JPS588387Y2 - Sedimentation tank sludge extraction equipment - Google Patents
Sedimentation tank sludge extraction equipmentInfo
- Publication number
- JPS588387Y2 JPS588387Y2 JP1979082761U JP8276179U JPS588387Y2 JP S588387 Y2 JPS588387 Y2 JP S588387Y2 JP 1979082761 U JP1979082761 U JP 1979082761U JP 8276179 U JP8276179 U JP 8276179U JP S588387 Y2 JPS588387 Y2 JP S588387Y2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- tank
- pipe
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Activated Sludge Processes (AREA)
Description
【考案の詳細な説明】 本考案は沈澱槽にむける汚泥引抜装置に関する。[Detailed explanation of the idea] The present invention relates to a sludge extraction device for a settling tank.
下水処理設備にむいて、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
込誉れ、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。For 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 sedimentation tank, 2 is a sludge pool provided at one end of the bottom of the sedimentation tank 1, and the sludge settled on the bottom surface 1a of the sedimentation tank is collected by a sludge scraper (not shown). 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
り出すポンプであり、他に図示していないが余剰汚泥を
汚澱濃縮機に送り出すポンプも設けられている。4 is a pump that sends the sludge in the sludge tank 3 to the aeration tank, and there is also a pump (not shown) that sends excess sludge to the sludge thickener.
ところで従来の汚泥引抜装置5は、一端が汚澱溜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Tを設けたも
のであシ、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 T 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、それに伴な
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カベ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 accordingly, the amount of sludge extracted by the sludge extraction device 5 also needs to follow the change in the amount of sludge sent. Some telescope valves 7 cannot be adjusted manually, 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、また装置の清掃が簡単にできる汚泥引抜装
置の提供を目的とする。The present invention solves these 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 the settling tank into the sludge tank, and also allows easy cleaning of the device. For the purpose of providing.
以下その実施例を第2図及び第3図により説明する。The embodiment will be described below with reference to FIGS. 2 and 3.
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
通して汚澱槽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28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 sump 2 at the bottom of the settling tank 1, passes through the partition wall 8, is guided into the sludge tank 3, and extends upward in the vertical direction, and the other end 11b opens into the sludge tank 2 at the liquid level 28 of the sludge tank 3. It protrudes upward and has an opening.
12は引抜管11の他端上方及び他端部外周を空間26
をあけかつ密封状態で覆う上端閉鎖の筒状体であって、
その横断面形状は正方形を成している。12 is a space 26 above the other end of the drawn pipe 11 and the outer periphery of the other end.
A cylindrical body with a closed top end that covers the body in an open and sealed state,
Its cross-sectional shape is square.
第3図において筒状体12は対向側片13.14から対
向側壁15.16が延設さへ この側壁15゜16の下
端縁と筒状体12の下端縁に連設した傾斜底板11が設
けられ、側壁15.16の上下方向端縁に沿って底板1
7に達する側板18が設けられ、溢流通路19が形成さ
れている。In FIG. 3, the cylindrical body 12 has an opposite side wall 15.16 extending from the opposite side piece 13.14, and an inclined bottom plate 11 connected to the lower edge of the side wall 15.16 and the lower edge of the cylindrical body 12. The bottom plate 1 is provided along the vertical edge of the side wall 15.16.
A side plate 18 reaching 7 is provided and an overflow passage 19 is formed.
この通路19は筒状体12下端の側壁15916間に設
けられた開口20に連通している。This passage 19 communicates with an opening 20 provided between side walls 15916 at the lower end of the cylindrical body 12.
一方側板18はガイドレール21.22間に遊嵌されて
おり上方に引抜くことが可能で、所謂角落しの堰板に構
成されている。The side plate 18 is loosely fitted between the guide rails 21 and 22 and can be pulled out upward, and is configured as a so-called corner-drop weir plate.
筒状体12の上端板24には管25の一端が貫通して筒
状体12内の空間26に連通し、また管21の一端が液
面28内に、所定長浸漬しておりこれら両管25.27
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 25 passes through the upper end plate 24 of the cylindrical body 12 and communicates with the space 26 inside the cylindrical body 12, and one end of the tube 21 is immersed in the liquid level 28 for a predetermined length, so that both of these are connected. tube 25.27
The other end 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、引抜管他端11bは沈澱槽1の液面9ようも下方で
かつその高さの差がHoに評定されているものとする。It is now assumed that the other end 11b of the drawn pipe is below the liquid level 9 of the settling tank 1 and that the difference in height is rated as Ho.
筐た管27の一端と汚泥槽3の液面28との高さの差が
偶々H1でHlはH8よりもhだけ小さく、さらに管2
9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、すると、管21内の圧力は
ヘッドH1に対応まる圧力p。It happens that the difference in height between one end of the pipe 27 and the liquid level 28 of the sludge tank 3 is H1, Hl is smaller than H8 by h, and
9 is supplied with air at a pressure p suitably higher than the head pressure of H1, then the pressure inside the pipe 21 is the pressure p corresponding to the head H1.
でであり、この管27に管25を介して連通ずる筒状体
12内の空間26における圧力もPlとなっている。The pressure in the space 26 inside the cylindrical body 12, which communicates with this pipe 27 via the pipe 25, is also Pl.
かくして汚泥溜2の汚泥はヘッドH8に対応するP。Thus, the sludge in the sludge pool 2 is P corresponding to the head H8.
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。The pressure difference between the pressure P1 and the pressure P1 causes the liquid to be discharged from the other end 11b of the drawn pipe.
筒状体12内に吐出した汚泥は筒状体12の下端が閉鎖
されているので一旦筒状体12内に溜った後、筒状体1
2内の空間26の圧力P1にによって下端開口部20か
ら溢流通路19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 12 is closed, the sludge discharged into the cylindrical body 12 once accumulates inside the cylindrical body 12 and is then removed from the cylindrical body 1.
Due to the pressure P1 in the space 26 in the sludge tank 2, the sludge flows from the lower end opening 20 through the overflow passage 19 and overflows from the upper end opening 30 thereof and enters the sludge tank 3.
ここでもし溢流通路19が無い場合は、液面28下にあ
る筒状体12の下端開口部20から直接汚泥槽3内に下
に向けて汚泥は吐出することになる。Here, if there is no overflow passage 19, the sludge will be discharged directly downward into the sludge tank 3 from the lower end opening 20 of the cylindrical body 12 below the liquid level 28.
このようにすると吐出する汚泥の状態は全く目視できな
いため、汚泥の性状を知るうえでの汚泥の色を観察した
9、汚泥の吐出量を観察することができないなどの不都
合が生ずる。If this is done, the state of the discharged sludge cannot be visually observed at all, resulting in inconveniences such as the inability to observe the color of the sludge to determine the properties of the sludge9 or the amount of sludge discharged.
そこでこの不都合を溢流通路19が解決しているもので
ある。Therefore, the overflow passage 19 solves this problem.
ところで吐出汚泥のヘッド、すなわち引抜管他端11b
と吐出液面との高さの差りはH8−Hlで与えうれかつ
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 other end of the drawing pipe 11b
The difference in height between and the discharge liquid level can be given by H8-Hl and is proportional to the amount of sludge drawn from the sludge reservoir 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2
8が下った場合には、Hlが小さくなるためH6−Hl
、すなわちhが大きくなり、汚泥の引抜き量が増大すも
一部ポンプ4の送泥量が少なくなって液面28が上ると
、Hlが大きくなるためhが小さくなう汚泥の引抜き量
が減少し、HlがH8になったとき引抜きが停止する。Next, from this state, the amount of mud fed by the pump 4 increases and the liquid level 2
If 8 falls, Hl becomes smaller, so H6-Hl
, that is, as h increases, the amount of sludge extracted increases, but when the amount of sludge sent by the pump 4 partially decreases and the liquid level 28 rises, Hl increases, so h decreases, and the amount of sludge extracted decreases. However, when Hl reaches H8, the extraction 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内に汚泥が引抜かへ液面28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 liquid level 28 is maintained substantially constant until the sludge is drawn into the sludge tank 3 according to the amount of sludge fed.
筐た汚泥が溢流通路19や筒状体12内に詰ったbして
清掃を行ないたい場合は、側板18を上に引き上げて取
外せば簡単に清掃を行なうことができる。If the overflow passage 19 or the cylindrical body 12 is clogged with cased sludge and you want to clean it, you can easily clean it by pulling up the side plate 18 and removing it.
更にこの側板18の取外しと併せバルブ31を閉じ管2
5の分岐管25aの先端バルブ34を開き筒状体12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内の清掃と共に筒状体12を清掃す
ることができる。Furthermore, when the side plate 18 is removed, the valve 31 is closed and the pipe 2 is closed.
By opening the tip valve 34 of the branch pipe 25a of No. 5 and releasing the inside of the cylindrical body 12 to atmospheric pressure, the sludge is discharged vigorously with a large pressure difference Po. The cylindrical body 12 can be cleaned together with cleaning.
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Sわらず、常に汚泥槽の液面を
一定に保つように沈澱槽の汚泥が引抜かれる。According to the present invention, as is clear from the above description, the sludge in the settling tank is always drawn out so as to keep the liquid level in the sludge tank constant regardless of changes in the amount of sludge fed by the pump.
すなわち送泥量に等しい量の汚泥を自動的に沈泥槽から
汚泥槽に引抜くことができる。That is, an amount of sludge equal to the amount of sludge sent can be automatically drawn from the silt tank to the sludge tank.
また汚泥引抜装置の溢流通路の側壁の少なくとも一部を
着脱自在の側板で構成し、汚泥引抜装置の清掃を行なう
場合はこの側板を取外して行ない得るようにしたもので
あるから、その清掃を効果的に行なうことができる。Furthermore, at least a part of the side wall of the overflow passage of the sludge extraction device is constructed with a removable side plate, and when cleaning the sludge extraction device, this side plate can be removed. It can be done effectively.
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図は本考案の実施例を示す断面図、第
3図は第2図における筒状体の平面図である。
1・・・・・・沈澱槽、2・・・・・・汚泥溜、3・・
・・・・汚泥槽、4・・・・・・ポンプ、11・・・・
・・引抜管、12・・・・・・筒状体、15.16・・
・・・・側壁、18・・・・・・側板、19・・・・・
・溢流通路、20・・・・・・開口、21.22・・・
・・・ガイド、25.27.29・・・・・・管、30
・・・・・・開口、31〜34・・・・・・バルブ。Fig. 1 is a schematic diagram showing the overall configuration of a settling tank together with a conventional sludge extraction device, Fig. 2 is a sectional view showing an embodiment of the present invention, and Fig. 3 is a plan view of the cylindrical body in Fig. 2. . 1...Sedimentation tank, 2...Sludge tank, 3...
...Sludge tank, 4...Pump, 11...
...drawn pipe, 12...tubular body, 15.16...
...Side wall, 18...Side plate, 19...
・Overflow passage, 20...Opening, 21.22...
...Guide, 25.27.29...Tube, 30
...Opening, 31-34...Valve.
Claims (1)
導き出して他端部を上向きに延出し、引抜管の他端部の
上方及び外周を空間をあけて覆う上端閉鎖の筒状体を設
け、該筒状体の下端開口に連通しかつ上方に延出された
上端開口の溢流通路を設け、該通路を形成する壁の少な
くとも一部を上端から下端に亘って着脱可能な側板で形
成し、前記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
る沈澱槽の汚泥引抜装置。A cylindrical shape whose top end is closed, with one end opening at the bottom of the sedimentation tank, the other end of the drawn pipe being guided into the sludge tank, the other end extending upward, and covering the upper and outer periphery of the other end of the drawn pipe with a space left. an overflow passage having an upper end opening communicating with the lower end opening of the cylindrical body and extending upward; and at least a part of the wall forming the passage being removable from the upper end to the lower end. The other end of a pipe formed of a side plate, one end of which communicates with the space inside the cylindrical body, and the other end of a pipe whose one end is immersed in the liquid level of the sludge tank are communicated with each other and connected to a common fluid supply source. A sludge extraction device for a settling tank characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1979082761U JPS588387Y2 (en) | 1979-06-15 | 1979-06-15 | Sedimentation tank sludge extraction equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1979082761U JPS588387Y2 (en) | 1979-06-15 | 1979-06-15 | Sedimentation tank sludge extraction equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56293U JPS56293U (en) | 1981-01-06 |
| JPS588387Y2 true JPS588387Y2 (en) | 1983-02-15 |
Family
ID=29315979
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1979082761U Expired JPS588387Y2 (en) | 1979-06-15 | 1979-06-15 | Sedimentation tank sludge extraction equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS588387Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2509131Y2 (en) * | 1988-05-11 | 1996-08-28 | 日本マタイ 株式会社 | Peeling label |
-
1979
- 1979-06-15 JP JP1979082761U patent/JPS588387Y2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56293U (en) | 1981-01-06 |
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