JPH0931486A - Purification of rolling oil - Google Patents

Purification of rolling oil

Info

Publication number
JPH0931486A
JPH0931486A JP7206755A JP20675595A JPH0931486A JP H0931486 A JPH0931486 A JP H0931486A JP 7206755 A JP7206755 A JP 7206755A JP 20675595 A JP20675595 A JP 20675595A JP H0931486 A JPH0931486 A JP H0931486A
Authority
JP
Japan
Prior art keywords
rolling oil
rolling
floating
oil
treating
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
JP7206755A
Other languages
Japanese (ja)
Inventor
Seiichiro Takahashi
聖一郎 高橋
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.)
Mitsubishi Kakoki Kaisha Ltd
Original Assignee
Mitsubishi Kakoki Kaisha 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 Mitsubishi Kakoki Kaisha Ltd filed Critical Mitsubishi Kakoki Kaisha Ltd
Priority to JP7206755A priority Critical patent/JPH0931486A/en
Publication of JPH0931486A publication Critical patent/JPH0931486A/en
Pending legal-status Critical Current

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  • Filtration Of Liquid (AREA)
  • Lubricants (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for purifying a rolling oil, by treating a rolling oil discharged from a metal rolling equipment, containing foreign matters such as fine metal powder, scum and a hydraulic fluid, etc. and efficiently removing the foreign matters to purify the rolling oil into one having required rolling performances. SOLUTION: In treating an emulsion type rolling oil discharged from a metal rolling equipment containing foreign matters, removing the foreign matters and recycling and using the purified rolling oil, the rolling oil is purified by passing through the processes shown below. (1) A floating and separating process for treating the rolling oil occurring from the rolling equipment by a floating and separating means to separate a floating substance consisting essentially of a working fluid and scum. (2) A centrifugal separation process for treating the floating substance, obtained by the floating and separating process, by a centrifugal separator to separate the sludge component and a liquid phase component. (3) A filtering process for treating the rolling oil flowing out from the floating and separating process by a filtering means to separate and remove a solid content such as metal powder, etc., in the rolling oil.

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、圧延油の浄化方法に関
し、さらに詳しくは、エマルジョン型圧延油中の各種異
物を除去して浄化する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying rolling oil, and more particularly to a method for purifying by removing various foreign matters in emulsion rolling oil.

【0002】[0002]

【従来の技術】金属の薄板圧延用あるいは製缶用の圧延
油としては、主にエマルジョン型圧延油が用いられる。
本発明でいうエマルジョン型圧延油とは、油を乳化剤や
その他の物質で、水中に分散した懸濁液に、油性向上
剤,酸化防止剤等を添加配合した1〜20%の水中油型
エマルジョン液を意味する(以下,圧延油という)。こ
の圧延油には、圧延の際に発生する金属の微粉,圧延油
中に添加されている前記各種の有機化合物が経時的に酸
化等して生ずるスカム分及び圧延設備で使用される作動
油等の各種異物が混入している。
2. Description of the Related Art Emulsion type rolling oil is mainly used as rolling oil for rolling thin metal sheets or for making cans.
The emulsion type rolling oil referred to in the present invention is a 1 to 20% oil-in-water emulsion obtained by adding and blending an oiliness improver, an antioxidant and the like to a suspension prepared by dispersing oil in water with an emulsifier or other substance. It means liquid (hereinafter referred to as rolling oil). The rolling oil includes fine metal powder generated during rolling, scum content produced by the various organic compounds added to the rolling oil over time, and hydraulic oil used in rolling equipment. Various foreign substances are mixed.

【0003】そして、この圧延油は使用量が多量であ
り、且つ高価であるため、クローズドシステムで循環し
て使用される。従って、上記の異物は常時除去しない
と、含有量が徐々に増加し、圧延油としての性能が低下
し、さらには圧延製品の表面欠陥等、圧延工程に悪い影
響を与える。この異物の除去方法に関しては、いくつか
の方法が現在まで提案されているが、その代表的な方法
としては、特公平4−64723号で提案された方法を
あげることができる。
Since this rolling oil is used in a large amount and is expensive, it is circulated and used in a closed system. Therefore, if the above-mentioned foreign matter is not always removed, the content gradually increases, the performance as rolling oil deteriorates, and further it has a bad influence on the rolling process such as surface defects of rolled products. Several methods have been proposed to date for removing the foreign matter, and a representative method thereof is the method proposed in Japanese Examined Patent Publication No. 4-64723.

【0004】上記の方法の要旨は、大略次の通りであ
る。すなわち、圧延設備から戻ってくる圧延油を浮上分
離処理して、浮上する作動油、スカム分等の比重の軽い
浮上物質を遠心分離機で処理して、重質側に主に金属粉
とスラッジの混合物を、軽質側に主に作動油等を、それ
ぞれ分離して回収する。一方浮上分離槽の下層部から抜
き出される、比重の軽い物質が除去された圧延油は、別
の遠心分離機で処理されて、金属粉及びスラッジが分離
除去され、浄化された圧延油として圧延設備に循環供給
する方法である。
The summary of the above method is as follows. That is, the rolling oil returned from the rolling equipment is separated by flotation, and the floating material with a low specific gravity, such as floating hydraulic oil and scum, is treated with a centrifuge, and mainly metal powder and sludge are added to the heavy side. The working oil and the like are separated and collected on the light side of the mixture. On the other hand, the rolling oil extracted from the lower layer of the flotation tank, from which the substance with a low specific gravity is removed, is processed by another centrifuge to separate and remove metal powder and sludge, and then rolled as purified rolling oil. This is a method of circulating supply to equipment.

【0005】本出願人は、上記の特公平4−64723
号で提案された方法を鋭意検討した結果、この方法には
次のような問題があることが分かった。すなわち、上記
方法においては、浮上分離槽で浮上物質が分離除去され
た圧延油は、その全量が遠心分離機で処理されるが、微
粒の金属粉を除去するため、高速回転による高い加速度
(G)のもとで処理されるため、圧延油中のエマルジョ
ン粒子は、この高いGによる圧力の作用を受けて破壊
し、圧延油としての必要な性能が低下することである。
The applicant of the present invention has the above-mentioned Japanese Patent Publication No. 4-64723.
As a result of diligent examination of the method proposed in the issue, it was found that this method has the following problems. That is, in the above method, the rolling oil from which the floating substances have been separated and removed in the flotation tank is entirely processed by the centrifuge, but since the fine metal powder is removed, a high acceleration (G ), The emulsion particles in the rolling oil are broken under the action of this high G pressure, and the performance required as the rolling oil is reduced.

【0006】[0006]

【発明が解決しようとする課題】本発明は、以上の従来
技術の問題点に鑑みて成されたものであって、金属微
粉,スカム分及び作動油等の異物を含有する金属圧延設
備から発生する圧延油を処理して、前記異物を効率よく
除去して必要な圧延性能を保持した圧延油として浄化す
る方法を提供することを課題とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems of the prior art, and is generated from a metal rolling facility containing fine particles of metal, scum, and foreign matter such as hydraulic oil. It is an object of the present invention to provide a method of treating a rolling oil to remove the foreign matter efficiently and purifying the rolling oil as a rolling oil having a required rolling performance.

【0007】[0007]

【課題を解決するための手段】金属粉,作動油及びスカ
ム分等の異物を含有する金属圧延設備から発生するエマ
ルジョン型圧延油を処理し、前記異物を除去して循環使
用するに際して、次の工程から構成されることを特徴と
する圧延油の浄化方法。 (1) 圧延設備から発生する圧延油を浮上分離手段で処理
して作動油及びスカム分を主とする浮上物質を分離する
浮上分離工程。 (2) 前記浮上分離工程で得られた浮上物質を遠心分離機
で処理してスラッジ分と液相分とに分離する遠心分離工
程。 (3) 前記浮上分離工程から流出する圧延油を濾過手段で
処理して圧延油中の金属粉等の固形分を分離除去する濾
過工程。
[Means for Solving the Problems] When emulsion type rolling oil generated from metal rolling equipment containing foreign matter such as metal powder, hydraulic oil and scum content is treated, and the foreign matter is removed and recycled, A method for purifying rolling oil, comprising a process. (1) A flotation separation step in which rolling oil generated from rolling equipment is treated by a flotation separation means to separate hydraulic oil and a floating substance mainly composed of scum. (2) A centrifugal separation step of treating the floating substance obtained in the floating separation step with a centrifuge to separate it into a sludge component and a liquid phase component. (3) A filtration step of treating the rolling oil flowing out from the floating separation step with a filtering means to separate and remove solid contents such as metal powder in the rolling oil.

【0008】[0008]

【作用】金属粉、作動油及びスカム分等の異物を含有す
るエマルジョン型圧延油は、最初に浮上分離処理され、
作動油及びスカム分等の比重の軽い成分が除去される。
この際、金属微粉の一部もスカム分に付着して浮上物質
として除去される。次いで圧延油は濾過処理され、主に
金属微粉等の固形分が濾材上に捕捉されて除去される。
以上のようにエマルジョン型圧延油中の各種異物を、そ
れぞれの性状に適した分離除去手段を最適に組み合わせ
た方法で処理することにより、エマルジョン粒子を破壊
することなく、圧延油を浄化できる。
[Function] The emulsion type rolling oil containing foreign matter such as metal powder, hydraulic oil and scum is first subjected to floating separation treatment,
Components with low specific gravity such as hydraulic oil and scum are removed.
At this time, part of the metal fine powder also adheres to the scum and is removed as a floating material. Next, the rolling oil is subjected to a filtration treatment, and solid components such as fine metal powder are mainly captured and removed on the filter medium.
As described above, by treating various foreign substances in the emulsion type rolling oil by a method in which the separating and removing means suitable for each property is optimally combined, the rolling oil can be purified without destroying the emulsion particles.

【0009】[0009]

【実施例】本発明の実施例について、図面に基づいて説
明する。図1は、本発明の実施例の系統図である。図に
おいて、1はアルミ,ステンレス等の薄板圧延機あるい
は製缶機等からなる圧延設備である。2は圧延機等で使
用された圧延設備から発生する圧延油(以下,ダーティ
圧延油という)の戻り管路であり、その下流端はダーテ
ィ油タンク3に接続している。このダーティ圧延油に
は、圧延時に発生する金属微粉,圧延機で使用されて混
入してくる作動油,圧延油に添加される各種の有機化合
物が酸化等して生じるスカム分等が異物として含有され
る。
Embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a system diagram of an embodiment of the present invention. In the figure, reference numeral 1 denotes a rolling facility including a thin plate rolling machine made of aluminum, stainless steel or the like or a can making machine. Reference numeral 2 is a return line for rolling oil (hereinafter referred to as dirty rolling oil) generated from rolling equipment used in a rolling mill or the like, and its downstream end is connected to a dirty oil tank 3. This dirty rolling oil contains fine particles of metal generated during rolling, hydraulic oil used in a rolling mill and mixed in, and scum generated by oxidation of various organic compounds added to rolling oil as foreign matter. To be done.

【0010】ダーティ油タンク3中の圧延油は、次いで
浮上分離槽4に流入する。浮上分離槽の型式としては、
圧延油中の作動油,スカム分等の比重の軽い成分を浮上
して除去できるものであれば、特に制限はないが、含油
廃水の油分の除去に汎用される傾斜板式の浮上分離槽が
特に適している。ダーティ圧延油は、傾斜板5からなる
スタック中を下降しながら、その含有している作動油,
スカム分等の比重の軽い成分を効率よく分離して、浮上
分離槽の下部を出る。
The rolling oil in the dirty oil tank 3 then flows into the floating separation tank 4. As the model of the floating separation tank,
There is no particular limitation as long as it can float and remove components with low specific gravity such as hydraulic oil and scum in rolling oil, but a sloping plate type flotation separation tank commonly used for removing oil from oil-containing wastewater is particularly preferable. Is suitable. The dirty rolling oil descends in the stack composed of the inclined plates 5, and the working oil contained therein,
Efficiently separates components with low specific gravity such as scum and leaves the bottom of the flotation tank.

【0011】浮上分離槽4の液面近くに濃縮された比重
の軽い浮上成分は、フロート式のスキマー6で選択的に
汲み取られて浮上物タンク7に流下して、一旦貯留され
る。次いで浮上成分は、ポンプ8により遠心分離機9に
供給される。遠心分離機としては、金属微粉と圧延油中
の水分と作動油等の油分との三相に分離できるものが最
も望ましいが、固形分と液相分の二相に分離するもので
もよい。いずれにしても高速回転型の分離板式遠心分離
機が特に適している。
The floating component having a low specific gravity concentrated near the liquid surface of the floating separation tank 4 is selectively taken up by a float type skimmer 6, flows down to a floating substance tank 7, and is temporarily stored. Next, the floating component is supplied to the centrifuge 9 by the pump 8. As the centrifuge, a centrifuge capable of separating into three phases of fine metal powder, water in rolling oil and oil such as hydraulic oil is most preferable, but a centrifuge may be separated into two phases of solid and liquid. In any case, a high-speed rotating separation plate type centrifugal separator is particularly suitable.

【0012】分離された主に金属粉からなる固形分は、
スラッジタンク10に排出され、作動油及び圧延油の水
分等からなる液相分は、回収液タンク11に排出され
る。液相分の量が多い時は、さらに水分等を分離してダ
ーティタンクに戻し、再使用に供することも可能であ
る。
The solid content mainly composed of the separated metal powder is
The liquid phase component discharged to the sludge tank 10 and composed of the water content of the hydraulic oil and the rolling oil is discharged to the recovery liquid tank 11. When the amount of the liquid phase component is large, it is possible to further separate water and the like and return it to the dirty tank for reuse.

【0013】浮上分離槽4の下部を出る圧延油は、次い
でポンプ12により、濾過機20に供給される。濾過機
20としては、圧延油中の金属粉等の固形分は捕捉する
が、エマルジョン粒子は透過する型式のものであれば特
に制限はないが、シート状の好適な濾材を任意に使用で
き、しかも濾過圧力も適宜高くすることができる等の多
くの利点を有する水平濾板式濾過機が特に適している。
The rolling oil leaving the lower part of the flotation tank 4 is then supplied to the filter 20 by the pump 12. The filter 20 is not particularly limited as long as it is a type that captures solids such as metal powder in the rolling oil, but permeates emulsion particles, but a suitable sheet-shaped filter medium can be optionally used. Moreover, a horizontal filter plate type filter, which has many advantages such that the filtration pressure can be appropriately increased, is particularly suitable.

【0014】図において、13は多段に積層される水平
濾板であり、14は濾板間に挿着され、図示はされない
濾材交換手段により自動交換されるシート状の濾材であ
る。ダーティ圧延油は、原液ヘッダ15を介して、各原
液室16に入り、金属粉等の固形分は濾材14上に捕捉
され、エマルジョン型圧延油を構成する水及びエマルジ
ョン状の油分は濾材14を透過して濾液室17に入り、
濾液ヘッダ18を介して、クリーン油タンク19に貯留
される。そしてポンプ21により、管路22を介して圧
延設備1に清浄化されたクリーン圧延油として、循環供
給される。
In the figure, 13 is a horizontal filter plate which is laminated in multiple stages, and 14 is a sheet-like filter medium which is inserted between the filter plates and is automatically replaced by a filter medium replacement means (not shown). The dirty rolling oil enters each stock solution chamber 16 through the stock solution header 15, solids such as metal powder are trapped on the filter medium 14, and water and emulsion oil components constituting the emulsion type rolling oil are filtered by the filter medium 14. Permeate into the filtrate chamber 17,
It is stored in the clean oil tank 19 via the filtrate header 18. Then, the pump 21 circulates and supplies it to the rolling equipment 1 via the pipe line 22 as clean rolling oil which has been cleaned.

【0015】[0015]

【発明の効果】以上の構成と作用を有する本発明によれ
ば、圧延設備で循環使用されるエマルジョン型圧延油中
の異物を、それぞれの性状に適した分離除去手段を最適
に組み合わせた方法で処理することにより、エマルジョ
ン粒子を破壊することなく浄化できるので、圧延油とし
ての必要な性能を維持して、さらには圧延製品に悪い影
響を与えることなく圧延油を長期間使用できる効果が得
られる。
EFFECTS OF THE INVENTION According to the present invention having the above-described structure and action, a method of optimally combining the separating and removing means suitable for each property of the foreign matter in the emulsion type rolling oil circulated and used in the rolling equipment is used. By treating it, the emulsion particles can be purified without breaking it, so that the required performance as a rolling oil can be maintained, and further the rolling oil can be used for a long period of time without adversely affecting the rolled product. .

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

【図1】本発明の実施例の系統図。FIG. 1 is a system diagram of an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1;圧延設備、2;管路、3;ダーティ油タンク、4;
浮上分離槽、5;傾斜板、6;スキマー、7;浮上物タ
ンク、8;ポンプ、9;遠心分離機、10;スラッジタ
ンク、11;回収液タンク、12;ポンプ、13;水平
濾板、14;濾材、15;原液ヘッダ、16;原液室、
17;濾液室、18;濾液ヘッダ、19;クリーン油タ
ンク、20;濾過機、21;ポンプ、22;管路。
1; rolling equipment, 2; pipeline, 3; dirty oil tank, 4;
Flotation tank, 5; inclined plate, 6; skimmer, 7; float tank, 8; pump, 9; centrifuge, 10; sludge tank, 11; recovered liquid tank, 12; pump, 13; horizontal filter plate, 14: filter medium, 15: stock solution header, 16; stock solution chamber,
17; filtrate chamber, 18; filtrate header, 19; clean oil tank, 20; filter, 21; pump, 22; pipeline.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】金属粉,作動油及びスカム分等の異物を含
有する金属圧延設備から発生するエマルジョン型圧延油
を処理し、前記異物を除去して循環使用するに際して、
次の工程から構成されることを特徴とする圧延油の浄化
方法。 (1) 圧延設備から発生する圧延油を浮上分離手段で処理
して作動油及びスカム分を主とする浮上物質を分離する
浮上分離工程。 (2) 前記浮上分離工程で得られた浮上物質を遠心分離機
で処理してスラッジ分と液相分とに分離する遠心分離工
程。 (3) 前記浮上分離工程から流出する圧延油を濾過手段で
処理して圧延油中の金属粉等の固形分を分離除去する濾
過工程。
1. When an emulsion type rolling oil generated from a metal rolling equipment containing foreign matter such as metal powder, hydraulic oil and scum content is treated, and the foreign matter is removed and reused,
A method for purifying rolling oil, comprising the following steps. (1) A flotation separation step in which rolling oil generated from rolling equipment is treated by a flotation separation means to separate hydraulic oil and a floating substance mainly composed of scum. (2) A centrifugal separation step of treating the floating substance obtained in the floating separation step with a centrifuge to separate it into a sludge component and a liquid phase component. (3) A filtration step of treating the rolling oil flowing out from the floating separation step with a filtering means to separate and remove solid contents such as metal powder in the rolling oil.
JP7206755A 1995-07-21 1995-07-21 Purification of rolling oil Pending JPH0931486A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7206755A JPH0931486A (en) 1995-07-21 1995-07-21 Purification of rolling oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7206755A JPH0931486A (en) 1995-07-21 1995-07-21 Purification of rolling oil

Publications (1)

Publication Number Publication Date
JPH0931486A true JPH0931486A (en) 1997-02-04

Family

ID=16528559

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7206755A Pending JPH0931486A (en) 1995-07-21 1995-07-21 Purification of rolling oil

Country Status (1)

Country Link
JP (1) JPH0931486A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003082382A (en) * 2001-09-14 2003-03-19 Japan Atom Energy Res Inst Method for purifying waste lubricating oil by water addition centrifugation
JP2007163077A (en) * 2005-12-15 2007-06-28 Ishikawajima Harima Heavy Ind Co Ltd Heat transport method and system
JP2009029987A (en) * 2007-07-30 2009-02-12 Mitsubishi Kakoki Kaisha Ltd Working oil purifying system
KR101008082B1 (en) * 2003-06-20 2011-01-13 재단법인 포항산업과학연구원 Treatment Method for Used Skin Pass Oil and Apparatus for the Method
CN102489053A (en) * 2011-12-20 2012-06-13 华东理工大学 Method and device for removing fine solid particles in cold continuous rolling emulsified liquid
WO2017099330A1 (en) * 2015-12-10 2017-06-15 (주)엔에스케이 엔지니어링 Device for recycling skin pass rolling oil
CN111411014A (en) * 2020-03-25 2020-07-14 宁波宝新不锈钢有限公司 Harmless treatment method for stainless steel rolling oil sludge
CN113201393A (en) * 2021-05-31 2021-08-03 内蒙古联晟新能源材料有限公司 Environment-friendly pollution-free aluminum coil rolling oil recovery system
JPWO2023002637A1 (en) * 2021-07-23 2023-01-26

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003082382A (en) * 2001-09-14 2003-03-19 Japan Atom Energy Res Inst Method for purifying waste lubricating oil by water addition centrifugation
KR101008082B1 (en) * 2003-06-20 2011-01-13 재단법인 포항산업과학연구원 Treatment Method for Used Skin Pass Oil and Apparatus for the Method
JP2007163077A (en) * 2005-12-15 2007-06-28 Ishikawajima Harima Heavy Ind Co Ltd Heat transport method and system
JP2009029987A (en) * 2007-07-30 2009-02-12 Mitsubishi Kakoki Kaisha Ltd Working oil purifying system
CN102489053A (en) * 2011-12-20 2012-06-13 华东理工大学 Method and device for removing fine solid particles in cold continuous rolling emulsified liquid
WO2017099330A1 (en) * 2015-12-10 2017-06-15 (주)엔에스케이 엔지니어링 Device for recycling skin pass rolling oil
CN111411014A (en) * 2020-03-25 2020-07-14 宁波宝新不锈钢有限公司 Harmless treatment method for stainless steel rolling oil sludge
CN113201393A (en) * 2021-05-31 2021-08-03 内蒙古联晟新能源材料有限公司 Environment-friendly pollution-free aluminum coil rolling oil recovery system
JPWO2023002637A1 (en) * 2021-07-23 2023-01-26
WO2023002637A1 (en) * 2021-07-23 2023-01-26 株式会社ティービーエム Device and method for separating and recovering highly pure oil from waste oil

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