JPH07851A - Method and apparatus for removing ferrous substance from rolling oil - Google Patents

Method and apparatus for removing ferrous substance from rolling oil

Info

Publication number
JPH07851A
JPH07851A JP5139664A JP13966493A JPH07851A JP H07851 A JPH07851 A JP H07851A JP 5139664 A JP5139664 A JP 5139664A JP 13966493 A JP13966493 A JP 13966493A JP H07851 A JPH07851 A JP H07851A
Authority
JP
Japan
Prior art keywords
rolling oil
oil
magnet
rolling
iron
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.)
Granted
Application number
JP5139664A
Other languages
Japanese (ja)
Other versions
JP3323933B2 (en
Inventor
Kenichiro Tsujii
謙一郎 辻井
Hirohiko Takei
宏彦 武居
Nobuo Uematsu
伸夫 植松
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 JP13966493A priority Critical patent/JP3323933B2/en
Publication of JPH07851A publication Critical patent/JPH07851A/en
Application granted granted Critical
Publication of JP3323933B2 publication Critical patent/JP3323933B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • 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

  • Metal Rolling (AREA)
  • Lubricants (AREA)

Abstract

PURPOSE:To make the concentration of ferrous impurities in rolling oil controllable and provide stainless steel products with good gloss by immersing a magnet saparator to which a magnet having specified magnetic flux density is attached in rolling oil in a rolling oil tank for a prescribed time to remove the ferrous impurities as low as a specified concentration or less. CONSTITUTION:The lower part of a chain conveyer 3 to which magnet plates 2 with 2000 gauss or more magnetic flux density are attached is immersed in an oil in a rolling oil tank 1 and the chain conveyer 3 is moved in direction shown as the arrow (a) or (b). While passing the liquid surface, the chain conveyer 3 rotates at 30-90 deg. tilting angle against the liquid surface. A plurality of the magnet plates 2 are immersed in the rolling oil for a prescribed time and while moving in the oil, the plates 2 absorb the ferrous impurities, squeeze the effective rolling oil including the ferrous impurities and separate the ferrous impurities based on the magnetic force function, and thus decrease the ferrous impurities concentration to 2000ppm or less in the rolling oil. Then, the absorbed ferrous impurities are scratched and recovered in a scum tank 7 through a scum guide 6.

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、ステンレス鋼板または
鋼帯(総称してステンレス鋼板という。)の冷間圧延に
おいて、鉱物油を水に懸濁したエマルジョンを圧延油と
して用い、表面光沢のよい製品を得るために当該圧延油
の鉄分夾雑物を除去する方法とその装置に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention uses an emulsion in which mineral oil is suspended in water as a rolling oil in cold rolling of a stainless steel plate or a steel strip (generally referred to as a stainless steel plate) and has a good surface gloss. The present invention relates to a method and an apparatus for removing iron impurities from the rolling oil to obtain a product.

【0002】[0002]

【従来の技術】ステンレス鋼板は、表面光沢のよい製品
が要求されることから冷間圧延の際、圧延油として鉱物
油がそのまま圧延油として用いられるが、高圧下高速圧
延を行った場合には鋼板の表面にヒート・ストリークと
呼ばれる焼付き現象が生じ、また中間挿入紙の焼付きが
発生する等の問題がある。一方、鉱物油を水に懸濁した
エマルジョンを圧延油として用いることは、冷却性や潤
滑性に優れている反面、冷間圧延すると圧延油の汚れが
激しいことから表面光沢のよい製品が得られないため一
部オーステナイト系鋼や研磨仕上げ製品用材料の冷間圧
延に使用されるのみで、SUS430等のフェライト系
鋼種或いはSUS410等のマルテンサイト系鋼種に対
しては鉱物油を水に懸濁したエマルジョンを圧延油とし
て高圧下高速の冷間圧延を行うことは不可能であった。
2. Description of the Related Art Since a stainless steel sheet is required to have a product with a good surface gloss, mineral oil is used as a rolling oil as it is during cold rolling, but when high-speed rolling under high pressure is carried out, There is a problem that a seizure phenomenon called heat streak occurs on the surface of the steel sheet, and seizure of the intermediate insertion sheet occurs. On the other hand, using an emulsion in which mineral oil is suspended in water as rolling oil has excellent cooling properties and lubricity, but on the other hand, cold rolling causes severe contamination of the rolling oil, resulting in products with good surface gloss. Since it is not used, it is only used for cold rolling of some austenitic steels and materials for polished finish products. Mineral oil was suspended in water for ferritic steel grades such as SUS430 or martensitic steel grades such as SUS410. It was impossible to carry out cold rolling at high pressure and high speed using the emulsion as rolling oil.

【0003】そこで、特開昭61−172604号公報
に開示されるように、Cr系ステンレス鋼板の冷間圧延
の際、鉱物油を基油とする圧延油エマルジョン中の鉄分
夾雑物の濃度を200ppm 以下に維持して圧延する方法
が提案されている。この方法は、使用された圧延油を回
収、収納するダーティータンク内でスカムおよび液面下
上層部の鉄分夾雑物濃度の高い圧延油を除去後、更にク
リーンタンク内にマグネットセパレーターを設けて、残
存鉄分夾雑物を除去し、かつ圧延油中の鉄分夾雑物の濃
度を200ppm 以下に維持するものである。このマグネ
ットセパレーターは、従来より普通鋼等の圧延分野に適
用されており、冷間圧延の際、圧延油中の鉄分夾雑物を
除去し、鉄分濃度を1000〜500ppm 以下にする目
的で使用されることは一般によく知られたことである
が、装着される磁石の磁束密度は1000〜1800ガ
ウスのものが主に用いられて来た。
Therefore, as disclosed in Japanese Patent Application Laid-Open No. 61-172604, at the time of cold rolling of a Cr-based stainless steel sheet, the concentration of iron contaminants in a rolling oil emulsion containing mineral oil as a base oil is 200 ppm. The following method of rolling is proposed. This method collects and stores the used rolling oil, removes the scum and the rolling oil with a high concentration of iron contaminants in the upper layer below the liquid surface, and then installs a magnetic separator in the clean tank to leave it. Iron impurities are removed and the concentration of iron impurities in the rolling oil is maintained at 200 ppm or less. This magnet separator has been conventionally applied to the field of rolling ordinary steel and the like, and is used for the purpose of removing iron impurities in the rolling oil during cold rolling to reduce the iron concentration to 1000 to 500 ppm or less. It is generally well known that a magnet having a magnetic flux density of 1000 to 1800 gauss has been mainly used.

【0004】この技術をそのままステンレス鋼板の圧延
に適用した場合には、鉄分夾雑物は普通鋼圧延油と同様
に強磁性体を含むが、普通鋼の鉄分夾雑物に比較して磁
性が低いため、磁束密度が1000〜1800ガウスの
磁石では吸着に長い浸漬時間(ほぼ1週間)と大きな接
液表面積が必要になりセパレーター長さが過大になると
共にタンク容量も大きくしなければならないという欠点
に加えて吸着鉄分夾雑物からの有効圧延油分の絞り出し
能力が低いために有効圧延油分を過剰に持ち出すという
欠点があった。そのため、この有効圧延油分を回収し、
再生するために実開昭57−141813号に開示され
るような圧延機と併設されたクーラントスカムの油分循
環回収装置の設置が必須であった。
When this technique is directly applied to the rolling of stainless steel plates, the iron impurities contain a ferromagnetic material like the ordinary steel rolling oil, but have a lower magnetism than the ordinary steel iron impurities. In addition, in the case of a magnet with a magnetic flux density of 1000 to 1800 Gauss, a long immersion time (approximately 1 week) and a large liquid contact surface area are required for adsorption, which makes the separator length too large and the tank capacity also large. However, since the ability to squeeze out the effective rolling oil from the adsorbed iron content impurities is low, there is a drawback in that the effective rolling oil is taken out excessively. Therefore, collect this effective rolling oil,
In order to regenerate, it was essential to install an oil content circulation and recovery device for the coolant scum, which was installed together with the rolling mill as disclosed in Japanese Utility Model Publication No. 57-141813.

【0005】このように、ステンレス鋼板の冷間圧延に
おいて、何ら追加的設備を必要とすることなく効果的に
圧延油の鉄分夾雑物を除去する方法とその装置の開発が
望まれていた。
As described above, in the cold rolling of stainless steel sheets, it has been desired to develop a method and an apparatus for effectively removing the iron contaminants in the rolling oil without requiring any additional equipment.

【0006】[0006]

【発明が解決しようとする課題】本発明は、上記要望を
充足し、良好な表面光沢を有する製品を得るために、ス
テンレス鋼板の冷間圧延系に設け循環使用する圧延油を
貯蔵する圧延油タンクに、圧延で使用された圧延油排油
を回収し、再利用するにあたって圧延油中に、より高い
磁束密度の磁石を所望の時間浸漬し、効果的に圧延油の
鉄分夾雑物の濃度を200ppm 以下に除去し濃度管理可
能なレベルに維持する方法と装置を提供することを目的
とするものである。
DISCLOSURE OF THE INVENTION The present invention satisfies the above-mentioned needs and, in order to obtain a product having a good surface gloss, a rolling oil which is provided in a cold rolling system of a stainless steel sheet and which stores a rolling oil to be circulated and used. When recovering the rolling oil waste oil used in rolling in the tank and reusing it, dip a magnet with a higher magnetic flux density in the rolling oil for a desired time to effectively reduce the concentration of iron contaminants in the rolling oil. It is an object of the present invention to provide a method and an apparatus for removing to less than 200 ppm and maintaining the concentration controllable level.

【0007】また、上記鉄分夾雑物の排出に伴う有効圧
延油分の排出を圧延油濃度管理可能なレベルに抑制する
ことを第二の目的とするものである。
A second object is to suppress the discharge of the effective rolling oil component accompanying the discharge of the iron contaminants to a level at which the rolling oil concentration can be controlled.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するた
め、本発明では、(1)ステンレス鋼板または鋼帯の冷
間圧延に使用される鉄分夾雑物を含む圧延油を回収し、
かつ貯蔵循環する圧延油の浄化方法において、圧延油タ
ンク内に、磁束密度2000ガウス以上の磁石を装着し
たマグネットセパレーターを圧延油液面に対し傾斜して
所定時間浸漬し、圧延油中の鉄分夾雑物の濃度を200
ppm 以下に低下することを特徴とする圧延油中の鉄分除
去方法、および(2)マグネットセパレーターの油面に
対する傾斜角度を30〜90°範囲にすると共に接液表
面積/圧延油(m2 /l)を3×10-52 /l(lは
リットル、以下同じ)以上に調整し、かつ各磁石の浸漬
時間を2分以上とすることを特徴とする前項記載の圧延
油中の鉄分除去方法、また(3)圧延設備から排出され
る圧延油を回収しかつ供給する圧延油を貯蔵する圧延油
タンクに、磁束密度2000ガウス以上の磁石板からな
るマグネットセパレーターを装着したコンベアを設ける
と共に該コンベアを液面に対して30〜90°の傾斜角
に配設し、圧延油タンク外部における磁石板と接し、磁
石板に吸着した鉄分夾雑物を掻き取るスクレーパーを備
えたことを特徴とする圧延油中の鉄分除去装置である。
In order to achieve the above object, in the present invention, (1) a rolling oil containing an iron contaminant used for cold rolling of a stainless steel plate or a steel strip is recovered,
In the method for purifying rolling oil that is stored and circulated, a magnet separator equipped with a magnet having a magnetic flux density of 2000 gauss or more is immersed in a rolling oil tank while being inclined with respect to the liquid level of the rolling oil for a predetermined time to contaminate iron in the rolling oil. The concentration of the object is 200
(2) A method for removing iron in rolling oil, which is characterized by decreasing to ppm or less, and (2) an angle of inclination of the magnet separator with respect to the oil surface within a range of 30 to 90 ° and a liquid contact surface area / rolling oil (m 2 / l). ) Is adjusted to 3 × 10 −5 m 2 / l (l is liter, the same applies hereinafter) and the immersion time of each magnet is set to 2 minutes or more. Iron removal from rolling oil according to the preceding paragraph, Method, and (3) a rolling oil tank for storing the rolling oil that collects and supplies the rolling oil discharged from the rolling equipment is provided with a conveyor equipped with a magnetic separator made of a magnet plate having a magnetic flux density of 2000 gauss or more. The conveyor is disposed at an inclination angle of 30 to 90 ° with respect to the liquid surface, is provided with a scraper that is in contact with a magnet plate outside the rolling oil tank and scrapes off iron impurities adsorbed on the magnet plate. An iron removing apparatus during rolling oil.

【0009】以下に本発明を詳細に説明する。一般に圧
延油はフィルターを通して循環使用しているが、圧延油
のエマルジョンの油滴の粒径は通常5μm程度であるか
ら、フィルターはこれよりも目の粗いものが用いられて
いる。クロム系ステンレス鋼を冷間圧延した場合、回収
した圧延油中に含有する鉄分夾雑物は、殆どが粒径1μ
m以下の微細なものであるから、フィルターで除去する
ことはできないとされている。また、鉄分夾雑物の濃度
は、新油の状態から1500トン程度圧延すると200
ppm を超えるが、圧延量と濃度上昇との関係は必ずしも
一定でなく、また新油入替えの頻度を増すことはコスト
的に好ましくない。従って、鉄分夾雑物の濃度を200
ppm 以下に維持するためには、一般にはダーティータン
ク内でスカム(鉄分夾雑物、グリース、ベアリング油、
老廃油等の不純物を含む。)および液面下上層部の鉄分
夾雑物濃度の高い圧延油を除去し、鉄分夾雑物濃度を3
50ppm 程度まで低下した後、更にクリーンタンク内に
マグネットセパレーターを設けて残存鉄分夾雑物を除去
し、鉄分夾雑物の濃度を200ppm 以下に低下させるこ
とが好ましい。
The present invention will be described in detail below. Generally, the rolling oil is circulated through the filter, but since the particle size of the oil droplets of the rolling oil emulsion is usually about 5 μm, a filter having a coarser mesh than this is used. When chrome-based stainless steel is cold-rolled, most of the iron impurities contained in the recovered rolling oil have a grain size of 1 μm.
It is said that it cannot be removed by a filter because it is a fine particle of m or less. In addition, the concentration of iron contaminants is 200 when rolled around 1500 tons from the state of fresh oil.
Although it exceeds ppm, the relationship between the rolling amount and the increase in concentration is not always constant, and increasing the frequency of new oil replacement is not preferable in terms of cost. Therefore, the concentration of iron impurities should be 200
To maintain below ppm, scum (iron contaminants, grease, bearing oil,
Contains impurities such as waste oil. ) And the oil above the liquid surface above which the concentration of iron contaminants is high, the concentration of iron contaminants is reduced to 3
After the concentration is reduced to about 50 ppm, it is preferable to further provide a magnet separator in the clean tank to remove the residual iron contaminants and reduce the concentration of the iron contaminants to 200 ppm or less.

【0010】油中の鉄分夾雑物を除去するにはクリーン
タンク内に磁石板を所定時間浸漬、移動させるのがよ
く、本発明では従来の低磁束密度の磁石に替え、200
0ガウス以上の高磁束密度の磁石を採用することで吸着
能力を向上させ、鉄分夾雑物濃度を200ppm 以下に低
下させている。図1は油中における鉄分含有量と磁石の
磁束密度との関係を調査したものであって、図から明ら
かのように、従来から使用されていた1000〜180
0ガウスの磁束密度を有する磁石では圧延油中の鉄分夾
雑物濃度を管理限界200ppm 或いはそれ以下を達成す
ることが不可能である。従って、本発明では2000ガ
ウス以上の高磁束密度の磁石を使用することが必須とな
る。
In order to remove iron contaminants in oil, it is preferable to immerse and move the magnet plate in a clean tank for a predetermined time. In the present invention, a conventional magnet having a low magnetic flux density is used.
By using a magnet with a high magnetic flux density of 0 gauss or more, the adsorption capacity is improved, and the concentration of iron impurities is reduced to 200 ppm or less. FIG. 1 shows the relationship between the iron content in the oil and the magnetic flux density of the magnet. As is clear from the figure, the conventional 1000 to 180
With a magnet having a magnetic flux density of 0 Gauss, it is impossible to achieve a control limit of 200 ppm or less for the concentration of iron impurities in rolling oil. Therefore, in the present invention, it is essential to use a magnet having a high magnetic flux density of 2000 Gauss or more.

【0011】一方、本発明において鉄分夾雑物濃度を管
理限界である200ppm 以下により安定して達成するた
めには、さらに次の条件を具備させることが好ましい。
まず、高磁束密度磁石の油中浸漬時間と、接液表面積が
所定の範囲になるようにすること、すなわち、磁石の接
液表面積率(接液表面積/圧延油(m2 /l))を3×
10-52 /l以上に調整することも重要な要件である
ことが判った。
On the other hand, in the present invention, it is preferable to further satisfy the following conditions in order to stably achieve the concentration of iron contaminants at the control limit of 200 ppm or less.
First, the immersion time of the high magnetic flux density magnet in oil and the wetted surface area should be within a predetermined range, that is, the wetted surface area ratio of the magnet (wetted surface area / rolling oil (m 2 / l)) 3x
It was found that adjusting to 10 -5 m 2 / l or more is also an important requirement.

【0012】図2に磁石の接液表面積率と圧延油中の鉄
分濃度との関係を示した通り、この率が3×10-52
/l未満では圧延油がマグネットセパレーター(磁石)
に接触する量が少くなり、鉄分吸着性能はあっても残留
する鉄分が多くなる。従って残留鉄分を200ppm 以下
とするには3×10-52 /l以上とする。
As shown in FIG. 2, which shows the relationship between the wetted surface area ratio of the magnet and the iron concentration in the rolling oil, this ratio is 3 × 10 -5 m 2
If it is less than / l, the rolling oil is a magnetic separator (magnet).
The amount of iron that remains is large even though it has the ability to adsorb iron. Therefore, in order to reduce the residual iron content to 200 ppm or less, the content should be 3 × 10 −5 m 2 / l or more.

【0013】また、磁石の浸漬(接油)時間の管理も必
要である。図3に磁石の鉄分吸着能力と油中浸漬時間と
の関係を示す。すなわち、圧延油中の鉄分は、鉄石けん
等の状態で存在し、親水性を示している。この状態で2
000ガウス以上の磁力によって引き寄せられる時に
は、多量の水分を伴っている(2000ガウス以下では
この状態で引き寄せる力が大きく落ちる)。つまり磁石
面に圧延油が堆積して吸着力が低下する。これが2分を
経過すると、鉄分のみが磁石面に引き寄せられることに
より水分が絞り出され、圧延油の堆積が解消される。こ
のため、鉄分吸着効率は急に上昇するが約5分でピーク
となる。以降は、濃い鉄分の吸着物が磁石表面に堆積す
ることにより、少しずつ接液面の磁力が低下して行く。
その傾きはゆるやかであるが、堆積物により表面磁力が
2000ガウス以下になると急激に吸着能力が低下す
る。10分の浸漬(2000ガウス)で効率がピークの
75%に低下する。このため、定期的な鉄分の除去が必
要となる。2分ではピークの90%に達する。他方吸着
される鉄分は、油分と共に磁石に付着する。
Further, it is necessary to control the immersion (oil contact) time of the magnet. Fig. 3 shows the relationship between the iron adsorption capacity of the magnet and the immersion time in oil. That is, the iron content in the rolling oil exists in the state of iron soap and the like, and exhibits hydrophilicity. 2 in this state
When attracted by a magnetic force of 000 Gauss or more, a large amount of water is involved (at 2000 Gauss or less, the attracting force in this state drops significantly). That is, rolling oil accumulates on the magnet surface and the adsorption force decreases. After 2 minutes, only the iron component is attracted to the magnet surface to squeeze out water, and the rolling oil is eliminated. Therefore, the iron adsorption efficiency rises sharply, but reaches a peak in about 5 minutes. After that, the concentrated iron adsorbate is deposited on the surface of the magnet, and the magnetic force of the liquid contact surface gradually decreases.
Although the inclination is gentle, the adsorption ability sharply decreases when the surface magnetic force becomes 2000 gauss or less due to the deposit. A 10 minute soak (2000 gauss) reduces efficiency to 75% of peak. Therefore, it is necessary to remove iron regularly. At 2 minutes it reaches 90% of the peak. On the other hand, iron that is adsorbed adheres to the magnet along with oil.

【0014】図4は本発明で使用する2000ガウスの
高磁束密度の磁石を用いて、鉄分選択吸着能力として吸
着全量/吸着鉄分の比と磁石浸漬時間との関係を示した
ものであり、これから明らかのように、圧延油に最適な
濃度の限界値は吸着鉄分に対する吸着全量の比が400
倍が限界値であることから磁石浸漬時間は2分以上とす
ることが鉄分選択吸着能力が著しく向上していくことが
判る。尚、吸着鉄分に対する吸着全量の比で400倍を
管理基準とするのは、これを超えると圧延油に必要な油
濃度低下が起こり圧延特性を阻害する原因となるためで
ある。
FIG. 4 shows the relationship between the total amount of adsorbed iron / adsorbed iron content as the iron selective adsorption capacity and the magnet immersion time, using the magnet of 2000 Gauss having a high magnetic flux density used in the present invention. As is apparent, the optimum concentration limit for rolling oil is 400% of the total amount of adsorbed iron to adsorbed iron.
Since the double is the limit value, it is understood that the iron selective adsorption ability is remarkably improved when the magnet immersion time is set to 2 minutes or more. The reason why the ratio of the total amount of adsorption to the amount of adsorbed iron is 400 times is set as a management standard, because when it exceeds this, the oil concentration required for the rolling oil decreases, which causes a hindrance to rolling characteristics.

【0015】本発明に使用する磁石は、永久磁石または
電磁石等の何れでもよいが、これを板状に形成するのが
好ましく、マグネットセパレーターとして例えばチェー
ンコンベア表面に装填され、圧延油タンク内に浸漬され
た状態で移動させることにより鉄分夾雑物を前記磁石表
面に吸着させる方法を採るのがよい。特に、コンベアを
液面に対し傾斜させ、すなわち30°以上、90°以下
の傾斜角度を維持することにより、磁石板の油中浸漬時
間を調整でき、油中鉄分夾雑物濃度を容易に200ppm
以下に低下させることが可能となる。更に、磁石板の接
液(油)表面積(m2 )を圧延油(l:リットル)当り
3×10-52 /l以上とすることにより油中鉄分夾雑
物を目標値により達成しやすくなる。
The magnet used in the present invention may be either a permanent magnet or an electromagnet, but it is preferable to form it into a plate shape. For example, the magnet separator is loaded on the surface of a chain conveyor and immersed in a rolling oil tank. It is advisable to adopt a method of adsorbing the iron contaminants on the surface of the magnet by moving the iron contaminants in the above state. In particular, by inclining the conveyor with respect to the liquid surface, that is, maintaining the inclination angle of 30 ° or more and 90 ° or less, the immersion time of the magnet plate in oil can be adjusted, and the concentration of iron contaminants in oil can easily be 200 ppm.
It becomes possible to reduce to the following. Further, by setting the wetted (oil) surface area (m 2 ) of the magnet plate to 3 × 10 −5 m 2 / l or more per rolling oil (l: liter), it is easy to achieve the iron content in oil to the target value. Become.

【0016】図5に本発明の油中鉄分除去装置の一例を
示す。すなわちダーティータンク(図示せず)からフィ
ルターを通して送られて来た圧延油は、圧延油タンク1
内の深部に導入され、マグネットプレート(磁石板)2
を装着したチェーンコンベア3の一部を油中に導入し、
モーターMの回動により減速機rを介して該チェーンコ
ンベア3を矢印aまたはb方向に作動する。このチェー
ンコンベア3は、液面を通過し、かつ液面に対し30°
以上、90°以下の傾斜角度で回動し、マグネットプレ
ート2を移動するよう設置される。チェーンコンベア3
に装着された複数のマグネットプレート2は、チェーン
コンベア3の動きと共に圧延油4に所定時間(2分以
上)浸漬され、液内を移動しつつ鉄分夾雑物を吸着し、
夾雑物を包む有効圧延油分を磁力の作用で絞り分離す
る。次いで、鉄分夾雑物を吸着したマグネットプレート
2はチェーンコンベア3の作動でタンク1外に移動し、
タンク1の近傍に、マグネットプレート2と接触する位
置に設置されたスクレーパ5にてマグネットプレート2
表面に吸着され、タンク1外に搬送された鉄分夾雑物を
掻き取りスカムガイド6を介してスカムタンク7に回収
する。
FIG. 5 shows an example of a device for removing iron in oil according to the present invention. That is, the rolling oil sent from the dirty tank (not shown) through the filter is the rolling oil tank 1
Magnet plate (magnet plate) 2 that is introduced deep inside
Introduce part of the chain conveyor 3 equipped with
By rotating the motor M, the chain conveyor 3 is operated in the direction of arrow a or b via the speed reducer r. This chain conveyor 3 passes the liquid surface and is at an angle of 30 ° to the liquid surface.
As described above, the magnet plate 2 is installed so as to rotate at an inclination angle of 90 ° or less and move the magnet plate 2. Chain conveyor 3
The plurality of magnet plates 2 mounted on the are immersed in the rolling oil 4 for a predetermined time (2 minutes or more) along with the movement of the chain conveyor 3, and while advancing in the liquid, adsorbing iron contaminants,
Effective rolling oil that encloses impurities is squeezed and separated by the action of magnetic force. Next, the magnet plate 2 that has adsorbed iron and foreign matters moves to the outside of the tank 1 by the operation of the chain conveyor 3,
A magnet plate 2 is provided by a scraper 5 installed near the tank 1 at a position in contact with the magnet plate 2.
The iron contaminants adsorbed on the surface and conveyed to the outside of the tank 1 are scraped off and collected in the scum tank 7 via the scum guide 6.

【0017】鉄分夾雑物除去効果を向上させるため、タ
ンク1内に貯蔵された圧延油4を何らかの手段で撹拌し
たり、タンク1に浸漬したチェーンコンベア3を揺動さ
せてもよい。また、減速機rは、鉄分夾雑物回収速度と
或いは、更に有効圧延油分絞り出し(分離)効率のため
の最適経済速度への微調整のための変速手段としても作
用する。
In order to improve the effect of removing iron contaminants, the rolling oil 4 stored in the tank 1 may be agitated by some means, or the chain conveyor 3 immersed in the tank 1 may be swung. Further, the speed reducer r also functions as a speed changing means for fine adjustment to the iron foreign matter recovery speed or further to the optimum economic speed for the effective rolling oil extraction (separation) efficiency.

【0018】[0018]

【実施例】20段ゼンジミア圧延機により、鉱物油を水
に懸濁したエマルジョンを圧延油として、SUS430
フェライト系ステンレス鋼を板厚3.8mmから0.6mm
まで冷間圧延した際の冷延板の反射率の推移を表1に示
す。圧延油の浄化方法は図3に示す装置により、本発明
法は磁束密度2500ガウスのマグネットプレートを用
い、油中浸漬部分のコンベア1周期を2分として、圧延
油に浸漬した。一方従来法では低磁束密度(1500〜
1800ガウス)のマグネットプレートを装着したチェ
ーンコンベアをタンク内油中に浸漬したままの状態で設
置したものである。
[Examples] SUS430 was prepared by using a 20-high Sendzimir rolling machine to prepare an emulsion obtained by suspending mineral oil in water as a rolling oil.
Ferrite stainless steel with a plate thickness of 3.8 mm to 0.6 mm
Table 1 shows changes in the reflectance of the cold-rolled sheet when cold-rolled up to. The rolling oil was purified by the apparatus shown in FIG. 3, and in the method of the present invention, a magnet plate having a magnetic flux density of 2500 gauss was used, and one cycle of the conveyor of the portion immersed in oil was set to 2 minutes, and the rolling oil was immersed. On the other hand, the conventional method has a low magnetic flux density (1500 to 1500).
A chain conveyor equipped with a magnet plate of 1800 gauss) was installed while being immersed in the oil in the tank.

【0019】[0019]

【表1】 [Table 1]

【0020】上記結果から判るように、従来法では累計
圧延量が2000トンで鉄分夾雑物濃度が200ppm を
超え、冷延板の光沢を表す反射率(JIS Z 874
1の方法4で測定)が劣化してフェライト系或いはマル
テンサイト系の2B仕上げ製品の採用が不可であったの
に対して、本発明による方法を採用することで鉄分夾雑
物濃度を200ppm 以下に抑制可能であり、冷延板反射
率は、16000トン圧延後で依然として低下すること
なく光沢を維持しており2B仕上げ製品が確保できた。
As can be seen from the above results, in the conventional method, the cumulative rolling amount is 2000 tons, the concentration of iron impurities exceeds 200 ppm, and the reflectance (JIS Z 874) which represents the gloss of the cold-rolled sheet.
However, it was impossible to use a ferrite-based or martensite-based 2B finished product (measured by Method 4 of 1), but the method of the present invention reduced the concentration of iron impurities to 200 ppm or less. It was possible to suppress, and the reflectance of the cold-rolled sheet remained glossy even after the rolling of 16000 tons, and the 2B finished product could be secured.

【0021】[0021]

【発明の効果】以上説明したように本発明により、ステ
ンレス鋼の冷間圧延に用いられる圧延油を循環使用する
際に圧延油内の鉄分夾雑物濃度を200ppm 以下に確実
に低下させることにより、光沢のよいステンレス鋼製品
が得られる。
As described above, according to the present invention, when the rolling oil used for cold rolling of stainless steel is circulated and used, by reliably lowering the iron contaminant concentration in the rolling oil to 200 ppm or less, A bright stainless steel product is obtained.

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

【図1】圧延油中の鉄分除去限界を鉄分含有量と吸着マ
グネットプレートの磁束密度との関係で示す図。
FIG. 1 is a diagram showing the iron removal limit in rolling oil by the relationship between the iron content and the magnetic flux density of an attraction magnet plate.

【図2】マグネットの接触面積率と圧延油中の鉄分濃度
との関係を示す図。
FIG. 2 is a diagram showing a relationship between a contact area ratio of a magnet and an iron content concentration in rolling oil.

【図3】マグネットの油中浸漬時間と鉄分吸着能力との
関係を示す図。
FIG. 3 is a diagram showing a relationship between a magnet immersion time in oil and iron adsorption capacity.

【図4】鉄分選択吸着能力を吸着全量/吸着鉄分の比と
浸漬時間との関係で示す図。
FIG. 4 is a diagram showing the iron selective adsorption capacity as a relationship between the ratio of total adsorption / adsorbed iron content and immersion time.

【図5】圧延油を浄化する装置の例を示す図。FIG. 5 is a diagram showing an example of a device for purifying rolling oil.

【符号の説明】[Explanation of symbols]

1 圧延油タンク 2 マグネットプレート 3 チェーンコンベア 4 圧延油 5 スクレーパ 6 スカムガイド a,b 移動方向 r 減速機 M モーター 1 Rolling Oil Tank 2 Magnet Plate 3 Chain Conveyor 4 Rolling Oil 5 Scraper 6 Scum Guide a, b Moving Direction r Reducer M Motor

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 ステンレス鋼板または鋼帯の冷間圧延に
使用される鉄分夾雑物を含む圧延油を回収し、かつ貯蔵
循環する圧延油の浄化方法において、圧延油タンク内
に、磁束密度2000ガウス以上の磁石を装着したマグ
ネットセパレーターを圧延油液面に対し傾斜して所定時
間浸漬し、圧延油中の鉄分夾雑物の濃度を200ppm 以
下に低下することを特徴とする圧延油中の鉄分除去方
法。
1. A method of purifying rolling oil which collects and stores and circulates rolling oil containing iron impurities used for cold rolling of stainless steel plate or steel strip, wherein a magnetic flux density of 2000 Gauss is stored in a rolling oil tank. A method for removing iron in rolling oil, which comprises lowering the concentration of iron contaminants in the rolling oil to 200 ppm or less by inclining the magnet separator equipped with the above magnets with respect to the liquid surface of the rolling oil and immersing the magnet separator for a predetermined time. .
【請求項2】 マグネットセパレーターの油面に対する
傾斜角度を30〜90°範囲にすると共に接液表面積/
圧延油(m2 /l)を3×10-5以上に調整し、かつ各
磁石の浸漬時間を2分以上とすることを特徴とする請求
項1記載の圧延油中の鉄分除去方法。
2. The inclination angle of the magnet separator with respect to the oil surface is set in the range of 30 to 90 °, and the liquid contact surface area /
The method for removing iron in rolling oil according to claim 1, wherein the rolling oil (m 2 / l) is adjusted to 3 × 10 −5 or more and the immersion time of each magnet is set to 2 minutes or more.
【請求項3】 圧延設備から排出される圧延油を回収し
かつ供給する圧延油を貯蔵する圧延油タンクに、磁束密
度2000ガウス以上の磁石板からなるマグネットセパ
レーターを装着したコンベアを設けると共に、該コンベ
アを液面に対して30〜90°の傾斜角に配設し、圧延
油タンク外部において磁石板と接し、磁石板に吸着した
鉄分夾雑物を掻き取るスクレーパーを備えたことを特徴
とする圧延油中の鉄分除去装置。
3. A rolling oil tank for storing the rolling oil that collects and supplies the rolling oil discharged from the rolling equipment is provided with a conveyor equipped with a magnetic separator made of a magnet plate having a magnetic flux density of 2000 gauss or more, and A rolling operation characterized in that the conveyor is arranged at an inclination angle of 30 to 90 ° with respect to the liquid surface, and is provided with a scraper that is in contact with a magnet plate outside the rolling oil tank and scrapes iron contaminants adsorbed on the magnet plate. Equipment for removing iron from oil.
JP13966493A 1993-06-10 1993-06-10 Method for removing iron from rolling oil Expired - Fee Related JP3323933B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13966493A JP3323933B2 (en) 1993-06-10 1993-06-10 Method for removing iron from rolling oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13966493A JP3323933B2 (en) 1993-06-10 1993-06-10 Method for removing iron from rolling oil

Publications (2)

Publication Number Publication Date
JPH07851A true JPH07851A (en) 1995-01-06
JP3323933B2 JP3323933B2 (en) 2002-09-09

Family

ID=15250549

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13966493A Expired - Fee Related JP3323933B2 (en) 1993-06-10 1993-06-10 Method for removing iron from rolling oil

Country Status (1)

Country Link
JP (1) JP3323933B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100972607B1 (en) * 2003-06-17 2010-07-27 주식회사 포스코 collecting apparatus for packaging vinyl and rust-prevention oil of roll
KR101223321B1 (en) * 2012-05-24 2013-01-16 (주)엔에스케이 엔지니어링 Iron making plant for disk type magnet filter
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101038868B1 (en) * 2003-10-20 2011-06-02 주식회사 포스코 Apparatus for removing an iron powder out of a roll oil of a cold rolling process
KR101358338B1 (en) 2013-08-19 2014-02-11 제이에스이엔지(주) Apparatus for separating iron from liquid compound
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100972607B1 (en) * 2003-06-17 2010-07-27 주식회사 포스코 collecting apparatus for packaging vinyl and rust-prevention oil of roll
KR101223321B1 (en) * 2012-05-24 2013-01-16 (주)엔에스케이 엔지니어링 Iron making plant for disk type magnet filter
CN114029344B (en) * 2021-11-09 2023-11-21 攀钢集团攀枝花钢钒有限公司 Method for controlling iron content in emulsion

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