JPS588390Y2 - Sludge extraction device with adjustable overflow - Google Patents

Sludge extraction device with adjustable overflow

Info

Publication number
JPS588390Y2
JPS588390Y2 JP1979082764U JP8276479U JPS588390Y2 JP S588390 Y2 JPS588390 Y2 JP S588390Y2 JP 1979082764 U JP1979082764 U JP 1979082764U JP 8276479 U JP8276479 U JP 8276479U JP S588390 Y2 JPS588390 Y2 JP S588390Y2
Authority
JP
Japan
Prior art keywords
sludge
pipe
tank
cylindrical body
amount
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.)
Expired
Application number
JP1979082764U
Other languages
Japanese (ja)
Other versions
JPS56296U (en
Inventor
中村哲郎
八代譲治
米田理之助
Original Assignee
株式会社クボタ
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Filing date
Publication date
Application filed by 株式会社クボタ filed Critical 株式会社クボタ
Priority to JP1979082764U priority Critical patent/JPS588390Y2/en
Publication of JPS56296U publication Critical patent/JPS56296U/ja
Application granted granted Critical
Publication of JPS588390Y2 publication Critical patent/JPS588390Y2/en
Expired legal-status Critical Current

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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

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  • Activated Sludge Processes (AREA)

Description

【考案の詳細な説明】 本考案は汚泥引抜管の上端に越流頂高さの調整部材を設
けた汚泥引抜装置に関する。
[Detailed Description of the Invention] The present invention relates to a sludge extraction device having an overflow top height adjusting member provided at the upper end of the sludge extraction pipe.

下水処理設備にわいて、エアレーションタンクで活性汚
泥による有機物の処理を終えた汚水は最終沈澱池に送り
込オれ、ここで汚泥と清澄水とに分離され、汚泥は沈澱
池底部に沈澱する。
In sewage treatment equipment, sewage that has been treated with organic matter using activated sludge in an aeration tank is sent to a final settling tank, where it is separated into sludge and clear water, and the sludge settles at the bottom of the settling tank.

この沈澱した汚泥は沈澱槽から引き抜かれ、その大部分
は再びエアレーションタンクに返送され再利用される。
This settled sludge is extracted from the settling tank, and most of it is returned to the aeration tank for reuse.

第1図において、1は沈澱槽、2は沈澱槽1の底部一端
に設けられた汚泥溜であり、沈澱槽の底面1aに沈澱し
た汚泥は汚泥掻寄機(図示せず)によってこの汚泥溜2
に集められる。
In FIG. 1, 1 is a settling tank, and 2 is a sludge pool provided at one end of the bottom of the settling tank 1. The sludge settled on the bottom surface 1a of the settling tank is collected by a sludge scraper (not shown) into this sludge pool. 2
are collected in.

3は仕切壁8を介して沈澱槽1に隣接して設けられた汚
泥槽で、前記汚泥溜2に溜められた汚泥は、汚泥引抜装
置5によってこの汚泥槽3に取出される。
A sludge tank 3 is provided adjacent to the settling tank 1 via a partition wall 8, and the sludge stored in the sludge reservoir 2 is taken out to the sludge tank 3 by a sludge extraction device 5.

4は汚泥槽3内の汚泥を前記エアレーションタンクに送
り出スポンプであり、他に図示していないが余剰汚泥を
汚泥濃縮機に送り出すポンプも設けられている。
Reference numeral 4 denotes a pump for sending the sludge in the sludge tank 3 to the aeration tank, and a pump (not shown) for sending excess sludge to the sludge thickener is also provided.

ところで従来の汚泥引抜装置5は、一端が汚泥溜2内に
開口した引抜管6の他端を汚泥槽3内に導き出して上向
きに延出し、その他端部にテレスコープ弁7を設けたも
のであり、その可動管体7aの上端を沈澱槽1の液面9
より下方に位置させることによって生ずる水位差りによ
って汚泥溜2の汚泥を汚泥槽3内に引抜く様にしたもの
である。
By the way, the conventional sludge drawing device 5 has one end opened into the sludge tank 2, the other end of the drawing pipe 6 guided into the sludge tank 3 and extended upward, and a telescope valve 7 provided at the other end. The upper end of the movable tube body 7a is connected to the liquid level 9 of the settling tank 1.
The sludge in the sludge tank 2 is drawn into the sludge tank 3 by the difference in water level created by locating it further down.

ところが、前記ポンプ4による送泥量は、絶えず変化す
る汚水量に対応して変化させる必要があり、それに併な
って汚泥引抜装置5による汚泥の引抜き量も送泥量の変
化に追随させる必要があるが、前記テレスコープ弁7は
手動調整するものであるため追随できず、そのためポン
プ4による送泥量が汚水量に対応し得ないことがある。
However, the amount of sludge sent by the pump 4 needs to be changed in response to the constantly changing amount of sewage, and at the same time, the amount of sludge extracted by the sludge extraction device 5 also needs to follow the change in the amount of sludge sent. However, since the telescope valve 7 is manually adjusted, it cannot follow the flow, and therefore the amount of mud fed by the pump 4 may not be able to correspond to the amount of sewage.

本考案はかかる従来の欠点を解消し、ポンプの送泥量に
等しい量の汚泥を自動的に沈澱槽から汚泥槽内に引抜く
ことができ、また装置の設置が容易な汚泥引抜装置の提
供を目的とする。
The present invention eliminates such conventional drawbacks and provides a sludge extraction device that can automatically pull out an amount of sludge equal to the amount of sludge sent by the pump from a settling tank into a sludge tank, and that is easy to install. With the goal.

以下その実施例を図面に基づいて説明する。Examples thereof will be described below based on the drawings.

第2図において、11は引抜管であって、その一端11
aは沈澱槽1底部の汚泥溜2内に開口し、仕切壁8を貫
通して汚泥槽3内に導き出されて鉛直方向上向きに延出
され、他端11bは汚泥槽3の液面12上に突出して開
口している。
In FIG. 2, 11 is a drawn pipe, one end of which 11
A opens into the sludge reservoir 2 at the bottom of the settling tank 1, penetrates the partition wall 8, is guided into the sludge tank 3, and extends upward in the vertical direction, and the other end 11b opens above the liquid level 12 of the sludge tank 3. It has a protruding opening.

引抜管11の上端11cにはリング13が嵌装されてい
る。
A ring 13 is fitted to the upper end 11c of the drawn pipe 11.

リング13は第3図に示すように引抜管11の上端11
cに螺合外嵌してむり軸方向に移動させてその高さ位置
を調整することができ、ロック用のナツト14により所
定位置に締着固定される。
The ring 13 is connected to the upper end 11 of the drawn tube 11 as shown in FIG.
The height position can be adjusted by screwing and externally fitting onto the shaft and moving it in the direction of the helical axis, and it is tightened and fixed in a predetermined position by a locking nut 14.

15は引抜管11の上端11cの上方及び他端部11b
の外周を空間16をあけかつ密封状態で覆う上端閉鎖の
筒状体であって、その横断面は第4図に示す正方形を成
している。
15 is an upper end 11b of the upper end 11c of the drawn pipe 11 and the other end 11b
It is a cylindrical body whose top end is closed and which covers the outer periphery of the body in a sealed manner with a space 16 left in between, and its cross section is a square shown in FIG.

筒状体150対向側片17.18から対向側壁19.2
0が延設され、この側壁19.20の下端縁ど筒状体1
5の下端縁に連接した傾斜底板21が設けられ、側壁1
9.20の上下方向端縁に沿って底板21に達する側板
22が設けられ、溢流通路23が形成されている。
Cylindrical body 150 opposite side piece 17.18 to opposite side wall 19.2
0 is extended, and the lower end edge of this side wall 19.20 is a cylindrical body 1
A sloped bottom plate 21 connected to the lower edge of the side wall 1 is provided.
A side plate 22 reaching the bottom plate 21 is provided along the vertical edge of 9.20, and an overflow passage 23 is formed.

この通路23は筒状体15下端の側壁19.20間に設
けられた開口24に連通している。
This passage 23 communicates with an opening 24 provided between the side walls 19, 20 at the lower end of the cylindrical body 15.

側板22はガイドレール25,26間に遊嵌されている
から上方に引抜くことができ、通路23に汚泥が詰った
場合は取外して掃除をすることができる。
Since the side plate 22 is loosely fitted between the guide rails 25 and 26, it can be pulled upward, and if the passage 23 is clogged with sludge, it can be removed and cleaned.

−力筒状体15の頭部15aは接合部15bのところで
上下に2分割できるよう構成され、リング13の高さ位
置を調整したい場合は頭部15aを取外して簡単に調節
することができる。
- The head 15a of the force cylindrical body 15 is constructed so that it can be divided into upper and lower halves at the joint 15b, and when it is desired to adjust the height position of the ring 13, the head 15a can be easily removed and adjusted.

筒状体15の上端板15cには管27の一端が貫通して
筒状体15内の空間16に連通し、筐た管28の一端が
液面12内に所定長浸漬してむす、これら両管27.2
8の他端は図外の空気圧供給源に接続された管29に接
続されている。
One end of a tube 27 passes through the upper end plate 15c of the cylindrical body 15 and communicates with the space 16 inside the cylindrical body 15, and one end of the housing tube 28 is immersed in the liquid level 12 for a predetermined length. Both pipes 27.2
The other end of 8 is connected to a pipe 29 connected to a pneumatic supply source (not shown).

次に作用を説明する。Next, the effect will be explained.

今、引抜管11の上端11cにおけるリング13の先端
は沈澱槽1の液面9よりも下方でかつその高さの差がH
oに設定されているものとする。
Now, the tip of the ring 13 at the upper end 11c of the drawn pipe 11 is below the liquid level 9 of the settling tank 1, and the height difference is H.
It is assumed that the value is set to o.

昔た管28の一端と汚泥槽3の液面12との高さの差が
偶々H1で、HlはHoよりもhだけ小さく、さらに管
29にはHlのヘッド圧よりも適当に高い圧力Pの空気
が供給されているものとする。
The difference in height between one end of the old pipe 28 and the liquid level 12 of the sludge tank 3 happens to be H1, Hl is smaller than Ho by h, and furthermore, the pipe 29 has a pressure P that is appropriately higher than the head pressure of Hl. It is assumed that air is supplied.

すると、管28内の圧力はヘッドH1に対応する圧力P
1であり、この管28に管27を介して連通ずる筒状体
15内の空間16における圧力もPlとなっている。
Then, the pressure inside the tube 28 becomes the pressure P corresponding to the head H1.
1, and the pressure in the space 16 inside the cylindrical body 15 communicating with this tube 28 via the tube 27 is also Pl.

かくして汚泥溜2の汚泥はヘッドHoに対応するPoな
る圧力と前記P1なる圧力との差圧によって引抜管他端
11bから吐出することになる。
In this way, the sludge in the sludge reservoir 2 is discharged from the other end 11b of the drawing pipe due to the differential pressure between the pressure Po corresponding to the head Ho and the pressure P1.

筒状体15内に吐出した汚泥は筒状体15の下端が閉鎖
されているので一旦筒状体15内に溜った後、筒状体1
5内の空間16の圧力Plによって下端開口部24から
溢流通路23を経てその上端開口30から溢流して汚泥
槽3内に入る。
Since the lower end of the cylindrical body 15 is closed, the sludge discharged into the cylindrical body 15 once accumulates in the cylindrical body 15 and is then transferred to the cylindrical body 1.
Due to the pressure Pl in the space 16 in the sludge tank 5, the sludge flows from the lower end opening 24 through the overflow passage 23 and overflows from the upper end opening 30 thereof and enters the sludge tank 3.

ところで吐出汚泥のヘッド、すなわち引抜管上端11c
に螺着されたリング13と吐出液面との高さの差りはH
o−Hlで与えられかつ汚泥溜2からの汚泥の引抜き量
に比例する。
By the way, the head of the discharged sludge, that is, the upper end of the drawing pipe 11c
The difference in height between the ring 13 screwed on and the discharge liquid level is H.
o-Hl and is proportional to the amount of sludge withdrawn from the sludge sump 2.

次にこの状態からポンプ4の送泥量が多くなって液面1
2が下った場合には、Hlが小さくなるためH8−Hl
、すなわちhが大きくなり、汚泥の引抜き量が増大する
Next, from this state, the amount of mud fed by the pump 4 increases and the liquid level becomes 1.
If 2 falls, Hl becomes smaller, so H8-Hl
, that is, h increases, and the amount of sludge extracted increases.

一方ポンプ4の送泥量が少なくなって液面12が上ると
、Hlが大きくなるためhが小さくなり汚泥の引抜き量
が減少し、HlがHQになったとき引抜きが停止する。
On the other hand, when the amount of sludge fed by the pump 4 decreases and the liquid level 12 rises, Hl increases, so h becomes smaller and the amount of sludge drawn decreases, and when Hl reaches HQ, the drawing stops.

かくしてポンプ4の送泥量が変化しても送泥量に応じて
汚泥槽3内に汚泥が引抜かれ、液面12はほぼ一定に保
持される。
In this way, even if the amount of sludge fed by the pump 4 changes, the sludge is drawn into the sludge tank 3 in accordance with the amount of sludge fed, and the liquid level 12 is maintained substantially constant.

なお、筒状体15の下端開口24が液面12下(Hlよ
りも下)にあれば、溢流通路23は設けずに直接に下端
開口24から汚泥槽3に吐出させても伺ら変りなく上記
と同じ結果が得られる。
Note that if the lower end opening 24 of the cylindrical body 15 is below the liquid level 12 (below Hl), the overflow passage 23 may not be provided and the sludge may be directly discharged from the lower end opening 24 into the sludge tank 3. You will get the same result as above.

しかしこの場合、吐出汚泥は液面12より下でしかも下
に向けて吐出することになるために、吐出汚泥の状態は
目視できなくなり汚泥の性状を知るうえでの汚泥の色を
観察したり、汚泥の吐出量を観察することができないな
どの点では不都合である。
However, in this case, since the discharged sludge is discharged below the liquid level 12 and in a downward direction, the condition of the discharged sludge cannot be visually observed, and the color of the sludge is used to determine the properties of the sludge. This is disadvantageous in that it is not possible to observe the amount of sludge discharged.

このようにリング13の高さすなわち越流頂の高さは、
前記Hoとして吐出量を定めるうえで最も重要なもので
ある。
In this way, the height of the ring 13, that is, the height of the overflow top, is
The Ho is the most important factor in determining the discharge amount.

そこで例えばこの引抜装置を数個設置して全体を一体管
理する場合に、設置誤差によって個々の引抜管11の上
端11cの高さ位置が一致してない場合、或は何らかの
原因で上端11c位置が変化した場合は、吐出量に差が
生じて管理が非常に困難になる。
Therefore, for example, when installing several of these drawing devices and managing the whole in an integrated manner, if the height positions of the upper ends 11c of the individual drawn pipes 11 do not match due to installation errors, or for some reason the upper ends 11c positions may not match. If it changes, there will be a difference in the discharge amount, making management very difficult.

しかし本考案では筒状体15の頭部15aを取外してリ
ング13の高さを調整することにより、越流頂の高さを
正規の高さに調整することが容易に行ない得る。
However, in the present invention, by removing the head 15a of the cylindrical body 15 and adjusting the height of the ring 13, the height of the overflow top can be easily adjusted to the normal height.

第5図は本考案の他の実施例を示したもので、引抜管1
1′の上端11′cには堰板41が設けられている。
FIG. 5 shows another embodiment of the present invention, in which a drawn pipe 1
A weir plate 41 is provided at the upper end 11'c of 1'.

堰板41は第6図にその拡大図を示すように引抜管11
′の上端11′cの一部を山形に切欠いたこの切欠部1
2を下から塞ぐようにして取付けられている。
The weir plate 41 is connected to the drawn pipe 11 as shown in an enlarged view in FIG.
This notch 1 is formed by cutting a part of the upper end 11'c into a chevron shape.
2 is installed so as to close it from below.

堰板41は長穴43にボルトを通して取付けるようにな
っているから、引抜管11′の軸方向に移動可能であっ
てその越流頂の高さを調整することができる。
Since the weir plate 41 is attached by passing bolts through the elongated holes 43, it is movable in the axial direction of the drawn pipe 11', and the height of the overflow crest can be adjusted.

また筒状体15′は橋形部材15′dを引抜管11′に
固着することにより構成され溢流通路23′は有底22
′aの橋形部材22′を橋形部材15′dに固着するこ
とによって形成されている。
Further, the cylindrical body 15' is constructed by fixing the bridge-shaped member 15'd to the drawn pipe 11', and the overflow passage 23' is formed by the bottomed 22'.
It is formed by fixing the bridge-shaped member 22' of 'a' to the bridge-shaped member 15'd.

また筒状体15′の頭部15′aは接合部15′bのと
ころで上下に2分割できるよう構成されている。
Further, the head 15'a of the cylindrical body 15' is configured to be divided into upper and lower halves at the joint portion 15'b.

そこで越流頂の高さを調整したい場合は、前記実施例と
同様に筒状体15′の頭部15′aを取外し、堰板41
を上下に移動することによって越流頂の高さを容易に調
整することができる。
Therefore, if you want to adjust the height of the overflow crest, remove the head 15'a of the cylindrical body 15' as in the previous embodiment, and
The height of the overflow crest can be easily adjusted by moving up and down.

なお筒状体15内に汚泥が詰ったりして清掃を行ないた
い場合は、側板22の取外しと併せバルブ31を閉じ管
27の分枝管27aの先端バルブ32を開き筒状体15
内を大気圧に開放することにより大きな圧力差Poをも
って汚泥を勢いよく吐出させれば、この吐出汚泥の勢い
によって引抜管11と一緒に清掃することができる。
If the cylindrical body 15 is clogged with sludge and you wish to clean it, remove the side plate 22, close the valve 31, open the tip valve 32 of the branch pipe 27a of the pipe 27, and remove the cylindrical body 15.
If the inside is opened to atmospheric pressure and the sludge is vigorously discharged with a large pressure difference Po, the force of the discharged sludge can be used to clean the drawing pipe 11 together.

本考案によれば、以上の説明から明らかのようにポンプ
による送泥量の変化にか\わらず、常に汚泥槽の液面を
一定に保てるから送泥量に等しい量の汚泥を自動的に沈
澱槽から汚泥槽に引抜くことができる。
According to the present invention, as is clear from the above explanation, the liquid level in the sludge tank can always be kept constant regardless of changes in the amount of sludge sent by the pump, so the amount of sludge equal to the amount of sludge sent is automatically pumped out. It can be drawn from the sedimentation tank to the sludge tank.

また汚泥引抜管の越流頂の高さは調整できるので設置誤
差などによって越流頂の高さが変化しても正しい高さに
調整することができ、装置の設置や管理の面で非常に便
利である。
In addition, the height of the overflow top of the sludge extraction pipe can be adjusted, so even if the height of the overflow top changes due to installation errors, it can be adjusted to the correct height, which is very convenient in terms of equipment installation and management. It's convenient.

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

第1図は沈澱槽の全体構成を従来の汚泥引抜装置と共に
示す概略図、第2図は本考案の一実施例を示す断面図、
第3図は汚泥引抜管の上端に嵌装されたリングの断面図
、第4図は筒状体の断面図、第5図は本考案の他の実施
例を示す断面図、第6図は第5図のA−A断面拡大図で
ある。 1・・・・・・沈澱槽、2・・・・・・汚泥溜、3・・
・・・・汚泥槽、4・・・・・・ポンプ、11.11’
・・・・・・引抜管、13・・・・・・リング、14・
・・・・・ナツト、15.15’・・・・・・筒状体、
16・・・・・・空間、23,23′・・・・・・溢流
通路、27.28.29・・・・・・管、31〜34・
・・・・・バルブ、41・・・・・・堰板、42・・・
・・・切欠部。
FIG. 1 is a schematic diagram showing the overall configuration of a settling tank together with a conventional sludge extraction device, and FIG. 2 is a sectional view showing an embodiment of the present invention.
Fig. 3 is a sectional view of the ring fitted to the upper end of the sludge drawing pipe, Fig. 4 is a sectional view of the cylindrical body, Fig. 5 is a sectional view showing another embodiment of the present invention, and Fig. 6 is a sectional view of the ring fitted to the upper end of the sludge drawing pipe. 6 is an enlarged cross-sectional view taken along line A-A in FIG. 5. FIG. 1...Sedimentation tank, 2...Sludge tank, 3...
...Sludge tank, 4...Pump, 11.11'
.....drawn pipe, 13.....ring, 14.
...Nut, 15.15'...Cylindrical body,
16...Space, 23, 23'...Overflow passage, 27.28.29...Pipe, 31-34.
...Valve, 41...Weir plate, 42...
...Notch.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 一端が沈澱槽底部に開口した引抜管を汚泥槽内に導き出
して他端部を上向きに延出し、この引抜管の上端に越流
高さ調整部材を軸方向に移動可能に設け、引抜管の他端
部の上方及び外周を空間をあけて覆いかつ頭部で上下に
2分割可能な上端閉鎖の筒状体を設け、該筒状体内の空
間に一端が連通した管の他端と汚泥槽の液面に一端が浸
漬した管の他端とを互いに連通ずると共に共通の流体供
給源に接続したことを特徴とする越流調整可能な汚泥引
抜装置。
A drawn pipe with one end opening at the bottom of the sedimentation tank is guided into the sludge tank and the other end is extended upward, and an overflow height adjustment member is provided at the upper end of the drawn pipe so as to be movable in the axial direction. A cylindrical body with a closed top end that covers the upper part and outer periphery of the other end with a space left therein and can be divided into two upper and lower parts at the head, and connects the other end of the pipe and the sludge tank with one end communicating with the space inside the cylindrical body. A sludge extraction device capable of adjusting overflow, characterized in that a pipe having one end immersed in a liquid level and the other end of the pipe communicate with each other and are connected to a common fluid supply source.
JP1979082764U 1979-06-15 1979-06-15 Sludge extraction device with adjustable overflow Expired JPS588390Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1979082764U JPS588390Y2 (en) 1979-06-15 1979-06-15 Sludge extraction device with adjustable overflow

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1979082764U JPS588390Y2 (en) 1979-06-15 1979-06-15 Sludge extraction device with adjustable overflow

Publications (2)

Publication Number Publication Date
JPS56296U JPS56296U (en) 1981-01-06
JPS588390Y2 true JPS588390Y2 (en) 1983-02-15

Family

ID=29315982

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1979082764U Expired JPS588390Y2 (en) 1979-06-15 1979-06-15 Sludge extraction device with adjustable overflow

Country Status (1)

Country Link
JP (1) JPS588390Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6194877U (en) * 1984-11-27 1986-06-18

Also Published As

Publication number Publication date
JPS56296U (en) 1981-01-06

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