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JPH0112525B2 - - Google Patents

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Publication number
JPH0112525B2
JPH0112525B2 JP61012188A JP1218886A JPH0112525B2 JP H0112525 B2 JPH0112525 B2 JP H0112525B2 JP 61012188 A JP61012188 A JP 61012188A JP 1218886 A JP1218886 A JP 1218886A JP H0112525 B2 JPH0112525 B2 JP H0112525B2
Authority
JP
Japan
Prior art keywords
separation tank
solids
inner cylinder
solid
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
Application number
JP61012188A
Other languages
Japanese (ja)
Other versions
JPS62171720A (en
Inventor
Tetsuo Nishida
Kazuo Hirahara
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 JP1218886A priority Critical patent/JPS62171720A/en
Publication of JPS62171720A publication Critical patent/JPS62171720A/en
Publication of JPH0112525B2 publication Critical patent/JPH0112525B2/ja
Granted legal-status Critical Current

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  • Centrifugal Separators (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、分離槽内を
旋回する一次流れが弱いため、分離効率を高くす
ることができないという欠点があつた。
[Problems to be Solved by the Invention] However, the conventional solid-liquid separator has a drawback in that it is not possible to increase the separation efficiency because the primary flow swirling in the separation tank is weak.

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到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を強制的に発
生させると共に、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 has been proposed in view of the above-mentioned conventional drawbacks, and the present invention forcibly generates a primary flow swirling in a separation tank, and also strengthens the generation of a secondary flow that is effective for solid-liquid separation. The purpose is to provide a practically effective solid-liquid separation device with improved efficiency.

[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
導く放出口を設けると共に、分離槽のほぼ中心部
に、内筒をその下端と分離槽の底面との間に固形
物溜りに向う固形物移動通路が形成されるように
支承し、その内筒を垂直軸回りに回転させる駆動
手段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 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 concave shape in the center. An inlet for introducing wastewater containing solids such as sand into the separation tank on the outer wall of the separation tank provided with a solid matter reservoir;
A discharge port is provided to guide the treated liquid from inside the separation tank to the outside after solids have been separated, and an inner cylinder is provided at approximately the center of the separation tank between its lower end and the bottom of the separation tank toward the solids reservoir. The solid-liquid separation device is characterized in that the solid-liquid separation device is supported so that a solid material transfer passage is formed and is provided with a driving means for rotating the inner cylinder around a vertical axis.

[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、垂直軸回りに回転する内筒によつて分離槽内
を強い一次流れとなつて旋回することになる。
又、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が大きくなる
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強くなる。その結果、排
水中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。他方、処理済液は放出口より放出さ
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 is forced into the separation tank by the inner cylinder rotating around the vertical axis. It becomes a primary flow and swirls.
In addition, 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 inside the separation tank is effective for solid-liquid separation. The occurrence of becomes stronger. As a result, the solids contained in the wastewater efficiently settle to the bottom of the separation tank due to the synergistic effect of the primary flow and secondary flow, and accumulate in the solids reservoir through the solids transfer passage. Become. On the other hand, the treated liquid will be discharged from the discharge port.

[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、中心よりやや外れた位置
に開口し、砂等の固形物6を含む排水7を分離槽
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. 5 is the outer wall 2 of the separation tank 1
The inlet is opened at a position slightly off center and is connected to an inlet passage 8 for guiding waste water 7 containing solid matter 6 such as sand into the separation tank 1.

9は分離槽1の外壁2に設けられたフイルター
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。
Reference numeral 9 denotes a discharge port having a filter provided on the outer wall 2 of the separation tank 1, and is connected to a discharge path 11 that guides the treated liquid 10 after separating the solid matter 6 from the inside of the separation tank 1 to the outside.

なお、放出口9は流入口5に対し約300〜330度
下流にずれた位置に設けられているが、放出口9
の前面には邪魔板12が設けられており、分離槽
1内を旋回する排水7が、直接放出口9に流れ込
まないように配慮されている。
Note that the outlet 9 is located at a position shifted approximately 300 to 330 degrees downstream from the inlet 5;
A baffle plate 12 is provided on the front surface of the separation tank 1 to prevent the waste water 7 swirling in the separation tank 1 from flowing directly into the discharge port 9.

次に13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い内筒又は傾斜角度
の小さい載頭円錐状の内筒で、その下端には浮力
によつて内筒13を支えるための円形の中空箱1
4が取付けられており、その中空箱14の外周に
は、三角形状に突き出た環状案内板15が設けら
れている。なお、内筒13及び環状案内板15の
表面には、円周方向の等分割位置に、凹状の縦溝
16が設けられており、内筒13の縦溝16内に
は、通水孔17が上下において密になるよう設け
られている。18は分離槽1の天井板19上に設
置されたモータで、その回転軸20の下端には、
内筒13が支承されており、モータ18を駆動す
ると、内筒13が矢印方向に回転するようになつ
ている。なお、21は内筒13の下端の中空箱1
4及び環状案内板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
形物溜り4に導くための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。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。
Next, reference numeral 13 denotes an inner cylinder having a relatively large diameter or a truncated conical shape with a small inclination angle, which is provided concentrically in the center of the separation tank 1, and the lower end of the inner cylinder is provided with a buoyant force. Circular hollow box 1 for supporting 13
4 is attached to the hollow box 14, and on the outer periphery of the hollow box 14, a triangularly protruding annular guide plate 15 is provided. Note that concave vertical grooves 16 are provided on the surfaces of the inner cylinder 13 and the annular guide plate 15 at equally divided positions in the circumferential direction. are arranged so that they are densely arranged above and below. 18 is a motor installed on the ceiling plate 19 of the separation tank 1, and the lower end of its rotating shaft 20 has a
An inner cylinder 13 is supported, and when a motor 18 is driven, the inner cylinder 13 rotates in the direction of the arrow. Note that 21 is a hollow box 1 at the lower end of the inner cylinder 13.
4 and an annular guide plate 15 and the bottom surface 3 of the separation tank 1 is a solid matter moving passage for guiding the solid matter 6 settled on the bottom surface 3 to the solid 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. It is. In addition, S in the figure
G 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より分離槽1
内に導かれた排水7は、垂直軸回りに回転する内
筒13によつて分離槽1内を強い一次流れSとな
つて旋回することになる。
In the solid-liquid separator of this embodiment having the above configuration, the separation tank 1 is connected to the inlet 5 through the inflow path 8.
The waste water 7 guided inside becomes a strong primary flow S and swirls inside the separation tank 1 by the inner cylinder 13 rotating around a vertical axis.

分離槽1内に強制的に発生せしめられたこの強
い一次流れSは、内側と外側との流速に差が生
じ、分離槽1内を旋回する一次流れS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
くなつて、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、強い一
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、分離層1の底面3上に沈降すること
になる。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、環状案内板15によつて案内されな
がら、固形物移動通路21を通つてスムーズに固
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、清浄となつた処理済液1
0は、邪魔板12の裏側にあるフイルターを有す
る放出口9より、静かに放出路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。
This strong primary flow S that is forcibly generated within the separation tank 1 has a difference in flow velocity between the inside and outside, and the primary flow S swirling inside the separation tank 1 flows from the outside to the inside of the separation tank 1. As the degree of change in circumferential velocity that reaches , becomes greater, the generation of secondary flow that is effective for solid-liquid separation and flows vertically within the separation tank 1 becomes stronger. Therefore, the solids 6 contained in the waste water 7 are efficiently separated by the synergistic effect of the strong primary flow S and the secondary flow G, and settle on the bottom surface 3 of the separation layer 1. The solids 6 that have settled on the bottom surface 3 of the separation tank 1 are gradually pushed toward the center by the secondary flow G, and are guided by the annular guide plate 15 through the solids transfer passage 21. The solids are smoothly collected in the solids reservoir 4, and are appropriately discharged by the discharge pump P1 . In this way, the solid matter 6 is sequentially sedimented and separated, and the treated liquid 1 becomes clean.
0 is quietly discharged into the discharge path 11 from the discharge port 9 having a filter on the back side of the baffle plate 12,
The water will be pumped up by pump P 2 and sent to the destination.

なお、本実施例においては、回転される内筒1
3の表面に縦溝16を設けて、一次流れSの発生
を強くすると共に、その縦溝16内の上下に、通
水孔17を設けているが、こうすると、二次流れ
Gの一部が内筒13内を通つて循環するため、二
次流れGがより強くなる利点がある。
In addition, in this embodiment, the inner cylinder 1 to be rotated
3 is provided with vertical grooves 16 on the surface thereof to strengthen the generation of the primary flow S, and water holes 17 are provided above and below within the vertical grooves 16. Since it circulates through the inner cylinder 13, there is an advantage that the secondary flow G becomes stronger.

次に、第3図は内筒13の他の実施例を区画し
て簡略的に示す断面図である。
Next, FIG. 3 is a sectional view schematically showing another embodiment of the inner cylinder 13.

内筒13は回転されるため、イで示すように単
なる円筒であつても一応の効果があるが、ロで示
すように通水孔17を設けたり、ハで示すように
凹状の縦溝16を設けたり、ニで示すように凸状
の縦突起片22を設けたり、単なる溝や突起を点
状に設けておけば、一次流れSをさらに強くする
ことができる。但し、必要に応じてイ〜ニで示す
実施例を組み合せても良い。
Since the inner cylinder 13 is rotated, it is effective to some extent even if it is a simple cylinder as shown in A, but it is possible to provide a water passage hole 17 as shown in B or a concave vertical groove 16 as shown in C. The primary flow S can be further strengthened by providing a convex vertical protrusion piece 22 as shown in D, or by providing simple grooves or protrusions in the form of dots. However, the embodiments shown in A to D may be combined as necessary.

又、第3図において点線で示すように、通水孔
17を有する内筒13の内部の上部に、縦突起片
23を放射状に設けておけば、内筒13の回転に
よつて内筒13内の排水7が、縦突起片23によ
つて掻き回され、遠心力の作用によつて通水孔1
7から内筒13の外部に抽出されるので、二次流
れGをさらに強くすることができる。
Further, as shown by dotted lines in FIG. 3, if vertical protrusions 23 are provided radially at the upper part of the inside of the inner cylinder 13 having the water passage hole 17, the rotation of the inner cylinder 13 will cause the inner cylinder 13 to The drainage water 7 inside is stirred by the vertical protrusion piece 23, and the water passage hole 1 is stirred by the action of centrifugal force.
7 to the outside of the inner cylinder 13, the secondary flow G can be made even stronger.

次に第4図は、内筒13のさらに他の実施例を
示す部分断面図である。第4図に示す内筒13内
には、スパイラル羽根24が設けられており、内
筒13の上部と下部に、比較的径の大きい通水孔
25が設けられている。このようにしておくと、
内筒13の回転によつて内筒13内の排水7が、
スパイラル羽根24のポンプ作用によつて下から
上に汲み上げられ、内筒13の下部の通水孔25
から内筒13内に入つた排水7は、内筒13の上
部の通水孔25から内筒13外に排出されること
になり、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Gの発生をさらに強くするこ
とができ、きわめて好都合である。
Next, FIG. 4 is a partial sectional view showing still another embodiment of the inner cylinder 13. A spiral blade 24 is provided inside the inner cylinder 13 shown in FIG. 4, and water holes 25 having a relatively large diameter are provided at the upper and lower parts of the inner cylinder 13. If you do it this way,
Due to the rotation of the inner cylinder 13, the drainage water 7 inside the inner cylinder 13 is
The water is pumped up from the bottom to the top by the pump action of the spiral vane 24, and the water is pumped up from the bottom to the top through the water passage hole 25 at the bottom of the inner cylinder 13.
The waste water 7 that has entered the inner cylinder 13 is discharged to the outside of the inner cylinder 13 from the water passage hole 25 at the top of the inner cylinder 13, which is effective for solid-liquid separation flowing vertically inside the separation tank 1. This is extremely advantageous because the generation of the secondary flow G can be further strengthened.

但し、内筒13を垂直軸回りに回転させる駆動
手段としては、ベルトやチエーン等を用いても良
く、その他の構造も、必要に応じて任意に設計変
更し得るものである。
However, as a driving means for rotating the inner cylinder 13 around the vertical axis, a belt, a chain, etc. may be used, and the design of other structures can be changed as desired.

[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強い一次流れを強制的に発生
させることができると共に、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。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。
[Effects of the Invention] As specifically explained above, according to the present invention, it is possible to forcibly generate a strong primary flow swirling in the separation tank, and also to generate a secondary flow effective for solid-liquid separation. Since the flow rate can be increased, solids can be efficiently separated due to the synergistic effect of the primary flow and the secondary flow. 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 sewage and sewage, and is used to separate solids from wastewater containing solids such as sand and obtain a clean treated liquid, and is extremely effective in practice. A separation device can be provided.

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

第1図は本発明の1実施例を示す固液分離装置
の第2図における矢視B−AB線に沿つて切断し
た断面図で、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、第3図は内筒の他の
実施例を区画して簡略的に示す断面図、第4図は
内筒のさらに他の実施例を示す部分断面図であ
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、8……流入路、9……放出口、10…
…処理済液、11……放出路、12……邪魔板、
13……内筒、14……中空箱、15……環状案
内板、16……縦溝、17……通水孔、18……
モータ、19……天井板、20……回転軸、21
……固形物移動通路、22……縦突起片、23…
…縦突起片、24……スパイラル羽根、25……
通水孔、S……一次流れ、G……二次流れ。
FIG. 1 is a sectional view taken along the line B-AB in FIG. 2 of a solid-liquid separator showing one embodiment of the present invention, and FIG. 2 is a sectional view taken along the line A-A in FIG. 1.
FIG. 3 is a cross-sectional view showing another embodiment of the inner cylinder, and FIG. 4 is a partial cross-sectional view showing still another embodiment of the inner cylinder. . 1...Separation tank, 2...Outer wall, 3...Bottom surface, 4...
...Solid matter reservoir, 5...Inflow port, 6...Solid matter, 7
...Drainage, 8...Inflow channel, 9...Outlet, 10...
... Treated liquid, 11 ... Discharge path, 12 ... Baffle plate,
13... Inner cylinder, 14... Hollow box, 15... Annular guide plate, 16... Vertical groove, 17... Water hole, 18...
Motor, 19... Ceiling plate, 20... Rotating shaft, 21
...Solid material transfer passage, 22...Vertical protrusion piece, 23...
... Vertical projection piece, 24 ... Spiral blade, 25 ...
Water hole, S...primary flow, G...secondary flow.

Claims (1)

【特許請求の範囲】[Claims] 1 外壁が円筒状或いは円筒状の導入側の一部に
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
を含む排水を分離槽内に導くほぼ接線方向に設け
た流入口と、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ると共に、分離槽
の中心部に、円形状の内筒をその下端と分離槽の
底面との間に固形物溜りに向かう固形物移動通路
が形成されるように支承し、その内筒を垂直軸回
りに回転させる駆動手段を設けたことを特徴とす
る固液分離装置。
1. An outer wall of a separation tank in which the outer wall is cylindrical or has an involute-shaped curved surface on a part of the cylindrical introduction side, the bottom surface slopes downward toward the center, and a concave solids reservoir is provided approximately at the center of the outer wall. In addition, an inlet is provided in the almost tangential direction to guide wastewater containing solids such as sand into the separation tank, and an outlet is provided to guide the treated liquid after solids have been separated from the separation tank to the outside. A circular inner cylinder is supported in the center of the tank so that a passage for moving solids toward the solids reservoir is formed between its lower end and the bottom of the separation tank, and the inner cylinder is rotated around a vertical axis. A solid-liquid separator characterized in that it is provided with a driving means for driving the solid-liquid separator.
JP1218886A 1986-01-24 1986-01-24 Solid-liquid separator Granted JPS62171720A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1218886A JPS62171720A (en) 1986-01-24 1986-01-24 Solid-liquid separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1218886A JPS62171720A (en) 1986-01-24 1986-01-24 Solid-liquid separator

Publications (2)

Publication Number Publication Date
JPS62171720A JPS62171720A (en) 1987-07-28
JPH0112525B2 true JPH0112525B2 (en) 1989-03-01

Family

ID=11798431

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1218886A Granted JPS62171720A (en) 1986-01-24 1986-01-24 Solid-liquid separator

Country Status (1)

Country Link
JP (1) JPS62171720A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02265605A (en) * 1989-04-06 1990-10-30 Tetsuo Nishida Solid-liquid separator
US6811697B2 (en) * 2001-10-26 2004-11-02 Smith & Loveless Apparatus and method for extracting particles from a fluid stream
JP4774491B2 (en) * 2006-06-09 2011-09-14 株式会社西原環境 Solid-liquid separation system

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6022912A (en) * 1983-07-15 1985-02-05 Tetsuo Nishida Solid separating apparatus

Also Published As

Publication number Publication date
JPS62171720A (en) 1987-07-28

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