JPH08252404A - Oil and water separating apparatus - Google Patents

Oil and water separating apparatus

Info

Publication number
JPH08252404A
JPH08252404A JP5861595A JP5861595A JPH08252404A JP H08252404 A JPH08252404 A JP H08252404A JP 5861595 A JP5861595 A JP 5861595A JP 5861595 A JP5861595 A JP 5861595A JP H08252404 A JPH08252404 A JP H08252404A
Authority
JP
Japan
Prior art keywords
oil
separation
holes
plates
hole
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.)
Pending
Application number
JP5861595A
Other languages
Japanese (ja)
Inventor
Tsunehiro Noda
倫弘 野田
Katsuhiko Tokunaga
雄彦 徳永
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP5861595A priority Critical patent/JPH08252404A/en
Publication of JPH08252404A publication Critical patent/JPH08252404A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE: To improve oil and water separating function with porous separation plates by differing the positrons of holes of first separation plates and second separation plates 2 in the up and down direction and making a liquid which passes the differing holes come into collision against the walls of separating plates set below. CONSTITUTION: While passing respective holes 23a, 23b of separation plates 21a, 21b laid in a multilayered state, a cleaning liquid which flows into an oil-water separating tank 10 flows down in the tank. Since those holes 23a, 23b are made to differ for every separation plate 21a, 21b, immediate after the cleaning liquid passes the holes 23a or holes 23b, the cleaning liquid surely comes into collision against the walls of the next separation plates 21b or 21a and coarsening function is effectively carried out and fine particles are converted into coarse particles. Further, during the process in which the coarse particles C flows slowly to the holes of the next separation plate at a proper flow rate on a hole-free tilting path E, oil-water separation of the coarse particles C can be carried out effectively based on the gravity difference. Consequently, oil particles C which float and are separated in the path E gather in the center part along the tilting faces in the rear sides of respective separation plates 21a, 21b and are collected in an oil collecting chamber 14.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、微粒子を含む液体の該
微粒子を粗粒子化し、その比重差により浮上分離させる
油水分離装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an oil / water separator for coarsening fine particles of a liquid containing fine particles and floating and separating them by the difference in specific gravity.

【0002】[0002]

【従来の技術】従来の多孔板を円錐状に形成した分離板
は、全面に孔が設けられており、同一の寸法、形状の複
数の分離板を隙間を設けて積み重ねている。したがっ
て、どうしても上下に隣り合った分離板の孔が部分的に
同じ位置になり、液体の流れが複数の分離板をショート
パスして複数の分離板を積み重ねた効果が低減し、油水
分離性能に悪影響を与えていた。
2. Description of the Related Art A conventional separator having a conical perforated plate is provided with holes on the entire surface, and a plurality of separators having the same size and shape are stacked with a gap. Therefore, the holes of the separating plates vertically adjacent to each other are partially located at the same position, and the effect of the liquid flow short-passing the separating plates and stacking the separating plates is reduced, and the oil-water separation performance is reduced. It had a bad effect.

【0003】[0003]

【発明が解決しようとする課題】本発明は、多孔分離板
による油水分離性能を向上した油水分離装置を提供する
ことを目的としている。
SUMMARY OF THE INVENTION It is an object of the present invention to provide an oil / water separator having improved oil / water separation performance by means of a porous separator.

【0004】[0004]

【課題を解決するための手段】本発明によれば、微粒子
を含む液体の該微粒子を粗粒子化し、その比重差により
浮上分離させる油水分離装置において、多孔を有し円錐
状に形成されて中央孔を備えた複数の第1及び第2の分
離板を、油水分離槽の内部に交互に隙間を設けて積み重
ねて構成し、第1の分離板と第2の分離板との孔の上下
方向の位置はずれていて孔を通過した液体が下方の分離
板の壁に衝突するように構成している。
According to the present invention, in an oil-water separation device in which the fine particles of a liquid containing fine particles are coarsened and float-separated by the difference in specific gravity thereof, the oil-water separation apparatus is formed into a conical shape having a perforation and has a central portion A plurality of first and second separation plates having holes are stacked inside the oil-water separation tank by alternately providing gaps, and the first separation plate and the second separation plate are arranged in the vertical direction of the holes. The liquid which has deviated from the position and has passed through the hole collides with the wall of the lower separating plate.

【0005】更に本発明によれば、前記第1および第2
の分離板の孔を通過した液体が次の分離板の壁に衝突し
て流れを変えた後に次の孔に流れる通路が第1および第
2の分離板の孔のない壁で挟まれて形成され、その通路
の断面形状が浮上分離作用をするように傾斜板状である また本発明によれば、微粒子を含む液体の該微粒子を粗
粒子化し、その比重差により浮上分離させる油水分離装
置において、多孔を有し円錐状に形成されて中央孔を備
えた複数の第1及び第2の分離板を、油水分離槽の内部
に交互に隙間を設けて積み重ね、前記第1の分離板の各
孔を外周部に設け、前記第2の分離板の各孔を内周部に
設けて両分離板の各孔の間にコワレッシング作用により
粗粒子化した油粒子が比重差により浮上分離しながら流
れる無孔の傾斜通路を形成している。
Further in accordance with the present invention, the first and second
The liquid that has passed through the holes of the first separating plate collides with the wall of the next separating plate and changes its flow, and then a passage that flows to the next hole is formed by being sandwiched between the walls without holes of the first and second separating plates. According to the present invention, the cross-sectional shape of the passage is a slanting plate shape so as to have a floating separation action. A plurality of first and second separation plates that are porous and formed in a conical shape and that have a central hole are alternately stacked inside the oil-water separation tank with a gap between them, and each of the first separation plates is A hole is provided in the outer peripheral portion, and each hole of the second separating plate is provided in the inner peripheral portion, and the oil particles coarsened by the showering action are floated and separated between the respective holes of both separating plates due to the difference in specific gravity. It forms a flowing non-perforated inclined passage.

【0006】更に本発明によれば、第1および第2の分
離板の各孔には、下向きのバーリング加工が施されてい
る そして本発明によれば、孔の位置が異なる第1および第
2の分離板が複数種類用意されている。
Further, according to the present invention, downward burring processing is applied to each hole of the first and second separation plates. According to the present invention, the first and second holes having different positions are provided. There are multiple types of separation plates.

【0007】[0007]

【作用】上記のように構成された油水分離装置において
は、液体はバーニング加工を施された孔を流下するごと
に、下方の分離板の壁に確実に衝突し、コワレッシング
作用により油微粒子が次々と粗粒子化される。そして、
無孔の傾斜通路を流れる間に、粗粒子化した油粒子が浮
上分離し、傾斜通路の上面に沿ってバーリング加工され
た孔の縁を回り中央孔を通り、浮上して外部に排出され
る。
In the oil-water separation device configured as described above, the liquid surely collides with the wall of the lower separation plate every time the liquid flows down through the burned hole, and the oil fine particles are separated by the showering action. Grains are made one after another. And
While flowing through the non-perforated inclined passage, the coarse oil particles are floated and separated, and along the upper surface of the inclined passage, around the edge of the burring hole, pass through the central hole, float, and are discharged to the outside. .

【0008】[0008]

【実施例】以下図面を参照して本発明の実施例を説明す
る。
Embodiments of the present invention will be described below with reference to the drawings.

【0009】図1において、図示の例では洗浄槽1の送
出口2は、送出回路L1により循環ポンプ3、流量計4
及びフィルタ5を介して全体を符号10で示す油水分離
槽の流入口12に接続されている。その油水分離槽10
の処理水出口13は、戻り回路L2により洗浄槽1の上
部に接続され、頂部の油抽出口15は、油水分離槽10
の内圧により油抽出回路L3を介して抽出油受け8に接
続されている。なお、送出回路L1には、圧力計6が設
けられている。
In FIG. 1, in the illustrated example, the outlet 2 of the cleaning tank 1 is a circulation pump 3 and a flow meter 4 by a delivery circuit L1.
Also, it is connected via a filter 5 to an inflow port 12 of the oil / water separation tank, which is generally designated by 10. The oil-water separation tank 10
The treated water outlet 13 is connected to the upper part of the cleaning tank 1 by the return circuit L2, and the oil extraction port 15 at the top is connected to the oil water separation tank 10
It is connected to the oil extraction receiver 8 via the oil extraction circuit L3 by the internal pressure of. A pressure gauge 6 is provided in the delivery circuit L1.

【0010】図2ないし図4において、油水分離槽10
の筒状の本体11の上部には、流入口12が設けられ、
底部には、処理水出口13が設けられ、頂部には、油溜
室14を介して油抽出口15が設けられている。
2 to 4, the oil-water separation tank 10 is shown.
An inflow port 12 is provided on the upper part of the cylindrical main body 11 of
A treated water outlet 13 is provided at the bottom, and an oil extraction port 15 is provided at the top via an oil reservoir chamber 14.

【0011】その本体11の内部には、下部の処理水溜
室16と頂部の油溜室14との間に、全体を符号20で
示す分離板積重体が収められている。その分離板積重体
20は、複数(図示の例ではそれぞれ5個)の第1の分
離板21aと第2の分離板21bとを、交互に隙間Dを
設け積み重ねて構成されている。
Inside the main body 11, between the lower treated water storage chamber 16 and the top oil storage chamber 14, there is housed a separation plate stack indicated by reference numeral 20 as a whole. The separator stack 20 is formed by stacking a plurality (five in the illustrated example) of first separators 21a and second separators 21b with a gap D alternately.

【0012】その第1の分離板21aは、中央に中央孔
22が設けられ下方に拡径する円錐状に形成されてお
り、外周部には複列(図示の例では2列)に多数の孔2
3aが形成されている。そして、孔23aには、バーリ
ング加工により分離板21aから下向きに湾曲したカエ
リ部である下向きの突縁部24が突設されている。
The first separating plate 21a is formed in a conical shape having a central hole 22 in the center and expanding downward, and a plurality of rows (two rows in the illustrated example) are formed in the outer peripheral portion. Hole 2
3a is formed. The hole 23a is provided with a downward protruding edge portion 24 which is a burring portion curved downward from the separating plate 21a by burring.

【0013】他方、第2の分離板21bは、第1の分離
板21aと実質的に同様に構成され、内周部には複列
(図示の例では3列)に突縁部24を備えた多数の孔2
3bが形成されている。したがって、分離板積重体20
の中央には、各中央孔22により中央通路Lが形成さ
れ、また、両分離板21a、21bの間には、孔23a
と孔23bとの間の孔23a、23bのない範囲Wに、
傾斜通路Eが形成されている。なお、傾斜通路Eの傾角
θは、例えば10°〜20°に形成されている。
On the other hand, the second separating plate 21b is configured substantially the same as the first separating plate 21a, and the inner peripheral portion is provided with the projecting edge portions 24 in a plurality of rows (three rows in the illustrated example). Many holes 2
3b is formed. Therefore, the separator stack 20
A central passage L is formed at the center of each of the central holes 22 and a hole 23a is formed between the separating plates 21a and 21b.
In a range W where there is no hole 23a, 23b between
An inclined passage E is formed. The inclination angle θ of the inclined passage E is set to, for example, 10 ° to 20 °.

【0014】次に、作用について説明する。Next, the operation will be described.

【0015】洗浄槽1の洗浄液(水、洗剤及び微粒油粒
子の混合液)Aは、循環ポンプ3により送出回路L1か
ら油水分離槽10の流入口12に送り込まれる。この
際、流量計4、圧力計及びフィルタ5により油水分離槽
10に流入する洗浄液Aの圧力及び流量がコントロール
され、スラッジが除去される。そこで、油水分離槽10
に流入した洗浄液Aは、多層に積み重ねられた分離板2
1a、21bの各孔23a、23bを通過しながら流下
する。それらの孔23a、23bは図5に示すように、
各分離板21a、21bごとに交互にずれているので、
洗浄液Aが孔23a又は孔23bを通過した直後に、次
の分離板21b又は21aの壁に確実に衝突し、コワレ
ッシング作用が効果的に行われて微細粗子が粗粒子化さ
れる。
The cleaning liquid (mixed liquid of water, detergent and fine oil particles) A in the cleaning tank 1 is sent from the delivery circuit L1 to the inlet 12 of the oil / water separation tank 10 by the circulation pump 3. At this time, the flow meter 4, the pressure gauge, and the filter 5 control the pressure and flow rate of the cleaning liquid A flowing into the oil / water separation tank 10 to remove sludge. Therefore, the oil-water separation tank 10
The cleaning liquid A that has flowed into the separation plate 2 is stacked in multiple layers.
It flows down while passing through the respective holes 23a and 23b of 1a and 21b. The holes 23a and 23b are, as shown in FIG.
Since the separation plates 21a and 21b are alternately displaced,
Immediately after the cleaning liquid A passes through the hole 23a or the hole 23b, it collides with the wall of the next separating plate 21b or 21a without fail, and the showering effect is effectively performed to coarsen the fine coarse particles.

【0016】更に、この粗粒子化した油粒子Cは、各分
離板21a、21b間の無孔の傾斜通路Eを適切な流速
でゆっくりと次の分離板の孔へ流れる過程で、その比重
差により油水分離が効果的に行われる。
Further, the coarse oil particles C flow through the non-perforated inclined passage E between the separation plates 21a and 21b slowly at an appropriate flow rate to the holes of the next separation plate, and the difference in specific gravity between them. This effectively separates oil and water.

【0017】これにより通路E内で浮上分離した油粒子
Cは、各分離板21a、21bの裏面の傾斜面に沿って
中央部に集り、中央通路Lを介して油溜室14に集る。
この際、油粒子Cは、孔23a、23bの突縁部24の
回りを回って移動するので、孔23a、23bを通過す
る洗浄液Aと再結合することが阻止される。
As a result, the oil particles C floated and separated in the passage E gather in the central portion along the inclined surfaces on the back surfaces of the separation plates 21a and 21b, and then in the oil reservoir 14 via the central passage L.
At this time, the oil particles C move around the projecting edge portions 24 of the holes 23a and 23b, so that they are prevented from recombining with the cleaning liquid A passing through the holes 23a and 23b.

【0018】そして、油溜室14に集った素粒子化した
油粒子Cは、内圧により油抽出回路L3を介して抽出油
受けに抽出され、粗粒子が分離された処理水Bは、処理
水出口13から戻り回路L2を介して洗浄槽1に戻され
る。
Then, the oil particles C which have been made into elementary particles and collected in the oil reservoir 14 are extracted by the internal pressure into the oil extraction receiver via the oil extraction circuit L3, and the treated water B from which the coarse particles are separated is treated. It is returned from the water outlet 13 to the cleaning tank 1 via the return circuit L2.

【0019】上記作用において、分離板21a、21b
の枚数を増減することにより、いわゆるコワレッシング
面積すなわち分離板面積の増減及び傾斜通路Eの合計長
さを自由に変え、油水分離効率を良くすることができ
る。
In the above operation, the separation plates 21a, 21b
By increasing / decreasing the number of sheets, it is possible to freely change the so-called collapsing area, that is, the area of the separating plate and the total length of the inclined passages E, and improve the oil / water separation efficiency.

【0020】[0020]

【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。 (1) 従来の分離板方式では分離板全面に孔を設けて
いたので、上下に隣り合った分離板の孔がどうしても重
なる部分があり、この部分では洗浄液の流れがショート
パスしてしまい、隣の分離板の壁に洗浄液の衝突動作が
なく、コワレッシング作用が減少する傾向があったが、
本発明においては確実にコワレッシング作用を行わせ、
微細油粒子を素粒子化させることができる。 (2) 各分離板の孔の位置をずらしたことにより、傾
斜通路を形成し、粗粒子化した油粒子の浮上分離を促進
することができる。 (3) したがって、油水分離性能を向上することがで
きる。
Since the present invention is configured as described above, it has the following effects. (1) In the conventional separation plate method, since holes are provided on the entire surface of the separation plate, there is a part where the holes of the separation plates that are vertically adjacent to each other inevitably overlap. There was no collision of the cleaning liquid on the wall of the separation plate, and the tending effect tended to decrease.
In the present invention, it surely causes the showering action,
Fine oil particles can be made into elementary particles. (2) By displacing the positions of the holes of each separation plate, it is possible to form an inclined passage and promote floating separation of the coarsened oil particles. (3) Therefore, the oil-water separation performance can be improved.

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

【図1】本発明の一実施例を示す概略構成図。FIG. 1 is a schematic configuration diagram showing an embodiment of the present invention.

【図2】図1の油水分離槽を示す側断面図。FIG. 2 is a side sectional view showing the oil-water separation tank of FIG.

【図3】第1の分離板の上面図。FIG. 3 is a top view of a first separation plate.

【図4】第2の分離板の上面図。FIG. 4 is a top view of a second separation plate.

【図5】第1、第2の分離板の側断面図。FIG. 5 is a side sectional view of first and second separation plates.

【符号の説明】[Explanation of symbols]

A・・・洗浄液 B・・・処理水 C・・・粗粒子化した油粒子 D・・・隙間 E・・・傾斜通路 L・・・中央通路 L1・・・送出回路 L2・・・戻り回路 L3・・・油抽出回路 W・・・範囲 1・・・洗浄槽 2・・・送出口 3・・・循環ポンプ 4・・・流量計 5・・・フィルタ 6・・・圧力計 8・・・抽出油受け 10・・・油水分離槽 11・・・本体 12・・・流入口 13・・・処理水出口 14・・・油溜室 15・・・油抽出口 16・・・処理水溜室 20・・・分離板積重体 21・・・分離板 21a・・・第1の分離板 21b・・・第2の分離板 22・・・中央孔 23、23a、23b・・・孔 24・・・突縁部 A ... Cleaning liquid B ... Treated water C ... Coarse-grained oil particles D ... Gap E ... Inclined passage L ... Central passage L1 ... Delivery circuit L2 ... Return circuit L3 ... Oil extraction circuit W ... Range 1 ... Washing tank 2 ... Outlet 3 ... Circulation pump 4 ... Flowmeter 5 ... Filter 6 ... Pressure gauge 8 ...・ Extracted oil receiver 10 ・ ・ ・ Oil water separation tank 11 ・ ・ ・ Main body 12 ・ ・ ・ Inflow port 13 ・ ・ ・ Processed water outlet 14 ・ ・ ・ Oil storage chamber 15 ・ ・ ・ Oil extraction port 16 ・ ・ ・ Processed water storage chamber 20 ... Separating plate stack 21 ... Separating plate 21a ... First separating plate 21b ... Second separating plate 22 ... Central hole 23, 23a, 23b ... Hole 24 ...・ Bridge

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 微粒子を含む液体の該微粒子を粗粒子化
し、その比重差により浮上分離させる油水分離装置にお
いて、多孔を有し円錐状に形成されて中央孔を備えた複
数の第1及び第2の分離板を、油水分離槽の内部に交互
に隙間を設けて積み重ねて構成し、第1の分離板と第2
の分離板との孔の上下方向の位置はずれていて孔を通過
した液体が下方の分離板の壁に衝突するように構成した
ことを特徴とする油水分離装置。
1. An oil-water separation device in which fine particles of a liquid containing fine particles are coarsened and float-separated by a difference in specific gravity thereof, and a plurality of first and first cone-shaped and central holes are provided. The two separation plates are alternately stacked inside the oil-water separation tank with a gap between them to form a first separation plate and a second separation plate.
The oil / water separation device is characterized in that the vertical position of the hole with respect to the separation plate is deviated, and the liquid passing through the hole collides with the wall of the lower separation plate.
【請求項2】 前記第1および第2の分離板の孔を通過
した液体が次の分離板の壁に衝突して流れを変えた後に
次の孔に流れる通路が第1および第2の分離板の孔のな
い壁で挟まれて形成され、その通路の断面形状が浮上分
離作用をするように傾斜板状である請求項1記載の油水
分離装置。
2. A passage through which the liquid that has passed through the holes of the first and second separation plates collides with the wall of the next separation plate to change its flow and then flows into the next hole has the first and second separation plates. The oil-water separation device according to claim 1, wherein the oil-water separation device is formed by being sandwiched by walls having no holes in the plate, and the cross-sectional shape of the passage is an inclined plate shape so as to perform a floating separation action.
【請求項3】 微粒子を含む液体の該微粒子を粗粒子化
し、その比重差により浮上分離させる油水分離装置にお
いて、多孔を有し円錐状に形成されて中央孔を備えた複
数の第1及び第2の分離板を、油水分離槽の内部に交互
に隙間を設けて積み重ね、前記第1の分離板の各孔を外
周部に設け、前記第2の分離板の各孔を内周部に設けて
両分離板の各孔の間にコワレッシング作用により粗粒子
化した油粒子が比重差により浮上分離しながら流れる無
孔の傾斜通路を形成したことを特徴とする油水分離装
置。
3. An oil-water separation device in which the fine particles of a liquid containing fine particles are coarsened and float-separated by the difference in specific gravity thereof, and a plurality of first and first conical holes each having a central hole are formed. The two separation plates are stacked alternately inside the oil-water separation tank with a gap therebetween, each hole of the first separation plate is provided in the outer peripheral portion, and each hole of the second separation plate is provided in the inner peripheral portion. An oil-water separation device is characterized in that a non-perforated inclined passage is formed between the holes of both separating plates, in which oil particles coarsened by a coalescing action flow while floating and separating due to a difference in specific gravity.
【請求項4】 第1および第2の分離板の各孔には、下
向きのバーリング加工が施されていることを特徴とする
請求項1記載の油水分離装置。
4. The oil-water separator according to claim 1, wherein each hole of the first and second separation plates is subjected to downward burring processing.
【請求項5】 孔の位置が異なる第1および第2の分離
板が複数種類用意されている請求項1記載の油水分離装
置。
5. The oil-water separator according to claim 1, wherein a plurality of types of first and second separation plates having different positions of holes are prepared.
JP5861595A 1995-03-17 1995-03-17 Oil and water separating apparatus Pending JPH08252404A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5861595A JPH08252404A (en) 1995-03-17 1995-03-17 Oil and water separating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5861595A JPH08252404A (en) 1995-03-17 1995-03-17 Oil and water separating apparatus

Publications (1)

Publication Number Publication Date
JPH08252404A true JPH08252404A (en) 1996-10-01

Family

ID=13089466

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5861595A Pending JPH08252404A (en) 1995-03-17 1995-03-17 Oil and water separating apparatus

Country Status (1)

Country Link
JP (1) JPH08252404A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4621803B1 (en) * 2010-03-18 2011-01-26 株式会社ワールドケミカル Self-priming oil / water separator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4621803B1 (en) * 2010-03-18 2011-01-26 株式会社ワールドケミカル Self-priming oil / water separator
JP2011194294A (en) * 2010-03-18 2011-10-06 World Chemical Co Ltd Self-suction oil-water separator
US8257588B2 (en) 2010-03-18 2012-09-04 World Chemical Co., Ltd. Oil-water separator with self-priming pump

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