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JPS6357089B2 - - Google Patents
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JPS6357089B2 - - Google Patents

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Publication number
JPS6357089B2
JPS6357089B2 JP11332286A JP11332286A JPS6357089B2 JP S6357089 B2 JPS6357089 B2 JP S6357089B2 JP 11332286 A JP11332286 A JP 11332286A JP 11332286 A JP11332286 A JP 11332286A JP S6357089 B2 JPS6357089 B2 JP S6357089B2
Authority
JP
Japan
Prior art keywords
sludge
water
sedimentation
tank
supernatant
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
JP11332286A
Other languages
Japanese (ja)
Other versions
JPS62269719A (en
Inventor
Toshiaki Hayakawa
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.)
Chubu Bando Kk
Original Assignee
Chubu Bando Kk
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 Chubu Bando Kk filed Critical Chubu Bando Kk
Priority to JP11332286A priority Critical patent/JPS62269719A/en
Publication of JPS62269719A publication Critical patent/JPS62269719A/en
Publication of JPS6357089B2 publication Critical patent/JPS6357089B2/ja
Granted legal-status Critical Current

Links

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  • Activated Sludge Processes (AREA)
  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は、各種の排水(生活排水、工場排水、
或は農水産排水、畜産排水等)や用水、或は上水
等の処理装置における沈澱槽の汚泥分離方法に関
するものである。
Detailed Description of the Invention "Field of Industrial Application" The present invention is applicable to various types of wastewater (domestic wastewater, industrial wastewater,
The present invention also relates to a method for separating sludge in a settling tank in a treatment device for treating wastewater from agricultural and fishery industries, livestock wastewater, etc.), industrial water, or tap water.

「従来の技術」 従来の前記の沈澱槽における汚泥の沈澱分離方
法は、第2図に例示する様に、摺り鉢状の底部3
を有する沈澱槽1の中央に、下端を底部3に臨ま
せて開口したセンターウエル5を設け、そのセン
ターウエル5から汚泥水11を流入させて汚泥水
11中の汚泥分12を底部3に沈澱させると共に
上澄水13をオーバーフロー部4から排出し、底
部3に沈澱した汚泥分12はセンターウエル5の
中心を通つて底部3に達する排泥パイプ10によ
つて吸上げ排出し、汚泥水11を汚泥分12と上
澄水13とに分離する方法に成つている。
``Prior Art'' The conventional method for sedimentation and separation of sludge in the above-mentioned settling tank is as illustrated in FIG.
A center well 5 is provided in the center of the sedimentation tank 1 with its lower end facing the bottom 3, and sludge water 11 is allowed to flow in from the center well 5, and the sludge component 12 in the sludge water 11 is settled on the bottom 3. At the same time, the supernatant water 13 is discharged from the overflow part 4, and the sludge 12 that has settled in the bottom part 3 is sucked up and discharged by the sludge pipe 10 that passes through the center of the center well 5 and reaches the bottom part 3, and the sludge water 11 is This method separates the sludge into a sludge component 12 and supernatant water 13.

「発明が解決しようとする問題点」 以上の従来方法は、摺り鉢状の底部3の中央直
上部分に開口したセンターウエル5から汚泥水1
1を集中的に流入し、ダイレクトに底部3に沈降
させる沈澱方法のため、例えば汚泥水を一時的に
多量に流入させたとき、底部3にさきに沈澱して
いる汚泥分12を捲き上げて撹乱流を生じ、沈澱
分離作用を妨げることがあると共に、センターウ
エル5から流入した汚泥水11中の水分が、底部
3の斜面3′から沈澱槽1の内壁に沿つて上昇す
る短絡流を生じ易く、センターウエル5の周囲に
水が流動しない滞溜水部14を生ずる傾向があ
る。
"Problems to be Solved by the Invention" In the conventional method described above, sludge water 1
Because of the sedimentation method in which sludge 1 flows in intensively and settles directly into the bottom 3, for example, when a large amount of sludge water temporarily flows in, the sludge 12 that has settled in the bottom 3 is rolled up first. This may cause a turbulent flow and impede the sedimentation separation action, and the moisture in the sludge water 11 flowing in from the center well 5 causes a short-circuit flow that rises from the slope 3' of the bottom part 3 along the inner wall of the settling tank 1. This tends to create a stagnant water area 14 around the center well 5 where water does not flow.

従つて、共通的に・汚泥分の沈降性能が悪く、
上質の上澄水が出来ないことがある・汚泥水の滞
溜時間が部分的に長くなり、汚泥水中の微生物が
死滅して腐敗し、泡状のスラツヂが浮上すること
がある・高濃度汚泥水の沈澱分離が困難な場合が
多く、沈澱槽機能が正常に作用しないことがあ
る。等の性能上の諸難点がある。
Therefore, the settling performance of sludge is generally poor;
High-quality supernatant water may not be produced. - The residence time of sludge water becomes longer in some areas, and microorganisms in the sludge water die and rot, resulting in foamy sludge floating to the surface. - Highly concentrated sludge water It is often difficult to separate the sediment, and the sedimentation tank function may not function properly. There are various performance problems such as.

本発明は、以上の従来技術における問題点を解
消するのが目的である。
It is an object of the present invention to solve the problems in the prior art described above.

「問題点を解決するための手段」 以上の目的を達成する本発明は「摺り鉢状の底
部を有する沈澱槽に、汚泥水を流入して汚泥分と
上澄水とに沈澱分離するにおいて、沈澱槽の中心
部分から沈澱槽の内壁に向つて概ね水平に伸びる
放射状の導入管に汚泥水を導き、しかるのち、該
導入管の先端部分から摺り鉢状底部の斜面に沿つ
て、汚泥水を分散流出させ、自然沈降させて汚泥
分と上澄水とに沈澱分離させる方法」に成つてい
る。
``Means for Solving the Problems'' The present invention achieves the above-mentioned objects. The sludge water is guided from the center of the tank to a radial introduction pipe that extends generally horizontally toward the inner wall of the settling tank, and then is dispersed from the tip of the introduction pipe along the slope of the mortar-shaped bottom. The sludge is separated into sludge and supernatant water by letting it flow out and letting it settle naturally.

「実施例」および「作用」 以下、本発明方法を用いた一実施例の沈澱槽を
引用して本発明の構成および作用を詳しく説明す
る。
"Example" and "Operation" The structure and operation of the present invention will be explained in detail below with reference to a settling tank of an example using the method of the present invention.

第1図はその一実施例の沈澱槽1を示したもの
である。図において、沈澱槽1は中空円柱状の主
部2の下端に、摺り鉢状の底部3が連設されると
共に、主部2の上端近傍には上澄水のオーバーフ
ロー部4が設けてある。そして、主部2の中心部
分には、汚泥水11を流入させるセンターウエル
5が立設されると共に、センターウエル5は底板
6によつて下端が閉じてある。そして、センター
ウエル5の下端から主部2の内壁に向つて概ね水
平に伸びる導入管7群が放射状に設けられ(図示
の実施例の導入管7は等分配列の八本)、それぞ
れの導入管7の先端には、主部2の内周に沿つて
円周方向に伸び、かつ先端を閉じた分散管8が取
付けられると共に、分散管8の下方には流出孔9
が数個づつ穿設されており、流出孔9は底部3の
斜面3′の上端に臨ませて配列してある。なお、
図中の10は底部3に沈澱した汚泥分12を吸上
げ排出させる排泥パイプである。
FIG. 1 shows a settling tank 1 of one embodiment. In the figure, a sedimentation tank 1 has a mortar-shaped bottom part 3 connected to the lower end of a hollow cylindrical main part 2, and an overflow part 4 for supernatant water near the upper end of the main part 2. A center well 5 is provided upright in the center of the main portion 2 to allow the sludge water 11 to flow in, and the center well 5 is closed at its lower end by a bottom plate 6. A group of 7 introduction pipes extending generally horizontally from the lower end of the center well 5 toward the inner wall of the main portion 2 is provided radially (in the illustrated embodiment, there are eight introduction pipes 7 arranged equally). At the tip of the tube 7, a dispersion tube 8 that extends in the circumferential direction along the inner periphery of the main part 2 and has a closed tip is attached.
The outflow holes 9 are arranged so as to face the upper end of the slope 3' of the bottom part 3. In addition,
10 in the figure is a sludge pipe that sucks up and discharges the sludge 12 that has settled on the bottom 3.

以上の沈澱槽1において、汚泥水11をセンタ
ーウエル5から導入管7に分散して導き、分散管
8を経由して流出孔9から底部3の斜面3′の上
端位置に分散流出させ、斜面3′の周面に沿つて
一様に自然流下させて上澄水13を上昇分離させ
ると共に、比重の重い汚泥分12を底部3に沈降
堆積させて固体分と水分とを分離する。
In the settling tank 1 described above, the sludge water 11 is distributed and guided from the center well 5 to the introduction pipe 7, and distributed and flows out from the outflow hole 9 to the upper end position of the slope 3' of the bottom part 3 via the distribution pipe 8. The supernatant water 13 is raised and separated by uniformly flowing down along the circumferential surface of the sludge 3', and the sludge component 12 with a heavy specific gravity is allowed to settle and accumulate on the bottom 3 to separate solids and water.

そして、上澄水13は順次上昇してオーバーフ
ロー部4から排出され、汚泥分12は排泥パイプ
10によつて槽外へ排出される。
Then, the supernatant water 13 gradually rises and is discharged from the overflow part 4, and the sludge portion 12 is discharged to the outside of the tank through the sludge pipe 10.

以上の本発明の沈澱分離方法によると、水平に
伸びる導入管7を流動する汚泥水11は、比重の
軽い上澄水と比重の重い汚泥分とが上下層に成る
ので、流動中に汚泥分と上澄水との分離が進行す
る作用があり、その分離が進行した状態の汚泥水
が底部3の斜面3′の上端に分散流出されるので、
汚泥分12は斜面3′を自然流下しながり上澄水
13を引続き分離して底部3に速やかに沈降堆積
する。そして、上澄水13は排出孔9から出た直
後に、導入管7内において分離した分が上昇する
と共に、さらに汚泥分12が斜面3′を滑つて底
部3に沈降するするまでの間に順次分離上昇し、
上澄水13と汚泥分12との分離が極めて促進さ
れる作用があり、分離性能が向上する。
According to the above-described sedimentation separation method of the present invention, the sludge water 11 flowing through the horizontally extending inlet pipe 7 has upper and lower layers of supernatant water with a light specific gravity and sludge with a heavy specific gravity, so that the sludge component and the sludge component during the flow. There is an effect that the separation from the supernatant water progresses, and the sludge water in a state where the separation has progressed is dispersed and flowed out to the upper end of the slope 3' of the bottom part 3.
The sludge component 12 naturally flows down the slope 3', continues to separate the supernatant water 13, and quickly settles and accumulates on the bottom 3. Immediately after the supernatant water 13 comes out of the discharge hole 9, the separated portion rises in the introduction pipe 7, and the sludge portion 12 slides down the slope 3' and settles to the bottom 3. Separation rises,
Separation between the supernatant water 13 and the sludge component 12 is greatly promoted, and the separation performance is improved.

そして、上澄水13が底部3の斜面3′から順
次上昇するので沈澱槽1内の上昇水流動が一様に
なり、従来方法の様な流動しない滞溜水がなく、
長期の槽内滞溜による腐敗が防止できる。さら
に、本発明方法によると、本発明は汚泥水11を
沈澱槽1の内周に沿つて一様に分散流下させるの
で、沈降堆積した汚泥分12を巻き上げる撹乱流
を生ずることがなく、上質の上澄液を分離生成す
ると共に、汚泥分12の沈降速度を速くする作用
がある。そして、多量の汚泥水11を一時的に流
入させても、それによつて沈澱分離作用が混乱し
たり低下することがなく、安定した沈澱分離作用
を維持することができる。
Since the supernatant water 13 rises sequentially from the slope 3' of the bottom part 3, the flow of rising water in the sedimentation tank 1 becomes uniform, and there is no stagnant water that does not flow as in the conventional method.
Corruption due to long-term retention in the tank can be prevented. Furthermore, according to the method of the present invention, the sludge water 11 is uniformly dispersed and flowed down along the inner circumference of the settling tank 1, so that a turbulent flow that stirs up the sedimented sludge 12 is not generated, and high-quality sludge is maintained. It has the effect of separating and producing a supernatant liquid and increasing the sedimentation rate of the sludge component 12. Even if a large amount of sludge water 11 is temporarily introduced, the sedimentation separation effect will not be confused or deteriorated thereby, and a stable sedimentation separation effect can be maintained.

「発明の効果」 以上の説明の様に、本発明の汚泥水の沈澱分離
方法は、汚泥水と上澄水との分離精度と分離速度
を向上して上質の上澄水を迅速にして安定して分
離生成する優れた効果がある。
"Effects of the Invention" As explained above, the sludge water sedimentation separation method of the present invention improves the separation accuracy and separation speed of sludge water and supernatant water, and quickly produces high-quality supernatant water in a stable manner. It has an excellent effect of separating and generating.

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

第1図:本発明の汚泥水の沈澱分離方法に用い
る一実施例の沈澱槽を示し、Aはその基本構造を
示す正面図、BはAのAA断面図、第2図:従来
技術の沈澱槽の基本構造を示す正面図。 主な符号、1……沈澱槽、2……主部、3……
底部、4……オーバーフロー部、5……センター
ウエル、6……底板、7……導入管、8……分散
管、9……排出孔、11……汚泥水、12……汚
泥分、13……上澄水。
Figure 1: Shows a settling tank of an embodiment used in the method of sedimentation and separation of sludge water of the present invention, A is a front view showing its basic structure, B is a cross-sectional view along line AA of A, Figure 2: Sedimentation according to the prior art FIG. 3 is a front view showing the basic structure of the tank. Main symbols: 1...Sedimentation tank, 2...Main part, 3...
Bottom, 4...Overflow part, 5...Center well, 6...Bottom plate, 7...Introduction pipe, 8...Distribution pipe, 9...Discharge hole, 11...Sludge water, 12...Sludge content, 13 ...Super clear water.

Claims (1)

【特許請求の範囲】[Claims] 1 摺り鉢状の底部を有する沈澱槽に、汚泥水を
流入させて汚泥分と上澄水とに沈澱分離するにお
いて、沈澱槽の中心部分から概ね水平にして放射
状に伸びる導入管に汚泥水を導き、しかるのち、
該導入管の先端部分から該汚泥水を分散流出させ
ると共に、摺鉢状底部の斜面に沿つて自然沈降さ
せ、汚泥分と上澄水とに沈澱分離することを特徴
とする沈澱槽における汚泥の沈澱分離方法。
1. When sludge water is introduced into a sedimentation tank having a mortar-shaped bottom and separated into sludge and supernatant water by sedimentation, the sludge water is introduced into an introduction pipe that extends radially from the center of the sedimentation tank in a generally horizontal manner. , and then,
Sedimentation of sludge in a settling tank characterized in that the sludge water is dispersed and flowed out from the tip of the introduction pipe, and is allowed to settle naturally along the slope of the mortar-shaped bottom to separate the sludge into sludge and supernatant water. Separation method.
JP11332286A 1986-05-16 1986-05-16 Method for settling and separating sludge in settling tank Granted JPS62269719A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11332286A JPS62269719A (en) 1986-05-16 1986-05-16 Method for settling and separating sludge in settling tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11332286A JPS62269719A (en) 1986-05-16 1986-05-16 Method for settling and separating sludge in settling tank

Publications (2)

Publication Number Publication Date
JPS62269719A JPS62269719A (en) 1987-11-24
JPS6357089B2 true JPS6357089B2 (en) 1988-11-10

Family

ID=14609292

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11332286A Granted JPS62269719A (en) 1986-05-16 1986-05-16 Method for settling and separating sludge in settling tank

Country Status (1)

Country Link
JP (1) JPS62269719A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0249988U (en) * 1988-09-30 1990-04-06
JPH02172689A (en) * 1988-12-22 1990-07-04 Ade Corp Robot arm for converting rotary motion into linear motion

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19830311A1 (en) * 1997-07-10 1999-01-14 Robert Dipl Ing Freimann Waste water treatment settlement circular basin
JP5634950B2 (en) 2011-06-22 2014-12-03 株式会社神戸製鋼所 Gravity sedimentation tank and method for producing ashless coal
CN103007592A (en) * 2011-09-20 2013-04-03 北京朗新明环保科技有限公司 Clarifier

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0249988U (en) * 1988-09-30 1990-04-06
JPH02172689A (en) * 1988-12-22 1990-07-04 Ade Corp Robot arm for converting rotary motion into linear motion

Also Published As

Publication number Publication date
JPS62269719A (en) 1987-11-24

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