JPH0363401B2 - - Google Patents
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- Publication number
- JPH0363401B2 JPH0363401B2 JP61012186A JP1218686A JPH0363401B2 JP H0363401 B2 JPH0363401 B2 JP H0363401B2 JP 61012186 A JP61012186 A JP 61012186A JP 1218686 A JP1218686 A JP 1218686A JP H0363401 B2 JPH0363401 B2 JP H0363401B2
- Authority
- JP
- Japan
- Prior art keywords
- separation tank
- solid
- inner cylinder
- solids
- center
- 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 - Lifetime
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- Centrifugal Separators (AREA)
- Cyclones (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、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
液を得るための固液分離装置に関するものであ
る。[Detailed Description of the Invention] [Industrial Application Field] The present invention is a method for separating solids from wastewater containing solids such as sand, such as sewage or sewage, to obtain a clean treated liquid. This invention relates to a solid-liquid separator.
[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は、分離槽内に
排水を導く流入路の内側液を分離槽内に一部突出
させて、分離槽内に導いた排水の一部が直接放出
口へ向かわないようにしているため、その突出部
で分離槽内の外壁に沿つて旋回する排水に乱流が
生じ、固液分離効率が悪くなるという欠点があつ
た。[Problems to be Solved by the Invention] However, in the conventional solid-liquid separator, a part of the liquid inside the inflow channel that leads wastewater into the separation tank protrudes into the separation tank, and the wastewater led into the separation tank is Since a part of the water does not go directly to the discharge port, the protrusion causes turbulence in the waste water swirling along the outer wall of the separation tank, resulting in poor solid-liquid separation efficiency.
又、従来の固液分離装置においては、分離槽内
の中心部に、浮遊する軽い固形物を集めて取り出
すための、比較的小径の吹出し管を設けることが
あるが、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致る周速の変化度合が小さい
ため、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く、分離効率があまり
良くないという欠点があつた。 In addition, in conventional solid-liquid separators, a relatively small-diameter blowout pipe is sometimes provided in the center of the separation tank to collect and take out floating light solids, but the Because the degree of change in the circumferential velocity of the primary flow from the outside to the inside of the separation tank is small, the generation of a secondary flow that is effective for solid-liquid separation that flows vertically in the separation tank is weak, and the separation efficiency is low. There was a drawback that it was not good.
本発明は上記従来の欠点に鑑みて提案されたも
ので、分離槽内を旋回する一次流れの外壁周辺に
おける乱流の発生をなくし、固液分離に有効な二
次流れの発生を強くして固液分離効率を高め、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 conventional drawbacks, and eliminates the generation of turbulence around the outer wall of the primary flow swirling in the separation tank, and strengthens the generation of the secondary flow that is effective for solid-liquid separation. The purpose of this invention is to improve the solid-liquid separation efficiency and provide a practically effective solid-liquid separation device.
[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、外壁が
円筒状或いはインボリユート状の曲面を持ち、底
面が中心に向つて下向きに傾斜し、そのほぼ中心
部に凹状の固形物溜りを設けた分離槽の外壁に、
砂等の固形物を含む排水を接線方向から分離槽内
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、放出口が流入口
より下流で上方に位置するように設けると共に、
分離槽の中心部に、中空状で且つ少なくとも上側
に通水孔を設けた内筒を配設し、内筒の下端を載
置する架台と分離槽の底面との間に、固形物溜り
に向かう固形物移動通路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。[Means for Solving the Problems] In order to solve the above-mentioned problems, the present invention has an outer wall having a cylindrical or involute curved surface, a bottom surface inclined downward toward the center, and a wall formed at approximately the center thereof. On the outer wall of the separation tank, which has a concave solid matter reservoir,
An inlet that leads wastewater containing solids such as sand into the separation tank from a tangential direction, and a discharge port that leads the treated liquid after solids have been separated from the separation tank to the outside.The discharge port is located downstream of the inlet. In addition to being located above,
A hollow inner cylinder with a water passage hole provided at least on the upper side is arranged in the center of the separation tank, and a solid material reservoir is placed between the base on which the lower end of the inner cylinder is placed and the bottom of the separation tank. This is characterized in that a solid-liquid separator is constructed by providing a passage for moving solids toward the solid material.
[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、流入口より接線方向から分離槽内に
導かれた排水は、分離槽内で外壁に沿つて乱流を
生じることなく旋回し、処理済液は流入する排水
と直接ぶつかり合うことなく、流入口より下流で
上方に位置する放出口より、放出されることにな
る。[Function] Since the solid-liquid separator of the present invention is configured as described above, the wastewater introduced into the separation tank from the inlet in a tangential direction does not cause turbulent flow along the outer wall within the separation tank. The treated liquid is discharged from the discharge port located downstream and above the inlet without directly colliding with the inflowing wastewater.
又、分離槽内を旋回する一次流れは、分離槽の
中心部に配設された円筒の表面の抵抗によつて旋
回がゆるくなり、分離槽内の外側から内側に致る
一次流れの周速の変化度合が大きくなる。その結
果、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なり、排水に含まれて
いる固形物は、一次流れと二次流れの相乗効果に
よつて効率良く分離槽の底面に沈降し、固形物移
動通路を通つて固形物溜りに溜ることになる。 In addition, the rotation of the primary flow inside the separation tank becomes slow due to the resistance on the surface of the cylinder installed in the center of the separation tank, and the circumferential velocity of the primary flow from the outside to the inside of the separation tank decreases. The degree of change increases. As a result, the generation of secondary flow that flows vertically in the separation tank and is effective for solid-liquid separation is strengthened, and the solids contained in the wastewater are efficiently removed by the synergistic effect of the primary flow and secondary flow. It often settles to the bottom of the separation tank, passes through the solids transfer passage, and accumulates in the solids reservoir.
[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。[Example] Hereinafter, the present invention will be specifically described based on an example shown in the drawings.
第1図は本発明の1実施例を示す固液分離装置
の断面図で、第2図は第1図における矢視A−A
線に沿つて切断した断面図である。 FIG. 1 is a cross-sectional view of a solid-liquid separator showing one embodiment of the present invention, and FIG. 2 is a cross-sectional view taken along arrow A-A in FIG.
FIG. 3 is a cross-sectional view taken along a line.
図中1は固液分離を行う分離槽で、その外壁2
は図示のように円筒状に形成されるか、或いはイ
ンボリユート状の曲面を持つように形成されてい
る。3は分離槽1の底面で、中心に向つて下向き
に傾斜しており、その中心部には凹状の固形物溜
り4が設けられている。5は分離槽1の外壁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。 In the figure, 1 is a separation tank that performs solid-liquid separation, and its outer wall 2
is formed into a cylindrical shape as shown in the figure, or is formed to have an involute-like curved surface. Reference numeral 3 denotes a bottom surface of the separation tank 1, which is inclined downward toward the center, and a concave solid matter reservoir 4 is provided at the center thereof. Reference numeral 5 denotes an inlet provided on the outer wall 2 of the separation tank 1, and is connected to an inflow path 8 for guiding waste water 7 containing solid matter 6 such as sand into the separation tank 1 from a tangential direction.
9は分離槽1の外壁2に設けられた放出口で、
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。 9 is a discharge port provided on the outer 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.
なお、放出口9は分離槽1内を旋回する流れか
ら見ると、流入口5より下流に位置し、流入口5
より上方に設けられている。 Note that the discharge port 9 is located downstream of the inlet 5 when viewed from the flow swirling in the separation tank 1;
It is located higher up.
12は分離槽1の中心部に例えば同心状に設け
られた比較的径の大き内筒で、その表面には、円
周方向の等分割位置に、流入口5側では少なく、
反対側では大きく半径方向に放射状に突出するひ
れ状の突起片13が設けられている。 Reference numeral 12 denotes an inner cylinder with a relatively large diameter, which is provided, for example, concentrically in the center of the separation tank 1, and on its surface, it is divided into equally divided positions in the circumferential direction, with a smaller number on the inlet port 5 side.
On the opposite side, a fin-like protrusion piece 13 that protrudes radially in a large radial direction is provided.
又、突起片13によつてはさまれた内筒12の
表面には、通水孔14が上下において密になるよ
うに設けられている。 Further, on the surface of the inner cylinder 12 sandwiched between the protruding pieces 13, water passage holes 14 are provided so as to be densely arranged in the upper and lower directions.
15は内筒12の下端を載置するソロバン玉状
の架台で、支持脚16を介して分離槽1の底面3
上に設置されている。17は内筒12の下端の架
台15と分離槽1の底面3との間に設けられた、
底面3上に沈降した固形物6を固定物溜り4に導
く固形物移動通路である。又、P1は固形物溜り
4に溜つた固形物6を排出するための排出ポンプ
であり、P2は放出路11に放出された処理済液
10を汲み上げて送水するための汲み上げポンプ
である。 Reference numeral 15 denotes a bead-shaped pedestal on which the lower end of the inner cylinder 12 is placed, and is attached to the bottom surface 3 of the separation tank 1 via support legs 16.
is installed on top. 17 is provided between the frame 15 at the lower end of the inner cylinder 12 and the bottom surface 3 of the separation tank 1;
This is a solid matter movement passageway that guides the solid matter 6 that has settled on the bottom surface 3 to the fixed matter reservoir 4. Further, P 1 is a discharge pump for discharging the solid matter 6 accumulated in the solid matter reservoir 4, and P 2 is a pump pump for pumping up the treated liquid 10 discharged into the discharge path 11 and supplying water. .
なお、図中Sは分離槽1内を旋回する一次流れ
を示し、Gは分離槽1内を垂直方向に流動する二
次流れを示す。 Note that in the figure, S indicates a primary flow swirling within the separation tank 1, and G indicates a secondary flow flowing vertically within the separation tank 1.
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を通つて流入口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1内
で外壁2に沿つて一次流れSで示すように旋回す
るが、分離槽1の中心部に配設した内筒12周り
を旋回する流れは、内筒12の表面に設けられた
突起片13によつて旋回が急速に減速され、固形
物6の一部は突起片13に衝突して沈降すること
になる。又、旋回する流れが内筒12の表面で急
速に減速されるため、分離槽1内の外側から内側
に致る一次流れSの周速の変化度合が大きくな
り、分離槽1内を垂直方向に流動する二次流れG
の発生が強くなる。従つて、排水7中に含まれて
いる固形物6は、一次流れSと二次流れGの相乗
効果によつて効率良く分離され、分離槽1の底面
3上に沈降することになる。 In the solid-liquid separator of this embodiment having the above configuration, the waste water 7 guided from the inflow port 5 into the separation tank 1 from the tangential direction through the inflow path 8 flows along the outer wall 2 inside the separation tank 1. The primary flow S swirls as shown, but the flow swirling around the inner cylinder 12 disposed at the center of the separation tank 1 is rapidly rotated by the projection piece 13 provided on the surface of the inner cylinder 12. The speed is reduced, and a portion of the solid matter 6 collides with the protrusion piece 13 and settles down. In addition, since the swirling flow is rapidly decelerated on the surface of the inner cylinder 12, the degree of change in the circumferential velocity of the primary flow S from the outside to the inside of the separation tank 1 increases, causing the inside of the separation tank 1 to move vertically. Secondary flow G flowing to
The occurrence of becomes stronger. Therefore, the solids 6 contained in the waste water 7 are efficiently separated by the synergistic effect of the primary flow S and the secondary flow G, and settle on the bottom surface 3 of the separation tank 1.
なお、分離槽1の底面3上に沈降した固形物6
は、二次流れGによつてしだいに中央に押し寄せ
られ、固形物移動通路17を通つて固形物溜り4
に集められ、排出ポンプP1によつて適宜排出さ
れることになる。こうして固形物6が順次沈降し
て分離され、清浄になつた処理済液10は、流入
口5から流入する排水7と直接ぶつかり合うこと
なく、流入口5より下流で上位に位置する放出口
9より、静かにオーバーフローして放出路11に
放出され、汲み上げポンプP2により汲み上げら
れて目的地まで送水されることになる。 In addition, the solid matter 6 that has settled on the bottom surface 3 of the separation tank 1
is gradually pushed to the center by the secondary flow G, and passes through the solid matter transfer passage 17 to the solid matter reservoir 4.
and will be appropriately discharged by the discharge pump P1 . In this way, the solid matter 6 is sequentially sedimented and separated, and the purified treated liquid 10 does not collide directly with the waste water 7 flowing in from the inlet 5, and the discharge port 9 located downstream and above the inlet 5 As a result, the water overflows quietly and is discharged into the discharge channel 11, and is pumped up by the pump P2 and sent to the destination.
なお、本実施例においては、内筒12の表面に
上下において密になるよう通水孔14を設けてい
るが、こうすると二次流れGの一部が内筒12内
を通つて循環するため、二次流れGがより強くな
り、かつ安定化する利点がある。 In this embodiment, the water passage holes 14 are provided on the surface of the inner cylinder 12 so as to be densely arranged in the upper and lower directions. , there is an advantage that the secondary flow G becomes stronger and stabilized.
但し、内筒12は単なる円筒であつても効果が
あることが確認されているが、内筒12周りを旋
回する流れを急速に減速させるための手段とし
て、例えば、内筒12の表面に縦に凹凸を設けた
り、点状に凹凸を設けたり、凹溝や半球状の溝を
設けたり、或いは円筒12の内部に通ずる各種形
状の孔を設けることができ、必要に応じてそれら
を組合せた形状を採用することにより、二次流れ
Gの強さを最適に設定することができる。 However, it has been confirmed that it is effective even if the inner cylinder 12 is a simple cylinder, but as a means to rapidly decelerate the flow swirling around the inner cylinder 12, for example, It is possible to provide unevenness, dotted unevenness, grooves or hemispherical grooves, or holes of various shapes that communicate with the inside of the cylinder 12, and these can be combined as necessary. By adopting this shape, the strength of the secondary flow G can be optimally set.
又、放出口9にフイルターを設置しておけば、
放出口9を流下する恐れのある微少な固形物6を
も完全に除去することができ、きわめて好都合で
ある。 Also, if a filter is installed at the discharge port 9,
It is extremely convenient that even minute solid matter 6 that may flow down the discharge port 9 can be completely removed.
又、本実施例においては、流入路8は湾曲させ
ているが、これを直線状にしても良く、自然流下
方式でも、ポンプにより排水7を強制的に分離槽
1内に導くようにしても良い。又、内筒12の表
面に設ける凹凸形状や内筒12の支持方法等は、
図示の実施例に限定されるものではなく、必要に
応じ任意に設計変更し得るものである。 Further, in this embodiment, the inflow channel 8 is curved, but it may be straight, or a gravity flow method may be used, or the waste water 7 may be forcibly guided into the separation tank 1 by a pump. good. In addition, the uneven shape provided on the surface of the inner cylinder 12, the method of supporting the inner cylinder 12, etc.
The present invention is not limited to the illustrated embodiment, and the design can be changed as necessary.
[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の、外壁周辺に
おける乱流の発生がなく、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、一次流
れと二次流れとの相乗効果によつて固形物を効率
的に分離することができる。[Effects of the Invention] As specifically explained above, according to the present invention, turbulence does not occur around the outer wall of the primary flow swirling in the separation tank, and the secondary flow is effective for solid-liquid separation. Since the generation can be strengthened, solids can be efficiently separated by the synergistic effect of the primary flow and the secondary flow.
又、内筒の中空状に形成し、底から二次流れの
一部を流入させ上側の通水孔から排出させている
ので、二次流れが強くなり、かつ安定化させるこ
とができる利点がある。 In addition, the inner cylinder is formed into a hollow shape, and a part of the secondary flow flows in from the bottom and is discharged from the upper water hole, which has the advantage of making the secondary flow stronger and more stable. be.
又、構造も比較的簡単で安価に製作することが
できると共に、故障も少なく、長期間安定して連
続運転することができる。等多くの利点を有し、
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。 In addition, the structure is relatively simple and can be manufactured at low cost, and there are few failures, and it can be operated stably and continuously for a long period of time. It has many advantages such as
It can be used to separate solids from wastewater containing solids such as sand, such as sewage or sewage, to obtain a clean treated liquid, and can provide a practically extremely effective solid-liquid separation device. It is.
第1図は本発明の1実施例を示す固液分離装置
の断面図で、第2図は第1図における矢視A−A
線に沿つて切断した断面図である。
1……分離槽、2……外壁、3……底面、4…
…固形物溜り、5……流入口、6……固形物、7
……排水、9……放出口、10……処理済液、1
2……内筒、13……突起片、15……架台、1
7……固形物移動通路、S……一次流れ、G……
二次流れ。
FIG. 1 is a cross-sectional view of a solid-liquid separator showing one embodiment of the present invention, and FIG. 2 is a cross-sectional view taken along arrow A-A in FIG.
FIG. 3 is a cross-sectional view taken along a line. 1...Separation tank, 2...Outer wall, 3...Bottom surface, 4...
...Solid matter reservoir, 5...Inflow port, 6...Solid matter, 7
... Drainage, 9 ... Outlet, 10 ... Treated liquid, 1
2... Inner cylinder, 13... Projection piece, 15... Frame, 1
7...Solid material transfer passage, S...Primary flow, G...
Secondary flow.
Claims (1)
持ち、底面が中心に向かつて下向きに傾斜し、ほ
ぼ中心部に凹状の固形物溜りを設けた分離槽の外
壁に、砂等の固形物を含む排水を接線方向から分
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、放出口が
流入口より下流で上方に位置するように設けると
共に、分離槽の中心部に、中空状で且つ少なくと
も上側に通水孔を設けた内筒を配設し、内筒の下
端を載置する架台と分離槽の底面との間に、固形
物溜りに向かう固形物移動通路を設けたことを特
徴とする固液分離装置。1 The outer wall of a separation tank has a cylindrical or involute-shaped curved surface, the bottom faces the center and slopes downward, and a concave solids reservoir is provided in the center. An inlet that introduces wastewater into the separation tank tangentially, and an outlet that guides the treated liquid after separating solids from the separation tank to the outside are provided so that the outlet is located downstream and above the inlet. At the same time, a hollow inner cylinder with a water passage hole provided at least on the upper side is arranged in the center of the separation tank, and a solid material is placed between the base on which the lower end of the inner cylinder is placed and the bottom of the separation tank. A solid-liquid separator characterized in that a solid matter moving path toward a reservoir is provided.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1218686A JPS62171718A (en) | 1986-01-24 | 1986-01-24 | Solid-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1218686A JPS62171718A (en) | 1986-01-24 | 1986-01-24 | Solid-liquid separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62171718A JPS62171718A (en) | 1987-07-28 |
| JPH0363401B2 true JPH0363401B2 (en) | 1991-10-01 |
Family
ID=11798376
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1218686A Granted JPS62171718A (en) | 1986-01-24 | 1986-01-24 | Solid-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62171718A (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6012108A (en) * | 1983-07-01 | 1985-01-22 | Ebara Corp | Solid-liquid separation apparatus |
| JPS60114307A (en) * | 1983-11-28 | 1985-06-20 | Unyusho Kowan Gijutsu Kenkyusho | Treating apparatus of surplus water from reclamation |
-
1986
- 1986-01-24 JP JP1218686A patent/JPS62171718A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62171718A (en) | 1987-07-28 |
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