JP3092013B2 - Oil-water separator - Google Patents

Oil-water separator

Info

Publication number
JP3092013B2
JP3092013B2 JP02407242A JP40724290A JP3092013B2 JP 3092013 B2 JP3092013 B2 JP 3092013B2 JP 02407242 A JP02407242 A JP 02407242A JP 40724290 A JP40724290 A JP 40724290A JP 3092013 B2 JP3092013 B2 JP 3092013B2
Authority
JP
Japan
Prior art keywords
oil
tank
water
sedation
separation device
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 - Fee Related
Application number
JP02407242A
Other languages
Japanese (ja)
Other versions
JPH04210201A (en
Inventor
可明 高倉
Original Assignee
可明 高倉
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Filing date
Publication date
Application filed by 可明 高倉 filed Critical 可明 高倉
Priority to JP02407242A priority Critical patent/JP3092013B2/en
Publication of JPH04210201A publication Critical patent/JPH04210201A/en
Application granted granted Critical
Publication of JP3092013B2 publication Critical patent/JP3092013B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は油水分離装置に関する
ものであり、特に油やオイルボール粒および油分含有汚
泥等を含む汚水等の被処理水を複数段に直列配置された
水槽に通してこれら油やオイルボール粒および油分含有
汚泥等を気泡と接着させて浮上分離する油水分離装置に
関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an oil / water separation apparatus, and more particularly to a method of passing water to be treated, such as sewage containing oil, oil ball particles and oil-containing sludge, through a water tank arranged in a plurality of stages in series. The present invention relates to an oil-water separation device that floats and separates oil, oil ball particles, oil-containing sludge, and the like by bonding them to air bubbles.

【0002】[0002]

【従来の技術】自動車修理または解体工場や、機械工作
工場あるいはガソリン給油所など、日常的に油を床に流
す恐れのある作業所においては、床洗浄水や雨水などの
排水は油やオイルボール粒および油分含有汚泥等を含む
汚水であり、この汚水は側溝に集められてから油水分離
装置に送られ、油分が除去されたのちに下水または河川
に放流される。
2. Description of the Related Art Drainage such as floor washing water and rainwater is drained from oil or oil balls in a work place where oil may flow to the floor on a daily basis, such as a car repair or dismantling factory, a machine shop or a gasoline gas station. This is wastewater containing particles and oil-containing sludge. This wastewater is collected in gutters, sent to an oil-water separator, and discharged to sewage or rivers after oil is removed.

【0003】従来の油水分離装置には、米国石油協会の
設計基準に準拠した所謂APIオイルセパレータ、槽内
に複数列の傾斜板を配置したPPIオイルセパレータ、
或いは波状の傾斜板を用いたCPIオイルセパレータな
どがあり、原理的には普通の横流式沈殿池又はそれに傾
斜板を組合せた重力式分離方式のものが主である。
Conventional oil / water separators include a so-called API oil separator conforming to the design standards of the American Petroleum Institute, a PPI oil separator in which a plurality of rows of inclined plates are arranged in a tank,
Alternatively, there is a CPI oil separator using a wavy inclined plate, and in principle, an ordinary horizontal flow type sedimentation basin or a gravity separation type in which an inclined plate is combined therewith is mainly used.

【0004】従来のAPIオイルセパレータでは、槽内
の被処理水の平均流速を制限値以下にするためには除去
すべき油滴の大きさが小さくなるほど槽の長さを長くし
なければならず、従って被処理水中の懸濁油滴をほぼ完
全に除去するには長大な設備面積が必要であり、さらに
は追加のフィルター式油除去装置を設けなければならな
い欠点があった。
In the conventional API oil separator, in order to keep the average flow velocity of the water to be treated in the tank below the limit value, the length of the tank must be increased as the size of the oil droplet to be removed becomes smaller. Therefore, there is a drawback that a large equipment area is required to almost completely remove suspended oil droplets in the water to be treated, and an additional filter type oil removing device must be provided.

【0005】またPPIオイルセパレータやCPIオイ
ルセパレータでは、槽内構造が複雑で規模が大きく、取
扱いや保守に特別な技術を要するほか、被処理水の流量
変動に対して処理能力の追従に限界があり、従って野外
の工場などの油分を含む排水の処理に対しては、雨天時
に油分が排水中に混入することが避けられない。
[0005] In addition, the PPI oil separator and the CPI oil separator have a complicated structure inside the tank and are large in scale, require special techniques for handling and maintenance, and have a limit in the ability of the treatment capacity to follow fluctuations in the flow rate of the water to be treated. Therefore, when treating wastewater containing oil in an outdoor factory or the like, it is inevitable that the oil will be mixed into the wastewater in rainy weather.

【0006】さらに水中の懸濁物質を浮上分離する方式
の一つに、密度が水よりも大きい懸濁物質に対して空気
の泡を接着させて見掛比重を小さくし、速やかに浮上さ
せて分離を行う加圧浮上方式も知られているが、この場
合は微細な気泡を発生させてやる必要があり、被処理水
を加圧して空気を溶解してから大気圧に開放するための
大がかりな設備が必要であるという欠点がある。
[0006] Further, as one of the methods of floating separation of suspended substances in water, air bubbles are adhered to suspended substances having a density higher than that of water to reduce the apparent specific gravity and to quickly float. A pressurized flotation method for separation is also known, but in this case, it is necessary to generate fine bubbles, and a large scale is used to pressurize the water to be treated and dissolve the air before releasing it to atmospheric pressure. There is a drawback that a complicated equipment is required.

【0007】[0007]

【発明が解決しようとする課題】この発明は、特に雨水
が混入する恐れのある施設における油やオイルボール及
び油分含有汚泥等を含む汚水の排水処理装置として好適
で、プレハブ組立て方式やユニット化などにより比較的
少ない設備面積で構成することのできる簡易構造の油水
分離装置を提供しようとするものである。
The present invention is suitable as a wastewater treatment device for wastewater containing oil, oil balls, oil-containing sludge, etc., particularly in facilities where there is a risk of rainwater mixing. Accordingly, an object of the present invention is to provide an oil-water separator having a simple structure which can be configured with a relatively small facility area.

【0008】[0008]

【課題を解決するための手段】請求項1に記載の発明に
係る油水分離装置は、油の混合した汚水等の被処理水を
複数段に直列配置された水槽に通して油を浮上分離する
油水分離装置において、前記被処理水を上部開口から受
入れる受入槽、該受入槽中の下層部からの被処理水を受
入れて順次鎮静させるために上流から下流へ直列状に配
列された複数段の鎮静槽、少なくとも下流端の前記鎮静
槽の表層油水を溢流として取り込む集油槽、前記鎮静槽
の被処理水中で空気の泡を発生する気泡発生装置、前記
集油槽に取り込まれた溢流を前記受入槽に還流させる循
環ポンプ手段、及び前記下流端の鎮静槽の底部から油分
離処理済みの水を外部へ排出する排水手段、を備えてな
るものである。
According to the first aspect of the present invention, there is provided an oil-water separation apparatus for separating and floating oil by passing water to be treated such as sewage mixed with oil through a plurality of water tanks arranged in series. In the oil-water separation device, a receiving tank for receiving the water to be treated from the upper opening, a plurality of stages arranged in series from upstream to downstream to receive and sequentially calm the water to be treated from the lower part in the receiving tank. A sedation tank, an oil collection tank that takes in at least the surface oil water of the sedation tank at the downstream end as an overflow, a bubble generator that generates air bubbles in the water to be treated in the sedation tank, and an overflow that is taken into the oil collection tank. It is provided with a circulation pump means for returning to the receiving tank, and a drain means for discharging the oil-separated water to the outside from the bottom of the calming tank at the downstream end.

【0009】また請求項2に記載の発明に係る油水分離
装置では、前記循環ポンプ手段が、前記集油槽に取り込
まれた溢流から固形物を除去する手段を備え、前記固形
物が除去された後の油水を前記受入槽に還流するように
構成されている。
In the oil-water separator according to the second aspect of the present invention, the circulating pump includes means for removing solids from the overflow taken into the oil collecting tank, and the solids are removed. It is configured so that the later oil / water is returned to the receiving tank.

【0010】また請求項3に記載の発明に係る油水分離
装置では、前記気泡発生装置が前記鎮静槽の底部に配置
された多孔ノズルと、該ノズルへ空気を送りこむ給気装
置とを含んでいる。
[0010] In the oil-water separation device according to the third aspect of the present invention, the bubble generating device includes a perforated nozzle arranged at the bottom of the calming tank, and an air supply device for sending air to the nozzle. .

【0011】また請求項4に記載の発明に係る油水分離
装置では、前記鎮静槽が底部で互いに連通した隣接鎮静
槽の対を含むものであり、更に請求項5に記載の油水分
離装置では、それに加えて前記隣接鎮静槽のうちの下流
側の鎮静槽に表層部で連通した別の鎮静槽を更に含むも
のである。
[0011] In the oil-water separator according to the fourth aspect of the present invention, the sedation tank includes a pair of adjacent sedation tanks communicating with each other at a bottom portion. In addition to the above, another sedation tank which is communicated with the sedation tank on the downstream side of the adjacent sedation tank at the surface layer portion is further included.

【0012】また請求項6に記載の発明に係る油水分離
装置では、前記受入槽がその底部の汚泥溜りの直上で立
上り流路によって上流端の前記鎮静槽に連通されてい
る。
In the oil-water separation device according to the invention, the receiving tank is connected to the calming tank at the upstream end by a rising flow path immediately above the sludge pool at the bottom.

【0013】また請求項7に記載の発明に係る油水分離
装置では、前記受入槽が循環ポンプ手段による油水の還
流を受けて最終的な油の収集除去がこの受入槽からバキ
ュームカーなどによって行われることから、前記受入槽
を前記鎮静槽の個々の槽より大容量にしたものである。
In the oil-water separator according to the present invention, the receiving tank receives the reflux of the oil and water by the circulation pump means, and the final collection and removal of the oil is performed from the receiving tank by a vacuum car or the like. For this reason, the receiving tank has a larger capacity than the individual tanks of the calming tank.

【0014】また請求項8に記載の発明に係る油水分離
装置では、前記集油槽に取り込まれた溢流の集油槽内で
のレベルを検出して前記循環ポンプ手段を前記溢流が維
持されるように駆動制御する制御手段を更に備えたもの
である。
In the oil-water separation device according to the present invention, the level of the overflow taken into the oil collecting tank in the oil collecting tank is detected to maintain the overflow of the circulation pump means. Control means for controlling the driving as described above.

【0015】また請求項9に記載の発明に係る油水分離
装置では、前記集油槽が、下流端の前記鎮静槽内にて被
処理水表面下に上縁が僅かに沈むように位置された独立
容器を備えている。
[0015] In the oil-water separation device according to the ninth aspect of the present invention, the oil collecting tank is positioned in the calming tank at the downstream end so that an upper edge thereof is slightly sunk below the surface of the water to be treated. It has.

【0016】請求項10に記載の発明に係る油水分離装
置は、前記独立容器を浮子原理により被処理水中に浮遊
支持させたものであり、請求項11に記載の油水分離装
置では、前記独立容器を支柱により前記上縁の高さ位置
を調整可能に支持したものである。
According to a tenth aspect of the present invention, there is provided an oil-water separator, wherein the independent vessel is suspended and supported in the water to be treated according to a floating principle. Are supported by a support so that the height position of the upper edge can be adjusted.

【0017】さらに請求項12に記載の発明に係る油水
分離装置では、請求項9に記載の油水分離装置におい
て、前記循環ポンプ手段が、前記独立容器内に配置され
た水中ポンプを含むものである。
According to a twelfth aspect of the present invention, in the oil-water separation device according to the ninth aspect, the circulating pump means includes a submersible pump disposed in the independent vessel.

【0018】[0018]

【作 用】請求項1に記載の発明に係る油水分離装置に
おいては、油やオイルボール及び油分含有汚泥等の混合
した汚水等の被処理水を、複数段に直列配置された水槽
に通して油を浮上分離するに際して、側溝等からの被処
理水は前記受入槽へその上部開口から流入する。
In the oil-water separator according to the first aspect of the present invention, the water to be treated, such as mixed sewage such as oil, oil balls and oil-containing sludge, is passed through a plurality of water tanks arranged in series. When the oil is floated and separated, the water to be treated from the gutter or the like flows into the receiving tank from the upper opening.

【0019】受入槽内では表層寄りの部分で乱流が発生
して混合が生じるが、比較的水深の深い底槽部では乱流
による混合は僅かであり、従って受入槽内でも油の浮上
による分離が起きている。この受入槽内の下層部の被処
理水は複数段の鎮静槽の上流端に導かれ、下流へ向うに
従って流れの乱れが鎮静されて浮上油の生成が促進され
る。
In the receiving tank, turbulence is generated near the surface layer to cause mixing. However, in the bottom tank having a relatively deep water depth, the mixing due to the turbulent flow is slight. Separation is taking place. The water to be treated in the lower part of the receiving tank is guided to the upstream end of the multistage calming tank, and the turbulence of the flow is calmed down toward the downstream to promote the generation of floating oil.

【0020】これら鎮静槽内の被処理水には、前記気泡
発生装置によって空気の泡が送り込まれており、水中の
オイルボールや油分含有汚泥の粒子はそれらの表面が水
よりも空気と接着を起こし易い油性界面であるので、こ
の気泡がこれらオイルボール粒や油分含有汚泥粒の表面
に付着し、これによってこれら粒子が速やかに浮上して
表層の浮渣となる。
Air bubbles are sent into the water to be treated in these calming tanks by the bubble generator, and the oil balls and oil-containing sludge particles in the water adhere to the air better than water on their surfaces. Because of the oily interface that is likely to occur, these air bubbles adhere to the surfaces of the oil ball particles and the oil-containing sludge particles, whereby these particles quickly float and become the surface residue.

【0021】これら鎮静槽の少なくとも下流端には集油
槽があり、被処理水の表層部が溢流として集油槽内に流
入すると、表層部に浮上していた浮渣は早い流速で勢い
よく集油槽内に取り込まれる。この集油槽内に取り込ま
れた溢流は浮渣を高い比率でに含み、この溢流は循環ポ
ンプ手段により前記受入槽にその上部開口から還流され
る。一方、前記鎮静槽の下流端側底部には油分を殆ど含
まない水が滞留しており、従ってこの油分離済みの水は
前記鎮静槽の下流側から外部の放流系統などへ流出され
て排出される。
An oil collecting tank is provided at least at the downstream end of these calming tanks. When the surface layer of the water to be treated flows into the oil collecting tank as an overflow, the floating residue floating on the surface layer is rapidly collected at a high flow velocity. It is taken into the oil tank. The overflow taken into the oil collecting tank contains a high proportion of floating residue, and the overflow is returned to the receiving tank from its upper opening by a circulation pump means. On the other hand, water containing almost no oil remains at the bottom of the downstream end of the calming tank, and thus the oil-separated water flows out from the downstream side of the calming tank to an external discharge system and is discharged. You.

【0022】本発明の油水分離装置では、下流側の鎮静
槽から上流の受入槽へ、集油槽と循環ポンプ手段による
油分濃度の高い油水の環流が行われるため、この還流に
よる油水の循環が継続されると、受入槽の上層に浮上油
と浮渣が次第に厚く溜ってくることになる。この受入槽
上層の浮上油と浮渣は、受入槽を上部開口から観察した
ときに容易に目視確認できるが、勿論、その溜り具合を
適当な水深に設置した油分検出器で自動検出してもよ
い。
In the oil / water separation device of the present invention, since the oil water having a high oil content is recirculated from the calming tank on the downstream side to the receiving tank on the upstream side by the oil collecting tank and the circulating pump means, the circulation of the oil water by the reflux is continued. As a result, the floating oil and floating residue gradually accumulate in the upper layer of the receiving tank. The floating oil and floating residue in the upper layer of the receiving tank can be easily visually confirmed when the receiving tank is observed from the upper opening, but of course, even if the state of the pool is automatically detected by an oil detector installed at an appropriate depth. Good.

【0023】受入槽の上層に浮上油と浮渣が或る程度ま
で溜ったら、この浮上油と浮残渣をバキュームで吸引し
て油処理業者に処理してもらえばよい。またこの際に、
受入槽の底に溜った沈殿汚泥もバキュームで吸引してや
れば好都合である。
When the floating oil and the floating residue accumulate to a certain extent in the upper layer of the receiving tank, the floating oil and the floating residue may be suctioned by a vacuum to be processed by an oil processing company. At this time,
It is convenient if the settled sludge collected at the bottom of the receiving tank is suctioned by vacuum.

【0024】このようにして定期的に、または不定期的
に受入槽から浮上油と浮渣および汚泥を吸引除去するこ
とにより、分離油分や汚泥を効率よく収集することがで
き、また前述の還流方式の油水分離システムによって効
率的な油分除去が行われるので、下流端の鎮静槽の底部
から取り出されて外部へ放流される処理済排水には殆ど
油分が認められないほどになる。
In this manner, the separated oil and sludge can be efficiently collected by sucking and removing the floating oil, floating residue and sludge from the receiving tank regularly or irregularly. Since the oil is efficiently removed by the oil-water separation system of the type, almost no oil is recognized in the treated wastewater which is taken out from the bottom of the calming tank at the downstream end and discharged to the outside.

【0025】この発明の油水分離装置は、各槽の構成が
従来のものに比べて極めて単純であり、また気泡発生装
置も加圧方式でなくてもよいので、槽構成は通常の鉄板
などによる溶接組立てでプレハブ化でき、或いは繊維強
化プラスチックによる成形品として提供することもでき
る。これにより、従来のコンクリート現場打ち構造のも
ので必要であった養生期間が不要となるため、例えばガ
ソリン給油所などの設置現場における他の業務利用を妨
げずに、例えば一夜で油水分離装置の設置を実現できる
ようにもなる。
In the oil / water separator of the present invention, the configuration of each tank is extremely simple as compared with the conventional one, and the bubble generator does not need to be of the pressurized type. It can be prefabricated by welding assembly or can be provided as a molded article of fiber reinforced plastic. This eliminates the need for the curing period required for the conventional concrete cast-in-place structure, so that the oil-water separator can be installed overnight, for example, without hindering other business uses at the installation site such as a gasoline filling station. Can be realized.

【0026】本願発明では上記のようなプレハブ構成や
成形体として構成するのが実際上は望ましいが、勿論、
本発明はコンクリート構造のものにも適用できる。また
本発明において前記気泡発生装置は鎮静槽の全てに気泡
を供給するものに限定されるわけではなく、或いはこの
気泡発生装置から前記受入槽にも気泡を供給するように
してもよい。さらに本発明の装置では、適宜の鎮静槽内
に流れに平行な邪魔板を若干傾斜させて縦配置すること
により、粒子の浮上を助長させるようにすることは妨げ
るものではない。
In the present invention, it is actually desirable to constitute the prefabricated structure or the molded body as described above.
The present invention is also applicable to concrete structures. Further, in the present invention, the bubble generating device is not limited to a device for supplying air bubbles to all of the sedation tank, or air bubbles may be supplied from the bubble generating device to the receiving tank. Further, in the apparatus of the present invention, it is not obstructive to promote the floating of particles by vertically disposing a baffle plate parallel to the flow slightly in an appropriate sedation tank.

【0027】また請求項2に記載の発明に係る油水分離
装置では、前記循環ポンプ手段が、前記集油槽内に取り
込まれた浮渣から固形物を除去する手段を備えているの
で、前記固形物が除去された後の油水のみが前記受入槽
に還流され、この油水は油分を高い濃度で含んでいる。
これにより受入槽では表層に浮上油が主に溜ることにな
り、浮渣の殆どは前記循環ポンプ手段中で別に除去・回
収され、浮渣が受入槽に流入するときの濡れ現象により
再び被処理水中に沈降してしまう恐れがなくなる。
In the oil-water separator according to the second aspect of the present invention, the circulating pump includes means for removing solids from the floating residue taken into the oil collecting tank. Only the oil water from which the oil has been removed is returned to the receiving tank, and this oil water contains a high concentration of oil.
As a result, the floating oil mainly accumulates on the surface layer in the receiving tank, and most of the floating residue is separately removed and collected in the circulation pump means, and is again treated by the wetting phenomenon when the floating residue flows into the receiving tank. There is no danger of sinking in water.

【0028】また請求項3に記載の発明に係る油水分離
装置では、前記気泡発生装置が前記鎮静槽の底部に配置
された多孔ノズルと、該ノズルへ空気を送りこむ給気装
置とを含んでおり、これにより通常のエアーポンプ(コ
ンプレッサ)と配管およびポーラスストーンや多数の細
い孔を有するパイプ状または平箱マット状ノズル体など
による多孔ノズルで気泡発生装置を簡単に構成できるも
のである。
In the oil-water separator according to the third aspect of the present invention, the bubble generator includes a perforated nozzle arranged at the bottom of the calming tank and an air supply device for sending air to the nozzle. Thus, the bubble generating device can be easily constituted by a normal air pump (compressor) and a pipe and a porous nozzle or a porous nozzle having a pipe-shaped or flat box-shaped nozzle having a large number of small holes.

【0029】また請求項4に記載の発明に係る油水分離
装置では、前記鎮静槽が底部で互いに連通した隣接鎮静
槽の対を含むものであり、これによってこの対の上流側
鎮静槽で浮上油を分離した被処理水が下流側鎮静槽に底
部から流入し、残っている油分粒子の重力分離効率を最
大限にして効率よく浮上させ、かくして隣接鎮静槽の各
々で油分の効率的な浮上分離が達成されるものである。
この場合、好ましくは隣接鎮静槽間の底部連通口は流れ
を出来るだけ乱れのない層流とするために幅広の開口と
するのがよい。
In the oil-water separator according to the fourth aspect of the present invention, the sedation tank includes a pair of adjacent sedation tanks that communicate with each other at a bottom portion, whereby the floating oil is settled on the upstream sedation tank. The separated water flows into the downstream calming tank from the bottom and maximizes the gravity separation efficiency of the remaining oil particles to efficiently float, thus efficiently floating and separating oil in each adjacent calming tank Is achieved.
In this case, it is preferable that the bottom communication port between the adjacent sedation tanks has a wide opening in order to make the flow as laminar as possible without disturbance.

【0030】請求項5に記載の油水分離装置では、前記
隣接鎮静槽のうちの下流側の鎮静槽に表層部で連通した
別の鎮静槽を更に連設したものであり、この別の鎮静槽
に前記集油槽を設置できるようにしたものである。この
ようにすると、この別の鎮静槽には上流側の鎮静槽の表
槽部に浮上した浮上油が層流となってシフトしてくるこ
とになり、直前の上流側鎮静槽における油分の浮上分離
に乱れを与えることなく浮上油を集油槽に取り込むこと
ができるようになる。この場合も、前記表層での連通は
広幅または全幅の通路で達成されるようにするのがよい
ことは述べるまでもない。
[0030] In the oil-water separation device according to the fifth aspect, another sedation tank connected to the downstream sedation tank of the adjacent sedation tank at the surface portion is further provided, and the other sedation tank is provided. The above-mentioned oil collecting tank can be set up. In this way, the floating oil floating on the surface of the upstream calming tank shifts as a laminar flow in the other calming tank, and the oil rises in the upstream calming tank immediately before. The floating oil can be taken into the oil collecting tank without disturbing the separation. Also in this case, it is needless to say that the communication at the surface layer is preferably achieved by a wide or full width passage.

【0031】また請求項6に記載の発明に係る油水分離
装置では、前記受入層がその底部の汚泥溜りの直上で立
上り流路によって前記鎮静槽の上流端に連通されてお
り、これは例えば立上り管等によって受入槽底部近傍の
被処理水を上向き流れにして鎮静槽上流端に導入するよ
うにし、これにより受入槽底部の汚泥が鎮静槽側へ流入
するのを、油粒子の過剰な混入を避けるのと同時に且つ
確実に防止するのである。
In the oil-water separation device according to the invention, the receiving layer is communicated with the upstream end of the calming tank by a rising flow path immediately above the bottom of the sludge reservoir. The water to be treated near the bottom of the receiving tank is made to flow upward by a pipe or the like and introduced into the upstream end of the calming tank, thereby preventing the sludge at the bottom of the receiving tank from flowing into the calming tank side due to excessive mixing of oil particles. It is simultaneously avoided and reliably prevented.

【0032】また請求項7に記載の発明に係る油水分離
装置では、前記受入槽が循環ポンプ手段による油水の還
流を受けて最終的な油の収集除去がこの受入槽からバキ
ュームなどによる吸引によって行われることから、前記
受入槽を前記鎮静槽の個々の槽より大容量にして浮上油
の蓄積容量を増し、吸引作業のインターバルに余裕を持
たせたものである。
In the oil-water separation device according to the present invention, the receiving tank receives the return of the oil water by the circulation pump means, and the final collection and removal of the oil is performed by suction from the receiving tank by a vacuum or the like. Therefore, the capacity of the receiving tank is made larger than the individual tanks of the sedation tank to increase the accumulated capacity of the floating oil, and the interval of the suction operation is given a margin.

【0033】また請求項8に記載の発明に係る油水分離
装置では、前記集油槽内に溢流してくる前記下流端の鎮
静槽の表層油水の集油槽内でのレベルを検出して前記循
環ポンプ手段を前記溢流が維持されるように駆動制御す
る制御手段を備えており、これによって集油槽の上縁の
水深が一定でも流入汚水の流量の応じて油水の循環処理
が安定して行われ、放水中に油分が混入するのを防止す
ることができるようになる。
In the oil / water separator according to the present invention, the circulating pump detects the level of the surface oil in the surface oil water of the sedation tank at the downstream end which overflows into the oil collection tank. Control means for driving and controlling the means so that the overflow is maintained, whereby even if the water depth of the upper edge of the oil collecting tank is constant, the circulation processing of the oil water is performed stably in accordance with the flow rate of the inflowing wastewater. In addition, it is possible to prevent oil from being mixed in the discharged water.

【0034】尚、本願発明においてはこのような集油槽
と循環ポンプ手段とによる浮上油の循環系を複数多重に
備えていてもよく、この場合は好ましくは下流側の複数
の鎮静槽に各々集油槽が配置され、各集油槽からの還流
が全て受入槽へ循環されるようにするのがよい。またこ
の場合、前記制御手段は外部からの汚水の流入流量に応
じて幾つかの循環系を選択的に作動させる機能を含んで
いてもよい。
In the present invention, a plurality of circulating systems of floating oil by such an oil collecting tank and a circulating pump means may be provided in a multiplex manner. In this case, it is preferable to collect the floating oil in a plurality of downstream calming tanks. Oil tanks are preferably arranged so that all reflux from each oil collection tank is circulated to the receiving tank. Further, in this case, the control means may include a function of selectively operating some of the circulating systems according to the flow rate of inflow of sewage from outside.

【0035】また請求項9に記載の発明に係る油水分離
装置では、前記集油槽が、下流端の前記鎮静槽内にて被
処理水表面下に上縁が僅かに沈むように位置された独立
容器を備えている。これは集油槽を鎮静槽の水面域内に
配置して集油槽の全周縁から溢流を取り込み、下流端の
鎮静槽において表面槽の流れを全周縁から中央へ向う流
れとすることにより浮上油を素早く収集できるようにす
ると共に、下流端の鎮静槽の表層に何れかの辺縁に向う
偏った流れが生じないようにして、表層での浮上油の偏
在による分離不良をなくすためのものである。
In the oil-water separation device according to the ninth aspect of the present invention, the oil collecting tank is located in the sedation tank at the downstream end so that the upper edge thereof is slightly sunk below the surface of the water to be treated. It has. This is because the oil collecting tank is arranged in the water surface area of the calming tank, the overflow is taken in from the entire periphery of the oil collecting tank, and the flow of the surface tank is made to flow from the entire periphery to the center in the calming tank at the downstream end. The purpose is to make it possible to collect quickly, and to prevent uneven flow toward any edge on the surface layer of the calming tank at the downstream end, and to eliminate poor separation due to uneven distribution of floating oil on the surface layer. .

【0036】請求項10に記載の発明に係る油水分離装
置においては、前記独立容器を浮子の原理により被処理
水中に浮遊支持させることにより、浮力バランスによっ
て独立集油槽の沈漬深度を自然に達成するようにしたも
のであり、この場合、独立容器に別の浮子を取付けて
も、或いは容器自体を浮子として機能するように構成し
てもよい。
In the oil-water separator according to the tenth aspect of the present invention, the independent vessel is floated and supported in the water to be treated by the principle of a float, thereby naturally achieving the immersion depth of the independent oil collecting tank by buoyancy balance. In this case, another floating member may be attached to the independent container, or the container itself may be configured to function as a floating member.

【0037】請求項11に記載の油水分離装置では、前
記独立容器を支柱により前記上縁の高さ位置を調整可能
に支持し、それによって独立集油槽の沈漬深度を被処理
水の水位に応じて調整できるようにしたものである。
[0037] In the oil-water separator according to the eleventh aspect, the height of the upper edge of the independent vessel is supported by a column so as to be adjustable, whereby the immersion depth of the independent oil collecting tank is adjusted to the level of the water to be treated. It can be adjusted accordingly.

【0038】さらに請求項12に記載の発明に係る油水
分離装置では、請求項9に記載の油水分離装置におい
て、前記循環ポンプ手段のポンプを前記独立容器内に配
置された水中ポンプとし、ポンプの保守点検を容易にし
たものである。この場合、このポンプ付き集油独立容器
を鎮静槽に対して着脱可能に構成しておけば、これを用
いて受入槽から回収油を別容器に回収することもでき
る。
According to a twelfth aspect of the present invention, in the oil-water separator according to the ninth aspect, the pump of the circulating pump means is a submersible pump disposed in the independent vessel. This facilitates maintenance and inspection. In this case, if the independent oil collecting container with the pump is configured to be detachable from the sedation tank, the collected oil can be collected from the receiving tank to another container by using this.

【0039】この発明の種々の特徴は以下の図面による
実施例の説明から更に明確に理解されよう。
The various features of the present invention will be more clearly understood from the following description of the embodiments with reference to the drawings.

【0040】[0040]

【実施例】図1には、この発明の好適な実施例に係る油
水分離装置が模式縦断面図で示されている。また図2は
その平面図に相当する。
FIG. 1 is a schematic longitudinal sectional view of an oil / water separator according to a preferred embodiment of the present invention. FIG. 2 is a plan view thereof.

【0041】図1および図2において、この装置は主要
槽構造が金属板の溶接や繊維強化プラスチックの成形等
によって一体化されたユニット1を構成している。ユニ
ット1は、全体としては複数の堅型槽が一列に側方へ向
って配列された多段槽構造となっており、上流端と下流
端には各々側溝との接続部1a,1bが形成されてい
る。
1 and 2, this apparatus constitutes a unit 1 in which a main tank structure is integrated by welding a metal plate, molding fiber-reinforced plastic, or the like. The unit 1 as a whole has a multi-stage tank structure in which a plurality of rigid tanks are arranged in a line toward the side, and connection portions 1a and 1b with the side grooves are formed at the upstream end and the downstream end, respectively. ing.

【0042】入側接続部1aは受入槽10に開口し、受
入槽10の下流には、第1〜第3鎮静槽11〜13と検
査槽14が順に配列されている。最下流の検査槽は下流
端で排出用の側溝1bに通じている。
The entrance-side connecting portion 1a opens to the receiving tank 10, and downstream of the receiving tank 10, first to third sedation tanks 11 to 13 and an inspection tank 14 are arranged in order. The most downstream inspection tank communicates with the discharge side groove 1b at the downstream end.

【0043】第2鎮静槽12には、底部にポーラススト
ーン製の複数本のノスル4が横置され、このノズル4に
は、槽外からエアーコンプレッサ6による空気が配管
(ホース)8を介して供給されている。これによりノズ
ル4から細かい気泡が発生し、これが槽内の被処理水中
のオイルボール粒や油分含有汚泥粒などに付着してその
浮上を行わせるようになっている。
A plurality of nosles 4 made of porous stone are horizontally disposed at the bottom of the second calming tank 12, and air from an air compressor 6 is supplied to the nozzle 4 from outside of the tank via a pipe (hose) 8. Supplied. As a result, fine air bubbles are generated from the nozzles 4 and adhere to oil ball particles or oil-containing sludge particles in the water to be treated in the tank and cause them to float.

【0044】受入槽10からは、その比較的下層部の被
処理水が立上り管15を介して第1鎮静槽11の表面に
放水されるようになされ、立上り管15の下端には粗大
な汚泥粒の流下を防ぐための簡単なフィルターが装着さ
れている。
From the receiving tank 10, water to be treated in a relatively lower part thereof is discharged to the surface of the first calming tank 11 through a rising pipe 15, and coarse sludge is provided at a lower end of the rising pipe 15. A simple filter is installed to prevent the particles from flowing down.

【0045】第1鎮静槽11は、第2鎮静槽12との隔
壁に穿たれた幅広穴16によりその比較的下層部で第2
鎮静槽12と直接連通している。
The first sedation tank 11 has a wide lower hole 16 formed in a partition wall of the first sedation tank 12 and a second lower sedation tank.
It is in direct communication with the sedation tank 12.

【0046】第2鎮静槽12は、第3鎮静槽13との隔
壁の上縁に形成された幅広凹部17によりその表層部で
第3鎮静槽13と直接連通されている。
The second calming tank 12 is in direct communication with the third calming tank 13 at the surface layer by a wide recess 17 formed on the upper edge of the partition wall with the third calming tank 13.

【0047】このような連通構造によって、入側接続部
1aから受入槽10に流入した被処理水が第2鎮静槽1
2まで上下に蛇行する経路をたどって流れるようになっ
ている。
With such a communication structure, the water to be treated that has flowed into the receiving tank 10 from the inlet-side connecting portion 1a is transferred to the second calming tank 1
It follows the path meandering up and down to 2.

【0048】第2鎮静槽12から第3鎮静槽13への流
れは表層部のみの単純な水平方向へのシフト流れであ
る。
The flow from the second calming tank 12 to the third calming tank 13 is a simple horizontal shift flow of only the surface layer.

【0049】第3鎮静槽13内には浮子式の浮遊する集
油槽20が配置されており、この集油槽20は内部に水
中汲み上げポンプ21を備えている。ポンプ21は集油
槽20に固定された図示しないレベルスイッチによって
集油槽20内の被処理水レベルが所定レベル以上になっ
ていることが検出されている間だけ作動するように制御
盤30によって制御されており、ポンプ21によって汲
み組み上げられた被処理水は、好ましくはフレキシブル
部分を含む配管22によって浮渣除去フィルタ26を介
して受入槽10に戻されるようになっている。
A floating oil collecting tank 20 of a floating type is arranged in the third calming tank 13, and the oil collecting tank 20 has a submersible pump 21 inside. The pump 21 is controlled by the control panel 30 so as to operate only while the level of the water to be treated in the oil collecting tank 20 is detected to be higher than a predetermined level by a level switch (not shown) fixed to the oil collecting tank 20. The to-be-processed water pumped and assembled by the pump 21 is preferably returned to the receiving tank 10 via the sediment removal filter 26 by a pipe 22 including a flexible portion.

【0050】この場合、集油槽20内のポンプ21が空
気を吸込まないように、スイッチが検出出力を生じてい
ないときも集油槽20内にはポンプ吸引口以上のレベル
で被処理水が入っているようにされており、この状態で
集油槽20の浮子バランスが平衡して集油槽20がその
上縁を第3鎮静槽13の水面レベルより所定深さで沈ま
せた状態になるようにしてある。従って集油槽20には
継続的に表層の被処理水が流入するが、この流入する被
処理水の集油槽内レベルが第3鎮静槽水面レベルに追い
付かないようにポンプ21が駆動される。
In this case, in order to prevent the pump 21 in the oil collecting tank 20 from sucking air, even when the switch does not generate a detection output, the water to be treated enters the oil collecting tank 20 at a level higher than the pump suction port. In this state, the float balance of the oil collecting tank 20 is balanced so that the oil collecting tank 20 is in a state where its upper edge is sunk at a predetermined depth from the water level of the third calming tank 13. It is. Therefore, the surface water to be treated continuously flows into the oil collecting tank 20, but the pump 21 is driven so that the level of the inflowing water to be treated in the oil collecting tank does not catch up with the third calming tank water level.

【0051】第3鎮静槽13とその下流の検査槽14と
の間は、第3鎮静槽13の下層部に一端が開口する立上
り管18によって接続されており、この立上り管18の
上端部は検査槽14の水面レベル近傍に開口している。
The third sedation tank 13 and the downstream inspection tank 14 are connected by a riser pipe 18 having one end opening in the lower part of the third sedation tank 13. It is open near the water surface level of the inspection tank 14.

【0052】検査槽14は流れの途中に油よけ板19を
有しており、流れはこの油よけ板19の下端をくぐって
出側接続部1bから排水側溝へ流出するようになってい
る。尚、この油よけ板19は、ユニット1の壁構造の一
部であってもよい。
The inspection tank 14 has an oil barrier 19 in the middle of the flow, and the flow passes through the lower end of the oil barrier 19 and flows out from the outlet connection portion 1b to the drain groove. I have. Note that the oil barrier 19 may be a part of the wall structure of the unit 1.

【0053】この実施例の油水分離装置では、入側接続
部1aから受入槽10に流入する側溝からの油水混合の
被処理水は、受入槽10の表層の油層中に流入して油を
巻込みながら下降するが、受入槽10はその表層からバ
キュームで油を別のタンク等に回収するのにも利用する
ため、図1に鎖線で示したように仕切り板または壁23
を設けてもよい。
In the oil / water separator of this embodiment, the water to be treated for mixing the oil / water from the gutter flowing into the receiving tank 10 from the inlet connection part 1a flows into the surface oil layer of the receiving tank 10 to wind the oil. The receiving tank 10 is also used for collecting oil from the surface layer of the receiving tank 10 into a separate tank or the like by vacuum. Therefore, as shown by a chain line in FIG.
May be provided.

【0054】さて、受入槽10に流入した被処理水は層
内の油やオイルボール粒及び油分含有汚泥粒等の懸濁粒
子を巻込みながら流下して多少の鎮静効果により油粒子
を浮上させながら多少の懸濁粒子を混合した状態で幅方
向二本の立上り管15を介して第1鎮静槽11にその表
面部から流入する。この場合、立上り管15の入口で水
中の粗大な粒子の流下が阻止され、したがってこれら粗
大粒子は受入槽10の底に汚泥となって溜ることにな
る。
The water to be treated, which has flowed into the receiving tank 10, flows down while entraining suspended particles such as oil and oil balls and oil-containing sludge particles in the layer, and floats the oil particles by a slight calming effect. While mixed with some suspended particles, the particles flow into the first calming tank 11 from the surface thereof through the two risers 15 in the width direction. In this case, the flow of the coarse particles in the water is prevented from flowing down at the inlet of the riser 15, and therefore, these coarse particles accumulate as sludge at the bottom of the receiving tank 10.

【0055】第1鎮静槽11では、二本の立上り管15
から表面近くで流れを受けるので攪乱は少なく、従って
被処理水は鎮静された油粒子の浮上が有効に行われる。
下層の油粒子の少ない被処理水は次いで幅広穴16を介
して第2鎮静槽12へ下から流入し、ここでも穴16が
幅広であるので攪乱は受けない。
In the first calming tank 11, two rising pipes 15 are provided.
The flow of water near the surface causes less disturbance, so that the treated water effectively floats calmed oil particles.
The water to be treated, which is low in oil particles in the lower layer, then flows into the second calming tank 12 from below through the wide hole 16, where the hole 16 is wide and is not disturbed.

【0056】第2鎮静槽12に下から流入した被処理水
は油粒子に充分な浮力の効果を発揮させて浮上させ、ま
たノズル4からの細かい気泡が浮上中に懸濁粒子に付着
してその見掛比重を小さくすることによりこれら懸濁粒
子をも速やかに浮上させ、したがって被処理水中の油粒
子やオイルボール粒及び油分含有汚泥粒を浮渣として殆
ど浮上させた状態となる。
The water to be treated which has flowed into the second calming tank 12 from below is caused to float by exerting a sufficient buoyancy effect on the oil particles, and fine bubbles from the nozzle 4 adhere to the suspended particles during the floating. By reducing the apparent specific gravity, these suspended particles also float quickly, so that the oil particles, oil ball particles and oil-containing sludge particles in the water to be treated are almost floated as floating residues.

【0057】この第2鎮静槽12の表層部の被処理水は
浮渣および浮上油と共に幅広凹部17を介して水平にシ
フトして第3鎮静槽13に流入するが、第3鎮静槽13
では先に述べたように集油槽20が表層の被処理水を吸
込んでおり、したがって表層の浮渣と浮上油は殆どが集
油槽20内に流入する。集油槽20への流入を逃れたの
は油粒子を殆ど全く含まない水であり、これは第3鎮静
槽13の下層から立上り管18を介して検査槽14の表
面レベルに流入し、さらに油よけ板19の下をくぐって
出側接続部1bから排水側溝へ流出する。検査槽14の
板18の上流側は最終排水の表面目視検査のために利用
され、その表面に油分が認められれば表層水を再循環へ
回すようにする。
The water to be treated in the surface layer of the second calming tank 12 shifts horizontally through the wide recess 17 and flows into the third calming tank 13 together with the residue and the floating oil.
As described above, the oil collecting tank 20 sucks the surface water to be treated as described above, so that most of the surface residue and floating oil flow into the oil collecting tank 20. What escaped the inflow into the oil collection tank 20 was water containing almost no oil particles, which flowed from the lower layer of the third calming tank 13 through the riser pipe 18 to the surface level of the inspection tank 14, It passes under the shield plate 19 and flows out of the outlet connection portion 1b into the drainage groove. The upstream side of the plate 18 of the inspection tank 14 is used for visual inspection of the surface of the final drainage, and if oil is recognized on the surface, the surface water is recirculated.

【0058】一方、集油槽20内に集められた被処理水
は第3鎮静槽13の表層の浮渣と浮上油を殆ど回収して
いるので油分を多く含む浮渣含有油水混合液である。こ
の混合液はポンプ21により配管22を介して浮渣除去
フィルタ24に導かれ、フィルタ24で浮渣と分離され
た油水が受入槽10へ循環される。この場合、フィルタ
24の油水出口は図1に鎖線で示した仕切り板23の上
流側にしてもよく、それによって仕切り板23の下流側
における受入槽10の表面部分をバキューム等による油
回収作業領域に専用の部分とすることができ、またその
部分での流入油水による回収油の水分含有量の増加を防
ぐこともできる。尚、フィルタ24で分離された浮渣は
油分含有固形物としてスコップなどで別に掻き出され
る。
On the other hand, the water to be treated collected in the oil collecting tank 20 is a floating residue-containing oil / water mixture containing a large amount of oil, since most of the floating residue and floating oil in the surface layer of the third calming tank 13 are recovered. This mixed solution is guided by a pump 21 to a residue removal filter 24 via a pipe 22, and the oil water separated from the residue by the filter 24 is circulated to the receiving tank 10. In this case, the oil water outlet of the filter 24 may be on the upstream side of the partition plate 23 shown by a dashed line in FIG. 1, whereby the surface portion of the receiving tank 10 on the downstream side of the partition plate 23 is used as an oil recovery work area by vacuum or the like. Can be used as a dedicated portion, and an increase in the water content of the recovered oil due to the inflowing oil water at that portion can be prevented. The floating residue separated by the filter 24 is scraped off as a solid containing oil by a scoop or the like.

【0059】前述の実施例では集油槽20を浮子式の浮
遊槽にした場合を説明したが、これは単なる例示のため
であって、本願発明はこれに限定されるものではない。
In the above-described embodiment, the case where the oil collecting tank 20 is a floating type floating tank has been described. However, this is merely an example, and the present invention is not limited to this.

【0060】第3図の変形例では、鎮静槽の側壁に開口
31を介して槽室33を設け、槽室内で開口31に下か
ら昇降可能なゲート32設置して開口レベルを可変と
し、槽室33内にポンプ21配置して集油槽としてい
る。
In the modification shown in FIG. 3, a tank chamber 33 is provided on the side wall of the sedation tank via an opening 31, and a gate 32 which can be lifted and lowered from below in the opening 31 is provided in the tank chamber to make the opening level variable. The pump 21 is disposed in the chamber 33 to form an oil collecting tank.

【0061】また第4図の変形例では、集油槽40を浮
子式とせずに、鎮静槽の壁に沿わせて縦に設置した支柱
41に集油槽40を高さ位置調整可能に支持させてい
る。
In the modification shown in FIG. 4, the oil collecting tank 40 is not floatable, but is supported by a column 41 installed vertically along the wall of the sedation tank so that the oil collecting tank 40 can be adjusted in height. I have.

【0062】この他にも変形は可能であり、例えば集油
槽を複数の鎮静槽に配置したり、また集油槽の外形も円
形に限らず種々の矩形形状を採用してもよい。
Other modifications are also possible. For example, the oil collecting tank may be arranged in a plurality of calming tanks, and the outer shape of the oil collecting tank is not limited to a circular shape but may be various rectangular shapes.

【0063】[0063]

【発明の効果】以上に述べたように、本発明の油水分離
装置は独特の循環方式と気泡混合方式を採用しているの
で油やオイルボール粒子及び油分含有汚泥粒子を短時間
で効率よく分離することができ、循環ポンプの制御によ
って被処理水の流入量が変化しても有効に対処すること
ができ、また気泡発生装置は通常の部品で簡略に構成で
きて保守も殆ど不要であり、更に槽ユニットの構造が比
較的簡単で設置に時間がかからないから、例えば給油所
などの雨水が混入する恐れのある業務施設における経済
的な油分含有汚水の油水分離装置として好適であり、プ
レハブ組立て方式やユニット化などにより比較的少ない
設備面積で短時間に構築することができるものである。
As described above, the oil-water separator of the present invention employs a unique circulation system and a bubble mixing system, so that oil, oil ball particles and oil-containing sludge particles can be efficiently separated in a short time. It is possible to effectively cope with the change in the inflow of the water to be treated by controlling the circulation pump, and the bubble generating device can be simply configured with ordinary parts and requires almost no maintenance. Furthermore, since the structure of the tank unit is relatively simple and the installation does not take much time, it is suitable as an oil-water separation device for economical oil-containing sewage in a business facility where rainwater may be mixed, for example, at a gas station. It can be constructed in a short time with a relatively small equipment area due to the unit and unitization.

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

【図1】この発明の好適な実施例に係る油水分離装置を
示す模式縦断面図である。
FIG. 1 is a schematic longitudinal sectional view showing an oil-water separator according to a preferred embodiment of the present invention.

【図2】前記実施例に係る油水分離装置の概略の平面図
である。
FIG. 2 is a schematic plan view of the oil-water separation device according to the embodiment.

【図3】前記実施例の変形例を示す部分模式断面図であ
る。
FIG. 3 is a partial schematic cross-sectional view showing a modification of the embodiment.

【図4】前記実施例の別の変形例を示す部分模式断面図
である。
FIG. 4 is a partial schematic sectional view showing another modification of the embodiment.

【符号の説明】[Explanation of symbols]

1 ユニット 4 ノズル 6 エアーコンプレッサ 8 配管(ホース) 10 受入槽 11 第1鎮静槽 12 第2鎮静槽 13 第3鎮静槽 14 検査槽 20 集油槽 21 ポンプ 22 配管 24 フィルタ 30 制御盤 DESCRIPTION OF SYMBOLS 1 Unit 4 Nozzle 6 Air compressor 8 Piping (hose) 10 Receiving tank 11 1st calming tank 12 2nd calming tank 13 3rd calming tank 14 Inspection tank 20 Oil collecting tank 21 Pump 22 Piping 24 Filter 30 Control panel

Claims (12)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 油の混合した汚水等の被処理水を複数段
に直列配置された水槽に通して油を浮上分離する油水分
離装置において、前記被処理水を上部開口から受入れる
受入槽、該受入槽中の下層部からの被処理水を受入れて
順次鎮静させるために上流から下流へ直列状に配列され
た複数段の鎮静槽、少なくとも下流端の前記鎮静槽の表
層油水を溢流として取り込む集油槽、前記鎮静槽の被処
理水中で空気の泡を発生する気泡発生装置、前記集油槽
に取り込まれた溢流を前記受入槽に還流させる循環ポン
プ手段、及び前記下流端の鎮静槽の底部から油分離処理
済みの水を外部へ排出する排水手段、を備えてなること
を特徴とする油水分離装置。
An oil-water separation device for separating and separating oil by floating water to be treated such as sewage mixed with oil through a plurality of water tanks arranged in series in a plurality of stages. A plurality of stages of sedation tanks arranged in series from upstream to downstream to receive and treat the water to be treated from the lower part in the receiving tank, and take in the surface oil water of at least the sedation tank at the downstream end as overflow. An oil collection tank, a bubble generator for generating air bubbles in the water to be treated in the sedation tank, a circulating pump means for returning an overflow taken in the oil collection tank to the receiving tank, and a bottom portion of the sedation tank at the downstream end An oil-water separation device, comprising: a drainage unit that discharges oil-separated water from the water to the outside.
【請求項2】 前記循環ポンプ手段が、前記集油槽に取
り込まれた溢流から固形物を除去する手段を備え、前記
固形物が除去された後の油水を前記受入槽に還流するよ
うに構成されていることを特徴とする請求項1に記載の
油水分離装置。
2. The circulating pump means includes means for removing solid matter from the overflow taken into the oil collecting tank, and is configured to return the oil water from which the solid matter has been removed to the receiving tank. The oil / water separation device according to claim 1, wherein the oil / water separation device is used.
【請求項3】 前記気泡発生装置が前記鎮静槽の底部に
配置された多孔ノズルと、該ノズルへ空気を送りこむ給
気装置とを含む請求項1に記載の油水分離装置。
3. The oil-water separator according to claim 1, wherein the bubble generator includes a perforated nozzle disposed at a bottom of the calming tank, and an air supply device for sending air to the nozzle.
【請求項4】 前記鎮静槽が底部で互いに連通した隣接
鎮静槽の対を含む請求項1に記載の油水分離装置。
4. The oil-water separator according to claim 1, wherein said sedation tank comprises a pair of adjacent sedation tanks communicating with each other at a bottom.
【請求項5】 前記鎮静槽が底部で互いに連通した隣接
鎮静槽の対を含むと共に、前記隣接鎮静槽のうちの下流
側の鎮静槽に表層部で連通した別の鎮静槽を更に含む請
求項1に記載の油水分離装置。
5. The sedation tank includes a pair of adjacent sedation tanks that communicate with each other at a bottom portion, and further includes another sedation tank that is communicated with a downstream sedation tank of the adjacent sedation tanks at a surface portion. 2. The oil-water separation device according to 1.
【請求項6】 前記受入槽が底部の汚泥溜りの直上で立
上り流路によって上流端の前記鎮静槽に連通されている
請求項1に記載の油水分離装置。
6. The oil / water separator according to claim 1, wherein the receiving tank is connected to the sedation tank at the upstream end by a rising flow path immediately above the sludge pool at the bottom.
【請求項7】 前記受入槽が前記鎮静槽の個々の槽より
大容量であることを特徴とする請求項1に記載の油水分
離装置。
7. The oil-water separator according to claim 1, wherein the capacity of the receiving tank is larger than that of each of the calming tanks.
【請求項8】 前記集油槽に取り込まれた溢流の集油槽
内でのレベルを検出して前記循環ポンプ手段を前記溢流
が維持されるように駆動制御する制御手段を更に備えた
ことを特徴とする請求項1に記載の油水分離装置。
8. A control means for detecting a level of the overflow taken into the oil collecting tank in the oil collecting tank and controlling the driving of the circulating pump means so as to maintain the overflow. The oil-water separation device according to claim 1, wherein:
【請求項9】 前記集油槽が、下流端の前記鎮静槽内に
て被処理水表面下に上縁が僅かに沈むように配置された
独立容器を備えている請求項1に記載の油水分離装置。
9. The oil-water separation device according to claim 1, wherein the oil collecting tank includes an independent vessel arranged such that an upper edge thereof is slightly set below the surface of the water to be treated in the calming tank at the downstream end. .
【請求項10】 前記独立容器が浮子原理により被処理
水中に浮遊支持されている請求項9に記載の油水分離装
置。
10. The oil-water separation device according to claim 9, wherein the independent vessel is suspended and supported in the water to be treated by a float principle.
【請求項11】 前記独立容器が支柱によりその前記上
縁の高さ位置を調整可能に支持されている請求項9に記
載の油水分離装置。
11. The oil-water separator according to claim 9, wherein the independent container is supported by a column so that a height position of the upper edge can be adjusted.
【請求項12】 前記循環ポンプ手段が、前記独立容器
内に配置された水中ポンプを含む請求項9に記載の油水
分離装置。
12. The oil / water separation device according to claim 9, wherein the circulation pump means includes a submersible pump disposed in the independent container.
JP02407242A 1990-12-08 1990-12-08 Oil-water separator Expired - Fee Related JP3092013B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP02407242A JP3092013B2 (en) 1990-12-08 1990-12-08 Oil-water separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP02407242A JP3092013B2 (en) 1990-12-08 1990-12-08 Oil-water separator

Publications (2)

Publication Number Publication Date
JPH04210201A JPH04210201A (en) 1992-07-31
JP3092013B2 true JP3092013B2 (en) 2000-09-25

Family

ID=18516861

Family Applications (1)

Application Number Title Priority Date Filing Date
JP02407242A Expired - Fee Related JP3092013B2 (en) 1990-12-08 1990-12-08 Oil-water separator

Country Status (1)

Country Link
JP (1) JP3092013B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001074469A1 (en) * 2000-04-04 2001-10-11 Oy Labko Ab A method for separation by gravity using settling tanks connected in series
KR20220080595A (en) 2020-12-07 2022-06-14 한국항공우주연구원 An oil separator including multi storage tanks which are overlapped

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Publication number Priority date Publication date Assignee Title
KR100417337B1 (en) * 2000-08-31 2004-02-05 이귀주 Apparatus for separating water and oil with nature circulation type
JP5425734B2 (en) * 2010-09-07 2014-02-26 中国電力株式会社 Oil-water separation method and oil-water separation system
CN106422433B (en) * 2016-09-23 2018-11-13 苏州市浒墅关化工添加剂有限公司 Solvent type dinonyl naphthalene sulfonate barium is layered continuous sedimentation tank
CN110304747B (en) * 2019-07-26 2024-02-20 广东普施德泽环保股份有限公司 Oil-water separator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001074469A1 (en) * 2000-04-04 2001-10-11 Oy Labko Ab A method for separation by gravity using settling tanks connected in series
KR20220080595A (en) 2020-12-07 2022-06-14 한국항공우주연구원 An oil separator including multi storage tanks which are overlapped

Also Published As

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