A filter membrane apparatus C1 for filtering water to be treated is installed in a sludge storage tank N2, and a filtrate transfer pipe A6 which transfers filtrate from the filter membrane apparatus C1 is installed in another tank adjacent to a sludge storage tank N2 from the sludge storage tank N2 to install in parallel with the filter membrane C1. In this way, since the sludge of the storage tank N2 is subjected to solid-liquid separation by the filter membrane apparatus C1, water can be extracted from the storage tank N2 to another water treatment tank. Besides, since solid components are remain in the storage tank N2, the sludge in the tank N2 can be concentrated to a high concentration. In this way, in the maintenance of a purification tank, the sludge in the tank N2 can be extracted in a state of a high concentration so that sludge in the purification tank can be removed enough even in a small amount of extraction.

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、槽内に発生する汚
泥を貯留する汚泥貯留槽を設けた浄化槽に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a septic tank provided with a sludge storage tank for storing sludge generated in the tank.

【0002】[0002]

【従来の技術】従来、この種の浄化槽においては、汚泥
貯留槽は単に汚泥貯留用の空間を設けてあるだけであっ
た。
2. Description of the Related Art Conventionally, in this type of septic tank, the sludge storage tank is simply provided with a space for sludge storage.

【0003】[0003]

【発明が解決しようとする課題】通常、汚泥貯留槽に貯
留された汚泥は、定期的に槽外へ引き抜き操作すること
により、槽内の汚泥量の増加を抑制出来る構成にしてあ
るものの、上述した従来の汚泥貯留槽によれば、単に汚
泥を貯留するだけの構成となっているため、たとえ静置
して沈殿濃縮したとしても、汚泥を高濃度にする事は難
しく、低濃度で汚泥を引き抜くことになると、所定量の
固形成分を引き抜くにも大量の汚泥を引き抜かねばなら
ず、頻繁に汚泥引き抜きを行わねばならなくなるなど、
メンテナンスに多大な労力を費やさねばならないという
欠点があった。
Normally, the sludge stored in the sludge storage tank is constructed so that the increase in the amount of sludge in the tank can be suppressed by periodically pulling the sludge out of the tank. According to the conventional sludge storage tank described above, since it is configured to simply store sludge, it is difficult to make the sludge a high concentration even if it is allowed to stand and precipitate and concentrate. When it comes to pulling out, even if a certain amount of solid components are pulled out, a large amount of sludge must be pulled out, and sludge pulling out must be performed frequently.
It had the drawback of requiring a great deal of maintenance effort.

【0004】従って、本発明の目的は、上記欠点に鑑
み、汚泥を高濃度に濃縮したのち引き抜き操作すること
の出来る浄化槽を提供することにある。
Therefore, in view of the above-mentioned drawbacks, it is an object of the present invention to provide a septic tank capable of concentrating sludge to a high concentration and then extracting it.

【0005】[0005]

【課題を解決するための手段】この目的を達成するため
の本発明の特徴構成は、汚泥貯留槽を設けた浄化槽であ
って、前記汚泥貯留槽に被処理水を濾過する濾過膜装置
を内装するとともに、前記汚泥貯留槽から汚泥貯留槽に
隣接する他の槽に前記濾過膜装置で濾過済の濾過水を移
送する濾過水移送管を設けて、前記濾過膜装置に連設し
てあることにあり、前記濾過膜装置を、前記汚泥貯留槽
上方に配置してあってもよく、前記汚泥貯留槽の水位
を、前記他の槽の水位よりも高く設定し、前記被処理水
移送管を、前記汚泥貯留槽の水位以下に設けるととも
に、前記濾過膜装置の下方に散気管を設けてあってもよ
く、前記濾過膜装置の下方に供給される被処理水を固液
分離するスクリーンを設けてあってもよく、その作用・
効果は以下の通りである。
A characteristic configuration of the present invention for achieving this object is a septic tank provided with a sludge storage tank, wherein the sludge storage tank is internally equipped with a filtration membrane device for filtering water to be treated. In addition, a filtered water transfer pipe for transferring filtered water that has been filtered by the filter membrane device from the sludge storage tank to another tank adjacent to the sludge storage tank is provided continuously with the filter membrane device. In the above, the filtration membrane device may be arranged above the sludge storage tank, the water level of the sludge storage tank is set higher than the water levels of the other tanks, and the treated water transfer pipe is , Provided below the water level of the sludge storage tank, an air diffuser may be provided below the filtration membrane device, and a screen for solid-liquid separation of the water to be treated supplied below the filtration membrane device is provided. It may be
The effects are as follows.

【0006】〔作用効果〕つまり、上述の構成により、
前記濾過膜装置で汚泥貯留槽内の汚泥を固液分離するか
ら、汚泥貯留槽内から水分を他の水処理槽へ引き抜き、
水処理に供することが出来、また、固液分離された固形
成分は、前記汚泥貯留槽内に残留するので、前記汚泥貯
留槽内の汚泥を高濃度に濃縮することが出来る。従っ
て、浄化槽をメンテナンスするときには前記汚泥貯留槽
内のの汚泥を引き抜くのに、高濃度の状態で引き抜きで
きて、少ない引き抜き量でも浄化槽内の汚泥を十分除去
できる。また、汚泥を高濃度な状態で蓄積するものであ
るから小さな汚泥貯留槽であっても、長期にわたって汚
泥の蓄積を許容できるから、メンテナンスをあまり行わ
ずとも浄化槽を安定運転する事が出来るようになって、
メンテナンスに要する労力を軽減出来るとともに、浄化
槽を全体として小さなものとでき、浄化槽の施工等を容
易に出来る。
[Operation and Effect] That is, according to the above configuration,
Since the sludge in the sludge storage tank is solid-liquid separated by the filtration membrane device, water is drawn from the sludge storage tank to another water treatment tank,
Since the solid component that can be subjected to water treatment and solid-liquid separated remains in the sludge storage tank, the sludge in the sludge storage tank can be concentrated to a high concentration. Therefore, when maintaining the septic tank, the sludge in the sludge storage tank can be extracted in a high-concentration state, and the sludge in the septic tank can be sufficiently removed even with a small extraction amount. In addition, since sludge is accumulated in a high concentration state, even a small sludge storage tank can allow accumulation of sludge for a long period of time, so that the septic tank can be operated stably without much maintenance. Become,
The labor required for maintenance can be reduced, and the septic tank can be made small as a whole to facilitate the construction of the septic tank.

【0007】また、前記濾過膜装置は、前記汚泥貯留槽
上方に配置してあれば、前記汚泥貯留槽で沈殿濃縮され
た汚泥の上澄液を固液分離することが出来、効率よく汚
泥濃縮を行うことが出来る。また、前記汚泥貯留槽の水
位を、前記他の槽の水位よりも高く設定し、前記被処理
水移送管を、前記汚泥貯留槽の水位以下に設けてあれ
ば、特に前記濾過膜装置に吸引濾過膜装置を設けること
無く、前記汚泥貯留槽の汚泥を常時濃縮運転することが
出来る。この構成において、前記濾過膜装置の下方に散
気管を設けてあれば、前記濾過膜装置に汚れが付着して
も、前記散気装置による気泡が前記濾過膜装置に衝突す
るから、前記気泡が前記濾過膜装置から汚れを剥離させ
つつ、前記濾過膜装置に汚れが定着するのを防止するの
で、被処理水を濃縮する機能を長期にわたって維持する
ことが出来る。尚、前記汚泥貯留槽においては、臭気が
発生しやすいが、散気による前記気泡は、臭気の除去に
も役立つ。また濾過膜装置の下方に固液分離用のスクリ
ーンを設けてあれば、比較的大きな固形成分が前記濾過
膜装置に付着するのを防止でき、前記濾過膜装置が目詰
まりする等の不都合を防止しやすい。
Further, if the filtration membrane device is arranged above the sludge storage tank, the supernatant of the sludge precipitated and concentrated in the sludge storage tank can be solid-liquid separated and the sludge can be efficiently concentrated. Can be done. Further, if the water level of the sludge storage tank is set higher than the water levels of the other tanks, and the treated water transfer pipe is provided below the water level of the sludge storage tank, it is particularly sucked into the filtration membrane device. The sludge in the sludge storage tank can be constantly concentrated and operated without providing a filtration membrane device. In this configuration, if an air diffusing pipe is provided below the filtration membrane device, even if dirt is attached to the filtration membrane device, bubbles due to the air diffusion device collide with the filtration membrane device. Since the dirt is prevented from fixing on the filtration membrane device while peeling the dirt from the filtration membrane device, the function of concentrating the water to be treated can be maintained for a long period of time. In the sludge storage tank, odor is likely to be generated, but the bubbles due to air diffusion are also useful for removing odor. Further, if a screen for solid-liquid separation is provided below the filtration membrane device, it is possible to prevent relatively large solid components from adhering to the filtration membrane device and prevent inconveniences such as clogging of the filtration membrane device. It's easy to do.

【0008】[0008]

【発明の実施の形態】以下に本発明の実施の形態を図面
に基づいて説明する。図1に示すように、本発明の浄化
槽は、円筒状の浄化槽本体Xの両端を鏡部X1,X2を
設けて内部に密閉空間を形成するとともに、内部の密閉
空間に仕切り壁を設けて区分けして、上流側から、流量
調整槽N1、脱窒素槽E1、汚泥貯留槽N2、膜分離槽
E2、放流ポンプ槽Tを形成してあり、前記各槽の上部
には、メンテナンス等に用いるマンホールHを設けてあ
る。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. As shown in FIG. 1, the septic tank of the present invention is divided into a cylindrical septic tank main body X by providing mirror portions X1 and X2 at both ends to form a sealed space inside and partition walls provided in the sealed space inside. Then, from the upstream side, a flow rate adjusting tank N1, a denitrification tank E1, a sludge storage tank N2, a membrane separation tank E2, and a discharge pump tank T are formed, and a manhole used for maintenance or the like is formed on the upper part of each tank. H is provided.

【0009】前記流量調整槽N1は、前記浄化槽本体X
の一方の鏡部X1に設けてなる流入口Iから浄化槽内に
流入した被処理水の原水を受けて、その被処理水中の夾
雑物を沈殿除去しつつ、内部に生育する嫌気性菌によ
り、被処理水を嫌気処理しつつ、被処理水を一時貯留す
る水処理室内に、被処理水を脱窒素槽E1に移送する第
一ポンプP1を設け、被処理水が大量に流入した場合
や、長期にわたって被処理水の流入が無い場合にも、被
処理水を定常的に脱窒素槽E1に移送して、後続の各水
処理室での水処理に支障をきたさないようにしてある。
The flow rate adjusting tank N1 is the septic tank main body X.
By receiving the raw water of the treated water that has flowed into the septic tank from the inflow port I provided in one of the mirror portions X1 and precipitating and removing the impurities in the treated water, the anaerobic bacteria growing inside the When the first pump P1 for transferring the treated water to the denitrification tank E1 is provided in the water treatment chamber for temporarily storing the treated water while anaerobically treating the treated water, and a large amount of the treated water flows in, Even if there is no inflow of water to be treated for a long period of time, the water to be treated is constantly transferred to the denitrification tank E1 so as not to hinder the water treatment in each subsequent water treatment chamber.

【0010】前記脱窒素槽E1は、前記流量調整槽N1
に隣接する水処理室に、前記流量調整槽N1からの被処
理水を流入させる流入管A1を、前記第一ポンプP1に
接続して設け、被処理水の流入路を構成してある。ま
た、第二ポンプP2を内装し、その第二ポンプP2に移
送管A2を設け、被処理水を前記膜分離槽E2へ移送す
る構成にしてある。また、槽内の被処理水を攪拌循環さ
せる攪拌ポンプP3を内装してあり、槽内の被処理水の
混合を図り、BOD負荷の高い被処理水と、硝化済の被
処理水とを混合し、高度な脱窒処理を行える構成にして
ある。
The denitrification tank E1 is the flow rate adjusting tank N1.
An inflow pipe A1 for introducing the water to be treated from the flow rate adjusting tank N1 into the water treatment chamber adjacent to is connected to the first pump P1 and constitutes an inflow passage for the water to be treated. Further, the second pump P2 is internally provided, and the transfer pipe A2 is provided in the second pump P2 to transfer the water to be treated to the membrane separation tank E2. In addition, a stirring pump P3 for stirring and circulating the water to be treated in the tank is provided to mix the water to be treated in the tank and mix the water to be treated with a high BOD load with the nitrified water to be treated. In addition, it is configured to perform advanced denitrification processing.

【0011】前記膜分離槽E2は、前記脱窒素槽E1と
の間を仕切る隔壁に、前記流入路を設けるとともに、前
記脱窒素槽E1から過剰に流入した被処理水を前記脱窒
素槽E1に返送する返送管A3を設けて、被処理水の返
送路を構成してある。また、多数の平板状の濾過膜板を
直立状態で平行に並設してなる膜分離装置Mを内装して
なり、前記膜分離装置Mは、濾過膜板の多数を整列して
保持する濾過膜板保持枠を設け、下部に前記濾過膜板保
持枠を支持する脚部を設け、前記脚部間にその濾過膜板
に気泡を供給して、その膜面に汚泥等の付着しすぎるの
を防止し、かつ、前記膜分離槽E2内に循環流を形成し
ながら被処理水に酸素を供給する散気装置Dを内装して
構成してある。また、前記膜分離装置Mのそれぞれの濾
過膜板には取水管M1を連設するとともに、前記取水管
M1からの濾過水を合流させて膜分離槽E2外へ導く集
水管M2を接続してあり、前記膜分離槽E2の水面より
も下方で前記膜分離槽E2に隣接する放流ポンプ槽Tに
連通接続してある。また、前記膜分離槽E2には、沈殿
汚泥をエアリフト作用によって前記汚泥貯留槽N2に移
送する沈殿汚泥移送管A4を内装してある。
The membrane separation tank E2 is provided with the inflow passage in a partition wall which separates the denitrification tank E1 from the denitrification tank E1, and the water to be treated which has excessively flown into the denitrification tank E1 is introduced into the denitrification tank E1. A return pipe A3 for returning the water is provided to form a return path for the water to be treated. In addition, a membrane separation device M in which a large number of flat plate-shaped filtration membrane plates are arranged in parallel in an upright state is installed, and the membrane separation device M is a filtration device that holds a large number of filtration membrane plates in alignment. A membrane plate holding frame is provided, and a leg portion for supporting the filtration membrane plate holding frame is provided at the lower portion, and air bubbles are supplied to the filtration membrane plate between the leg portions so that sludge or the like adheres too much to the membrane surface. And a diffusing device D for supplying oxygen to the water to be treated while forming a circulating flow in the membrane separation tank E2. Further, a water intake pipe M1 is connected to each of the filtration membrane plates of the membrane separation device M, and a water collection pipe M2 for joining the filtered water from the water intake pipe M1 and guiding it to the outside of the membrane separation tank E2 is connected. Yes, it is connected to the discharge pump tank T adjacent to the membrane separation tank E2 below the water surface of the membrane separation tank E2. The membrane separation tank E2 is equipped with a settling sludge transfer pipe A4 for transferring the settling sludge to the sludge storage tank N2 by an air lift action.

【0012】前記汚泥貯留槽N2は、前記脱窒素槽E1
と、前記膜分離槽E2との間に水処理空間を区分けして
設けてある。前記汚泥貯留槽N2の上方には前記脱窒素
槽E1から、膜分離槽E2に被処理水を移送する移送管
A2を横架姿勢で配置してある。前記移送管A2の、前
記汚泥貯留槽N2上方部分には、固液分離用のスクリー
ン濾過装置Sを介装してある。前記スクリーン濾過装置
Sは、図2,3に示すように、固液分離用の多数の櫛歯
S1aを備えてなる櫛型スクリーンS1と、前記櫛歯S
1a間に多数の突起S2aを挿通させて前記櫛型スクリ
ーンS1に引っ掛かった固形物をかきとるローラーS2
とを備えてなり、前記移送管A2を介して移送される被
処理水のうち、比較的大きな固形成分を前記櫛型スクリ
ーンS1で濾過するとともに、前記櫛歯S1aを通過し
た被処理水を前記膜分離槽E2に移送させ、かつ、前記
櫛歯S1aに引っ掛かった固形物は、前記ローラーS2
によって上方にかきあげられ、最終的に前記汚泥貯留槽
N2に落下させられる構成にしてあり、前記固形物は前
記汚泥貯留槽内に蓄積される。また、前記沈殿汚泥移送
管A4は、前記膜分離槽E2と前記汚泥貯留槽N2の間
にわたって設けてあり、前記膜分離槽E2底部に沈殿す
る比較的高濃度の沈殿汚泥は、前記沈殿汚泥移送管A4
によって、前記汚泥貯留槽N2に返送され貯留される構
成にしてある。さらに、図1に示すように、前記汚泥貯
留槽N2の上部には、被処理水を濾過する濾過膜装置C
1を内装するとともに、前記汚泥貯留槽N2から脱窒素
槽E1に前記濾過膜装置C1で濾過済の濾過水を移送す
る濾過水移送管A6を設けて、前記濾過膜装置C1に連
設してある。また、前記濾過膜装置C1は、上下両端を
開放状態にしてあるケーシングC2で覆うとともに、そ
のケーシングC2の下部開口には、パンチングメタルか
らなるスクリーンC3を設けて、粗大な固形成分が前記
濾過膜装置C1に付着するのを防止するように構成して
ある。前記ケーシングC2内で前記濾過膜装置C1の下
方には前記濾過膜装置C1に気泡を供給する散気装置D
1を設け、前記スクリーンC3の下方には、前記スクリ
ーンC3に気泡を供給する散気装置D2を設けて、汚泥
上澄に上昇流を形成させ、前記濾過膜装置C1や、前記
スクリーンC3に付着した汚れを剥離させるとともに、
前記汚泥貯留槽N2内の臭気成分を酸化除去して緩和可
能にする構成にしてある。尚、前記汚泥貯留槽N2の水
位は、通常脱窒素槽E1の水位よりも高くなるように設
定してあるとともに、濾過水移送管A6には逆止弁A7
を設けて脱窒素槽E1の被処理水が逆流するのを防止し
てある。
The sludge storage tank N2 is the denitrification tank E1.
And the membrane separation tank E2 are divided into water treatment spaces. Above the sludge storage tank N2, a transfer pipe A2 for transferring the water to be treated from the denitrification tank E1 to the membrane separation tank E2 is arranged in a horizontal posture. A screen filtration device S for solid-liquid separation is interposed above the sludge storage tank N2 of the transfer pipe A2. As shown in FIGS. 2 and 3, the screen filtering device S includes a comb-shaped screen S1 including a large number of comb teeth S1a for solid-liquid separation, and the comb teeth S1.
A roller S2 for scraping the solid matter caught on the comb-shaped screen S1 by inserting a large number of protrusions S2a between the rollers 1a.
Of the water to be treated transferred through the transfer pipe A2, a relatively large solid component is filtered by the comb-shaped screen S1, and the water to be treated that has passed through the comb teeth S1a is The solid matter transferred to the membrane separation tank E2 and caught on the comb teeth S1a is the roller S2.
It is scraped up by the above and finally dropped into the sludge storage tank N2, and the solid matter is accumulated in the sludge storage tank. The sedimentation sludge transfer pipe A4 is provided between the membrane separation tank E2 and the sludge storage tank N2, and the relatively high-concentration sedimentation sludge settling at the bottom of the membrane separation tank E2 is transferred by the sedimentation sludge transfer. Tube A4
By this, it is configured to be returned and stored in the sludge storage tank N2. Further, as shown in FIG. 1, a filtration membrane device C for filtering the water to be treated is provided above the sludge storage tank N2.
1 is installed inside, and a filtered water transfer pipe A6 for transferring filtered water filtered by the filter membrane device C1 from the sludge storage tank N2 to the denitrification tank E1 is provided and connected to the filter membrane device C1. is there. Further, the filtration membrane device C1 is covered with a casing C2 whose upper and lower ends are in an open state, and a screen C3 made of punching metal is provided at a lower opening of the casing C2 so that a coarse solid component is contained in the filtration membrane. It is configured to prevent adhesion to the device C1. An air diffuser D for supplying air bubbles to the filtration membrane device C1 below the filtration membrane device C1 in the casing C2.
1 is provided, and below the screen C3, an air diffuser D2 for supplying air bubbles to the screen C3 is provided so that an upward flow is formed in the sludge supernatant and adheres to the filtration membrane device C1 and the screen C3. While removing the dirt
The odorous component in the sludge storage tank N2 is oxidized and removed so that it can be alleviated. The water level in the sludge storage tank N2 is set to be higher than the water level in the denitrification tank E1, and a check valve A7 is attached to the filtered water transfer pipe A6.
Is provided to prevent the water to be treated in the denitrification tank E1 from flowing backward.

【0013】この様な構成により、前記汚泥貯留槽N2
内には、前記スクリーン濾過装置Sからの固形成分や、
前記膜分離槽E2からの沈殿汚泥等(以下単に汚泥等と
略称する)、水処理上に悪影響を及ぼす虞のある成分を
貯留し、沈殿濃縮するとともに、前記濾過膜装置C1に
より、前記汚泥貯留槽N2と、脱窒素槽E1との水頭差
によって前記汚泥貯留槽N2の上澄から固液分離した濾
過水を前記脱窒素槽E2に返送することによって、さら
に濃縮可能な構成となり、固形成分を高濃度に貯留する
ことが出来るようになり、汚泥等の引き抜き操作を行う
時には、効率よく行えるようになった。
With such a configuration, the sludge storage tank N2
In the inside, solid components from the screen filtration device S,
Precipitated sludge and the like from the membrane separation tank E2 (hereinafter simply referred to as “sludge and the like”) and other components that may adversely affect water treatment are stored and concentrated, and the sludge storage is performed by the filtration membrane device C1. By returning the filtered water that has been solid-liquid separated from the supernatant of the sludge storage tank N2 due to the head difference between the tank N2 and the denitrification tank E1, to the denitrification tank E2, it becomes possible to further concentrate the solid component. It became possible to store it at a high concentration, and it became possible to efficiently perform the operation of pulling out sludge and the like.

【0014】前記放流ポンプ槽Tは、消毒槽Q1と、貯
留槽Q2とからなり、前記消毒槽Q1は、前記膜分離槽
E2と、前記放流ポンプ槽Tとを仕切る隔壁に処理水受
け容器を設け、その壁面に小孔を設けて構成してあり、
前記消毒槽Q1に流入した濾過水は、消毒されたのち貯
留槽Q2に流入する。前記貯留槽Q2は、第三ポンプP
4を内装してあり、前記処理水を貯留したのち、放流ポ
ンプP1で処理水を汲み上げ、排出管A5を介して放流
口Zから浄化槽外へ放流可能に構成してある。これによ
り、消毒済の処理水が前記貯留槽Tからほぼ定量的に浄
化槽外に放流される。
The discharge pump tank T is composed of a disinfection tank Q1 and a storage tank Q2. The disinfection tank Q1 has a partition for partitioning the membrane separation tank E2 and the discharge pump tank T with a treated water receiving container. It is provided with a small hole on its wall surface,
The filtered water that has flowed into the disinfection tank Q1 is sterilized and then flows into the storage tank Q2. The storage tank Q2 is a third pump P
4 is installed inside, and after storing the treated water, the treated water can be pumped up by the discharge pump P1 and discharged from the discharge port Z to the outside of the septic tank via the discharge pipe A5. As a result, the disinfected treated water is discharged from the storage tank T almost quantitatively to the outside of the septic tank.

【0015】尚、特許請求の範囲の項に、図面との対照
を便利にするために符号を記すが、該記入により本発明
は添付図面の構成に限定されるものではない。
In the claims, reference numerals are provided for convenience of comparison with the drawings, but the present invention is not limited to the configuration shown in the attached drawings.

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

【図1】浄化槽の縦断側面図FIG. 1 is a vertical side view of a septic tank.

【図2】スクリーン濾過装置の全体斜視図FIG. 2 is an overall perspective view of a screen filtration device.

【図3】スクリーン濾過装置の要部平面図FIG. 3 is a plan view of a main part of a screen filtration device.

【符号の説明】[Explanation of symbols]

A6 被処理水移送管 C1 濾過膜装置 C3 スクリーン D1 散気管 N2 汚泥貯留槽 A6 Treated water transfer pipe C1 Filtration membrane device C3 Screen D1 Air diffuser N2 Sludge storage tank

フロントページの続き (72)発明者 本田 和之 滋賀県甲賀郡甲西町高松2番地の1 株式 会社クボタ滋賀工場内 (72)発明者 浜田 勝己 滋賀県甲賀郡甲西町高松2番地の1 株式 会社クボタ滋賀工場内 (72)発明者 古瀬 真一 滋賀県甲賀郡甲西町高松2番地の1 株式 会社クボタ滋賀工場内Front Page Continuation (72) Inventor Kazuyuki Honda, 1 Takamatsu, Kosai-cho, Koga-gun, Shiga 1 Kubota Shiga factory (72) Inventor Katsumi Hamada 1-Kuma, Koga-cho, Shiga, Kubota 1-share company Shiga Factory (72) Inventor Shinichi Furuse 1 of 2 Takamatsu, Kosai Town, Koga District, Shiga Prefecture Kubota Shiga Factory

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 汚泥貯留槽(N2)を設けた浄化槽であ
って、前記汚泥貯留槽(N2)に被処理水を濾過する濾
過膜装置(C1)を内装するとともに、前記汚泥貯留槽
(N2)から汚泥貯留槽(N2)に隣接する他の槽に前
記濾過膜装置(C1)で濾過済の濾過水を移送する濾過
水移送管(A6)を設けて、前記濾過膜装置(C1)に
連設してある浄化槽。
1. A septic tank provided with a sludge storage tank (N2), wherein the sludge storage tank (N2) is internally provided with a filtration membrane device (C1) for filtering water to be treated, and the sludge storage tank (N2). ), A filtered water transfer pipe (A6) for transferring the filtered water filtered by the filter membrane device (C1) to another tank adjacent to the sludge storage tank (N2) is provided to the filter membrane device (C1). A septic tank that is installed in series.
【請求項2】 前記濾過膜装置(C1)を、前記汚泥貯
留槽(N2)上部に配置してある請求項1に記載の浄化
槽。
2. The septic tank according to claim 1, wherein the filtration membrane device (C1) is arranged above the sludge storage tank (N2).
【請求項3】 前記汚泥貯留槽(N2)の水位を、前記
他の槽の水位よりも高く設定し、前記被処理水移送管
(A6)を、前記汚泥貯留槽(N2)の水位以下に設け
るとともに、前記濾過膜装置(C1)の下方に散気管
(D1)を設けてある請求項1〜2のいずれかに記載の
浄化槽。
3. The water level of the sludge storage tank (N2) is set higher than the water levels of the other tanks, and the treated water transfer pipe (A6) is set below the water level of the sludge storage tank (N2). The septic tank according to any one of claims 1 and 2, which is provided with an air diffuser (D1) below the filtration membrane device (C1).
【請求項4】 前記濾過膜装置(C1)の下方に供給さ
れる被処理水を固液分離するスクリーン(C3)を設け
てある請求項1〜3のいずれかに記載の浄化槽。
4. The septic tank according to claim 1, further comprising a screen (C3) for solid-liquid separating the water to be treated supplied below the filtration membrane device (C1).
JP29505795A 1995-11-14 1995-11-14 Septic tank Expired - Lifetime JP3271882B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29505795A JP3271882B2 (en) 1995-11-14 1995-11-14 Septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29505795A JP3271882B2 (en) 1995-11-14 1995-11-14 Septic tank

Publications (2)

Publication Number Publication Date
JPH09136096A true JPH09136096A (en) 1997-05-27
JP3271882B2 JP3271882B2 (en) 2002-04-08

Family

ID=17815764

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29505795A Expired - Lifetime JP3271882B2 (en) 1995-11-14 1995-11-14 Septic tank

Country Status (1)

Country Link
JP (1) JP3271882B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002205087A (en) * 2001-01-09 2002-07-23 Kubota Corp Air diffuser
JP2003024959A (en) * 2001-07-17 2003-01-28 Fuji Clean Kogyo Kk Method and apparatus for treating wastewater
JP2008055324A (en) * 2006-08-31 2008-03-13 Hitachi Housetec Co Ltd Sewage cleaning tank
JP2012000585A (en) * 2010-06-18 2012-01-05 Kubota Corp Wastewater treatment facility, wastewater treatment method and method of reconstructing wastewater treatment facility

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002205087A (en) * 2001-01-09 2002-07-23 Kubota Corp Air diffuser
JP2003024959A (en) * 2001-07-17 2003-01-28 Fuji Clean Kogyo Kk Method and apparatus for treating wastewater
JP2008055324A (en) * 2006-08-31 2008-03-13 Hitachi Housetec Co Ltd Sewage cleaning tank
JP2012000585A (en) * 2010-06-18 2012-01-05 Kubota Corp Wastewater treatment facility, wastewater treatment method and method of reconstructing wastewater treatment facility

Also Published As

Publication number Publication date
JP3271882B2 (en) 2002-04-08

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