JPS6150610A - Apparatus for treating waste water - Google Patents

Apparatus for treating waste water

Info

Publication number
JPS6150610A
JPS6150610A JP17090384A JP17090384A JPS6150610A JP S6150610 A JPS6150610 A JP S6150610A JP 17090384 A JP17090384 A JP 17090384A JP 17090384 A JP17090384 A JP 17090384A JP S6150610 A JPS6150610 A JP S6150610A
Authority
JP
Japan
Prior art keywords
wastewater
tank
water
treatment
treatment 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.)
Granted
Application number
JP17090384A
Other languages
Japanese (ja)
Other versions
JPH0555162B2 (en
Inventor
Toru Matsuoka
松岡 通
Minoru Takayasu
稔 高安
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP17090384A priority Critical patent/JPS6150610A/en
Publication of JPS6150610A publication Critical patent/JPS6150610A/en
Publication of JPH0555162B2 publication Critical patent/JPH0555162B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5281Installations for water purification using chemical agents

Abstract

PURPOSE:To efficiently treat a suspended floating substance to a tolerant level, by arranging a partition cylinder in a treatment tank having a treating water introducing port and a treated water flooding port at the upper end part thereof and a precipitated suspended floating substance discharge port at the lower end part thereof. CONSTITUTION:Waste water is introduced into the upper part of a sedimentation pipe 8 from an introducing port 1 and a precipitated and separated suspended floating substance is accumulated in the vicinity of a discharge port 3 and discharged through a discharge pipe 10 according to necessity. Treated water is withdrawn from the flooding port 2 provided to the uppermost part of a water stream reversal rising region 7. Waste water is moved downwardly and passed between the suspended low end part of a partition cylinder 6 and the lower end part of a treatment tank 4 and reversed in its flow direction to rise. The floating substance does not pass through the drilled holes 9 provided to the peripheral wall of the sedimentation pipe 8 and moves gradually to the lower direction to be precipitated along the inclined surface of the lower end part of the treatment tank 4.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は廃水処理装置に係り、特に種々の性状の懸濁浮
遊物を含む廃水を静置状態で固液分離方式により処理す
る廃水処理装置に関する。
Detailed Description of the Invention (Industrial Application Field) The present invention relates to a wastewater treatment device, and particularly to a wastewater treatment device that treats wastewater containing suspended solids of various properties by a solid-liquid separation method in a stationary state. Regarding.

(従来技術の問題点) 従来廃水を簡便に処理する装置としては,比重差を利用
して沈澱池等で固体物を沈降分離するものまたはこれに
バックルやフィルタ等を組合わせたもの等種々の形式の
装置が広く知られている。
(Problems with the prior art) Conventionally, there are various types of devices that can easily treat wastewater, such as those that use the difference in specific gravity to settle and separate solids in a sedimentation tank or the like, or those that combine this with buckles, filters, etc. This type of device is widely known.

しかし、被処理水が比較的粒径の小さな種々の懸濁浮遊
物を含む場合にはこのような従来の装置ではその分離が
必ずしも容易ではなかった.さらに懸濁浮遊物の種類に
応じて種々の構成の装置を使い分けなければならず、か
つ実用」;充分な処理効果を挙げるためには装置が大規
模化し設備や維持コストが増大する場合が多い。
However, when the water to be treated contains various suspended solids with relatively small particle sizes, it is not always easy to separate them using such conventional equipment. Furthermore, it is necessary to use equipment with various configurations depending on the type of suspended solids, and in order to achieve sufficient treatment effects, the equipment often becomes large-scale and equipment and maintenance costs increase. .

(発明の目的) 本発明の目的はこのような従来技術の欠点を解消し、種
々の懸濁浮遊物を含む廃水を簡便な構造により許容でき
るレベルまで効率的に処理することのできる廃水処理装
置を提供することにある。
(Object of the Invention) The object of the present invention is to provide a wastewater treatment device that eliminates the drawbacks of the prior art and can efficiently treat wastewater containing various suspended solids to an acceptable level with a simple structure. Our goal is to provide the following.

(発明の構成) 前記目的を達成するための本発明の廃水処理装置は被処
理水の導入口および処理後の排水の溢瀉口を夫々上端部
に有しかつ被処理水から沈降、分離された懸濁浮遊物の
排出口を下端部に有する処理槽と、前記処理槽の内部の
上端部から下端部にわたって垂設され槽の内部を被処理
水の沈降領域と該沈降領域に下端部付近で連通ずる処理
後の水流の反転上昇域とに仕切区分する仕切筒と、前記
仕切筒の内部に径方向の間隙をもってほぼ同心的に重設
され一ヒ端部が前記廃水の導入口に接続され下端部が前
記懸濁浮遊物の排出口側に開口されζ かつ周壁に多数の透孔を形成された沈降パイプとを備え
ていることを特徴とする。
(Structure of the Invention) To achieve the above object, the wastewater treatment apparatus of the present invention has an inlet for treated water and an overflow port for treated wastewater at the upper end thereof, and the wastewater treatment apparatus has an inlet for treated water and an overflow port for treated wastewater, and the wastewater treatment apparatus has an inlet for treated water and an overflow port for treated wastewater. a treatment tank having a discharge port for suspended solids at its lower end; and a treatment tank that is vertically disposed from the upper end to the lower end of the inside of the treatment tank, and the inside of the tank is connected to a settling area of the water to be treated, and a part near the lower end of the settling area. A partition tube that partitions into a reversal and rising region of the water flow after treatment, and a partition tube that is installed almost concentrically with a radial gap inside the partition tube, and one end is connected to the wastewater inlet. The settling pipe is characterized in that the lower end thereof is opened toward the discharge port side of the suspended solids, and the settling pipe has a peripheral wall formed with a large number of through holes.

(発明の実施例) 前記本発明のさらに具体的な構成ならびにそれに基いて
得られる作用効果を以下図面に示す実施例に基いてさら
に詳細に説明する。
(Embodiments of the Invention) More specific configurations of the present invention and the effects obtained based thereon will be explained in more detail below based on embodiments shown in the drawings.

第1図および第2図は夫々本発明に係る廃水処理装置の
一実施例の概要を示す」−面図および縦断面図である。
FIG. 1 and FIG. 2 are a plan view and a longitudinal cross-sectional view, respectively, showing an outline of an embodiment of a wastewater treatment apparatus according to the present invention.

図中、断面円形の竪形の円筒型の処理槽4は後述するよ
うに上端部の導入口1から処理される廃木を導入し、槽
中で沈降、分離された廃水中の懸濁浮遊物を下端部の排
出口3から濃縮スラリの形態として排出すると共に、処
理された排水を上端部の溢流口2から外部に放出するよ
うになされている。
In the figure, a vertical cylindrical treatment tank 4 with a circular cross section introduces waste wood to be treated from an inlet 1 at the upper end as described later, and the waste wood is suspended and suspended in wastewater that is settled and separated in the tank. Materials are discharged in the form of concentrated slurry from a discharge port 3 at the lower end, and treated wastewater is discharged to the outside from an overflow port 2 at the upper end.

前記処理槽4の内部にはその上端部から下端部にかけて
断面円形の円筒型の仕切筒6をほぼ垂直に垂設し処理槽
4の内部を廃水の沈降領域5と処理後の排水の反転上昇
域7とに区分するようにな       1されている
Inside the treatment tank 4, a cylindrical partition tube 6 with a circular cross section is vertically installed from the upper end to the lower end, and the inside of the treatment tank 4 is divided into a sedimentation area 5 for wastewater and an inversion and rise area for wastewater after treatment. It is divided into 7 regions and 1.

前記仕切筒6の垂設下端部は前記処理槽4の下端部の懸
濁浮遊物の排出口3側に開口している。
The lower end of the partition tube 6 is opened toward the discharge port 3 of the suspended solids at the lower end of the processing tank 4 .

この垂設下端部の開口縁部は処理槽4の下端部の周壁に
対して所定の間隙りを介して対向させてあり、仕切筒6
の内部に形成された沈降領域5を通して下降する水流を
間隙りを通して反転上昇させ仕切板6の外側の排水の反
転上昇域7中を処理槽4の上端部に向けて上昇させるよ
うになされている。
The opening edge of this hanging lower end is opposed to the peripheral wall of the lower end of the processing tank 4 with a predetermined gap therebetween, and the partition tube 6
The water flow that descends through the sedimentation area 5 formed inside the tank is reversely raised through the gap, and is caused to rise in the drainage reversal and rise area 7 outside the partition plate 6 toward the upper end of the treatment tank 4. .

ここで前記仕切筒6の垂設下端部に対して間隙りをもっ
て対向している処理槽4の周壁は」1方に向って所定の
角度で傾斜されている。
Here, the peripheral wall of the processing tank 4, which faces the vertical lower end of the partition tube 6 with a gap therebetween, is inclined at a predetermined angle in one direction.

さらに、前記仕切筒6の内部にはこれも断面円形の円筒
状の沈降パイプ8を仕切筒に対して径方向の間隙をもっ
て同心状に垂設し、その上端部に前記廃水の導入口lを
接続し、その下端部は前記仕切筒6の下端部と同様にし
て懸濁浮遊物の排出口3側に開口させである。この沈降
パイプ8の周面には多数の透孔9.9112.を適宜な
上下方向および周方向のピッチで穿設して、そのパイプ
内部の流域を前記仕切筒6の内部に形成された沈降領域
5と流通させるようになされている。
Further, inside the partition tube 6, a cylindrical settling pipe 8 also having a circular cross section is vertically disposed concentrically with a radial gap with respect to the partition tube, and the waste water inlet 1 is connected to the upper end of the settling pipe 8. The lower end thereof is opened to the suspended matter discharge port 3 side in the same way as the lower end of the partition tube 6. The peripheral surface of this settling pipe 8 has a large number of through holes 9.9112. are bored at appropriate pitches in the vertical and circumferential directions so that the basin inside the pipe communicates with the settling region 5 formed inside the partition tube 6.

さらに、本発明の図示の実施例においては前記処理槽4
の下端部の濃縮スラリーの排出口3に対して排出管10
を接続し、処理槽4の側壁に沿ってほぼその上端部まで
立上げである。排出管10の上方の排出端部IQAは可
撓性の大きなプラスチック管等で形成され、これを屈曲
することによって処理槽4の水面に対する排出管上端部
の相対的な高さを調節できるようになされている。10
Bは排出管の支持部材である。
Furthermore, in the illustrated embodiment of the present invention, the treatment tank 4
Discharge pipe 10 for concentrated slurry discharge port 3 at the lower end of
is connected and raised along the side wall of the processing tank 4 almost to its upper end. The upper discharge end IQA of the discharge pipe 10 is formed of a large flexible plastic pipe or the like, and by bending it, the relative height of the upper end of the discharge pipe with respect to the water surface of the treatment tank 4 can be adjusted. being done. 10
B is a support member for the discharge pipe.

(作用および効果) 前記第1図および第2図に示す廃水処理装置で懸濁浮遊
物を含む廃水を処理する際には、廃水を導入口1から処
理槽4内の沈降パイプ8の上部に徐々に注入する。処理
の進行中には廃水から沈降、分離された懸濁浮遊物が処
理槽4の下端部の排出口3付近に蓄積され必要に応じて
排出管10を通して排出される。一方処理後の排水は処
理槽4の水流の反転上昇域7の最上部に設けられた溢流
口2からi![!統帥に引抜かれる。
(Functions and Effects) When treating wastewater containing suspended solids with the wastewater treatment apparatus shown in FIGS. Inject gradually. During the progress of the treatment, suspended solids settled and separated from the wastewater are accumulated near the discharge port 3 at the lower end of the treatment tank 4 and are discharged through the discharge pipe 10 as necessary. On the other hand, the treated wastewater is discharged from the overflow port 2 provided at the top of the water flow reversal and rise area 7 of the treatment tank 4. [! He is pulled out by the commander.

ここで前記仕切筒6の沈降領域5中の廃水は沈降パイプ
8の上部から絶えず注入される廃水によって徐々に下方
に移動し、仕切筒6の垂設下端部の周縁と処理槽4の下
端部との間の間隙りを通して流れの方向を反転し、仕切
筒6の外部と処理槽4との間の水流の上昇域7に入る。
Here, the wastewater in the settling area 5 of the partition tube 6 is gradually moved downward by the waste water continuously injected from the upper part of the settling pipe 8, and the periphery of the hanging lower end of the partition tube 6 and the lower end of the treatment tank 4 are gradually moved downward. The direction of the flow is reversed through the gap between the two, and the water enters the rising region 7 between the outside of the partition tube 6 and the treatment tank 4.

上昇域7に入った木は沈降パイプ8に連続的に注入され
る廃水の水圧によって上昇し、最上端部の溢流口2から
処理済の排水として引抜かれる。
The wood that has entered the rising area 7 is raised by the water pressure of wastewater continuously injected into the settling pipe 8, and is pulled out as treated wastewater from the overflow port 2 at the top end.

一方、この廃水中に含まれている懸濁浮遊物は導入口l
から沈降パイプ8の上部に注入される廃水の下方への移
動にともなって沈降領域5中を下方に運ばれるが、この
場合、処理槽4の容量(本実施例では約12m3)を注
入される廃水の量(たとえば、20017分)に比較し
て十分に大きくしておけば沈降領域5中の廃水の下降速
度は極めて緩やかになる。そして、特に沈降パイプ8に
注入された廃水の中の大部分の流れがパイプ周壁に穿設
された透孔9を通して一旦仕切筒6との間の間隙に水平
方向に排出されてから筒内を降下する経路をとるので、
沈降領域5を降下する懸濁浮遊物は全体として比較的長
い流路を長時間にわたって徐々に下方に移動する。そし
て仕切筒6の下端部に至ると、はとんどの懸濁浮遊物が
水から分離されて排出口3の付近に沈積する。
On the other hand, the suspended solids contained in this wastewater are
As the wastewater is injected into the upper part of the settling pipe 8, it is transported downward through the settling area 5, but in this case, the capacity of the treatment tank 4 (approximately 12 m3 in this example) is injected. If the amount is made sufficiently large compared to the amount of wastewater (for example, 20017 minutes), the descending speed of the wastewater in the settling region 5 will be extremely slow. In particular, most of the wastewater injected into the settling pipe 8 passes through a through hole 9 drilled in the peripheral wall of the pipe and is once discharged horizontally into the gap between it and the partition cylinder 6, and then flows into the cylinder. Since it takes a descending route,
The suspended solids descending through the sedimentation region 5 gradually move downward over a long period of time through a relatively long flow path as a whole. When reaching the lower end of the partition tube 6, most of the suspended solids are separated from the water and deposited near the discharge port 3.

ここで粒径の小さな一部の懸濁浮遊物は仕切筒6の垂設
下端部で間隙りを通して反転上昇する排水にともなわれ
て浮上しようとするが、開口面積の狭い間隙りからより
広い反転上昇域7に出る際に浮遊懸濁物はほとんど運動
エネルギを失ない、大部分のものが処理槽4の下端部の
傾斜面に沿って再び排出口3に沈積する。その後、反転
上昇域7を排水と共に上昇する間にその中に含まれてい
る残余の懸濁浮遊物の相当量の部分がさらに沈降し、上
昇域7の最上端の溢流口2から引抜かれる処理後の排水
に残存する懸濁浮遊物はその粒径にして約300メツシ
ユより小さなもののみとなる。
Here, some of the suspended solids with a small particle size try to float up along with the drainage that reverses and rises through the gap at the lower end of the partition tube 6, but from a gap with a narrow opening area to a wider The floating suspended matter loses almost no kinetic energy when exiting the inversion and rise region 7, and most of it is deposited again at the discharge port 3 along the slope at the lower end of the treatment tank 4. Thereafter, while rising in the inversion rising area 7 along with the drainage water, a considerable portion of the remaining suspended solids contained therein further settles and is drawn out from the overflow port 2 at the top end of the rising area 7. The suspended solids remaining in the wastewater after treatment are only particles smaller than about 300 mesh in particle size.

本実施例においては前記装置仕様および処理条件で、S
S濃度約200ppmの廃水を連続的に処理した結果、
得られる処理後の排水のSS濃度は約20ppmに低下
する。
In this example, with the above device specifications and processing conditions, S
As a result of continuous treatment of wastewater with an S concentration of approximately 200 ppm,
The SS concentration of the resulting treated wastewater is reduced to about 20 ppm.

一方、廃水から沈降、分離されて処理槽4の下端部の排
出口3に沈積した懸濁浮遊物は槽内の水圧に押されて排
出管10中を通って上昇し、処理槽4の水面の高さ付近
に位置された排出端部10Aから濃縮スラリーの形態と
して槽外に排出される。
On the other hand, the suspended solids that have been sedimented and separated from the wastewater and deposited at the discharge port 3 at the lower end of the treatment tank 4 are pushed by the water pressure in the tank and rise through the discharge pipe 10 to rise to the water surface of the treatment tank 4. The concentrated slurry is discharged to the outside of the tank from the discharge end 10A located near the height of the slurry.

ここで、たとえば廃水処理作業中において排出端部1O
Aの高さを処理槽4の水面より高くしておけばスラリは
排出されず、また所望の時期にこの可撓性の排出端部1
0Aを下方に屈曲させてその高さを水面以下に下げるこ
とにより管内の濃厚なスラリか槽外に排出される。この
場合、下方の排出管10を支持部材10Bから取外して
排出端部10Aの高さを大幅に下げれば槽内の沈積物が
廃水と共に一挙に排出されて処理槽4内が簡単に清掃さ
れる・このように本発明の実施例においては、処理槽4
に注入される廃水を仕切筒6によって槽内に区分して形
成された沈降領域5を通して降下させた後、仕切筒6の
垂設下端部と処理槽4の下端部との間の狭い間隙りを通
して反転上昇域7の溢流口2側に反転上昇させるように
しであるので、廃水中に含まれる懸濁浮遊物はこの廃水
の沈降、」1昇の間に固液分離されて槽底に沈積する。
Here, for example, during wastewater treatment work, the discharge end 1O
If the height of A is set higher than the water surface of the treatment tank 4, the slurry will not be discharged, and this flexible discharge end 1 can be removed at the desired time.
By bending 0A downward and lowering its height below the water surface, the thick slurry inside the pipe is discharged to the outside of the tank. In this case, if the lower discharge pipe 10 is removed from the support member 10B and the height of the discharge end 10A is significantly lowered, the deposits in the tank will be discharged at once together with the waste water, and the inside of the treatment tank 4 will be easily cleaned. - In this way, in the embodiment of the present invention, the processing tank 4
After the wastewater injected into the tank is allowed to fall through the settling area 5 formed by dividing the tank by the partition tube 6, a narrow gap between the hanging lower end of the partition tube 6 and the lower end of the treatment tank 4 is formed. As the wastewater is inverted and raised to the overflow port 2 side of the inversion and rise area 7 through the inversion rising area 7, the suspended solids contained in the wastewater are separated into solid and liquid during the sedimentation of this wastewater and are deposited at the bottom of the tank. Deposit.

そして特に本発明の実施例では前記仕切筒6の沈降領域
5中にさらに沈降パイプ8を設けてその周壁に穿設され
た多数の透孔9を介して廃水の流れを水平方向に変えて
沈降領域5中に流出させるようにしであるので、槽内で
の廃水の流路長が増大すると共に流れが極めて緩かでか
つ乱れのないものとなる。したがって、廃水中に含まれ
ている大部分の懸濁浮遊物を徐々に沈降、分離しながら
排出口3側に効率的に沈積させて廃水から分離すること
ができる。
Particularly, in the embodiment of the present invention, a settling pipe 8 is further provided in the settling area 5 of the partition tube 6, and the flow of wastewater is changed horizontally through a large number of through holes 9 bored in the peripheral wall of the settling pipe 8, and the wastewater is allowed to settle. Since the waste water is allowed to flow out into the region 5, the flow path length of the waste water in the tank is increased, and the flow is extremely slow and undisturbed. Therefore, most of the suspended solids contained in the wastewater can be gradually settled and separated, efficiently deposited on the discharge port 3 side, and separated from the wastewater.

さらに本実施例でな前記処理槽4の下端部の懸濁浮遊物
の排出口にサイフオン式の排出管10を接続しであるの
で、沈積した固体物を極めて簡単に槽外に排出回収する
ことができる。すなわちこの排出管10の上端部の高さ
を処理槽内の水面より幾分低くしておけば水圧によって
沈澱した固体物を常時連続的に排出することができ、ま
た固体含有分が比較的少ない廃水の場合では必要な時だ
け排水管の高さを低くしてスラリを一時に排出させるこ
ともできる。このような調節は排出管端部10Aを可撓
性の大きな材質のもので形成するこにより容易にt+な
われる。さらに、排出管10全体を支持部10Bからは
ずして端部を大幅に引下げれば槽内の沈積物を廃水と共
に一挙に排出させることができ槽の清掃および保守が極
めて容易になる。
Furthermore, in this embodiment, a siphon-type discharge pipe 10 is connected to the discharge port of the suspended solids at the lower end of the treatment tank 4, so that the settled solids can be discharged and recovered from the tank very easily. I can do it. In other words, by setting the height of the upper end of the discharge pipe 10 to be somewhat lower than the water level in the treatment tank, the precipitated solids can be continuously discharged by water pressure, and the solid content is relatively small. In the case of wastewater, the height of the drain pipe can be lowered to discharge the slurry all at once only when necessary. Such adjustment can be easily achieved by forming the discharge pipe end 10A from a highly flexible material. Furthermore, if the entire discharge pipe 10 is removed from the support part 10B and the end is pulled down significantly, the deposits in the tank can be discharged all at once together with the waste water, making cleaning and maintenance of the tank extremely easy.

以トのように本発明の実施例は極めて簡単な構造によっ
て廃水中の懸濁浮遊物を長時間の静置を要することなく
連続的に沈降、分離させることができる。さらにこの実
施例においては、基本的にはその処理のために何等の化
学的ないしは生物化学的手段や運転のための動力を必要
とせず、したがって−置設nしたあとでは通常はとんど
保守、調整を要することがない。
As described above, the embodiments of the present invention are capable of continuously settling and separating suspended solids in wastewater with an extremely simple structure without requiring them to stand still for a long time. Moreover, this embodiment essentially does not require any chemical or biochemical means for its treatment or power for operation, and therefore - after installation, it usually requires little maintenance. , no adjustment is required.

本実施例では約200ppmの廃水のss濃度をその性
状、種類にはかかわりなく約20 PPIIに低下させ
ることができかつ約300メツシユまでの浮遊懸濁物を
ほとんど除くことができた。
In this example, the ss concentration of wastewater of about 200 ppm could be reduced to about 20 PPII regardless of its nature and type, and most of the suspended solids up to about 300 mesh could be removed.

しかし、本発明によればSSa度がさらに高い濃厚廃水
(たとえば、s s 10.000以上の畜産汚水等)
についても予じめこれを適宜に水で耗釈した後に前記処
理槽に導入することによって同様な固液分離処理を行な
うことができる。また廃水中に金属スラッジ等が含まれ
ていて凝集剤処理が必要な場合にはかかる処理を施こさ
れた後のフロック氷を同様にして前記実施例の処理槽で
処理することができる。
However, according to the present invention, concentrated wastewater with a higher SSa degree (for example, livestock sewage with an s s of 10.000 or more)
A similar solid-liquid separation treatment can also be carried out by preliminarily diluting this with water as appropriate and then introducing it into the treatment tank. Furthermore, if the wastewater contains metal sludge or the like and requires coagulant treatment, the flocculated ice after such treatment can be treated in the same manner as in the treatment tank of the above embodiment.

尚、前記実施例で処理された廃水は直接河川等への放流
を許容される程度のものであるが、本実施例はこれを土
砂等の除去を前提とする1−水1rI処理や微生物活性
を利用した廃水処理の前処理装置として用いると本来の
処理装置の負荷を著しく軽減させることができる。した
がって本発明は巾なる廃水の処理に限らず広く一般の水
処理に用いられるいわゆる固液分離装置ないしはシラフ
ナとして広範囲な用途を有する。          
       1以」一本発明を比較的小型でかつコン
パクトな円筒状の形状を有する一実施例について説明し
たが、もとより本発明は用途に応じてその他の種々の形
態として実施することができる。たとえば、前記処理槽
は第1図および第2図に示すような円筒状に限らず、断
面方形の角柱状としてもよい。この場合第1図における
処理槽4あるいは必要によっては仕切筒6、沈降パイプ
8等の断面を夫々互いに同心的な方形の形状に変更する
だけでよい。
The wastewater treated in the above example is of a level that allows direct discharge into rivers, etc., but in this example, it is treated with 1-water 1rI treatment that assumes the removal of sediment, etc., and microbial activation. When used as a pre-treatment device for wastewater treatment, the load on the original treatment device can be significantly reduced. Therefore, the present invention has a wide range of applications as a so-called solid-liquid separator or Shirafuna used not only in the treatment of wide-scale wastewater but also in general water treatment.
Although the present invention has been described with reference to an embodiment having a relatively small and compact cylindrical shape, the present invention can of course be implemented in various other forms depending on the application. For example, the processing tank is not limited to a cylindrical shape as shown in FIGS. 1 and 2, but may also have a prismatic shape with a square cross section. In this case, it is only necessary to change the cross sections of the processing tank 4 in FIG. 1 or, if necessary, the partition tube 6, settling pipe 8, etc., to concentric rectangular shapes.

さらにまた、沈降パイプに穿設する透孔の形状、大きさ
および配設ピッチならびに処理槽下端部の間隙りや傾斜
角度等も必要に応じて種々の寸法、形状に設計すること
ができる。
Furthermore, the shape, size, and arrangement pitch of the through holes drilled in the settling pipe, as well as the gap and inclination angle of the lower end of the processing tank, etc., can be designed to have various dimensions and shapes as necessary.

第3図および第4図に比較的大容量の工場廃水の処理に
適した本発明の別の実施例を示す。
FIGS. 3 and 4 show another embodiment of the invention suitable for treating relatively large volumes of industrial wastewater.

第3図および第4図の実施例中に示す各部分の中、前記
第1図および第2図に対応する符号で示したものは夫々
前記実施例において説明したのと同一の機能を有してい
る0本実施例では、仕切筒6と処理槽4との間に形成さ
れる水流の反転上昇域が隔離板11によって比較的面積
の大きな捕集域12および排水取出域13に区分され捕
集域12にはシュータ14が設けられている。
Among the parts shown in the embodiments of FIGS. 3 and 4, those indicated by the reference numerals corresponding to those in FIGS. 1 and 2 have the same functions as explained in the embodiments, respectively. In this embodiment, the water flow reversal and rise region formed between the partition tube 6 and the treatment tank 4 is divided by the separator 11 into a collection region 12 and a wastewater extraction region 13, each having a relatively large area. A shooter 14 is provided in the catchment area 12.

ここで導入された廃水を仕切筒6および沈降パイプ8等
により処理し、かつ沈降、分離したスラリを取出す態様
は前記第1図および第2図に示した実施例の場合と基本
的には同一である。
The manner in which the introduced wastewater is treated by the partition tube 6 and the settling pipe 8, etc., and the sedimented and separated slurry is taken out is basically the same as in the embodiment shown in FIGS. 1 and 2. It is.

第3図および第4図の実施例ではほとんどの懸濁浮遊物
の分離後に間隙りから反転−h昇する廃水はまず捕集域
12の下方に導かれる。ここで廃水中に含有されていた
比重の小さな木屑および場合によっては油類等が急速に
浮上して捕集域12の水面に集められシュータ14を通
して槽外に排出処理される。廃水はさらに徐々に上昇し
て廃水取出域13に至り溢泣口15から排出される。
In the embodiment of FIGS. 3 and 4, the waste water rising from the gap after separation of most of the suspended solids is first directed below the collection zone 12. Here, wood chips with a small specific gravity and, in some cases, oil, etc. contained in the wastewater rapidly float to the surface, are collected on the water surface of the collection area 12, and are discharged to the outside of the tank through the chute 14. The wastewater further gradually rises to reach the wastewater extraction area 13 and is discharged from the overflow spout 15.

本実施例は廃水の処理量が大きく、殊に木屑や油類等の
比較的比重の小さな浮遊物を多量に含む工場廃水の処理
用途に適している。
This embodiment can treat a large amount of wastewater, and is particularly suitable for treating factory wastewater containing a large amount of floating matter with relatively low specific gravity such as wood chips and oils.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例の」−面図、第2図は前記実
施例の縦断面図、第3図は本発明の別の実施例の」二面
図、第4図は前記実施例の縦断面図である。 169.廃水の導入口  298.廃水の溢流口391
.沈積物の排出口 410.処理槽501.沈降領域 
   690.仕切筒700.水波の反転上昇域 810.沈降パイプ   909.透孔10、、、損出
管 特許出願人  松  岡    通 量        高  安     稔第3図 第4図 シ4  。 1−、   −” −’l−″ −[ 4:i:l  6 A I葺17(へ ”IOB
FIG. 1 is a top view of one embodiment of the present invention, FIG. 2 is a vertical sectional view of the embodiment, FIG. 3 is a two-sided view of another embodiment of the invention, and FIG. 4 is a top view of the embodiment. FIG. 3 is a longitudinal cross-sectional view of the embodiment. 169. Wastewater inlet 298. Wastewater overflow port 391
.. Sediment outlet 410. Processing tank 501. Sedimentation area
690. Partition tube 700. Reversal and rise area of water waves 810. Settling pipe 909. Through hole 10... Loss and output pipe patent applicant: Michiru Matsuoka, Minoru Takayasu, Figure 3, Figure 4, C4. 1-, -"-'l-" -[ 4:i:l 6 A Ibuki 17 (to"IOB

Claims (3)

【特許請求の範囲】[Claims] (1)被処理水の導入口および処理後の排水の溢流口を
夫々上端部に有しかつ被処理水から沈降、分離された懸
濁浮遊物の排出口を下端部に有する処理槽と、前記処理
槽の内部の上端部から下端部にわたつて垂設され槽の内
部を被処理水の沈降領域と該沈降領域に下端部付近で連
通する処理後の水流の反転上昇域とに仕切区分する仕切
筒と、前記仕切筒の内部に径方向の間隙をもつてほぼ同
心的に垂設され上端部が前記廃水の導入口に接続され下
端部が前記懸濁浮遊物の排出口側に開口されかつ周壁に
多数の透孔を形成された沈降パイプとを備えていること
を特徴とする廃水処理装置。
(1) A treatment tank having an inlet for treated water and an overflow port for treated wastewater at the upper end, and an outlet for suspended matter that has settled and separated from the treated water at the lower end. , which is installed vertically from the upper end to the lower end of the treatment tank and partitions the inside of the tank into a settling region of the water to be treated and a reversal rising region of the water flow after treatment, which communicates with the settling region near the lower end. a partition tube for partitioning, and a partition tube that is vertically disposed substantially concentrically with a radial gap inside the partition tube, with an upper end connected to the wastewater inlet and a lower end facing the suspended solids discharge port. 1. A wastewater treatment device comprising: a settling pipe which is open and has a number of through holes formed in its surrounding wall.
(2)前記処理槽の懸濁浮遊物の排出口に排出端の高さ
を調節可能とした排出管を接続したことを特徴とする前
記特許請求の範囲第1項記載の廃水処理装置。
(2) The wastewater treatment apparatus according to claim 1, characterized in that a discharge pipe whose height at the discharge end is adjustable is connected to the discharge port of the suspended solids in the treatment tank.
(3)前記仕切筒の垂設下端部に対して連通間隙を介し
て対向する前記処理槽の下端部の槽壁が上方に向けて所
定の角度で傾斜されていることを特徴とする前記特許請
求の範囲第1項記載の廃水処理装置。
(3) The above-mentioned patent characterized in that the tank wall at the lower end of the processing tank, which faces the vertical lower end of the partition tube through a communication gap, is inclined upward at a predetermined angle. A wastewater treatment device according to claim 1.
JP17090384A 1984-08-16 1984-08-16 Apparatus for treating waste water Granted JPS6150610A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17090384A JPS6150610A (en) 1984-08-16 1984-08-16 Apparatus for treating waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17090384A JPS6150610A (en) 1984-08-16 1984-08-16 Apparatus for treating waste water

Publications (2)

Publication Number Publication Date
JPS6150610A true JPS6150610A (en) 1986-03-12
JPH0555162B2 JPH0555162B2 (en) 1993-08-16

Family

ID=15913468

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17090384A Granted JPS6150610A (en) 1984-08-16 1984-08-16 Apparatus for treating waste water

Country Status (1)

Country Link
JP (1) JPS6150610A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5800715A (en) * 1994-02-16 1998-09-01 Baker Hughes Incorporated Separation of a suspension into its component parts
JP2006263670A (en) * 2005-03-25 2006-10-05 Nishihara Environment Technology Inc Solid-liquid separator
JP2012066233A (en) * 2010-09-21 2012-04-05 Torao Inoue Device for removing precipitate in water tank
WO2012139201A1 (en) * 2011-04-12 2012-10-18 Norcan Water Resources Inc. Inlet tube for producing laminar flow in a sedimentation vessel

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4526055Y1 (en) * 1965-07-26 1970-10-12
JPS4726569U (en) * 1971-04-20 1972-11-25
JPS499765A (en) * 1972-05-27 1974-01-28
JPS575896U (en) * 1980-06-12 1982-01-12
JPS58183912A (en) * 1982-04-22 1983-10-27 Kawasaki Steel Corp Precipitation basin
JPS5926108A (en) * 1982-08-02 1984-02-10 Oji Paper Co Ltd Apparatus for concentrating slurry

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5246165A (en) * 1975-10-07 1977-04-12 Nagata Seiki Kk Jacquard pattern socks product for flat pearl round hosiery knitting machine* method and device for producing same

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4526055Y1 (en) * 1965-07-26 1970-10-12
JPS4726569U (en) * 1971-04-20 1972-11-25
JPS499765A (en) * 1972-05-27 1974-01-28
JPS575896U (en) * 1980-06-12 1982-01-12
JPS58183912A (en) * 1982-04-22 1983-10-27 Kawasaki Steel Corp Precipitation basin
JPS5926108A (en) * 1982-08-02 1984-02-10 Oji Paper Co Ltd Apparatus for concentrating slurry

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5800715A (en) * 1994-02-16 1998-09-01 Baker Hughes Incorporated Separation of a suspension into its component parts
JP2006263670A (en) * 2005-03-25 2006-10-05 Nishihara Environment Technology Inc Solid-liquid separator
JP2012066233A (en) * 2010-09-21 2012-04-05 Torao Inoue Device for removing precipitate in water tank
WO2012139201A1 (en) * 2011-04-12 2012-10-18 Norcan Water Resources Inc. Inlet tube for producing laminar flow in a sedimentation vessel
US20140110333A1 (en) * 2011-04-12 2014-04-24 Richard Kibbee Solid from liquid separation apparatus

Also Published As

Publication number Publication date
JPH0555162B2 (en) 1993-08-16

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