JPH08913A - Sludge waste water treatment apparatus - Google Patents

Sludge waste water treatment apparatus

Info

Publication number
JPH08913A
JPH08913A JP6141450A JP14145094A JPH08913A JP H08913 A JPH08913 A JP H08913A JP 6141450 A JP6141450 A JP 6141450A JP 14145094 A JP14145094 A JP 14145094A JP H08913 A JPH08913 A JP H08913A
Authority
JP
Japan
Prior art keywords
sludge
settling tank
pipe
tank
waste 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
JP6141450A
Other languages
Japanese (ja)
Inventor
Hiroshi Sato
宏史 佐藤
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP6141450A priority Critical patent/JPH08913A/en
Publication of JPH08913A publication Critical patent/JPH08913A/en
Pending 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

  • Activated Sludge Processes (AREA)

Abstract

PURPOSE:To provide a sludge waste water treatment apparatus preventing that the water channel due to a supernatant liquid is formed to a settled sludge bed and settled sludge is stagnated on the bottom of a sedimentation tank as it is and capable of drawing out settled sludge efficiently and continuously while discharging a supernatant liquid. CONSTITUTION:Drain pipes 101, 201 for discharging settled sludge formed by arranging perforated pipes having drain holes provided thereto in a dispersed state are provided to the flat bottom parts of sedimentation tanks 1, 2 performing the sedimentation treatment of sludge of waste water, and the sedimentation tanks 1, 2 and the drain pipes 101, 201 are all connected by a circulation route provided with a pump 15.

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、工場等で発生する汚泥
廃水、特に脱水機により脱水処理された濾布洗浄廃水の
処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for treating sludge wastewater generated in factories and the like, particularly filter cloth washing wastewater dehydrated by a dehydrator.

【0002】[0002]

【従来の技術】従来、工場廃水の活性汚泥処理法による
汚泥廃水は、ベルトプレス方式の脱水機により脱水処理
し、濾過された水は放流により排水し、汚泥分はロータ
リーキルンにより焼却されている。上記の脱水機に用い
られた濾布には掻き取り残しの汚泥分が付着しているた
め、水洗の必要がある。ところが、この水洗に用いられ
た濾布の洗浄廃水は浮遊物質が多いため、そのままで放
流することができない。
2. Description of the Related Art Conventionally, sludge wastewater obtained by an activated sludge treatment method of factory wastewater is dehydrated by a belt press type dehydrator, filtered water is discharged by discharge, and sludge content is incinerated by a rotary kiln. The filter cloth used in the above dehydrator has a sludge content left unscraped and therefore needs to be washed with water. However, since the cleaning wastewater of the filter cloth used for this water washing contains a large amount of suspended substances, it cannot be discharged as it is.

【0003】従って、汚泥分の沈降が速いのを利用し
て、汎用の平底の槽を沈澱槽として用い、汚泥分を沈降
により沈澱させて水分と分離し、上澄み液は放流し、汚
泥分は沈澱槽の底からボールバルブを使用してヘッドに
より抜き出し、再び脱水機にかけて、第2次の沈澱処理
を行うようになされた汚泥廃水処理装置が用いられてい
る。
[0003] Therefore, by utilizing the fact that sludge sedimentation is fast, a general-purpose flat-bottomed tank is used as a sedimentation tank, sludge is sedimented by sedimentation and separated from water, and the supernatant liquid is discharged and sludge is separated. A sludge wastewater treatment device is used which is adapted to withdraw from a bottom of a settling tank by a head using a ball valve and to be dehydrated again to perform a second settling process.

【0004】上記の汚泥廃水処理装置以外のものについ
ては、例えば、特開昭63−16094号公報におい
て、小規模の下水、廃水処理プラントにおいて用いられ
る余剰汚泥の引抜き装置が記載されている。
With respect to devices other than the above-mentioned sludge wastewater treatment device, for example, Japanese Unexamined Patent Publication (Kokai) No. 63-16094 discloses a device for extracting excess sludge used in a small-scale sewage / wastewater treatment plant.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記前
者の汚泥廃水処理装置においては、沈澱槽の平底に沈降
して溜まった汚泥分は、使用頻度が多く、長期に亘って
くると、汚泥層に上澄み液のみず道、或いは空気の通り
道ができて、汚泥が完全に抜き出せずに、堆積してゆく
といった問題がある。
However, in the former sludge wastewater treatment device, the sludge component settling on the flat bottom of the settling tank is frequently used, and when it is used for a long period of time, it becomes a sludge layer. There is a problem that not only the supernatant liquid but also the passage for the air can be formed, and the sludge can be accumulated without being completely extracted.

【0006】又、後者の特開昭63−16094号公報
に記載された余剰汚泥の引抜き装置は、小規模の廃水処
理には有効であるが、工場等における大規模の処理に
は、不向きであるといった問題がある。
Further, the latter device for removing excess sludge described in JP-A-63-16094 is effective for treating small-scale wastewater, but is not suitable for large-scale treatment in factories and the like. There is such a problem.

【0007】本発明は、このような上記の問題点に着目
してなされたものであり、その目的とするところは、こ
れらの問題点を解消し、沈澱汚泥層に上澄み液によるみ
ず道ができて沈澱汚泥が沈澱槽の底に滞留したままとな
るのを防止し、効率よく継続的に沈澱汚泥分を抜き出す
とともに、上澄み液を放流することができる汚泥廃水処
理装置を提供することにある。
The present invention has been made by paying attention to the above problems, and the purpose thereof is to eliminate these problems and to form a water path in the settling sludge layer by the supernatant liquid. It is an object of the present invention to provide a sludge wastewater treatment device capable of preventing the settled sludge from staying at the bottom of the settling tank, efficiently and continuously extracting the settled sludge, and discharging the supernatant.

【0008】[0008]

【課題を解決するための手段】本発明の汚泥廃水処理装
置においては、廃水の汚泥の沈澱処理を行う沈澱槽の平
底部に、沈澱汚泥の排出用の排水孔の穿設された有孔管
が分散配置された沈澱汚泥排出用の排水管が設けられ、
上記沈澱槽と排水管がポンプを経由する循環経路により
接続されていることを特徴とする。
In the sludge wastewater treatment apparatus of the present invention, a perforated pipe having a drainage hole for discharging the settled sludge is provided in a flat bottom of a settling tank for treating the sludge of the wastewater. A drainage pipe for disposing the settled sludge is installed.
The settling tank and the drainage pipe are connected by a circulation path via a pump.

【0009】本発明の汚泥廃水処理装置における排水管
は、排水孔が穿設された合成樹脂管、例えば、塩化ビニ
ル樹脂管でできた有孔管を、排水孔を下方に向けて沈澱
槽の平坦な平底部にほぼ均等に分散配置されてなるもの
である。
The drainage pipe in the sludge wastewater treatment apparatus of the present invention is a synthetic resin pipe having a drainage hole, for example, a perforated pipe made of a vinyl chloride resin pipe, and the drainage hole is directed downward to a settling tank. It is arranged almost evenly on a flat flat bottom.

【0010】[0010]

【作用】本発明の汚泥廃水処理装置においては、沈澱槽
の平底部の沈澱汚泥を効率よく攪拌し排出させるため
に、排水孔が穿設された有孔管が分散配置された排水管
が設けられることにより、沈澱汚泥層に上澄み液による
みず道ができて沈澱汚泥が沈澱槽の底に滞留したままと
なるのを防止し、効率よく継続的に汚泥分を抜き出すと
ともに、上澄み液を放流することができる。
In the sludge wastewater treatment apparatus of the present invention, in order to efficiently stir and discharge the settled sludge at the flat bottom of the settling tank, the drainage pipes in which the perforated pipes having the drainage holes are dispersed are provided. As a result of this, it is possible to prevent the sediment sludge layer from forming a water path in the sediment sludge layer and prevent the sediment sludge from staying at the bottom of the sedimentation tank, efficiently and continuously extracting the sludge component and discharging the supernatant liquid. be able to.

【0011】[0011]

【実施例】以下、本発明の実施例を図面を参照して説明
する。図1は、本発明の汚泥廃水処理装置の一例を示す
装置全体のフロー図である。図1において、1は上方に
設けられた第一沈澱槽であり、この第一沈澱槽1の平底
部には排水管101が設けられている。上記第一沈澱槽
1の下方には第二沈澱槽2が設けられ、この第二沈澱槽
2の平底部には排水管201が設けられている。3は脱
水機であり、この脱水機3の下方に位置して濾布洗浄廃
水槽4が設けられている。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a flow chart of the entire apparatus showing an example of the sludge wastewater treatment apparatus of the present invention. In FIG. 1, reference numeral 1 denotes a first precipitation tank provided above, and a drain pipe 101 is provided at a flat bottom portion of the first precipitation tank 1. A second precipitation tank 2 is provided below the first precipitation tank 1, and a drain pipe 201 is provided at the flat bottom portion of the second precipitation tank 2. Reference numeral 3 denotes a dehydrator, and a filter cloth washing wastewater tank 4 is provided below the dehydrator 3.

【0012】上記脱水機3が運転により作動されて濾布
洗浄廃水槽4に貯蔵された濾布洗浄排水を第一沈澱槽1
に給送するために、濾布洗浄廃水槽4と第一沈澱槽1の
間に水中ポンプ5が、配管5aにより接続されて設けら
れている。
The dewatering machine 3 is operated to drive the filter cloth cleaning waste water stored in the filter cloth cleaning waste water tank 4 into the first settling tank 1.
A submersible pump 5 is provided between the filter cloth washing wastewater tank 4 and the first settling tank 1 for the purpose of feeding it to the pipe.

【0013】水中ポンプ5により第一沈澱槽1に給送さ
れた濾布洗浄廃水が満杯になると、溢れた濾布洗浄廃水
はオーバーフローにより、配管1aより第二沈澱槽2へ
送り込まれる。
When the filter cloth washing wastewater fed to the first settling tank 1 by the submersible pump 5 becomes full, the overflowing filter cloth washing wastewater is sent to the second settling tank 2 from the pipe 1a by overflow.

【0014】この後、脱水機3の運転が停止されて、バ
ルブ6、バルブ7、バルブ8、バルブ9、バルブ10、
及びバルブ11が開かれ、第一沈澱槽1、及び第二沈澱
槽2のヘッドを利用して、ポンプ15にて配管10aと
配管11aの空気が抜き取られる。
Thereafter, the operation of the dehydrator 3 is stopped, and the valves 6, 7, 8 and 9, valve 10,
The valve 11 is opened, and the heads of the first settling tank 1 and the second settling tank 2 are used to extract air from the pipe 10a and the pipe 11a by the pump 15.

【0015】この状態で第一沈澱槽1、及び第二沈澱槽
2の廃水中の汚泥の沈澱がほぼ3時間に亘って行われ
る。ほぼ3時間の経過後、第一沈澱槽1、及び第二沈澱
槽2のそれぞれのバルブ12、及びバルブ13が開かれ
て上澄み液が側溝14へ排出されて処理され、排出完了
とともにバルブ12、及びバルブ13は閉鎖される。
In this state, the sludge in the wastewater of the first settling tank 1 and the second settling tank 2 is settled for about 3 hours. After a lapse of about 3 hours, the valves 12 and 13 of the first precipitation tank 1 and the second precipitation tank 2 are opened and the supernatant liquid is discharged to the side groove 14 for processing. And the valve 13 is closed.

【0016】次に、バルブ6、及びバルブ7を閉じると
ともに、ポンプ15を作動させて、ほぼ2分後に開き、
第一沈澱槽1の沈澱汚泥の初期攪拌が行われる。これに
引き続き、バルブ6が閉じられ、ポンプ15の作動によ
り、配管6a、7a、及び10aを経由して、第一沈澱
槽1内の沈澱汚泥の循環と攪拌が排水管101を通過さ
せて行われ、同時に第一沈澱槽1内の沈澱汚泥の輸送
が、配管8aを経由して第二沈澱槽2へ行われる。
Next, the valves 6 and 7 are closed, the pump 15 is operated, and after about 2 minutes, it is opened.
Initial stirring of the settled sludge in the first settling tank 1 is performed. Subsequent to this, the valve 6 is closed, and the pump 15 is operated to circulate and agitate the settled sludge in the first settling tank 1 through the drain pipe 101 via the pipes 6a, 7a, and 10a. At the same time, the settling sludge in the first settling tank 1 is transported to the second settling tank 2 via the pipe 8a.

【0017】上記の第一沈澱槽1内の沈澱汚泥の循環と
攪拌は、第一沈澱槽1の平底に設けられた排水管101
を通過させて行われ、この排水管101には下方に向け
て排水孔が穿設された有孔管が分散配置されているの
で、この槽の底に溜まった汚泥は攪拌され、且つ、みず
道の発生を防止することができる。
The circulation and agitation of the settled sludge in the first settling tank 1 described above is performed by the drain pipe 101 provided at the flat bottom of the first settling tank 1.
Since the perforated pipes having the drainage holes formed downward are dispersedly arranged in the drainage pipe 101, the sludge accumulated at the bottom of the tank is agitated and Roads can be prevented from occurring.

【0018】続いて、プレッシャースイッチ16の作動
により、ポンプ15の運転が止められると、バルブ10
とバルブ8が閉じられる。上記プレッシャースイッチ1
6はポンプの空運転を防止するために設けられたもので
あり、沈澱汚泥が少なくなって圧力が低下すると、この
圧力を感知して自動的にポンプの作動を停止させるもの
である。
Subsequently, when the operation of the pump 15 is stopped by the operation of the pressure switch 16, the valve 10
And the valve 8 is closed. Pressure switch 1 above
Reference numeral 6 is provided to prevent the pump from running dry, and when the settled sludge is reduced and the pressure drops, the pressure is sensed and the pump operation is automatically stopped.

【0019】次いで、バルブ17、及びバルブ6が開か
れて第一沈澱槽1へ、配管6aを経由して工業用水が送
り込まれ、約1分間の第一沈澱槽1の洗浄が行われ、洗
浄が終了した時点で、バルブ17、バルブ6、及びバル
ブ7が閉じられる。この状態で濾布洗浄廃水の第一沈澱
槽1への、新たな給送が行えるようになる。
Next, the valve 17 and the valve 6 are opened, industrial water is sent to the first settling tank 1 through the pipe 6a, and the first settling tank 1 is washed for about 1 minute and washed. The valve 17, the valve 6, and the valve 7 are closed at the time when the process ends. In this state, the filter cloth washing wastewater can be newly fed to the first settling tank 1.

【0020】次に、バルブ8、及びバルブ9を開いてポ
ンプ15を作動させ、配管8a、及び9aを経由して第
二沈澱槽2の沈澱汚泥の初期攪拌が行われ、ほぼ2分後
に閉じられる。
Next, the valves 8 and 9 are opened, the pump 15 is operated, the sludge in the second settling tank 2 is initially stirred via the pipes 8a and 9a, and closed after about 2 minutes. To be

【0021】これに引き続き、バルブ18bが開かれ、
ポンプ15の作動により、第二沈澱槽2内の沈澱汚泥の
循環と攪拌が、排水管201を通過して行われ、同時に
第二沈澱槽2内の沈澱汚泥の輸送が、配管18aを経由
して脱水機3に給送され、再脱水が実施される。上記排
水管201の効果は、前記第一沈澱槽におけると同様で
ある。
Following this, the valve 18b is opened,
By the operation of the pump 15, circulation and agitation of the settled sludge in the second settling tank 2 is performed through the drain pipe 201, and at the same time, the transport of the settled sludge in the second settling tank 2 is performed via the pipe 18a. Is fed to the dehydrator 3 and re-dehydrated. The effect of the drainage pipe 201 is similar to that in the first settling tank.

【0022】続いて、プレッシャースイッチ16の作動
により、ポンプ15の運転が止められると、バルブ11
が閉じられる。
Subsequently, when the operation of the pump 15 is stopped by the operation of the pressure switch 16, the valve 11
Is closed.

【0023】しかる後、バルブ6、及びバルブ8が開か
れて工業用水による第二沈澱槽2の洗浄が行われ、ほぼ
1分間の洗浄の終了とともにバルブ6、及びバルブ8が
閉じられる。
Thereafter, the valves 6 and 8 are opened to wash the second precipitation tank 2 with industrial water, and the valves 6 and 8 are closed when the washing for about 1 minute is completed.

【0024】この処理工程において、バルブ18、バル
ブ19、及びバルブ20は常時開かれ、第一沈澱槽1、
及び第二沈澱槽2の底に設けられたバルブ23、及びバ
ルブ24は、ドレーン抜き以外は常時閉じられている。
又、21は流量調整用に設けられたバルブであり、22
は空気の吹き込み時に開かれるバルブである。
In this processing step, the valve 18, the valve 19 and the valve 20 are always opened, and the first settling tank 1,
The valves 23 and 24 provided at the bottom of the second precipitation tank 2 are always closed except for the drain drain.
Further, 21 is a valve provided for adjusting the flow rate, and 22
Is a valve that opens when air is blown in.

【0025】以上により、本発明の汚泥廃水処理装置に
よる、濾布洗浄廃水の汚泥処理の1サイクルが終了され
る。
As described above, one cycle of sludge treatment of the filter cloth washing wastewater by the sludge wastewater treatment apparatus of the present invention is completed.

【0026】図2は、本発明の汚泥廃水処理装置の排水
部の一例を示す平面図であり、図3は図2のA部の拡大
裏面図である。図2、及び図3において、30は第一沈
澱槽1、或いは第二沈澱槽2の側壁であり、31は平坦
な平底である。
FIG. 2 is a plan view showing an example of a drainage section of the sludge wastewater treatment apparatus of the present invention, and FIG. 3 is an enlarged rear view of section A of FIG. 2 and 3, 30 is a side wall of the first precipitation tank 1 or the second precipitation tank 2, and 31 is a flat flat bottom.

【0027】40は平底部に設けられた排水管であり、
この排水管40は、センターに設けられた主管41と、
この主管41より両側に分岐して交互に千鳥に配列して
設けられた有孔管42、42a、・42c、及び43、
43a、・・43dにより構成されている。
Reference numeral 40 is a drainage pipe provided at the flat bottom,
The drain pipe 40 includes a main pipe 41 provided at the center,
Perforated pipes 42, 42a, 42c, and 43, which are branched from the main pipe 41 on both sides and arranged alternately in a staggered manner,
.. 43d.

【0028】上記有孔管の数は限定されないが、沈澱汚
泥を効率よく排出するために左右ほぼ同数設けられるの
が好ましい。又、有孔管42、42a、・42c、及び
43、43a、・・43dの裏側には、図3に示すよう
に排水孔44が穿設されて、沈澱汚泥の排水がなされる
ようになっている。
Although the number of the perforated pipes is not limited, it is preferable that the left and right pipes are provided in the same number in order to efficiently discharge the settled sludge. Further, as shown in FIG. 3, drainage holes 44 are bored on the back side of the perforated pipes 42, 42a, 42c and 43, 43a, 43d so that the settled sludge is drained. ing.

【0029】32は給水口であり、この給水口32より
上記説明の沈澱汚泥が供給されるようになっている。3
3は排水口であり、この排水口33は、第一沈澱槽1の
場合には、ポンプ15により第一沈澱槽1へ配管接続さ
れ、第二沈澱槽の場合には、ポンプ15により脱水機3
に沈澱汚泥が給送されるようになっている。
Reference numeral 32 denotes a water supply port through which the settled sludge described above is supplied. Three
Denoted at 3 is a drain port, and this drain port 33 is connected to the first settling tank 1 by a pump 15 in the case of the first settling tank 1, and in the case of the second settling tank, the pump 15 makes the dehydrator. Three
Settled sludge is now being delivered to.

【0030】50は排水管40の支持台であり、この支
持台50の上面の主管41に当接する位置までの高さ
は、ほぼ50ミリメートルとなっており、主管41は締
結バンド51により支持台50に締結されて固定されて
いる。
Reference numeral 50 is a support for the drain pipe 40, and the height of the upper surface of the support 50 up to the position where it abuts the main pipe 41 is about 50 mm. The main pipe 41 is supported by the fastening band 51. It is fastened and fixed to 50.

【0031】図3において、本実施例では、主管41と
有孔管42bには塩化ビニル樹脂管が用いられている。
有孔管42bは主管41よりほぼ直角に突き出して設け
られた接続分岐41aに挿入されて接着材により固着さ
れている。
In FIG. 3, a vinyl chloride resin pipe is used for the main pipe 41 and the perforated pipe 42b in this embodiment.
The perforated pipe 42b is inserted into a connection branch 41a provided so as to protrude from the main pipe 41 at a substantially right angle, and is fixed by an adhesive material.

【0032】上記有孔管42bの外径は50〜70ミリ
メートル程度が好適であり、又、適宜間隔で穿設された
排水孔の直径は、本実施例においては12ミリメートル
となっているが、8〜15ミリメートルが好適に用いら
れる範囲である。
The outer diameter of the perforated pipe 42b is preferably about 50 to 70 mm, and the diameter of the drain holes formed at appropriate intervals is 12 mm in this embodiment. A range of 8 to 15 mm is preferably used.

【0033】[0033]

【発明の効果】本発明の汚泥廃水処理装置においては、
沈澱槽の平底部の沈澱汚泥を効率よく攪拌し排出させる
ために、排水孔が穿設された有孔管が分散配置された排
水管が設けられることにより、沈澱汚泥層に上澄み液に
よるみず道ができて沈澱汚泥が沈澱槽の底に滞留したま
まとなるのを防止し、効率よく継続的に汚泥分を抜き出
すとともに、上澄み液を放流することができる。従っ
て、汚泥廃水処理装置として好適である。
According to the sludge wastewater treatment apparatus of the present invention,
In order to efficiently stir and discharge the settled sludge at the flat bottom of the settling tank, a drainage pipe with dispersed perforated pipes with drainage holes is provided, so that the sedimented sludge layer can be treated by the supernatant liquid. As a result, it is possible to prevent the settled sludge from staying at the bottom of the settling tank, efficiently and continuously withdraw sludge, and to discharge the supernatant liquid. Therefore, it is suitable as a sludge wastewater treatment device.

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

【図1】本発明の汚泥廃水処理装置の一例を示す装置全
体のフローチャート。
FIG. 1 is a flowchart of the entire apparatus showing an example of a sludge wastewater treatment apparatus of the present invention.

【図2】本発明の汚泥廃水処理装置の排水管の一例を示
す平面図。
FIG. 2 is a plan view showing an example of a drainage pipe of the sludge wastewater treatment device of the present invention.

【図3】図2のA部の拡大裏面図。FIG. 3 is an enlarged back view of a portion A of FIG.

【符号の説明】[Explanation of symbols]

1 第一沈澱槽 2 第二沈澱槽 101、201 排水管 3 脱水機 4 濾布洗浄廃水槽 5 水中ポンプ 6、7、8、9、10、11、12、13、17、1
8、19、20、21 22 バルブ 14 側溝 15 ポンプ 16 プレッシャースイッチ 30 側壁 31 平底 32 給水口 33 排水口 40 排水管 41 主管 42、43 有孔管 50 支持台 51 締結バンド
1 1st settling tank 2 2nd settling tank 101, 201 Drain pipe 3 Dehydrator 4 Filter cloth washing waste water tank 5 Submersible pump 6, 7, 8, 9, 10, 11, 12, 13, 17, 1
8, 19, 20, 21 22 Valve 14 Gutter 15 Pump 16 Pressure switch 30 Side wall 31 Flat bottom 32 Water inlet 33 Drainage port 40 Drain pipe 41 Main pipe 42, 43 Perforated pipe 50 Support base 51 Fastening band

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 廃水の汚泥の沈澱処理を行う沈澱槽の平
底部に、沈澱汚泥の排出用の排水孔の穿設された有孔管
が分散配置された沈澱汚泥排出用の排水管が設けられ、
上記沈澱槽と排水管がポンプを経由する循環経路により
接続されていることを特徴とする汚泥廃水処理装置。
1. A drainage pipe for discharging settling sludge, in which perforated pipes having drainage holes for discharging settling sludge are dispersedly arranged in a flat bottom of a settling tank for treating sludge of wastewater. The
A sludge wastewater treatment device, wherein the settling tank and the drainage pipe are connected by a circulation path via a pump.
JP6141450A 1994-06-23 1994-06-23 Sludge waste water treatment apparatus Pending JPH08913A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6141450A JPH08913A (en) 1994-06-23 1994-06-23 Sludge waste water treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6141450A JPH08913A (en) 1994-06-23 1994-06-23 Sludge waste water treatment apparatus

Publications (1)

Publication Number Publication Date
JPH08913A true JPH08913A (en) 1996-01-09

Family

ID=15292206

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6141450A Pending JPH08913A (en) 1994-06-23 1994-06-23 Sludge waste water treatment apparatus

Country Status (1)

Country Link
JP (1) JPH08913A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1584609A1 (en) * 2004-04-06 2005-10-12 H.H. Ide A method and a plant for producing a liquid fertilizer from slurry manure
GB2436730B (en) * 2006-03-31 2009-08-19 Siemens Ag A method for producing a superconducting magnet coil and a magnetic resonance apparatus
CN114632374A (en) * 2022-03-03 2022-06-17 呼伦贝尔安泰热电有限责任公司海拉尔热电厂 Efficient treatment equipment for coal-containing wastewater

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1584609A1 (en) * 2004-04-06 2005-10-12 H.H. Ide A method and a plant for producing a liquid fertilizer from slurry manure
GB2436730B (en) * 2006-03-31 2009-08-19 Siemens Ag A method for producing a superconducting magnet coil and a magnetic resonance apparatus
CN114632374A (en) * 2022-03-03 2022-06-17 呼伦贝尔安泰热电有限责任公司海拉尔热电厂 Efficient treatment equipment for coal-containing wastewater
CN114632374B (en) * 2022-03-03 2023-07-14 呼伦贝尔安泰热电有限责任公司海拉尔热电厂 High-efficient treatment facility of coal-containing waste water

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