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JPS6342757A - Solid-liquid separation device - Google Patents

Solid-liquid separation device

Info

Publication number
JPS6342757A
JPS6342757A JP18420586A JP18420586A JPS6342757A JP S6342757 A JPS6342757 A JP S6342757A JP 18420586 A JP18420586 A JP 18420586A JP 18420586 A JP18420586 A JP 18420586A JP S6342757 A JPS6342757 A JP S6342757A
Authority
JP
Japan
Prior art keywords
solids
separation tank
solid
center
secondary flow
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
JP18420586A
Other languages
Japanese (ja)
Other versions
JPH0365234B2 (en
Inventor
Tetsuo Nishida
哲夫 西田
Kazuo Hirahara
平原 一雄
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 JP18420586A priority Critical patent/JPS6342757A/en
Publication of JPS6342757A publication Critical patent/JPS6342757A/en
Publication of JPH0365234B2 publication Critical patent/JPH0365234B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To stabilize a primary flow revolving in a separating vessel and to strongly generate a secondary flow by forming the inner wall of the separating vessel with a curved surface, and forming the bottom surface in such a way that the outer peripheral part is almost plane and then the surface is slanted upward for the center and a sinkhole is formed in the center. CONSTITUTION:The inner wall 3 of the separating vessel 1 is formed with cylindrical or involute-curved surface and the bottom surface 3 is formed in such a way that the outer peripheral part is plane 3a and the surface is changed to a slanted surface 3b gradually slanted upward for the center where a recessed sinkhole 4 for solids is provided. And an inflow opening 5 is provided to the inner wall 2 of the separating vessel 1 and a discharged water containing solids such as sands is introduced through said opening, and the treated water 10 separated from solids is discharged from a discharge opening 9 provided with a filter. In this way, the primary flow revolving in the separating vessel is stabilized and the generation of the secondary flow separating solids from liquid is strengthened and the solid-liquid separation is efficiently and effectively carried out by the multiplied effect of the primary flow and the secondary flow.

Description

【発明の詳細な説明】 [発明の目的] (産業上の利用分野) 本発明は、雨水や汚水のように、砂等の固形物を含む排
水から固形物を分離して、清浄な処理済液を得るための
固液分離装置に関するものである。
[Detailed Description of the Invention] [Objective of the Invention] (Industrial Field of Application) The present invention is directed to separating solids from wastewater, such as rainwater or sewage, that contains solids such as sand, thereby producing a clean and treated wastewater. The present invention relates to a solid-liquid separation device for obtaining a liquid.

[従来の技術] 一般に、砂等の固形物を含む排水から固形物を分離して
清浄な処理済液を得るには、自然流下方式で排水を接線
方向から分離槽内に導き、排水を旋回させながら固形物
を沈降させる固液分離装置が広く用いられている。
[Prior art] Generally, in order to separate solids from wastewater containing solids such as sand and obtain a clean treated liquid, the wastewater is guided tangentially into a separation tank using a gravity flow method, and then the wastewater is swirled. Solid-liquid separators are widely used, which allow solids to settle while allowing the solids to settle.

[発明が解決しようとする問題点] ところが、従来の固液分離装置においては、中心部に凹
状の固形物溜りを有する分離槽の底面が、中心に向かう
に従って下り勾配の傾斜となっているため、分離槽内を
旋回する一次流れの、分離槽内の外側から内側に到る周
速の変化度合が小さく、分離槽内を垂直方向に流動する
固液分離に有効な二次流れの発生が弱いため、分離効率
があまりよくないばかりか、分離槽の中心部の水深が深
いため、構造物を設置する工事費が嵩むという欠点があ
った。
[Problems to be Solved by the Invention] However, in conventional solid-liquid separators, the bottom surface of the separation tank, which has a concave solids reservoir in the center, slopes downward toward the center. , the degree of change in circumferential velocity of the primary flow swirling inside the separation tank from the outside to the inside of the separation tank is small, and the generation of a secondary flow that flows vertically inside the separation tank and is effective for solid-liquid separation. Not only is the separation efficiency not very good due to its weakness, but the water depth at the center of the separation tank is deep, which has the disadvantage of increasing construction costs for installing the structure.

本発明は上記従来の欠点に鑑みて提案されたもので、分
離槽内を垂直方向に流動する固液分離に有効な二次流れ
の発生が強く、効率よく固液分離を行うことができると
共に、構造物を設置する工事費を節減することができる
、実用上有効な固液分離装置を提供せんとするものであ
る。
The present invention was proposed in view of the above-mentioned drawbacks of the conventional art, and it strongly generates a secondary flow that is effective for solid-liquid separation that flows vertically in the separation tank, making it possible to efficiently perform solid-liquid separation. The present invention aims to provide a practically effective solid-liquid separator that can reduce construction costs for installing a structure.

[発明の構成] (問題点を解決するための手段) 本発明は上記問題点を解決するために、内壁が円筒状或
はインボリュート状の曲面を持ち、底面が外周部でほぼ
平面であり、中心部に向かうに従って上り勾配の傾斜を
有し、中心部に凹状の固形物情りを設けた分離槽に、砂
等の固形物を含む排水を分離槽内に導く流入口と、固形
物を分離後の処理済液を分離槽内から外部に導く放出口
を設けて、固液分離装置を構成したことを特徴とするも
のである。
[Structure of the Invention] (Means for Solving the Problems) In order to solve the above-mentioned problems, the present invention has an inner wall having a cylindrical or involute curved surface, a bottom surface having a substantially flat surface at the outer periphery, The separation tank has an upward slope toward the center and has a concave solid matter groove in the center, and has an inlet for introducing wastewater containing solids such as sand into the separation tank, and an inlet for introducing the solid matter into the separation tank. A solid-liquid separator is constructed by providing a discharge port for guiding the separated treated liquid from inside the separation tank to the outside.

[作 用] 本発明の固液分離装置は上記のように構成されているの
で、流入口より分離槽内に導かれた排水は、分離槽の内
壁に沿って一次流れとなって旋回するが、その−次流れ
は、分離槽の底面が外周部でほぼ平面であり、中心部に
向かうに従って上り勾配の傾斜となっているため、相対
的に外周部の一次流れの運動量が大きくなる。従って分
離槽内を旋回する一次流れは、分離槽内の外側から内側
に到る周速の変化度合か大きくなるため、分gi槽内な
垂直方向に流動する固液分離に有効な二次流れの発生が
強くなる。その結果、排水中に含まれている固形物は、
−次流れと二次流れの相乗効果によって効率よく分離さ
れ、分離槽の底面に沈降した固形物は、二次流れによっ
て斜面を掻き上げられて中心部の固形物情りに溜ること
になる。
[Function] Since the solid-liquid separator of the present invention is configured as described above, the waste water led into the separation tank from the inlet turns as a primary flow along the inner wall of the separation tank, but As for the secondary flow, the bottom surface of the separation tank is almost flat at the outer periphery and slopes upward toward the center, so that the momentum of the primary flow at the outer periphery is relatively large. Therefore, the degree of change in circumferential velocity of the primary flow swirling inside the separation tank increases from the outside to the inside of the separation tank, so the secondary flow that flows vertically in the separation tank is effective for solid-liquid separation. occurrence becomes stronger. As a result, the solids contained in wastewater are
- The solids are efficiently separated by the synergistic effect of the secondary flow and the solids that settle to the bottom of the separation tank are scraped up the slope by the secondary flow and accumulate in the center of the solids.

他方、処理済液は放出口より放出されることになるう [実施例] 以下、本発明を図面に示す実施例に基づいて具体的に説
明する。
On the other hand, the treated liquid will be discharged from the discharge port. [Example] The present invention will be specifically described below based on an example shown in the drawings.

第1図は本発明の1実施例を概念的に示す固液分離装置
の断面図で、第2図はその平面図である。
FIG. 1 is a sectional view of a solid-liquid separator conceptually showing one embodiment of the present invention, and FIG. 2 is a plan view thereof.

図中1は固液分離を行う分離槽て、その内壁2は図示の
ように円筒状に形成されるか、或はインポリコート状の
曲面を持つように形成されている。但し、本実施例にお
いては、内壁2の上部だけを内側に少し傾斜させている
が、内壁2全体を内側に少し傾斜させてもよい。このよ
うに、内壁2の一部又は全部を内側に傾斜させた円筒状
にしておくと、内壁2に沿って旋回する一次流れAに対
し、内壁2に沿って上方から下方に向かう下降流が強化
され、その結果として分離槽1内を垂直方向に流動する
固液分離に有効な二次流れBの発生をさらに強めること
ができる。
In the figure, reference numeral 1 denotes a separation tank for performing solid-liquid separation, and its inner wall 2 is formed into a cylindrical shape as shown in the figure, or is formed to have an impoly coated curved surface. However, in this embodiment, only the upper part of the inner wall 2 is slightly inclined inward, but the entire inner wall 2 may be slightly inclined inward. In this way, if part or all of the inner wall 2 is formed into a cylindrical shape that is inclined inward, the primary flow A that swirls along the inner wall 2 is caused to flow downward from above to below along the inner wall 2. As a result, the generation of the secondary flow B, which is effective for solid-liquid separation and flows vertically within the separation tank 1, can be further strengthened.

次に、3は分離槽lの底面で、その外周部は平面3aと
なっているが、中心部に向かうに従って上り勾配の傾斜
3bを有し、中心部には凹状の固形物情り4が設けられ
ている。5は分離槽lの内壁2に設けられた流入口で、
砂等の固形物6を含む排水7を、接線方向から分離槽1
内に導くための流入路8と接続されている。9は分離槽
1の内壁2に設けられたフィルターを有する放出口で、
固形物6を分離後の処理済液10を、分離槽1内から外
部に導く放出路11と接続されている。
Next, reference numeral 3 denotes the bottom surface of the separation tank l, whose outer periphery is a flat surface 3a, but has an upward slope 3b toward the center, and a concave solid matter surface 4 is formed at the center. It is provided. 5 is an inlet provided on the inner wall 2 of the separation tank l;
Waste water 7 containing solid matter 6 such as sand is tangentially transferred to a separation tank 1
It is connected to an inflow path 8 for guiding the inside of the tank. 9 is a discharge port provided with a filter on the inner wall 2 of the separation tank 1;
It is connected to a discharge path 11 that guides the treated liquid 10 from which the solid matter 6 has been separated from the separation tank 1 to the outside.

但し、本実施例においては、放出口9は流入口5よりも
約3000程度下流で流入口5よりも上方に位置するよ
うに設けられているが、例えば、構造物の深さが少し深
くなるが流入口5を暗きょ状とすることにより流入口5
よりも3600下流、つまり流入口5とほぼ同位置で、
流入口5よりも上方の位置に放出口9′を設け、流入口
5の上面に短絡防止のため屋根板を設けてもよい。
However, in this embodiment, the discharge port 9 is located about 3000 degrees downstream of the inlet 5 and above the inlet 5, but for example, the depth of the structure may be a little deeper. By making the inlet 5 into a dark hole, the inlet 5
3600 downstream, that is, at almost the same position as inlet 5,
The outlet 9' may be provided at a position above the inlet 5, and a roof plate may be provided on the upper surface of the inlet 5 to prevent short circuits.

次に、12は分離槽糟1の中心部に同心状に設置された
、固形物情り4と略同径の内筒で、その下端は脚13に
よって支持されており、分離槽1の底面3上に沈降した
固形物6は、二次流れBによって傾斜3bの斜面を掻き
上げられ、脚13間の間隔を介して固形物情り4内に落
下して溜められるようになっている。なお、14は固形
物情り4内に溜った固形物6を排出するための排出ポン
プである。
Next, reference numeral 12 denotes an inner cylinder which is installed concentrically in the center of the separation tank 1 and has approximately the same diameter as the solid material support 4. Its lower end is supported by legs 13, and the bottom of the separation tank 1 The solids 6 that have settled on the solids 3 are scraped up the slope of the slope 3b by the secondary flow B, and fall into the solids holder 4 through the gap between the legs 13 and are collected therein. In addition, 14 is a discharge pump for discharging the solid matter 6 accumulated in the solid matter container 4.

ところで、本実施例においては、分離槽1の中心部に内
筒12を設けたが、このように内筒12を設置すると、
−次流れAや二次流れBが安定化すると共に、分離槽1
の底面3上に沈降し・;固形物6が中心部に移動しても
、内筒12の下端部は一次流れAや二次流れBの影響を
ほとんど受けないので、固定物6は再浮上することはな
く、スムーズに固形物情り4内に落下することができ、
きわめて好都合である。
By the way, in this embodiment, the inner cylinder 12 was provided at the center of the separation tank 1, but when the inner cylinder 12 is installed in this way,
-The secondary flow A and the secondary flow B are stabilized, and the separation tank 1
Even if solid matter 6 moves to the center, the lower end of inner cylinder 12 is hardly affected by primary flow A or secondary flow B, so fixed matter 6 will not resurface. Solid objects can fall smoothly into the container without causing any damage.
This is extremely convenient.

次に、第3図は内筒12の異なる形状(イ)。Next, FIG. 3 shows a different shape of the inner cylinder 12 (A).

(ロ)、(ハ)、(ニ)を、1つの断面の嵐ずつに区分
して示す断面図で、第4図はその外周面の展開図である
。   ゛ 内筒12は、(イ)で示すように全体を単なる素管にし
てもよいが、(ロ)で示すように外周面に多数の孔を設
けたり、(ハ)で示すように点状に多数の各種凹凸を設
けたり、又は(ニ)で示すように内筒12の長平方向に
縦の凹凸条を設けるか、或は上記(イ)、(ロ)、(ハ
)、(ニ)を適宜組合せた外周面とすれば、内筒12の
外周面に沿った一次流れAに対する抵抗が大きくなり、
分離槽1の中心部での一次流れが弱まって、分離槽1内
の外側から内側に到る周速の変化度合が大きくなるので
、固液分離に有効な二次流れの発生を一段と強めること
ができる。
(B), (C), and (D) are sectional views showing each section of the storm, and FIG. 4 is a developed view of the outer peripheral surface thereof.゛The inner cylinder 12 may be made entirely of a plain tube as shown in (A), but it may have many holes on its outer circumferential surface as shown in (B), or dotted holes as shown in (C). A large number of various unevennesses may be provided on the inner cylinder 12, or vertical unevenness lines may be provided in the longitudinal direction of the inner cylinder 12 as shown in (d), or (a), (b), (c), and (d) above. If the outer circumferential surface is an appropriate combination of
Since the primary flow at the center of the separation tank 1 weakens and the degree of change in circumferential velocity from the outside to the inside of the separation tank 1 increases, the generation of a secondary flow effective for solid-liquid separation is further strengthened. Can be done.

上記構成よりなる本実施例の固液分離装置においては、
流入路8を通って流入口5より接線方向から分離槽1内
に導かれた排水7は、分離槽l内を強く安定した一次流
れAとなって旋回するが、この−次流れAは、分離槽1
の底面3が外周部で平面であり、中心部に向かうに従っ
て上り勾配の傾斜となっているため、相対的に外周部の
一次流れAの運動量は大きくなる。従って、分離槽1内
を旋回する一次流れAは、分離槽1内の外側から内側に
到る周速の変化度合が大きくなるため、分離槽1内を垂
直方向に流動する固液分離に有効な二次流れBの発生が
強くなり、排水7中に含まれている固形物6は、−次流
れAと二次流れBの相乗効果によって効率よく分離され
ることになる。
In the solid-liquid separator of this example having the above configuration,
The waste water 7 tangentially led into the separation tank 1 from the inlet 5 through the inflow channel 8 swirls in the separation tank 1 as a strong and stable primary flow A, but this secondary flow A is Separation tank 1
Since the bottom surface 3 of is flat at the outer periphery and slopes upward toward the center, the momentum of the primary flow A at the outer periphery becomes relatively large. Therefore, the degree of change in circumferential velocity of the primary flow A swirling inside the separation tank 1 from the outside to the inside of the separation tank 1 becomes large, so it is effective for solid-liquid separation flowing vertically inside the separation tank 1. The generation of the secondary flow B becomes stronger, and the solids 6 contained in the waste water 7 are efficiently separated by the synergistic effect of the secondary flow A and the secondary flow B.

なお、分離された分離槽lの底面3上に沈降した固形物
6は、丁度二次流れBの案内強化に役立つ傾斜3bの斜
面を、二次流れBによって中心方向に掻き寄せられ、順
次固形物情り4内に落下して、適宜排水ポンプ14によ
って排出されることになる。他方、固形物6が分離され
て清浄となった処理済液10は、流入口5から新たに流
入する排水7と直接ぶつかることなく、放出口9より静
かに放出路11に放出されることになる。
The solids 6 that have settled on the bottom surface 3 of the separated separation tank 1 are just scraped toward the center by the secondary flow B on the slope of the slope 3b that serves to strengthen the guidance of the secondary flow B, and the solids are successively The water will fall into the water tank 4 and will be drained out by the drainage pump 14 as appropriate. On the other hand, the treated liquid 10 from which the solid matter 6 has been separated and is now clean is quietly discharged into the discharge path 11 from the discharge port 9 without directly colliding with the waste water 7 newly flowing in from the inlet 5. Become.

なお、本実施例においては、内壁2を内側に傾斜させた
円筒状としたが、内壁2は傾斜させなくても良い。
In this embodiment, the inner wall 2 has a cylindrical shape that is inclined inward, but the inner wall 2 does not need to be inclined.

又、本実施例においては、分離槽lの中心部に内筒12
を設置しているが、分離槽1の内壁が小径のものは内筒
がなくても良い。そして、内筒12は必要に応じて最適
寸法形状のものを設置すれば良い。
In addition, in this embodiment, an inner cylinder 12 is provided at the center of the separation tank l.
However, if the inner wall of the separation tank 1 has a small diameter, the inner cylinder may not be provided. The inner cylinder 12 may have an optimal size and shape as required.

[発明の効果] 以上具体的に説明したように、本発明によれば、分離槽
内を旋回する一次流れを安定化させ、固液分離に有効な
二次流れの発生を強くすることができるので、−次流れ
と二次流れとの相乗効果によって、固形物を効率的に分
離することができる。又、分離槽の底面に沈降した固形
物は、二次流れによってスムーズに固形物情りに落下さ
せる、ことができる。又従来のように、分離槽の底面が
中心に向かうに従って下り勾配となっているものと比較
して、分離槽の中心部の水深を浅くすることができ、そ
の分だけ構造物を設置する工事費を節減することができ
る。等大きな利点を有し、下水や汚水のように、砂等の
固形物を含む排水から固形物を分離して清浄な処理済液
を得る場合に使用して、実用上きわめて有効な固液分離
装置を提供し得るものである。
[Effects of the Invention] As specifically explained above, according to the present invention, it is possible to stabilize the primary flow swirling in the separation tank and strengthen the generation of the secondary flow effective for solid-liquid separation. Therefore, solids can be efficiently separated by the synergistic effect of the secondary flow and the secondary flow. In addition, the solid matter that has settled on the bottom of the separation tank can be smoothly dropped to the solid matter by the secondary flow. In addition, compared to conventional separation tanks where the bottom slopes downward toward the center, the water depth at the center of the separation tank can be made shallower, making it easier to install structures by that amount. Costs can be saved. This solid-liquid separation method is extremely effective in practice and is used to separate solids from wastewater that contains solids such as sand, such as sewage and sewage, to obtain a clean treated liquid. The device can be provided.

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

第1図は本発明の1実施例を概念的に示す固液分離装置
の断面図で、第2図はその平面図、第3図は内筒の異な
る形状(イ)、(ロ)、(ハ)。 (ニ)を1つの断面の属ずつに区分して示す断面図で、
第4図はその外周面の展開図である。 1・・・分離槽、2・・・内壁、3・・・底面(3a・
・・平面、3b・・・傾斜)、4・・・固形物情り、5
・・・流入口、6・・・固形物、7・・・排水、8・・
・流入路、9・・・放出口、10・・・処理済液、11
・・・放出路、12・・・内筒、13・・・脚、[4排
水ポンプ、A・・・−次流れ、B・・・二次流れ。 第1図 第2図
FIG. 1 is a sectional view of a solid-liquid separator conceptually showing an embodiment of the present invention, FIG. 2 is a plan view thereof, and FIG. c). A cross-sectional view showing (d) divided into each genus of one cross section,
FIG. 4 is a developed view of its outer peripheral surface. 1...Separation tank, 2...Inner wall, 3...Bottom surface (3a/
...plane, 3b...tilt), 4...solid matter, 5
...Inlet, 6...Solid matter, 7...Drainage, 8...
- Inflow path, 9... Outlet, 10... Treated liquid, 11
...Discharge path, 12...Inner cylinder, 13...Legs, [4 Drain pump, A...-Secondary flow, B...Secondary flow. Figure 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims]  内壁が円筒状或はインボリュート状の曲面を持ち、底
面が外周部でほぼ平面であり、中心部に向かうに従って
上り勾配の傾斜を有し、中心部に凹状の固形物溜りを設
けた分離槽に、砂等の固形物を含む排水を分離槽内に導
く流入口と、固形物を分離後の処理済液を分離槽内から
外部に導く放出口を設けたことを特徴とする固液分離装
置。
A separation tank with an inner wall having a cylindrical or involute curved surface, a bottom surface that is almost flat at the outer periphery, an upward slope toward the center, and a concave solids reservoir in the center. , a solid-liquid separation device characterized by being provided with an inlet for guiding wastewater containing solids such as sand into a separation tank, and an outlet for guiding a treated liquid after separating solids from the separation tank to the outside. .
JP18420586A 1986-08-07 1986-08-07 Solid-liquid separation device Granted JPS6342757A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18420586A JPS6342757A (en) 1986-08-07 1986-08-07 Solid-liquid separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18420586A JPS6342757A (en) 1986-08-07 1986-08-07 Solid-liquid separation device

Publications (2)

Publication Number Publication Date
JPS6342757A true JPS6342757A (en) 1988-02-23
JPH0365234B2 JPH0365234B2 (en) 1991-10-11

Family

ID=16149195

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18420586A Granted JPS6342757A (en) 1986-08-07 1986-08-07 Solid-liquid separation device

Country Status (1)

Country Link
JP (1) JPS6342757A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0590396A3 (en) * 1992-09-17 1994-08-31 Hugo Schmitz

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0590396A3 (en) * 1992-09-17 1994-08-31 Hugo Schmitz

Also Published As

Publication number Publication date
JPH0365234B2 (en) 1991-10-11

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