JPH04338201A - Method and equipment for disintegration treatment of emulsion oil - Google Patents

Method and equipment for disintegration treatment of emulsion oil

Info

Publication number
JPH04338201A
JPH04338201A JP13972991A JP13972991A JPH04338201A JP H04338201 A JPH04338201 A JP H04338201A JP 13972991 A JP13972991 A JP 13972991A JP 13972991 A JP13972991 A JP 13972991A JP H04338201 A JPH04338201 A JP H04338201A
Authority
JP
Japan
Prior art keywords
oil
tank
water
emulsion
pipe
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
JP13972991A
Other languages
Japanese (ja)
Inventor
Hiroshi Ueda
上田 博司
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.)
UEDA SERBO KIKAI KK
Original Assignee
UEDA SERBO KIKAI KK
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 UEDA SERBO KIKAI KK filed Critical UEDA SERBO KIKAI KK
Priority to JP13972991A priority Critical patent/JPH04338201A/en
Publication of JPH04338201A publication Critical patent/JPH04338201A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To efficietly separate emulsion oil into a water component and an oil component. CONSTITUTION:Emulsion oil 17 stored in an emulsion oil tank 4 is supplied to a heat exchanger 5 in a water tank 1 heated to a proper temperature through the first piping 7 and heated, and at the same time a pressure adjusting valve 15 arranged in the second piping 9 connected to the line outlet of the heat exchanger 5 adjusts pressure in the piping to pressurize the emulsion oil 17 flowing through the line. By the heating and pressurizing, the emulsion oil 17 is forcibly separated into a water component and an oil component to make it flow in an oil reservoir 8.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明はメッキ工程や精密部品の
洗浄工程、焼き入れ工程等の金属加工において使用され
る切削油や潤滑油、ギヤーオイル或いはマシン油などの
使用済の油を分解処理する方法と、その方法を実施する
ための装置に関するものである。
[Industrial Application Field] The present invention decomposes used oils such as cutting oils, lubricating oils, gear oils, and machine oils used in metal processing such as plating processes, precision parts cleaning processes, and hardening processes. The present invention relates to a method for carrying out the method and an apparatus for carrying out the method.

【0002】0002

【従来の技術】上記のような使用済の油の大半は乳化油
、即ちエマルジョン油として回収されているが、このよ
うなエマルジョン油を分離収集するには、従来から遠心
分離機や濾過機などを使用して機械的に行う方法や、乳
化破壊剤(エマルジョンブレーカ)を混入して分離させ
る方法、或いは、比重差を利用して槽内で油分を浮上さ
せる方法などが採用されている。
[Prior Art] Most of the used oil mentioned above is recovered as emulsion oil, but in order to separate and collect such emulsion oil, conventional methods such as centrifuges and filters have been used. The methods used include a mechanical method using an emulsion breaker, a method of mixing an emulsion breaker to separate the oil, and a method of floating the oil in a tank using a difference in specific gravity.

【0003】0003

【発明が解決しようとする課題】しかしながら、上記の
機械的分離方法によれば、分離処理に時間が掛かる上に
確実な分離収集ができないものであり、さらに、乳化破
壊剤を混入する方法においても時間の経過を待たなけれ
ばならなく、そのメインテナンスが煩わしいものである
。又、比重差による方法では乳化破壊剤の使用と同様に
自然的に分離させているために多くの処理時間を必要と
する上にエマルジョン油から油分のみを確実に分離させ
ることが困難である等の問題点を有する。
[Problems to be Solved by the Invention] However, according to the above-mentioned mechanical separation method, separation processing takes time and reliable separation and collection is not possible. The maintenance is troublesome as one has to wait for the passage of time. In addition, the method based on specific gravity difference requires a lot of processing time because the oil is separated naturally like using a demulsifier, and it is difficult to reliably separate only the oil from the emulsion oil. It has the following problems.

【0004】本発明は、エマルジョン油は熱が高くなれ
ばなる程、また圧力を加えるとその結合が急速に分離さ
れることを見出し、この点に着目してエマルジョン油か
ら油分を能率よく且つ確実に分離、回収し得るエマルジ
ョン油の分解処理方法とその方法の実施に使用する装置
の提供を目的とするものである。
The present invention has discovered that the higher the heat and the more pressure is applied to emulsion oil, the more rapidly the bonds are separated. Focusing on this point, the present invention efficiently and reliably removes oil from emulsion oil. The object of the present invention is to provide a method for decomposing emulsion oil that can be separated and recovered, and an apparatus used to carry out the method.

【0005】[0005]

【課題を解決るための手段】上記目的を達成するために
、本発明のエマルジョン油の分解処理方法は、槽内のエ
マルジョン油を配管内を通じて加圧しながら加熱するこ
とにより油分と水分とを強制的に分離させ、油溜槽に導
出して該槽内で分離層を形成させることを特徴とするも
のである。
[Means for Solving the Problems] In order to achieve the above object, the emulsion oil decomposition treatment method of the present invention forcibly removes oil and moisture by heating the emulsion oil in a tank while pressurizing it through piping. This method is characterized in that the oil is separated from the oil, and then led to an oil storage tank to form a separated layer within the tank.

【0006】又、この方法を実施するための装置として
は、適宜な温度に加熱される水槽内にエマルジョン油を
収容した乳化油槽と熱交換器を配設すると共に、該水槽
外に油溜槽を設け、乳化油槽と熱交換器、および熱交換
器と油溜槽間を、それぞれ送液ポンプを有する第1配管
、および圧力調整バルブを有する第2配管を通じて連通
させ、前記油溜槽に水分排出管と油分排出管とを接続し
てなる構造を有しているものである。そして、この装置
において、上記水槽外に乳化破壊剤槽を配設して該槽内
の乳化破壊剤を上記乳化油槽内に供給するように構成し
ているものである。
[0006] Furthermore, as an apparatus for implementing this method, an emulsified oil tank containing emulsion oil and a heat exchanger are arranged in a water tank heated to an appropriate temperature, and an oil storage tank is provided outside the water tank. The emulsified oil tank and the heat exchanger, and the heat exchanger and the oil sump tank are connected through a first pipe having a liquid feed pump and a second pipe having a pressure regulating valve, respectively, and a moisture discharge pipe and a water discharge pipe are connected to the oil sump tank. It has a structure in which it is connected to an oil discharge pipe. In this apparatus, a demulsifier tank is provided outside the water tank, and the demulsifier in the tank is supplied into the emulsified oil tank.

【0007】[0007]

【作用】乳化油槽内に収容しているエマルジョン油を配
管を通じて熱交換器に供給することによって加熱すると
共に圧力調整バルブにより配管中を流動するエマルジョ
ン油を一定の圧力に加圧すると、該エマルジョン油中の
油の分子と水の分子とが急速に分離することになる。こ
のような物理的分離処理を行ったエマルジョン油を油溜
槽内に流出させると、該槽内において直ちに油層と水層
とに分離する。
[Operation] The emulsion oil stored in the emulsified oil tank is heated by being supplied to the heat exchanger through the piping, and the emulsion oil flowing in the piping is pressurized to a constant pressure by the pressure adjustment valve. The oil molecules and water molecules therein will rapidly separate. When the emulsion oil subjected to such physical separation treatment is discharged into an oil storage tank, it immediately separates into an oil layer and a water layer in the tank.

【0008】この際、水層には上記操作によって分離で
きない油質の油分が存在している場合があり、この場合
には、油溜槽内の分離水層を再び乳化油槽内に戻すと共
に該槽内に乳化破壊剤を供給し、上記管路を通じて油分
と水分とに分離、回収するものである。
[0008] At this time, the aqueous layer may contain oil that cannot be separated by the above operation, and in this case, the separated aqueous layer in the oil reservoir tank is returned to the emulsified oil tank and the tank is A demulsifying agent is supplied into the tank, and is separated into oil and water and recovered through the pipe.

【0009】[0009]

【実施例】次に、本発明の実施例を図面について説明す
ると、1は水槽であって、その内底部に加熱用ヒータ2
を配設してあり、このヒータ2は槽外に設けた制御盤(
図示せず)によって適宜な温度に自動調整されるように
なっている。又、水槽1内にはエマルジョン油3を収容
する乳化油槽4と熱交換器5とが配設されてあり、乳化
油槽4の底部と熱交換器5の管路入口とを送液ポンプ6
を備えている第1配管7によって連結、連通してある。
[Embodiment] Next, an embodiment of the present invention will be explained with reference to the drawings. 1 is a water tank, and a heater 2 is installed at the inner bottom of the tank.
This heater 2 is connected to a control panel (
(not shown) to automatically adjust the temperature to an appropriate temperature. Furthermore, an emulsified oil tank 4 containing an emulsion oil 3 and a heat exchanger 5 are arranged in the water tank 1, and a liquid sending pump 6 connects the bottom of the emulsified oil tank 4 and the pipe inlet of the heat exchanger 5.
They are connected and communicated by a first pipe 7 provided with.

【0010】8は水槽1の外部適所に配設した油溜槽で
、その上端部と前記熱交換器5の管路出口とを第2配管
9を通じて連結、連通してあり、その底面と下端部とに
バルブ10、11を有する水分取出管12と油分取出管
13とを夫々接続していると共に、前記第2配管9に圧
力メータ14と圧力調整バルブ15とを設けてある。
Reference numeral 8 denotes an oil storage tank disposed at a suitable location outside the water tank 1. Its upper end and the pipe outlet of the heat exchanger 5 are connected and communicated through a second pipe 9, and its bottom and lower end A water extraction pipe 12 and an oil extraction pipe 13 having valves 10 and 11 are respectively connected to the second pipe 9, and a pressure meter 14 and a pressure regulating valve 15 are provided in the second pipe 9.

【0011】16は水槽外の適所に設置した乳化破壊剤
(エマルジョンブレーカ)17を収容している液剤槽で
、乳化破壊剤添加用定量ポンプ18を有する供給管19
を通じて前記乳化油槽4に連通してある。この連通構造
は、該供給管19の一端開口部を液剤槽16の内底部に
まで没入させていると共に他端開口部を乳化油槽4内の
内底部に開口している前記第1配管7の開口端に臨ませ
てある。20は水分取出管12に接続したバルブ21並
びに戻しポンプ22を備えた戻し管で、前記乳化油槽4
に連通させてあるが、必ずしも設けておく必要はない。
Reference numeral 16 denotes a liquid tank containing a demulsifier (emulsion breaker) 17 installed at a suitable location outside the water tank, and a supply pipe 19 having a metering pump 18 for adding the demulsifier.
It communicates with the emulsified oil tank 4 through the emulsified oil tank 4. This communication structure includes the first pipe 7, which has one end opening of the supply pipe 19 immersed in the inner bottom of the liquid agent tank 16, and the other end opening of the first pipe 7, which opens into the inner bottom of the emulsified oil tank 4. It is facing the open end. 20 is a return pipe equipped with a valve 21 and a return pump 22 connected to the water extraction pipe 12, and is connected to the emulsified oil tank 4.
It is not necessary to provide this connection.

【0012】このように構成したエマルジョン分解処理
装置を使用してエマルジョン油を水分と油分とに分解す
るには、まず、処理しようとするエマルジョン油を乳化
油槽4内に収容すると共に、水槽1内に乳化油槽4の上
端部近傍に達して熱交換器5が没入する深さまで水23
を入れたのち、ヒータ2のスイッチを入れると共に温度
調整を行って槽内の水23を80℃位の温度に保持する
In order to decompose emulsion oil into water and oil using the emulsion decomposition treatment apparatus constructed as described above, first, the emulsion oil to be treated is stored in the emulsified oil tank 4, and the water tank 1 is The water 23 reaches a depth near the upper end of the emulsified oil tank 4 and the heat exchanger 5 is immersed therein.
After that, the heater 2 is turned on and the temperature is adjusted to maintain the water 23 in the tank at a temperature of about 80°C.

【0013】この状態にして送液ポンプ6を作動させる
と、乳化油槽4内のエマルジョン油3は第1配管7を通
じて熱交換器5に圧送されて加熱され、該熱交換器5を
通じて第2配管9に流出する。この時、該第2配管9に
配設している圧力調整バルブ15により、配管内の圧力
が9kg/cm2=以上、好ましくは9kg/cm2=
〜12kg/cm2=に調整し、配管内を流通するエマ
ルジョン油を加圧する。
When the liquid sending pump 6 is operated in this state, the emulsion oil 3 in the emulsified oil tank 4 is pumped through the first pipe 7 to the heat exchanger 5 and heated, and then passed through the heat exchanger 5 to the second pipe. It leaks to 9th. At this time, the pressure within the pipe is controlled by the pressure regulating valve 15 disposed in the second pipe 9 to be equal to or higher than 9 kg/cm2, preferably 9 kg/cm2.
The emulsion oil flowing through the piping is pressurized by adjusting the pressure to ~12 kg/cm2.

【0014】従って、熱交換器5内を流通するエマルジ
ョン油3は、上記加熱と加圧によって水の分子と油の分
子との分離作用が加速され、第1配管7から第2配管9
を流動中に急速に分離させられて油溜槽8に流出する。
Therefore, in the emulsion oil 3 flowing through the heat exchanger 5, the separation action between water molecules and oil molecules is accelerated by the above heating and pressurization, and the emulsion oil 3 flows from the first pipe 7 to the second pipe 9.
The oil is rapidly separated during the flow and flows into the oil storage tank 8.

【0015】油溜槽8に流出すると、上記水の分子と油
の分子とに分離させられたエマルジョン油は、直ちに、
水分と油分とに分離集合し、上層部が油層24に、下層
部が水層25となる。この水層25をバルブ10の開放
によって取出管12を通じて油溜槽8から排出したのち
、油層24をバルブ11の開放によって取出管13を通
じて回収するものである。
[0015] When the emulsion oil flows into the oil storage tank 8, the emulsion oil separated into water molecules and oil molecules immediately
Water and oil are separated and aggregated, and the upper layer becomes an oil layer 24 and the lower layer becomes an aqueous layer 25. After this water layer 25 is discharged from the oil reservoir tank 8 through the take-out pipe 12 by opening the valve 10, the oil layer 24 is recovered through the take-out pipe 13 by opening the valve 11.

【0016】一方、エマルジョン油によっては、上記加
熱、加圧による物理的な方法では水分と油分とに分離で
きない油質のものがあり、その油分が水層25内に混入
した状態となる。この場合には、バルブ10、21を開
放させることにより、戻し管20を通じて該水層25を
乳化油槽4に再び戻す。なお、戻し管20を設けること
なく、水分取出管12から排出された油混入水分を適宜
な容器に収容し、これを乳化油槽4に投入してもよい。
On the other hand, some emulsion oils cannot be separated into water and oil by the physical method of heating and pressurizing, and the oil is mixed into the water layer 25. In this case, the water layer 25 is returned to the emulsified oil tank 4 through the return pipe 20 by opening the valves 10 and 21. Note that, without providing the return pipe 20, the oil-containing water discharged from the water extraction pipe 12 may be stored in a suitable container and then introduced into the emulsified oil tank 4.

【0017】そして、熱交換器5の温度並びに圧力調整
バルブ15による圧力を上記の条件に維持した状態で、
定量ポンプ18を作動させ、液剤槽16内の乳化破壊剤
17を供給管19を通じて一定量宛、乳化油槽4の内底
部に供給すると、該乳化破壊剤17は第1配管7の吸い
込み口に臨んでいるため、送液ポンプ6の作動による吸
引力で乳化油槽4内のエマルジョン油3に攪拌混合され
ながら第1配管7に吸入される。乳化破壊剤17として
は、商品名ネオデマルジョンS、又はネオデマルジョン
U(株式会社永井表面技術研究所製)が使用され、この
乳化破壊剤を使用した場合にはその添加量は3%以下で
充分である。
Then, while maintaining the temperature of the heat exchanger 5 and the pressure by the pressure regulating valve 15 under the above conditions,
When the metering pump 18 is operated and a fixed amount of the demulsifying agent 17 in the liquid agent tank 16 is supplied to the inner bottom of the emulsified oil tank 4 through the supply pipe 19, the demulsifying agent 17 faces the suction port of the first pipe 7. Therefore, the liquid is sucked into the first pipe 7 while being stirred and mixed with the emulsion oil 3 in the emulsified oil tank 4 by the suction force generated by the operation of the liquid feeding pump 6. As the demulsifier 17, the trade name Neodemulsion S or Neodemulsion U (manufactured by Nagai Surface Technology Laboratory Co., Ltd.) is used, and when this demulsifier is used, the amount added is 3% or less. is sufficient.

【0018】この第1配管7から熱交換器5を通じて第
2配管9を流通中に上記同様に加熱、加圧作用を受けて
水の分子と油の分子とに分離させられると共に乳化破壊
剤17によって物理的に分離できない油分が化学的に分
離され、油溜槽8内に流出して上記同様に油層24と水
層25に分離する。以下、該水層25を再び乳化油槽4
に供給し、上記同様に乳化破壊剤17の添加によってエ
マルジョンを破壊させ、この工程を数回、繰り返し行っ
て完全に油分と水分とに分離させた状態にし、取出管1
2、13を開放して夫々回収するものである。
While flowing through the second pipe 9 from the first pipe 7 through the heat exchanger 5, it is heated and pressurized in the same manner as described above to be separated into water molecules and oil molecules, and the demulsifier 17 The oil that cannot be physically separated is chemically separated, flows into the oil reservoir tank 8, and is separated into an oil layer 24 and a water layer 25 in the same manner as described above. Thereafter, the aqueous layer 25 is redistributed into the emulsified oil tank 4.
The emulsion is broken by adding the demulsifying agent 17 in the same manner as above, and this step is repeated several times to completely separate the oil and water.
2 and 13 are opened and collected respectively.

【0019】なお、エマルジョン油を上記のように、加
熱、加圧による水分と油分との物理的操作によって完全
に分離可能な油質のものであれば、乳化破壊剤17の添
加は不必要となるものであり、又、乳化破壊剤17を初
めから使用して上記装置により分離処理を行うことも可
能である。
[0019] If the emulsion oil is of an oil quality that can be completely separated by physical manipulation of water and oil by heating and pressurizing, the addition of the demulsifier 17 is unnecessary. It is also possible to use the demulsifier 17 from the beginning and perform the separation process with the above apparatus.

【0020】[0020]

【発明の効果】以上のように本発明によれば、槽内のエ
マルジョン油を配管内を通じて加圧しながら加熱するこ
とにより油分と水分とを強制的に分離させ、油溜槽に導
出して該槽内で分離層を形成させるものであるから、エ
マルジョン油が配管内を通過中に加熱、加圧によって水
分と油分とに急速に分解してその分離処理を短時間で能
力よく行うことができ、大量のエマルジョン油であって
も、容器内に貯溜させておくことなく、小規模な装置に
よって容易に且つ実に分離処理が可能となって、油分の
回収が効率よく行えるものである。
As described above, according to the present invention, the emulsion oil in the tank is heated while being pressurized through the piping to forcibly separate oil and water, and the oil and water are led out to the oil storage tank. Since a separation layer is formed inside the piping, the emulsion oil is rapidly decomposed into water and oil by heating and pressurization while passing through the piping, and the separation process can be performed efficiently in a short time. Even a large amount of emulsion oil can be easily and effectively separated using a small-scale device without being stored in a container, and the oil can be efficiently recovered.

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

【図1】エマルジョン分解装置の簡略縦断側面図。FIG. 1 is a simplified longitudinal sectional side view of an emulsion decomposition device.

【符号の説明】[Explanation of symbols]

1  水槽 2  ヒータ 3  エマルジョン油 4  乳化油槽 5  熱交換器 6  送液ポンプ 7  第1配管 8  油溜槽 9  第2配管 15  圧力調整バルブ 16  液剤槽 17  乳化破壊剤 1 Aquarium 2 Heater 3 Emulsion oil 4 Emulsified oil tank 5 Heat exchanger 6 Liquid pump 7 First piping 8 Oil storage tank 9 Second piping 15 Pressure adjustment valve 16 Liquid agent tank 17 Demulsifier

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】  槽内のエマルジョン油を配管内を通じ
て加圧しながら加熱することにより油分と水分とを強制
的に分離させ、油溜槽に導出して該槽内で分離層を形成
させることを特徴とするエマルジョン油の分離処理方法
[Claim 1] The emulsion oil in the tank is heated while being pressurized through piping to forcibly separate oil and water, and the oil and water are forcibly separated, and the oil and water are led out to an oil storage tank and a separated layer is formed in the tank. A method for separating emulsion oil.
【請求項2】  適宜な温度に加熱される水槽内にエマ
ルジョン油を収容した乳化油槽と熱交換器を配設すると
共に、該水槽外に油溜槽を設け、乳化油槽と熱交換器、
および熱交換器と油溜槽間を、それぞれ送液ポンプを有
する第1配管、および圧力調整バルブを有する第2配管
を通じて連通させ、前記油溜槽に水分排出管と油分排出
管とを接続していることを特徴とするエマルジョン油の
分解処理装置。
2. An emulsified oil tank containing emulsion oil and a heat exchanger are arranged in a water tank heated to an appropriate temperature, and an oil storage tank is provided outside the water tank, the emulsified oil tank and the heat exchanger,
The heat exchanger and the oil reservoir are communicated through a first pipe having a liquid pump and a second pipe having a pressure regulating valve, respectively, and a water discharge pipe and an oil discharge pipe are connected to the oil reservoir. An emulsion oil decomposition treatment device characterized by:
【請求項3】  水槽外に乳化破壊剤槽を配設して該槽
内の乳化破壊剤を上記乳化油槽内に供給するように構成
している請求項2記載のエマルジョン油の分解処理装置
3. The emulsion oil decomposition treatment apparatus according to claim 2, further comprising a demulsifier tank disposed outside the water tank, and the demulsifier in the tank is supplied into the emulsified oil tank.
JP13972991A 1991-05-14 1991-05-14 Method and equipment for disintegration treatment of emulsion oil Pending JPH04338201A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13972991A JPH04338201A (en) 1991-05-14 1991-05-14 Method and equipment for disintegration treatment of emulsion oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13972991A JPH04338201A (en) 1991-05-14 1991-05-14 Method and equipment for disintegration treatment of emulsion oil

Publications (1)

Publication Number Publication Date
JPH04338201A true JPH04338201A (en) 1992-11-25

Family

ID=15252033

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13972991A Pending JPH04338201A (en) 1991-05-14 1991-05-14 Method and equipment for disintegration treatment of emulsion oil

Country Status (1)

Country Link
JP (1) JPH04338201A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50649A (en) * 1973-05-08 1975-01-07
JPH0263503A (en) * 1988-07-11 1990-03-02 Henkel Kgaa Demulsifying method

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50649A (en) * 1973-05-08 1975-01-07
JPH0263503A (en) * 1988-07-11 1990-03-02 Henkel Kgaa Demulsifying method

Similar Documents

Publication Publication Date Title
JPH07507003A (en) Oil tank cleaning method and device
US4686049A (en) Method and apparatus for reprocessing aqueous, oily and greasy cleaning solutions
US3716480A (en) Method and apparatus for cleaning solids coated with oil
MX2007014366A (en) Oil-based sludge separation and treatment system.
CN105001906B (en) Device and method for removing water and metal salt in crude oil
CN105087057A (en) Device and method for removing water soluble salt in crude oil
US3896828A (en) Treatment of pickle liquor rinse water
SE532313C2 (en) Method and apparatus for purifying so-called debris oil
US2025570A (en) Filtering apparatus
DE1266267C2 (en) Method and device for removing oily deposits from the inner surfaces of container walls by washing the walls with a cleaning fluid
US5965029A (en) System and method for treating an oil gas well stream
JPH04338201A (en) Method and equipment for disintegration treatment of emulsion oil
US8834724B1 (en) Method and apparatus for separation of fluids by means of induced gas flotation and advances in said technology
DE2330200B2 (en) PROCESS AND DEVICE FOR SEPARATING OIL OR FLOATING PARTICLES FROM EMULSIONS OR DISPERSIONS
US8101071B2 (en) Oil removal reclamation clarifier system and process for use
US8192631B1 (en) Fluid treatment device and method
EP3560572A1 (en) Degassing system and method for carrying out a degasification process of a liquid and drinks treatment machine
US1152769A (en) Apparatus for treating solid-bearing solutions.
US4705755A (en) Apparatus for collecting lysozyme from egg white by adsorption
US1186510A (en) Method of and apparatus for handling and treating rendering-tank residuum.
JPH0716576A (en) Cleaning device of waste washing water for processed part or the like
JP2018161600A (en) Waste liquid reducing equipment and method for reducing oil waste liquid
JPH06154772A (en) Separating device for water-bloom and the like
US20240083795A1 (en) Apparatus and process for mineralizing drinking water using a vertical manifold
RU2290979C1 (en) Method for extraction of plant material and apparatus for performing the same