JPH0148076B2 - - Google Patents

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Publication number
JPH0148076B2
JPH0148076B2 JP58217769A JP21776983A JPH0148076B2 JP H0148076 B2 JPH0148076 B2 JP H0148076B2 JP 58217769 A JP58217769 A JP 58217769A JP 21776983 A JP21776983 A JP 21776983A JP H0148076 B2 JPH0148076 B2 JP H0148076B2
Authority
JP
Japan
Prior art keywords
oil
pipe
tank
valve
floating oil
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
JP58217769A
Other languages
Japanese (ja)
Other versions
JPS60110684A (en
Inventor
Tooru Kimura
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.)
JFE Engineering Corp
Original Assignee
Nippon Kokan Ltd
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 Nippon Kokan Ltd filed Critical Nippon Kokan Ltd
Priority to JP58217769A priority Critical patent/JPS60110684A/en
Publication of JPS60110684A publication Critical patent/JPS60110684A/en
Publication of JPH0148076B2 publication Critical patent/JPH0148076B2/ja
Granted legal-status Critical Current

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  • Removal Of Floating Material (AREA)

Description

【発明の詳細な説明】 本発明は、セツトリングタンク内の油分回収装
置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an oil recovery device in a settling tank.

油タンカーのタンク洗浄水は、環境汚染を防止
するために一旦セツトリングタンク内に導入さ
れ、さらに該タンク内で浮上油と油水混合液とに
重力分離される。そしてこの油水混合液はさらに
油水分離機に導かれ油と水に強制分離して処理さ
れるが浮上油は比較的油分が多いために直接油水
分離機にかけることはしないで、別の方法で回収
して処理するようにしている。
In order to prevent environmental pollution, tank wash water from an oil tanker is once introduced into a settling tank, and then separated by gravity into floating oil and an oil-water mixture within the tank. This oil-water mixture is then led to an oil-water separator where it is forcibly separated into oil and water for treatment, but since the floating oil has a relatively high oil content, it is not passed directly through the oil-water separator, but instead is treated using another method. We are trying to collect and process it.

第1図に従来の浮上油回収装置を示す。同図に
おいて1はセツトリングタンク、2及び3はそれ
ぞれセツトリングタンク1内だ重力分離した浮上
油及び油水混合液である。4は浮上油2と油水混
合液3の中間の比重を有するフロートで、該フロ
ート4に設けられた吸引口4aは常に浮上油2の
層内に開口している。5はフレキシブルホース
で、その一端はフロート4の吸引口4aに連通し
ており、他端はタンク囲壁1aに設けられた排出
管6に連結されている。7はポンプ、8はバルブ
である。
FIG. 1 shows a conventional floating oil recovery device. In the figure, 1 is a settling tank, and 2 and 3 are floating oil and an oil-water mixture separated by gravity in the settling tank 1, respectively. Reference numeral 4 denotes a float having a specific gravity intermediate between that of the floating oil 2 and the oil-water mixture 3, and a suction port 4a provided on the float 4 is always open into the layer of the floating oil 2. 5 is a flexible hose, one end of which communicates with the suction port 4a of the float 4, and the other end connected to a discharge pipe 6 provided in the tank surrounding wall 1a. 7 is a pump, and 8 is a valve.

なお、第1図には油水混合液3の排出手段は示
されていないが、これは通常のポンプ手段でよい
ものである。
Although a means for discharging the oil-water mixture 3 is not shown in FIG. 1, a conventional pump means may be sufficient as this.

上記従来装置の構成によれれば、セツトリング
タンク1内の浮上油2のみをフロート4の、吸引
口4aよりフレキシブルホース5及び排出管6を
通して回収することができ、また浮上油2のレベ
ルが変動してもフレキシブルホース5がそれに応
じて伸縮するので、浮上油2のレベルいかんにか
かわらず回収することができるものである。
According to the configuration of the conventional device described above, only the floating oil 2 in the settling tank 1 can be collected from the suction port 4a of the float 4 through the flexible hose 5 and the discharge pipe 6, and the level of the floating oil 2 can be Even if the floating oil 2 fluctuates, the flexible hose 5 expands and contracts accordingly, so that it can be recovered regardless of the level of the floating oil 2.

しかしながら上記のような構成では、セツトリ
ングタンクが陸上に設置される場合には問題はな
いが、バージ上に設置する場合も少なくなく、こ
のような場合セツトリングタンクの動揺によりフ
ロート4がタンク内壁と激く衝突してしばしば故
障を生ずるという欠点があつた。
However, with the above configuration, there is no problem when the settling tank is installed on land, but there are many cases where it is installed on a barge, and in such cases, the float 4 may be damaged by the movement of the settling tank and the tank inner wall. The drawback was that they collided violently with each other, often resulting in breakdowns.

本発明は上記の欠点を解消するためになされた
もので、上記のようにセツトリングタンクの動揺
による影響を受けるフロート式の吸引方式に代え
て、サイホン原理を応用することによりセツトリ
ングタンク内の油分回収システムとしての故障の
生じない効率的な油分回収装置を提供しようとす
るものである。
The present invention has been made to solve the above-mentioned drawbacks, and instead of using the float-type suction method that is affected by the fluctuation of the settling tank as described above, it uses the siphon principle to reduce the amount of water inside the settling tank. The present invention aims to provide an efficient oil recovery device that does not cause failures as an oil recovery system.

本発明によるセツトリングタンク内の油分回収
装置は、油水を重力分離するタンクと、排出側に
弁及びポンプを有し前記タンク内に設けられた逆
U字状のサイホン管と、該サイホン管の頂部に連
結された大気連通管と、前記サイホン管の頂部と
ほぼ同一レベルの位置において前記タンクの側壁
に開口せしめた浮上油吸引口と、該浮上油吸引口
と前記ポンプ間を弁を介して連結した浮上油排出
管と、前記ポンプが前記大気連通管または浮上油
吸引口からの空気を吸い込み始めたことを感知し
て前記サイホン管の弁及び浮上油排出管の弁の開
閉を切替える手段とを備え、前記サイホン管の内
部頂点と前記浮上油吸引口の下部口縁とを同一レ
ベルに位置せしめたものであることを特徴とする
ものである。
The oil recovery device in a settling tank according to the present invention includes a tank that separates oil and water by gravity, an inverted U-shaped siphon pipe provided in the tank and having a valve and a pump on the discharge side, and a siphon pipe of the siphon pipe. An atmosphere communication pipe connected to the top, a floating oil suction port opened in the side wall of the tank at a position approximately at the same level as the top of the siphon pipe, and a valve connected between the floating oil suction port and the pump. a floating oil discharge pipe connected thereto, and means for detecting that the pump starts sucking air from the atmospheric communication pipe or the floating oil suction port and switching the opening and closing of the valve of the siphon pipe and the valve of the floating oil discharge pipe; It is characterized in that the internal apex of the siphon pipe and the lower lip of the floating oil suction port are located at the same level.

以下図面を参照しながら本発明の一実施例を説
明する。
An embodiment of the present invention will be described below with reference to the drawings.

第2図は本発明の一実施例を示す説明図で、第
3図は第2図のA部の拡大詳細図である。これら
の図において、1はセツトリングタンクであり、
この実施例ではさらに該タンク1内は隔壁10に
より1次分離槽11と2次分離槽12に区画され
ている。13は被処理水たるタンク洗浄水を1次
分離槽11に導入するための導入管である。14
は1次分離槽11内の比較的油分の多い被処理水
を2次分離槽12に導入するべく両分離槽11,
12間を連絡する1次分離水用導入管であり、そ
の一端は1次分離槽11内にあつて該分離槽11
内で重力分離された浮上油2aの分離面近傍でラ
ツパ状に開口している。他端は弁15−8を介し
て2次分離槽12の下部に開口している。16は
2次分離槽12内に設けられたサイホン管であ
り、その排出側には弁15−1及びポンプ7が設
けられている。17はサイホン管16の吸込端に
設けられたフイルタである。サイホン管16の逆
U字状に屈曲された頂部16aには大気連通管1
8が連結され、大気連通管18には弁15−7が
設けられている。19はサイホン管16の頂部1
6aとほぼ同一レベルの位置において2次分離槽
12の側壁12aに開口された浮上油吸引口であ
る。20は浮上油吸引口19を開閉する開度調整
可能な弁である。そしてこの弁20の下部口縁が
サイホン管16の頂部6aの内部頂部6bと同一
レベルに位置するようになされる(第3図参照)。
2次分離槽12内で重力分離された浮上油2bは
常にこのレベル21より上方に位置することにな
る。なお、浮上油2bの分離面22は第3図の状
態のときにはレベル21と同一か、もしくはそれ
より若干下方になる。23は一端が浮上油吸引口
19に、他端がポンプ7の吸込側に連結された浮
上油排出管である。浮上油排出管23には弁15
−3が設けられている。24は1次分離槽11の
下部とポンプ7の吸込側間を連絡する油水混合液
排出管であり、フイルタ25及び弁15−1を有
る。
FIG. 2 is an explanatory view showing one embodiment of the present invention, and FIG. 3 is an enlarged detailed view of section A in FIG. In these figures, 1 is a settling tank;
In this embodiment, the inside of the tank 1 is further divided by a partition wall 10 into a primary separation tank 11 and a secondary separation tank 12. Reference numeral 13 denotes an introduction pipe for introducing tank washing water, which is water to be treated, into the primary separation tank 11. 14
In order to introduce the relatively oil-rich treated water in the primary separation tank 11 into the secondary separation tank 12, both separation tanks 11,
12, one end of which is in the primary separation tank 11, and one end of which is in the primary separation tank 11
It opens in the shape of a flap near the separation surface of the floating oil 2a separated by gravity inside. The other end opens to the lower part of the secondary separation tank 12 via a valve 15-8. 16 is a siphon pipe provided in the secondary separation tank 12, and a valve 15-1 and a pump 7 are provided on the discharge side of the siphon pipe. 17 is a filter provided at the suction end of the siphon pipe 16. Atmospheric communication pipe 1 is installed at the top 16a of the siphon pipe 16, which is bent into an inverted U shape.
8 are connected, and the atmosphere communication pipe 18 is provided with a valve 15-7. 19 is the top 1 of the siphon pipe 16
This is a floating oil suction port opened in the side wall 12a of the secondary separation tank 12 at a position substantially on the same level as 6a. 20 is a valve that opens and closes the floating oil suction port 19 and whose opening degree can be adjusted. The lower lip of this valve 20 is positioned at the same level as the inner top 6b of the top 6a of the siphon tube 16 (see FIG. 3).
The floating oil 2b separated by gravity in the secondary separation tank 12 is always located above this level 21. Note that the separation surface 22 of the floating oil 2b is at the same level as the level 21 or slightly below it in the state shown in FIG. 23 is a floating oil discharge pipe connected to the floating oil suction port 19 at one end and to the suction side of the pump 7 at the other end. The floating oil discharge pipe 23 has a valve 15.
-3 is provided. Reference numeral 24 denotes an oil-water mixed liquid discharge pipe that communicates between the lower part of the primary separation tank 11 and the suction side of the pump 7, and includes a filter 25 and a valve 15-1.

ポンプ7の吐出側には弁15−2を介して油水
分離機26に油水混合液を導入する油水混合液導
入管27と、弁15−4を介してオイルタンク2
8に浮上油を導入させる浮上油導入管29とが設
けらている。30は2次分離槽12に被処理水を
必要に応じて循環し再処理するため循環用導入管
で、弁15−6を備えている。31は油水分離機
26で強制分離された分離水の排水管で、弁32
を備え、この実施例ではバージ33の排水口34
に連絡されている。35は油水分離機26で強制
分離された、分離油の排油管で弁36を備えオイ
ルタンク28に連絡されている。37は2次分離
槽12に設けられたレベルスイツチである。
On the discharge side of the pump 7, there is an oil/water mixture inlet pipe 27 for introducing the oil/water mixture into the oil/water separator 26 via a valve 15-2, and an oil/water mixture inlet pipe 27 for introducing the oil/water mixture into the oil/water separator 26 via a valve 15-4.
8 is provided with a floating oil introduction pipe 29 through which floating oil is introduced. Reference numeral 30 denotes a circulation introduction pipe for circulating and reprocessing the water to be treated in the secondary separation tank 12 as needed, and is equipped with a valve 15-6. 31 is a drain pipe for separated water forcibly separated by the oil-water separator 26, and a valve 32
In this embodiment, the drain port 34 of the barge 33
has been contacted. Reference numeral 35 denotes a drain pipe for the separated oil that has been forcibly separated by the oil-water separator 26, and is equipped with a valve 36 and connected to the oil tank 28. 37 is a level switch provided in the secondary separation tank 12.

本実施例は上記のように構成されているもので
あり、次にその作用を説明する。
The present embodiment is constructed as described above, and its operation will be explained next.

まず、油タンカーのタンク洗浄水は導入管13
を通じて一旦1次分離槽11に導入され該分離槽
11内で浮上油2と油水混合液3に重力分離され
る。次に、1次分離用導入管14の弁15−8を
開いて1次分離槽11内の比較的油分の多い被処
理水を2次分離槽12に導入する。このとき大気
連通管18の弁15−7も開いておく。この被処
理水が第2図破線で示す位置まで導入されると弁
15−8は閉じられ、1次分離槽11の場合と同
様に重力分離される。この場合、2次分離槽12
内で分離された浮上油2bの厚さは1次分離槽1
1内の浮上油2aのそれより大きくなり、以後浮
上油2bの排出を後記するごとくより効率的に行
うことができる。
First, the oil tanker's tank cleaning water is supplied to the inlet pipe 13.
The oil is once introduced into the primary separation tank 11 through the separation tank 11, where it is separated by gravity into the floating oil 2 and the oil-water mixture 3. Next, the valve 15-8 of the primary separation introduction pipe 14 is opened to introduce the relatively oily water to be treated in the primary separation tank 11 into the secondary separation tank 12. At this time, the valve 15-7 of the atmosphere communication pipe 18 is also kept open. When this water to be treated is introduced to the position shown by the broken line in FIG. 2, the valve 15-8 is closed and the water is separated by gravity as in the case of the primary separation tank 11. In this case, the secondary separation tank 12
The thickness of the floating oil 2b separated in the primary separation tank 1
This becomes larger than that of the floating oil 2a in 1, and henceforth, the floating oil 2b can be discharged more efficiently as will be described later.

1次分離槽11及び2次分離槽12内の比較的
油分の少ない油水混合液3a,3bは弁15−
1,15−5及び15−2を開いたのちポンプ7
を作動させれば、それぞれサイホン管16及び油
水混合液排出管24を通じ、さらに共通の油水混
合液導入管27を経て油水分離機26に導入され
る。油水分離機26で強制分離された分離水すな
わち処理済みの水は次に弁32を開いて排水管3
1の排水口34より海水中へ放出され、分離油は
弁36を開いて排出管35を通じオイルタンク2
8内に回収される。
The oil/water mixed liquids 3a and 3b with relatively low oil content in the primary separation tank 11 and the secondary separation tank 12 are separated by a valve 15-.
After opening 1, 15-5 and 15-2, pump 7
When activated, the oil is introduced into the oil-water separator 26 through the siphon pipe 16 and the oil-water mixture discharge pipe 24, and further through the common oil-water mixture introduction pipe 27. The separated water, that is, the treated water forcibly separated by the oil-water separator 26, is then drained into the drain pipe 3 by opening the valve 32.
The separated oil is discharged into the seawater from the drain port 34 of No. 1, and the separated oil is discharged into the oil tank 2 through the discharge pipe 35 by opening the valve 36.
It will be collected within 8 days.

2次分離槽12内の油水混合液3bを上記のよ
うに排出しながら処理するに伴い、その分離面2
2が次第に下降する。そして分離面22がサイホ
ン管16の頂部16aの内部頂部16bに達する
と、ポンプ7は大気連通管18を通じて空気を吸
込むことになる。したがつて、2次分離槽12内
の浮上油2b及び油水混合液3bの降下はレベル
21の位置で停止し、それ以上下降しないと共に
ポンプ7による空気吸込みに感知して弁15−
1,15−5及び15−2が閉じ、一方弁15−
3及び15−4が開く。そして浮上油吸引口19
の弁20を開度を調整して開くと浮上油吸引口1
9とほぼ同一レベルにある2次分離槽12内の浮
上油2bを浮上油排出管23及び浮上油導入管2
9を通じオイルタンク28に回収することができ
る。この場合、浮上油2bが前述のごとく厚く形
成されているため、濃度の高い浮上油2bを効率
的に回収することができる。そしてポンプ7が空
気を吸込み始めると、同時に弁15−3及び15
−4は閉じ、逆に弁15−1,15−5及び15
−2が開いて上記の動作がくり返えされる。な
お、1次分離槽11内の油水混合液3aは油水混
合液排出管24及び循環用導入管30を通じて2
次分離槽12に導入して再処理したのち油水分離
機26にかけるようにしてもよい。
As the oil-water mixture 3b in the secondary separation tank 12 is discharged and treated as described above, the separation surface 2
2 gradually decreases. When the separation surface 22 reaches the inner top 16b of the top 16a of the siphon pipe 16, the pump 7 will suck air through the atmosphere communication pipe 18. Therefore, the descending of the floating oil 2b and the oil-water mixture 3b in the secondary separation tank 12 stops at the level 21 and does not descend any further, and upon sensing the air suction by the pump 7, the valve 15-
1, 15-5 and 15-2 are closed, and one-way valve 15-
3 and 15-4 open. And floating oil suction port 19
When the valve 20 is opened by adjusting the opening degree, the floating oil suction port 1 is opened.
9, the floating oil 2b in the secondary separation tank 12 is transferred to the floating oil discharge pipe 23 and the floating oil inlet pipe 2.
9 and can be collected in the oil tank 28. In this case, since the floating oil 2b is thick as described above, the floating oil 2b with a high concentration can be efficiently recovered. Then, when the pump 7 starts sucking air, the valves 15-3 and 15 simultaneously
-4 is closed, and conversely valves 15-1, 15-5 and 15
-2 is opened and the above operation is repeated. Note that the oil/water mixture 3a in the primary separation tank 11 is discharged through the oil/water mixture discharge pipe 24 and the circulation introduction pipe 30.
The oil may then be introduced into the separation tank 12 for reprocessing and then passed through the oil/water separator 26.

本発明において、セツトリングタンクを上記実
施例のように1次、2次の分離槽に区画する必要
は必ずしもないが、そうした方がより効果的に油
分の回収ができるものである。
In the present invention, it is not necessary to divide the settling tank into primary and secondary separation tanks as in the above embodiment, but oil can be recovered more effectively if this is done.

以上説明したように、本発明によれば、セツト
リングタンク内に導入された被処理水をサイホン
原理を応用してシステム的に油と水に分離処理す
ることができると共に効率が良く、またすべて配
管による構成であり、タンク内には油水の動揺を
常時受けるフロートやレベルスイツチのような故
障原因となるものが設けられていないためタンク
の動揺による故障を激減することができるもので
ある。
As explained above, according to the present invention, the water to be treated introduced into the settling tank can be systematically separated into oil and water by applying the siphon principle. It is constructed with piping, and there are no components in the tank that can cause failures, such as floats or level switches, which are constantly subject to the agitation of oil and water, so it is possible to drastically reduce failures due to agitation of the tank.

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

第1図は従来の油分回収装置の説明図、第2図
は本発明による一実施例を示す説明図、第3図は
第2図のA部の拡大詳細図である。 1:タンク、7:ポンプ、15−1,15−
5:弁、16:サイホン管、18:大気連通管、
19:浮上油吸引口、23:浮上油排出管。
FIG. 1 is an explanatory diagram of a conventional oil recovery device, FIG. 2 is an explanatory diagram showing an embodiment according to the present invention, and FIG. 3 is an enlarged detailed view of section A in FIG. 1: Tank, 7: Pump, 15-1, 15-
5: Valve, 16: Siphon pipe, 18: Atmospheric communication pipe,
19: Floating oil suction port, 23: Floating oil discharge pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 油水を重力分離するタンクと、排出側に弁及
びポンプを有し前記タンク内に設けられた逆U字
状のサイホン管と、該サイホン管の頂部に連結さ
れた大気連通管と、前記サイホン管の頂部とほぼ
同一レベルの位置において前記タンクの側壁に開
口せしめた浮上油吸引口と、該浮上油吸引口と前
記ポンプ間を弁を介して連結した浮上油排出管
と、前記ポンプが前記大気連通管または浮上油吸
引口からの空気を吸い込み始めたことを感知して
前記サイホン管の弁及び浮上油排出管の弁の開閉
を切替える手段とを備え、前記サイホン管の内部
頂点と前記浮上油吸引口の下部口縁とを同一レベ
ルに位置せしめたことを特徴とするセツトリング
タンク内の油分回収装置。
1. A tank that separates oil and water by gravity, an inverted U-shaped siphon pipe provided in the tank with a valve and a pump on the discharge side, an atmosphere communication pipe connected to the top of the siphon pipe, and the siphon. a floating oil suction port opened in the side wall of the tank at a position approximately at the same level as the top of the pipe; a floating oil discharge pipe connecting the floating oil suction port and the pump via a valve; means for detecting that air has started to be sucked in from the atmosphere communication pipe or the floating oil suction port and switching the opening and closing of the valve of the siphon pipe and the valve of the floating oil discharge pipe, the internal apex of the siphon pipe and the floating oil An oil recovery device in a settling tank, characterized in that the lower lip of the oil suction port is located at the same level.
JP58217769A 1983-11-21 1983-11-21 Oil recovery device in settling tank Granted JPS60110684A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58217769A JPS60110684A (en) 1983-11-21 1983-11-21 Oil recovery device in settling tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58217769A JPS60110684A (en) 1983-11-21 1983-11-21 Oil recovery device in settling tank

Publications (2)

Publication Number Publication Date
JPS60110684A JPS60110684A (en) 1985-06-17
JPH0148076B2 true JPH0148076B2 (en) 1989-10-17

Family

ID=16709441

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58217769A Granted JPS60110684A (en) 1983-11-21 1983-11-21 Oil recovery device in settling tank

Country Status (1)

Country Link
JP (1) JPS60110684A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0339879U (en) * 1989-08-30 1991-04-17

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0722651B2 (en) * 1990-06-20 1995-03-15 ゼオテック・エル・アール・シー株式会社 Oil-water separation device and oil-water separation method
JP2013223832A (en) * 2012-04-20 2013-10-31 Mikasa Kankyo Service:Kk Separation tank

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59110005U (en) * 1983-01-14 1984-07-25 大東工業株式会社 oil/water separator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0339879U (en) * 1989-08-30 1991-04-17

Also Published As

Publication number Publication date
JPS60110684A (en) 1985-06-17

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