JPS6124086B2 - - Google Patents

Info

Publication number
JPS6124086B2
JPS6124086B2 JP55154696A JP15469680A JPS6124086B2 JP S6124086 B2 JPS6124086 B2 JP S6124086B2 JP 55154696 A JP55154696 A JP 55154696A JP 15469680 A JP15469680 A JP 15469680A JP S6124086 B2 JPS6124086 B2 JP S6124086B2
Authority
JP
Japan
Prior art keywords
oil
rolling
iron
tank
rolling 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
JP55154696A
Other languages
Japanese (ja)
Other versions
JPS5779016A (en
Inventor
Tsutomu Tamya
Hiroaki Yamabuchi
Masato Akioka
Yoshihiro Hioki
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Steel Corp filed Critical Nippon Steel Corp
Priority to JP55154696A priority Critical patent/JPS5779016A/en
Publication of JPS5779016A publication Critical patent/JPS5779016A/en
Publication of JPS6124086B2 publication Critical patent/JPS6124086B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21BROLLING OF METAL
    • B21B45/00Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills
    • B21B45/02Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills for lubricating, cooling, or cleaning
    • B21B45/0269Cleaning
    • B21B45/029Liquid recovering devices
    • B21B45/0296Recovering lubricants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21BROLLING OF METAL
    • B21B45/00Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills
    • B21B45/02Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills for lubricating, cooling, or cleaning
    • B21B45/0239Lubricating
    • B21B45/0245Lubricating devices
    • B21B45/0248Lubricating devices using liquid lubricants, e.g. for sections, for tubes
    • B21B45/0251Lubricating devices using liquid lubricants, e.g. for sections, for tubes for strips, sheets, or plates
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Lubricants (AREA)
  • Metal Rolling (AREA)

Description

【発明の詳細な説明】 本発明は、鋼板の冷間圧延における圧延油の循
環使用方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for circulating rolling oil in cold rolling of steel sheets.

鋼板の冷却圧延においては、冷却と潤滑の両方
を兼ねて圧延油(俗にクーラントとも呼ばれる)
が大量に使用される。この方法は、ダイレクトシ
ステムとリサーキユレーシヨンシステムの二つに
大別される。ダイレクトシステムは、新しい圧延
油だけ使用するものであり、リサーキユレーシヨ
ンシステムは圧延油を循環使用するものである。
During cooling rolling of steel plates, rolling oil (also commonly called coolant) is used for both cooling and lubrication.
is used in large quantities. This method is broadly divided into two types: direct system and recirculation system. Direct systems use only new rolling oil, and recirculation systems recycle rolling oil.

リサーキユレーシヨンシステムにおいては、水
に油を混合して撹拌し所定濃度のエマルジヨンと
した圧延油を圧延機及び被圧延材に供給し、使用
後フイルターで圧延時に混入した異物を取り除き
タンクに回収しこれを循環使用する。
In the recirculation system, rolling oil is mixed with water and stirred to form an emulsion with a predetermined concentration, which is supplied to the rolling mill and the rolled material. After use, a filter removes foreign matter mixed in during rolling and the oil is collected in a tank. Then use this cyclically.

圧延油には、各種添加剤が配合されているのが
普通である。このように圧延油を循環使用する
と、圧延油は圧延時の圧延ロール間で劣化し、あ
るいは製品に付着して持ちさられるため循環初期
の性能が変化する。そのため、タンクにおいて新
油の補給を行なう。ところが、新油はタンク内の
圧延油と均一に混合するにはかなりの時間がかか
るためその間所望性状の圧延油が得られないとい
う難点がある。
Rolling oil usually contains various additives. When the rolling oil is recycled in this manner, the rolling oil deteriorates between the rolling rolls during rolling, or is attached to the product and carried on, resulting in a change in performance at the initial stage of circulation. Therefore, replenish new oil in the tank. However, it takes a considerable amount of time to uniformly mix the new oil with the rolling oil in the tank, so there is a problem in that rolling oil with desired properties cannot be obtained during that time.

また、タンクには循環使用中に圧延油に混入し
た微細な鉄粉を除去するべくマグネツトセパレー
タが設けられるが、このマグネツトセパレータは
油中の鉄分に同伴して圧延油をタンク外に持ち去
る。この持ち去る量は重量で、Fe2部に対し油6
〜7部、水2部くらいである。
In addition, a magnetic separator is installed in the tank to remove fine iron powder mixed into the rolling oil during circulation, but this magnetic separator carries the rolling oil out of the tank along with the iron in the oil. . The amount carried away is 6 parts oil to 2 parts Fe.
~7 parts, about 2 parts water.

また、圧延油に添加される添加剤の中には鉄と
結合しやすい性質をもつたもの、例えば極圧添加
剤があり、これもかなり持ち去られることが観察
される。さらに、上記補給される新圧延油は、普
通循環使用中の圧延油より高濃度であるが、タン
ク中において充分に均一化されないうちにマグネ
ツトセパレータで系外に持ち去られ無駄になる場
合がある。
Additionally, some additives added to rolling oil have the property of easily bonding with iron, such as extreme pressure additives, and it has been observed that these are also removed to a large extent. Furthermore, although the new rolling oil replenished has a higher concentration than the rolling oil normally used in circulation, it may be carried away from the system by the magnetic separator and wasted before it is sufficiently homogenized in the tank. .

このように、マグネツトセパレータによつても
圧延油は消耗する。このマグネツトセパレータに
よる消耗は、上記したように水にくらべて油を持
ち去る割合が高いため圧延油濃度を低下させると
ともに添加剤濃度を低下させる。そして、このマ
グネツトセパレータによりスカム状で循環系外に
持ち去られた油分は従来廃棄されていたのであ
る。
In this way, rolling oil is also consumed by the magnetic separator. As described above, the wear caused by the magnetic separator lowers the concentration of rolling oil and the concentration of additives since the rate of oil carried away is higher than that of water. Conventionally, the oil removed from the circulation system in the form of scum by the magnetic separator was discarded.

このように、従来のマグネツトセパレータ等の
鉄分除去装置を備えた圧延油リサーキユレーシヨ
ンシステムは種々の難点を有しており、本発明は
これらの難点を解消するものであつて、その要旨
とするところは、圧延油リサーキユレーシヨンシ
ステムにおいて、鉄分除去装置により鉄分と一緒
に循環系の外に持ち去られた油を回収して回収油
を得、該回収油に添加剤を添加するとともに濃度
を調整した後被圧延材、またはロールに供給する
ことによつて循環系に合流させることを特徴とす
る圧延油リサーキユレーシヨンシステムにおける
給油方法である。
As described above, conventional rolling oil recirculation systems equipped with iron removal devices such as magnetic separators have various drawbacks, and the present invention is intended to solve these drawbacks. This is because in a rolling oil recirculation system, the iron removal device collects the oil that has been taken out of the circulation system along with iron to obtain recovered oil, and then adds additives to the recovered oil. This is a method of supplying oil in a rolling oil recirculation system, characterized in that after adjusting the concentration, the oil is supplied to a material to be rolled or to a roll to join a circulation system.

本発明においては、圧延油タンクに設けた鉄分
回収装置により循環系外に排出した鉄分と圧延油
の混合物(スカム状)を遠心分離機等にかけて鉄
分を分離除去して圧延油のみを回収し、この回収
した圧延油に乳化剤、油性向上剤、極圧添加剤等
添加剤を適宜量添加して回収した圧延油の性状を
向上させる。次で、使用態様(その時の圧延条件
など)に応じてこの回収した圧延油に水(温
水)、新油等を加えることによりその濃度を調節
し、撹拌してエマルジヨン化しそれを前記循環系
と別の供給系統で被圧延材、あるいは圧延ロール
に直接供給することにより循環系の圧延油に合流
させる。圧延中においては、ストリツプやヒユー
ム等による圧延油の持ち出しがある。この持出量
はマグネツトセパレータ等で鉄分と一緒に持ち去
る油量に較べるとはるかに少ないが、循環系の圧
延油濃度が変化(低下)する。この濃度を補うべ
く新油も補給するものである。
In the present invention, a mixture of iron and rolling oil (in the form of scum) discharged outside the circulation system by an iron recovery device installed in a rolling oil tank is passed through a centrifuge or the like to separate and remove the iron, and only the rolling oil is recovered. Appropriate amounts of additives such as emulsifiers, oiliness improvers, and extreme pressure additives are added to the recovered rolling oil to improve the properties of the recovered rolling oil. Next, the concentration is adjusted by adding water (warm water), new oil, etc. to the recovered rolling oil according to the usage mode (rolling conditions at that time, etc.), and the mixture is stirred to form an emulsion, which is then added to the circulation system. It is fed directly to the material to be rolled or to the rolling rolls in a separate supply system, and is made to join the rolling oil in the circulation system. During rolling, rolling oil is carried out by strips, humps, etc. Although this amount of oil is much smaller than the amount of oil that is removed together with iron by a magnetic separator or the like, the concentration of rolling oil in the circulation system changes (decreases). New oil is also supplied to compensate for this concentration.

第1図は、このようにして回収された圧延油の
性状を摩擦係数で示したものである。第1図aに
は、回収圧延油の摩擦係数を使用比率とともに示
しており、摩擦係数は回収圧延油のみであつても
0.18であり充分使用できることがわかる。
FIG. 1 shows the properties of the rolling oil thus recovered in terms of friction coefficient. Figure 1a shows the friction coefficient of recovered rolling oil along with the usage ratio, and even if only recovered rolling oil is used, the friction coefficient is
It can be seen that it is 0.18 and can be used satisfactorily.

第1図bは、回収圧延油と新油を等量混合した
ものに極圧添加剤を添加した場合の摩擦係数の変
化示しており、2%弱の極圧添加剤の添加により
約0.09まで摩擦係数を低下できることがわかる。
Figure 1b shows the change in the coefficient of friction when an extreme pressure additive is added to a mixture of equal amounts of recovered rolling oil and new oil, and the coefficient of friction decreases to about 0.09 by adding just under 2% of the extreme pressure additive. It can be seen that the coefficient of friction can be lowered.

このようにして回収された圧延油を、循環系と
別の供給系統で直接被圧延材、または圧延ロール
に供給してやると、循環系に合流する際圧延潤滑
に使用されて混りやすくなり、更に各圧延スタン
ド下部の回収ピツト、配管、ポンプ等を通過する
過程で充分に混合撹拌されることになる。そし
て、同時に鉄分除去装置で鉄分とともに失われた
圧延油中の添加剤不足を行なうことになる。
If the rolling oil recovered in this way is supplied directly to the material to be rolled or to the rolling rolls through a supply system separate from the circulation system, it will be used for rolling lubrication when it joins the circulation system, making it more likely to get mixed up. The materials are thoroughly mixed and agitated as they pass through the collection pits, piping, pumps, etc. at the bottom of each rolling stand. At the same time, there is a shortage of additives in the rolling oil that are lost together with the iron in the iron removal device.

リサーキユレーシヨンシステムにおいては、回
収した圧延油をそのままの状態で使用すると、循
環使用するうちに極圧添加剤等が経時的に変化減
少し、ついには圧延潤滑性(特に境界膜強度)が
劣化してヒートスリツプ等のロール疵発生の原因
となるので前述したように添加剤を適宜添加する
ことが必要である。
In a recirculation system, if the recovered rolling oil is used as is, extreme pressure additives, etc. will change and decrease over time as it is recycled, and eventually the rolling lubricity (particularly the boundary film strength) will deteriorate. Since it deteriorates and causes roll defects such as heat slips, it is necessary to add additives appropriately as described above.

このように、本発明によると従来鉄分除去装置
で除去した鉄分とともに処分されて、回収使用さ
れて、回収使用されなかつた高価な圧延油を効果
的に循環系において再使用できるので油資源を節
約できる。更に、本発明の副次的効果をあげる
と、回収油の性状、濃度を適宜調整して循環系と
別の供給統で直接被圧延材に供給することができ
るので圧延における潤滑能を調節できるとともに
クーラント系統全体の濃度を一定に保つことがで
きることである。たとえば、タンデム圧延機で特
に高負荷がかかる後段スタンドのみに性状のよい
高濃度の油を供給し潤滑性の向上をはかる、ある
いは各スタンド毎にストリツプ咬み込み通板時、
および尻抜け時の高張力圧延時のみに供給油量を
増やして潤滑をよくして高張力圧延にともなう形
状悪化を防止することもできるし、高圧下圧延に
も有利である。第2図は、従来の一般的な圧延油
リサーキユレーシヨンシステムを示す図である。
図中1は冷間圧延機スタンド群、2は油回収ピツ
ド、3は回収ピツトから使用済の汚れた油を受け
るとダーテイータンク、4はダーテイータンクの
油を連続的に漏過するホフマンフイルター、5は
クリーンタンク、6は圧延油(新油)補給装置、
7,8はマグネツトセパレータ、9,10は撹拌
機(Agitator)Sは被圧延材(ストリツプ)であ
る。循環使用される油は、クリーンタンク5にお
いて、市販の圧延油と水、あるいは温水と混合し
適宜の濃度(例えば薄物圧延時4〜6%、厚物圧
延時1〜3%)に調整し撹拌してエマルジヨンと
される。
As described above, according to the present invention, the expensive rolling oil that was previously disposed of with the iron removed by the iron removal device, recovered and used, and was not recovered and used can be effectively reused in the circulation system, thereby saving oil resources. can. Furthermore, a secondary effect of the present invention is that the properties and concentration of the recovered oil can be appropriately adjusted and supplied directly to the material to be rolled through a supply system separate from the circulation system, making it possible to adjust the lubrication ability during rolling. At the same time, the concentration of the entire coolant system can be kept constant. For example, in a tandem rolling mill, high-concentration oil with good properties is supplied only to the latter stand, which is subject to particularly high loads, to improve lubricity, or when strip is passed through each stand,
It is also possible to increase the amount of oil supplied only during high-tension rolling at the time of tail-off to improve lubrication and prevent deterioration of shape due to high-tension rolling, which is also advantageous for high-reduction rolling. FIG. 2 is a diagram showing a conventional general rolling oil recirculation system.
In the figure, 1 is a group of cold rolling mill stands, 2 is an oil recovery pit, 3 is a dirty tank that receives used dirty oil from the recovery pit, and 4 is a Hoffmann that continuously leaks oil from the dirty tank. Filter, 5 is a clean tank, 6 is a rolling oil (new oil) supply device,
7 and 8 are magnetic separators, 9 and 10 are agitators, and S is a rolled material (strip). The oil to be circulated is mixed with commercially available rolling oil and water or hot water in a clean tank 5, adjusted to an appropriate concentration (for example, 4 to 6% for thin rolling, 1 to 3% for thick rolling), and stirred. It is called an emulsion.

市販の圧延油には下記の例のような添加剤が配
合されている。
Commercially available rolling oils contain additives such as those listed below.

油性向上剤 1.5% (重量比) 界面活性剤 0.5 (重量比) 極圧添加剤 2.0 ( 〃 ) その他添加剤 1.5 ( 〃 ) 撹拌機9によつて撹拌されたエマルジヨンは循
環油としてクリーンタンク5からポンプP1により
フイルターF、クーラーCを経て供給配管11に
より圧延機1に供給ヘツダー12、ノズル13,
14を介してストリツプS及びロールRに噴射さ
れ、ロールの冷却と圧延の潤滑に使用された後、
回収ピツト2に集められた回収配管15を径て、
まずダーテイタンク3においてマグネツトセパレ
ータ7により鉄分が除去されるのであるが、ここ
で鉄分と一緒に油分がスカム状で系外に持ちさら
れるのである。更に、循環油には鉄分と結合しや
すい添加剤が配合されているので除去される鉄分
に帯同して添加剤もとつてしまう。そのため循環
油の添加剤濃度が低下することになり不都合であ
る。ポンプP2によりダーテイータンク3を出た循
環油はホフマンフイルタ4にて異物(木片、鉄片
等)がとりのぞかれ、ポンプP3によりクリーンタ
ンク5に戻る。クリータンク5にも、マグネツト
セパレータ8を設けることがある。クリーンタン
ク5には、補給装置6から新しい圧延油(新油)
が供給されるのであるが、既に述べたように新油
は循環油より高濃度であるためタンク内で均一に
撹拌するには時間がかかる。
Oiliness improver 1.5% (weight ratio) Surfactant 0.5 (weight ratio) Extreme pressure additive 2.0 (〃) Other additives 1.5 (〃) The emulsion stirred by the stirrer 9 is sent from the clean tank 5 as circulating oil. A pump P1 supplies the rolling mill 1 via a filter F and a cooler C via a supply pipe 11 to a header 12, a nozzle 13,
After being injected onto the strip S and roll R through 14 and used for cooling the rolls and lubricating the rolling process,
Through the collection pipe 15 collected in the collection pit 2,
First, in the dirty tank 3, the iron content is removed by the magnetic separator 7, but here, along with the iron content, oil content is carried out of the system in the form of scum. Furthermore, since the circulating oil contains additives that easily bind to iron, the additives are removed along with the iron that is removed. Therefore, the additive concentration in the circulating oil decreases, which is disadvantageous. The circulating oil leaving the dirty tank 3 by the pump P 2 is filtered by a Hoffman filter 4 to remove foreign matter (wood chips, iron pieces, etc.), and then returned to the clean tank 5 by the pump P 3 . A magnetic separator 8 may also be provided in the cree tank 5. New rolling oil (new oil) is supplied to the clean tank 5 from the supply device 6.
However, as mentioned above, new oil has a higher concentration than circulating oil, so it takes time to stir it uniformly in the tank.

このような従来のリサーキユレーシヨンシステ
ムを改良した本発明の実施態様の一例を第3図に
示す。第1図と重複するものには同符号を付し
て、以下その説明を省く。
FIG. 3 shows an example of an embodiment of the present invention, which is an improvement on such a conventional recirculation system. Components that are the same as those in FIG. 1 are given the same reference numerals, and their explanations will be omitted below.

第3図においては、マグネツトセパレータ7及
び8により鉄分を含有したスカムを遠心分離機1
6にかけて鉄分と油分に分離し、その鉄分を排出
系17に排出し、油分をアジヤストメントタンク
18に導く。アジヤストメントタンク18におい
ては、回収した油の性状を確認したのち添加剤供
給装置19から添加剤(乳化剤、油性向上剤、極
圧添加剤等)を所要量添加し新油に近似した性状
の油となすのである。
In Fig. 3, the scum containing iron is removed from the centrifuge 1 by magnetic separators 7 and 8.
6 to separate iron and oil, the iron is discharged to a discharge system 17, and the oil is led to an adjustment tank 18. In the adjustment tank 18, after confirming the properties of the recovered oil, the required amount of additives (emulsifier, oiliness improver, extreme pressure additive, etc.) is added from the additive supply device 19 to obtain a product with properties similar to new oil. It's oil and eggplant.

次でその油をミキシングタンク20に導き、水
分と混合して所要の濃度の圧延油エマルジヨンを
得る。この所要の濃度とした圧延油をポンプP4
有する供給系21によりヘツダー22、ノズル2
3を介してストリツプSに供給するのである。図
中24は、新油補給用のタンクである。
The oil is then led to a mixing tank 20 and mixed with water to obtain a rolling oil emulsion of the desired concentration. The rolling oil with the required concentration is supplied to the header 22 and the nozzle 2 by a supply system 21 having a pump P4 .
3 to the strip S. 24 in the figure is a tank for replenishing new oil.

このような本発明は、従来の循環系と別の供給
系統を有しているため、新系統に配したアジヤス
トメントタンク18及びミキシング20におい
て、回収した油を予め充分調整して所要の性状、
濃度の圧延油エマルジヨンとなし、ストリツプ
S、あるいはロールRに供給して一旦潤滑及び冷
却に使用後に循環系に合流させるので、従来法の
如く直接循環系に混合する方法と比べて循環中の
油と補給される油とが混合しやすい特長がある。
そして、循環中の油の性状を向上させるのであ
る。
Since the present invention has a supply system separate from the conventional circulation system, the recovered oil is sufficiently adjusted in advance to obtain the required properties in the adjustment tank 18 and mixing 20 arranged in the new system. ,
Since a concentrated rolling oil emulsion is supplied to the strip S or roll R, used for lubrication and cooling, and then mixed into the circulation system, the oil in the circulation is It has the feature that it is easy to mix the oil and the oil being replenished.
This improves the properties of circulating oil.

また、必要に応じて補給油供給装置24からの
供給油量を加減することにより、高濃度で性状の
良い油を供給することもできる。そのときは、ミ
キシングタンク20において充分撹拌混合して均
質なエマルジヨンとなし、高性状の圧延油エマル
ジヨンを直接ストリツプS、あるいはロールRに
供給するのである。これは、鉄石けんの生成防止
につながる。
Further, by adjusting the amount of oil supplied from the replenishment oil supply device 24 as necessary, it is possible to supply oil with high concentration and good properties. At that time, the emulsion is sufficiently stirred and mixed in the mixing tank 20 to form a homogeneous emulsion, and the high-quality rolling oil emulsion is directly supplied to the strip S or roll R. This leads to prevention of iron soap formation.

本発明法では従来の供給配管11とは別の供給
系21を有しているため供給系21を通じてスト
リツプS、またはロールRに油を供給する上記以
外の態様としては、バルブ25を操作してストリ
ツプ圧延時における特に高い張力がストリツプに
かかる通板時(咬み込み当初)尻抜時において各
スタンドに特に多量に圧延油を供給して潤滑を良
くし、高張力がかかることによる板破断トラブル
やストリツプの形状悪化を防止することができ
る。また、薄物圧延時の特に負荷の大きな圧延ス
タンド群の後段にのみ給油してやることにより、
この後段スタンドの潤滑を良くする供給方法も可
能である。これ等の実施にあたつて、バルプ25
の開閉、あるいは調節は適宜公知の自動制御手段
を採用することができる。
Since the method of the present invention has a supply system 21 separate from the conventional supply piping 11, the method other than the above for supplying oil to the strip S or roll R through the supply system 21 is to operate the valve 25. During strip rolling, a particularly high amount of rolling oil is supplied to each stand at the time of passing the strip (at the beginning of biting) and at the time of strip removal to improve lubrication and prevent problems such as strip breakage due to the application of high tension. Deterioration of the shape of the strip can be prevented. In addition, by supplying oil only to the latter part of the rolling stand group, which is subjected to particularly heavy loads during thin-material rolling,
A supply method that improves the lubrication of this latter stage stand is also possible. In implementing these measures, Valp 25
For the opening/closing or adjustment of the opening/closing, known automatic control means can be employed as appropriate.

このように本発明によると、圧延油リサーキユ
レーシヨンシステムにおいて給油系統を2系列に
分離したため、鉄分除去装置で除去される鉄分が
持ち去る油を、循環系内に効果的に連れ戻して、
補給油を節約できるとともに循環中の油の性状を
向上させ圧延油の濃度調整制御圧延が可能となる
効果がある。
According to the present invention, since the oil supply system is separated into two lines in the rolling oil recirculation system, the oil carried away by the iron removed by the iron removal device is effectively brought back into the circulation system.
This has the effect of saving make-up oil, improving the properties of circulating oil, and enabling controlled rolling by adjusting the concentration of rolling oil.

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

第1図aは回収圧延油の性状も使用割合毎に摩
擦係数で表示した図、第1図bは回収圧延油の極
圧添加剤の添加により摩擦係数の変化を表示した
図、第2図は、従来の圧延油リサーキユレーシヨ
ンシステムの1例を示す図、第3図は、本発明の
圧延油リサーキユレーシヨンシステムの1例を示
す図である。 1……冷間圧延機群、2……油回収ピツト、3
……ダーテイータンク、5……クリーンタンク、
7,8……マグネツトセパレータ、13,14…
…ノズル、16……遠心分離機、18……アジヤ
ストメントタンク、19……添加剤供給装置、2
0……ミキシングタンク、S……ストリツプ、R
……圧延ロール。
Figure 1a shows the properties of recovered rolling oil in terms of friction coefficient for each usage ratio, Figure 1b shows changes in the friction coefficient due to the addition of extreme pressure additives to recovered rolling oil, and Figure 2 FIG. 3 is a diagram showing an example of a conventional rolling oil recirculation system, and FIG. 3 is a diagram showing an example of the rolling oil recirculation system of the present invention. 1... Cold rolling mill group, 2... Oil recovery pit, 3
...Dirty tank, 5...Clean tank,
7, 8... Magnetic separator, 13, 14...
... Nozzle, 16 ... Centrifugal separator, 18 ... Adjustment tank, 19 ... Additive supply device, 2
0...Mixing tank, S...Strip, R
...Rolling roll.

Claims (1)

【特許請求の範囲】[Claims] 1 圧延油リサーキユレーシヨンシステムにおい
て、鉄分除去装置により鉄分と一緒に循環系の外
に持ち去られた油を回収して回収油を得、該回収
油に添加剤を添加するとともに濃度を調整した後
前記循環系と別の供給系統で被圧延材またはロー
ルに供給することによつて循環系に合流させるこ
とを特徴とする圧延油リサーキユレーシヨンステ
ムにおける結油方法。
1. In a rolling oil recirculation system, oil removed from the circulation system along with iron was collected by an iron removal device to obtain recovered oil, and additives were added to the recovered oil and the concentration was adjusted. A method for consolidating oil in a rolling oil recirculation system, characterized in that the oil is then fed to the material to be rolled or to the rolls through a supply system separate from the circulation system to join the circulation system.
JP55154696A 1980-11-05 1980-11-05 Supplying method for oil to rolling mill oil circulation system Granted JPS5779016A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55154696A JPS5779016A (en) 1980-11-05 1980-11-05 Supplying method for oil to rolling mill oil circulation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55154696A JPS5779016A (en) 1980-11-05 1980-11-05 Supplying method for oil to rolling mill oil circulation system

Publications (2)

Publication Number Publication Date
JPS5779016A JPS5779016A (en) 1982-05-18
JPS6124086B2 true JPS6124086B2 (en) 1986-06-09

Family

ID=15589939

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55154696A Granted JPS5779016A (en) 1980-11-05 1980-11-05 Supplying method for oil to rolling mill oil circulation system

Country Status (1)

Country Link
JP (1) JPS5779016A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2305934B (en) * 1995-10-03 1999-08-18 Croda Int Plc Metal working
WO2001066277A1 (en) * 2000-03-09 2001-09-13 Nkk Corporation Rolling oil supplying method for cold rolling
JP4715564B2 (en) * 2006-03-08 2011-07-06 Jfeスチール株式会社 Cold rolling method
CN110560494B (en) * 2019-09-17 2020-10-23 山西太钢不锈钢股份有限公司 Control method for preventing overflow of emulsion oil return box of continuous rolling mill

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5641011A (en) * 1979-09-12 1981-04-17 Kawasaki Steel Corp Feeding method for rolling mill oil to cold rolling mill

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5641011A (en) * 1979-09-12 1981-04-17 Kawasaki Steel Corp Feeding method for rolling mill oil to cold rolling mill

Also Published As

Publication number Publication date
JPS5779016A (en) 1982-05-18

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