JPS6052877B2 - separation tank - Google Patents

separation tank

Info

Publication number
JPS6052877B2
JPS6052877B2 JP57021914A JP2191482A JPS6052877B2 JP S6052877 B2 JPS6052877 B2 JP S6052877B2 JP 57021914 A JP57021914 A JP 57021914A JP 2191482 A JP2191482 A JP 2191482A JP S6052877 B2 JPS6052877 B2 JP S6052877B2
Authority
JP
Japan
Prior art keywords
sewage
separation tank
area
purified water
tank according
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
JP57021914A
Other languages
Japanese (ja)
Other versions
JPS58139714A (en
Inventor
和致 矢倉
聰一郎 湊
哲滋 矢倉
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.)
MURAKAWA KEIICHIRO
SHINOHARA YOSHIJI
Original Assignee
MURAKAWA KEIICHIRO
SHINOHARA YOSHIJI
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 MURAKAWA KEIICHIRO, SHINOHARA YOSHIJI filed Critical MURAKAWA KEIICHIRO
Priority to JP57021914A priority Critical patent/JPS6052877B2/en
Priority to PCT/JP1983/000035 priority patent/WO1983002767A1/en
Priority to KR1019830000226A priority patent/KR840003218A/en
Publication of JPS58139714A publication Critical patent/JPS58139714A/en
Publication of JPS6052877B2 publication Critical patent/JPS6052877B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/24Treatment of water, waste water, or sewage by flotation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/40Devices for separating or removing fatty or oily substances or similar floating material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D17/00Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02Separation of non-miscible liquids
    • B01D17/0208Separation of non-miscible liquids by sedimentation

Description

【発明の詳細な説明】 本発明は分離槽に関し、汚物、例えば油、■ル、CO
D、、SSや溶融物(塩分、色素等)が混入した汚水か
ら汚物を分離排除し、水を浄化するための分離槽の改良
にかかる。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a separation tank that is capable of handling waste materials such as oil, oil, CO2, etc.
D. Improvement of a separation tank for purifying water by separating and removing filth from wastewater contaminated with SS and molten substances (salt, pigments, etc.).

例えば船舶などに設置され、油が混入したエンジン冷
却水から油分を排除して水を浄化させるための分離槽は
、限られた量の散水を循環浄化しながら使用しなければ
ならない。
For example, a separation tank installed on a ship to purify water by removing oil from oil-containing engine cooling water must be used while circulating and purifying a limited amount of water.

このため、水を捨てないで油のみが排除でき、しかも効
率のよい分離能力をつ分離槽が要求される。併しながら
、従来の分離槽は単に槽上部に溜つた油を(以下汚物と
いう)を汚物排送管により電磁弁を介して排出するよう
にしていた。しかも、分離槽のカバーは平坦頂面をなし
、槽内圧力によつて生ずみの汚物が排出される際、前記
排送管が接続される付近の汚物のみがおし出され、それ
につれて、水までも一緒に排出される危険性があつた。
特に、船の傾きにつれて分離槽が傾いた時、水面が排送
管の開・口部まで来る現象が発生し、水が排出され易か
つた。また、従来のものは汚物の粗粒化が不良で、粗粒
化部材が汚れ過ぎる等の問題点があつた。本発明は上記
欠点を除き、汚物の粗粒化が促進させ、汚物の分離性能
を高め、しかも、水が浮上分離された汚物と共に排出す
ることにない分離槽を提供することを目的とする。以下
本発明の一実施例を図面にもとづいて説明する。
For this reason, there is a need for a separation tank that can remove only the oil without discarding the water and has efficient separation capabilities. However, in the conventional separation tank, oil accumulated in the upper part of the tank (hereinafter referred to as filth) is simply discharged through a filth discharge pipe via a solenoid valve. Moreover, the cover of the separation tank has a flat top surface, and when the built-up waste is discharged due to the internal pressure of the tank, only the waste near where the discharge pipe is connected is pushed out, and as a result, There was a risk that water would also be discharged together.
In particular, when the separation tank tilted as the ship tilted, a phenomenon occurred in which the water surface reached the opening/mouth of the discharge pipe, making it easy for water to be discharged. In addition, the conventional method had problems such as poor coarsening of dirt and the coarsening member was too dirty. It is an object of the present invention to eliminate the above-mentioned drawbacks, to provide a separation tank that promotes the coarsening of waste, improves the separation performance of the waste, and does not discharge water together with the floated and separated waste. An embodiment of the present invention will be described below based on the drawings.

第1図および第2図に示す如く、分離槽は底壁11に汚
水入口11a1浄水出口11bを有する有底角筒からな
る容器状槽本体1と、前記槽本体1の上側を覆うカバー
2と、該カバー2の上端に接続された汚物排出用のエル
ボ3と、前記入口11aと出口11bとの間に設けれ、
かつ、本体1の下部を入口側汚水上昇域1Aと出口側浄
水下降域1b(第1図)とに仕切る仕切板4と支持部材
5により支持される汚物粗粒化部材6と、汚物蓄積量検
知部7と、洗滌用空気管8と、ドレーン抜管9とを有す
る。
As shown in FIGS. 1 and 2, the separation tank includes a container-shaped tank main body 1 made of a bottomed rectangular cylinder having a sewage inlet 11a and a purified water outlet 11b on a bottom wall 11, and a cover 2 that covers the upper side of the tank main body 1. , provided between an elbow 3 for discharging dirt connected to the upper end of the cover 2, and the inlet 11a and the outlet 11b,
Also, a dirt coarsening member 6 supported by a support member 5 and a partition plate 4 that partitions the lower part of the main body 1 into an inlet side sewage rising area 1A and an outlet side purified water falling area 1b (FIG. 1), and a dirt accumulation amount. It has a detection part 7, a cleaning air pipe 8, and a drain extraction pipe 9.

そして、本体1の上部より上方の部分が浮上汚物溜り部
Sとなる。しかして、前記カバー2は実施例によると、
段階的に積重された2つの縮径部2a,2bが形成され
る。
A portion above the upper portion of the main body 1 becomes a floating dirt storage portion S. According to the embodiment, the cover 2 has the following features:
Two reduced diameter portions 2a and 2b are formed which are stacked in stages.

即ち、第1縮径部2aは左右側壁が上向小径となるよう
縮径され、上壁は液体の上向流路に対し、その流動を阻
止する水平段部21とされる。そして、該上壁の中央に
、側壁が直円筒をなし、上壁が前記と同様の水平段部2
2とされた第2縮径部2bが接続される。更に、該第2
縮径部2bの水平段部22の中央には径違いエルボ3の
大径部が連結される。該エルボの小径部には図示外の間
欠開閉される電磁弁を備えた汚物排送管が接続されてい
る。前記仕切板4の上端部より下方.位置には支持部材
5が水平に設けられ、該支持部材5上に複数枚の金網が
重ね合わせた汚物粗粒化部材6(汚水域1a側が6a1
浄水域1b側が6b)が載置固定される。汚物蓄積量検
知部7は電極7aを利用した第1.油検出部71と第2
油量検出部72とからなり、第1縮径部2aの後壁と槽
本体1の上部後壁とに突設されている。
That is, the diameter of the first reduced diameter portion 2a is reduced so that the left and right side walls have a smaller diameter in the upward direction, and the upper wall is formed into a horizontal step portion 21 that blocks the upward flow of the liquid. At the center of the upper wall, the side wall forms a right cylinder, and the upper wall has a horizontal stepped portion 2 similar to the above.
2 is connected to the second reduced diameter portion 2b. Furthermore, the second
The large diameter portion of the reducing elbow 3 is connected to the center of the horizontal stepped portion 22 of the reduced diameter portion 2b. A waste discharge pipe equipped with a solenoid valve (not shown) that is opened and closed intermittently is connected to the small diameter portion of the elbow. Below the upper end of the partition plate 4. A supporting member 5 is provided horizontally at the position, and a filth coarsening member 6 (on the sewage area 1a side is 6a1
6b) is mounted and fixed on the purified water area 1b side. The filth accumulation amount detection section 7 uses a first sensor using an electrode 7a. Oil detection section 71 and second
The oil amount detection section 72 is provided in a protruding manner on the rear wall of the first reduced diameter section 2a and the upper rear wall of the tank body 1.

洗滌用空気管8は槽本体1の底部に左右一対設けられ、
両端が閉止され、上面に多数の空気噴出孔81aを有し
て水平にとりつけ・られたU字状管81に接続部材82
を介して空気が送入される。ドレーン抜管9は前記仕切
板4を挾む両側底壁11に左右一対設けられる。なお、
図中10aは底壁11の対角線位置2個所に設けられた
脚、10bは分離槽から突設された動振止部材、31は
自動排気弁取付座である。
A pair of cleaning air pipes 8 are provided at the bottom of the tank body 1 on the left and right sides.
A connecting member 82 is connected to a U-shaped tube 81 which is closed at both ends and is installed horizontally and has a large number of air jet holes 81a on the upper surface.
Air is introduced through the A pair of left and right drain pipes 9 are provided on both side bottom walls 11 sandwiching the partition plate 4. In addition,
In the figure, 10a is a leg provided at two diagonal positions on the bottom wall 11, 10b is a dynamic vibration damping member protruding from the separation tank, and 31 is an automatic exhaust valve mounting seat.

以上において、次にその動作状態を説明する。汚物が混
入された水はポンプ圧力が加えられて、入口11aより
槽内の入口側汚水域1aに送入される。該汚水域1a内
の混入汚物のうぢ大粒のものは大きな浮力によつて金網
6aの目を通つて浮上し、カバー2の下面付近に集合す
る。一方、浮力の弱い微粒状汚物は金網6a層内で他の
l微粒状汚物と結合して粗粒化され、浮力が増して浮上
する。カバー2の下面付近に集合した汚物は間欠的に電
磁弁(図示外)が開かれることによりエルボ3を経て圧
送排出される。しかして、上記排出に際し、エルボ3、
特にカバー2が下部が大きく開口し上部が小径となるよ
う縮径されているため、貯溜汚物は分離槽頂部全面積に
わたつて圧し出される。
In the above, the operating state will be explained next. The water mixed with filth is pumped under pump pressure and is sent from the inlet 11a to the inlet-side sewage area 1a in the tank. The large particles of the mixed filth in the sewage area 1a float through the wire mesh 6a due to the large buoyant force and collect near the bottom surface of the cover 2. On the other hand, fine particulate dirt with weak buoyancy is combined with other fine particulate dirt in the layer of wire mesh 6a to become coarse particles, and its buoyancy increases and it floats to the surface. The dirt collected near the bottom surface of the cover 2 is forced out through the elbow 3 by opening a solenoid valve (not shown) intermittently. However, when discharging the above, elbow 3,
In particular, since the cover 2 is reduced in diameter so that the lower part is largely open and the upper part is small in diameter, the accumulated dirt is forced out over the entire top area of the separation tank.

また、このような形状のカバーの場合、分離槽が相当量
傾いたときでも第2縮径部2bの下部開口に水面が到達
して汚物の代りに水が圧し出される懸念がない。このよ
うに浄化された水は出口側浄水域1bを経て出口11b
より排出される。この排出に際し粗粒化汚物が排出され
ないように浄水域1b上方の金網6bは汚物泊過材の役
目をする。第1油検出器71は、カバー2の下面付近に
汚物が充満し、該汚物のため水面がおし下げられ、水と
汚物との界面が前記油量検出器71の位置まで下つたこ
とを感知して汚物排送管の電磁弁を開放させる役目をす
る。また、第2油検出器72は界面が該器の設置高さま
で下つたとき、、前記電磁弁の開放を制御するのに役立
つ。このようにして界面は常時、前記第1第2油検出器
71,72の設置位置との間の高さに維持される。洗滌
用空気管8は分離槽内の清掃時に空気を噴射させ、槽内
部および前記汚物粗粒化部材6に付着する油成分に対し
て気泡会合を起させて油塊状とし浮上させるためのもの
である。
Moreover, in the case of a cover having such a shape, even when the separation tank is tilted by a considerable amount, there is no fear that the water surface will reach the lower opening of the second reduced diameter portion 2b and water will be squeezed out instead of waste. The water purified in this way passes through the outlet-side purified area 1b and reaches the outlet 11b.
more excreted. During this discharge, the wire mesh 6b above the purified water area 1b serves as a filth trapping material so that coarse-grained filth is not discharged. The first oil detector 71 detects that the vicinity of the bottom surface of the cover 2 is filled with dirt, the water level is lowered due to the dirt, and the interface between the water and dirt has fallen to the position of the oil amount detector 71. It senses and opens the solenoid valve of the waste discharge pipe. A second oil detector 72 also serves to control the opening of the solenoid valve when the interface drops to the installation height of the vessel. In this way, the interface is always maintained at a height between the installation positions of the first and second oil detectors 71 and 72. The cleaning air pipe 8 is for injecting air when cleaning the inside of the separation tank, causing air bubbles to associate with oil components adhering to the inside of the tank and the dirt coarsening member 6, and making them float in the form of oil lumps. be.

本発明によると、汚物粗粒化部材6として金網、合成樹
脂網や金属、合成樹脂繊維体をランダムに積層した網目
状体層が使用されるので、従来の板、バイブ等の多数を
組合せ、これに汚物を付着させて分離させていた方式に
比べて、汚物の付着率が低く、掃除が容易である。
According to the present invention, since a wire mesh, a synthetic resin mesh, metal, and a mesh layer made of randomly laminated synthetic resin fiber bodies are used as the waste coarsening member 6, a large number of conventional plates, vibrators, etc. are combined, Compared to the method in which dirt is attached and separated, the rate of dirt adhesion is lower and cleaning is easier.

第3図は槽内が円筒状仕切板40で仕切られ、入口汚水
域1aと出口浄水域1bとに分割された他の実施例の横
断面を示す。
FIG. 3 shows a cross section of another embodiment in which the inside of the tank is partitioned by a cylindrical partition plate 40 and divided into an inlet wastewater area 1a and an outlet purified area 1b.

該実施例ては槽本体1の中央に設けられた汚水域1aの
中心に入口11aが、また前記仕切板40の外周に形成
された浄水域1b内に複数の出口11bが設けられてい
る。また、第4図は大量の汚水を処理可能とした2つの
槽本体1A,1Bを有する分離槽の実施例の一部切欠側
面図である。
In this embodiment, an inlet 11a is provided at the center of a sewage area 1a provided in the center of the tank body 1, and a plurality of outlets 11b are provided in a purified area 1b formed around the outer periphery of the partition plate 40. Moreover, FIG. 4 is a partially cutaway side view of an embodiment of a separation tank having two tank bodies 1A and 1B that can treat a large amount of wastewater.

即ち、第1分離槽1Aと第2分離槽1BとはZ状に曲折
された接続管10て連結され、第1分離槽1Aの中央下
向に元口10aが、また第2分離槽1Bの中央上向に先
口10Bが開口される。先口10bは帽状の酒適用金網
62で包装されている。この実施例構造によると下隅部
に設けられた入口11aから汚水が導入されると汚物は
浮上して金網61を通過するとき粗大化される。また、
汚水は接続管10を経て第2分離槽Bへ送られ帽状金網
62によつて再び粗粒化作用が付与されると共に、ろ過
される。浄化水は出口11bより送り出される。前記金
網61,62により粗粒化された汚物は浮力が付され、
縮径部20,20に溜められ、エルボ状排出管30,3
0を経て夫々圧送排出される。縮径部2,20は第4図
に示す如く段付ではくてもよい。また、排出管3,20
は上方への汚物噴流が直線状に噴きあがるのを阻止する
ような曲管であれば必ずしも縮径されていなくてもよい
。本発明は以上の如く構成するため、排除汚物中に水が
混入することがなく節水でき、汚物の粗粒化が容易で分
離効率が高い。
That is, the first separation tank 1A and the second separation tank 1B are connected by a connecting pipe 10 bent in a Z shape, and the main port 10a is located downward in the center of the first separation tank 1A, and the main port 10a is located downward in the center of the first separation tank 1A. A tip 10B is opened upward in the center. The tip 10b is wrapped with a cap-shaped wire mesh 62 for liquor use. According to the structure of this embodiment, when waste water is introduced from the inlet 11a provided at the lower corner, the waste floats to the surface and becomes coarse when passing through the wire mesh 61. Also,
The sewage is sent to the second separation tank B via the connecting pipe 10, where it is again given a coarse graining effect by the cap-shaped wire mesh 62 and is filtered. Purified water is sent out from the outlet 11b. The dirt coarsened by the wire meshes 61 and 62 is given buoyancy,
It is stored in the reduced diameter portions 20, 20, and the elbow-shaped discharge pipes 30, 3
0 and then pumped out. The reduced diameter portions 2, 20 may not be stepped as shown in FIG. In addition, the discharge pipes 3, 20
The diameter of the pipe does not necessarily need to be reduced as long as it is a curved pipe that prevents the upward jet of dirt from rising in a straight line. Since the present invention is configured as described above, water is not mixed into the waste to be removed, so water can be saved, the waste can be easily coarsened, and separation efficiency is high.

また、使用中分離槽が傾きことがあつても水が排出され
ることがないなどの大きな効果を発揮することになつた
In addition, even if the separation tank tilts during use, water will not be discharged, resulting in great effects.

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

第1図は本発明の一実施例を示す切欠正面図、第2図は
側面図、第3図は他の実施例を示す槽本体の横断面図、
第4図は更に他の実施例を示す切欠正面図である。 1・・・槽本体、11a・・・汚水入口、11b・・・
浄水出口、2・・・カバー、2a・・・第1縮径部、2
b・・・第2縮径部、3・・・径違いエルボ、4・・・
仕切板、6・・・・汚物粗粒化部材、8・・・洗滌用空
気管。
FIG. 1 is a cutaway front view showing one embodiment of the present invention, FIG. 2 is a side view, and FIG. 3 is a cross-sectional view of the tank body showing another embodiment.
FIG. 4 is a cutaway front view showing still another embodiment. 1...Tank body, 11a...Sewage inlet, 11b...
Purified water outlet, 2... Cover, 2a... First reduced diameter part, 2
b...Second diameter reducing part, 3...Reducing diameter elbow, 4...
Partition plate, 6... Dirt coarsening member, 8... Air pipe for cleaning.

Claims (1)

【特許請求の範囲】 1 下部の汚水入口から導入された汚水を上方に流動す
るように案内する汚水上昇域と、該汚水上昇域からの汚
水をその流動方向を変えて下方に流動するように案内し
、下部の汚水出口から排出するようにし浄水下降域と、
前記両域の上方に設けられ、少なくとも一部に上狭縮径
部を持つ浮上汚物溜り部とを含む分離槽。 2 前記汚水上昇域と前記浄水下降域とは1個の容器状
本体に仕切板を介して構成された特許請求の範囲第1項
記載の分離槽。 3 前記汚水上昇域と前記浄水下降域とは別個の容器状
本体内に構成され、これら容器状本体は接続管で連結さ
れた特許請求の範囲第1項記載の分離槽。 4 前記汚水上昇域に網目状体層からなる汚物粗粒化部
材が設けられた特許請求の範囲第1項又は第2項又は第
3項記載の分離槽。 5 前記浄水下降域に網目状体層からなる汚物濾過体が
設けられた特許請求の範囲第4項記載の分離槽。
[Scope of Claims] 1. A sewage rising area that guides the sewage introduced from the sewage inlet at the bottom so that it flows upward, and a sewage rising area that guides the sewage introduced from the sewage inlet at the lower part so that it flows downward by changing the direction of flow of the sewage from the sewage rising area. The purified water is guided and discharged from the waste water outlet at the bottom, and the purified water descends from the area.
A separation tank that is provided above both of the areas and includes a floating dirt collection section that has an upper narrow diameter section at least in part. 2. The separation tank according to claim 1, wherein the sewage rising area and the purified water falling area are constructed in one container-shaped main body with a partition plate interposed therebetween. 3. The separation tank according to claim 1, wherein the sewage rising region and the purified water descending region are constructed in separate container-like bodies, and these container-like bodies are connected by a connecting pipe. 4. The separation tank according to claim 1, 2, or 3, wherein a filth coarsening member made of a mesh layer is provided in the sewage rising region. 5. The separation tank according to claim 4, wherein a filth filter consisting of a mesh layer is provided in the purified water descending region.
JP57021914A 1982-02-12 1982-02-12 separation tank Expired JPS6052877B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP57021914A JPS6052877B2 (en) 1982-02-12 1982-02-12 separation tank
PCT/JP1983/000035 WO1983002767A1 (en) 1982-02-12 1983-02-07 Separating tank
KR1019830000226A KR840003218A (en) 1982-02-12 1983-02-12 Separation tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57021914A JPS6052877B2 (en) 1982-02-12 1982-02-12 separation tank

Publications (2)

Publication Number Publication Date
JPS58139714A JPS58139714A (en) 1983-08-19
JPS6052877B2 true JPS6052877B2 (en) 1985-11-21

Family

ID=12068350

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57021914A Expired JPS6052877B2 (en) 1982-02-12 1982-02-12 separation tank

Country Status (3)

Country Link
JP (1) JPS6052877B2 (en)
KR (1) KR840003218A (en)
WO (1) WO1983002767A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0231127Y2 (en) * 1986-10-02 1990-08-22
CN111439808B (en) * 2020-03-28 2021-05-18 江西绿色盾牌环境工程有限公司 Domestic sewage treatment and discharge device with high oil stain content

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1011888A (en) * 1972-12-13 1977-06-07 Improved Machinery Inc. Apparatus and methods for clarifying an influent water

Also Published As

Publication number Publication date
KR840003218A (en) 1984-08-20
WO1983002767A1 (en) 1983-08-18
JPS58139714A (en) 1983-08-19

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