JP4370996B2 - Descaling method and descaling equipment in hot rolling - Google Patents

Descaling method and descaling equipment in hot rolling Download PDF

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JP4370996B2
JP4370996B2 JP2004219450A JP2004219450A JP4370996B2 JP 4370996 B2 JP4370996 B2 JP 4370996B2 JP 2004219450 A JP2004219450 A JP 2004219450A JP 2004219450 A JP2004219450 A JP 2004219450A JP 4370996 B2 JP4370996 B2 JP 4370996B2
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rolled
scraper
water
descaling
scattered
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達也 陣内
義郎 土屋
剛二 亀山
横山  稔
秀明 枝広
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JFE Steel Corp
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Description

本発明は、鋼材等を熱間で圧延する熱間圧延ラインにおいて、被圧延材表面に発生するスケールを高圧水の噴射によって除去するデスケーリング方法及びデスケーリング設備に関するものである。   The present invention relates to a descaling method and descaling equipment for removing scale generated on the surface of a material to be rolled by jetting high-pressure water in a hot rolling line for hot rolling steel or the like.

熱間圧延ラインにおいては、高温の被圧延材表面に酸化スケールが発生し、そのまま圧延機に噛み込ませるとロール表面や被圧延材表面に疵が入り、品質を低下させることから、圧延機に噛み込ませる前に、このスケールを除去する必要があり、通常、被圧延材の搬送ラインの下流側から上流側に向けて被圧延材表面に噴射ノズルから高圧水を噴射して被圧延材表面に発生するスケールを除去するデスケーリング設備が設けられている。   In the hot rolling line, oxidized scale is generated on the surface of the hot rolled material, and if it is caught in the rolling mill as it is, wrinkles enter the surface of the roll and the rolled material, reducing the quality. It is necessary to remove this scale before it is bitten, and usually the surface of the material to be rolled by injecting high pressure water from the injection nozzle onto the surface of the material to be rolled from the downstream side to the upstream side of the conveying line of the material to be rolled. Descaling equipment is provided to remove the scale generated in the system.

その際に、噴射水が被圧延材の表面に衝突したあと飛散して搬送ラインの上流側へ流れ、その飛散水が被圧延材の温度を低下させてしまったり、設備侵食を起こしたり、また搬送ライン方向に複数列の噴射ノズルが使用されている場合には下流側の噴射ノズルからの飛散水が上流側の噴射ノズルからの噴射水と干渉してデスケーリング効率を低下させるといった問題が生じる。そのため、従来より、被圧延材の表面に衝突した後の飛散水をすくいあげて回収するための板状のスクレーパ(水切板)を噴射ノズルの上流側に設置し、スクレーパ下端を被圧延材表面に接触させて飛散水を回収することが行われているが、高圧の噴射水に対抗するためにスクレーパは相当の重量があり、スクレーパの下端によって被圧延材に疵をつける危険性がある。   At that time, the spray water scatters after colliding with the surface of the material to be rolled and flows to the upstream side of the conveying line, and the scattered water lowers the temperature of the material to be rolled, causes equipment erosion, When a plurality of rows of spray nozzles are used in the transport line direction, there is a problem in that the scattered water from the downstream spray nozzle interferes with the spray water from the upstream spray nozzle and reduces the descaling efficiency. . Therefore, conventionally, a plate-shaped scraper (draining plate) for scooping up and collecting the scattered water after colliding with the surface of the material to be rolled is installed upstream of the spray nozzle, and the lower end of the scraper is placed on the surface of the material to be rolled. Although the scattered water is collected by contacting the scraper, the scraper has a considerable weight in order to counter the high-pressure jet water, and there is a risk of wrinkling the material to be rolled by the lower end of the scraper.

そこで、被圧延材に疵をつけないようにするために、噴射ノズルの上流側に、被圧延材表面から若干すきまを設けてスクレーパを配置し、このスクレーパのさらに上流側に、被圧延材表面と接触して、前記スクレーパのすきまを通り過ぎた飛散水の流れを遮る水切りロールを配置したデスケーリング設備が提案されている(例えば、特許文献1参照。)。   Therefore, in order to prevent wrinkling of the material to be rolled, a scraper is arranged on the upstream side of the injection nozzle with a slight clearance from the surface of the material to be rolled, and the surface of the material to be rolled is further upstream of this scraper. There has been proposed a descaling facility in which a draining roll that blocks the flow of scattered water passing through the gap of the scraper is disposed (see, for example, Patent Document 1).

同様に、噴射ノズルの上流側に、被圧延材表面から若干すきまを設けて1段目のスクレーパを配置し、このスクレーパのさらに上流側に、被圧延材表面と接触して、前記スクレーパのすきまを通り過ぎた飛散水を回収する軽量の2段目スクレーパを配置したデスケーリング設備が提案されている(例えば、特許文献2参照。)。
実開昭61−107409号公報 実開平05−044304号公報
Similarly, a first-stage scraper is disposed on the upstream side of the injection nozzle with a slight clearance from the surface of the material to be rolled, and in contact with the surface of the material to be rolled on the further upstream side of the scraper, the clearance of the scraper is arranged. There has been proposed a descaling facility in which a lightweight second-stage scraper that collects scattered water that has passed through is disposed (see, for example, Patent Document 2).
Japanese Utility Model Publication No. 61-107409 Japanese Utility Model Publication No. 05-044304

しかし、前記特許文献1及び特許文献2に示されているデスケーリング設備においては、噴射ノズルの上流側に配置したスクレーパのさらに上流側に、水切りロールあるいは2段目スクレーパを配置する必要があるため、設備構成が複雑になる。また、通常、他の設備との関係でデスケーリング設備の設置スペースは限られており、限られたスペースに水切りロールあるいは2段目スクレーパを配置することは難しい。さらに搬送ライン方向に複数列の噴射ノズルが使用される場合には、1段目のスクレーパでの飛散水の回収が充分ではないために、上流側の噴射ノズルからの噴射水によるデスケーリング効率が低下するという問題がある。   However, in the descaling equipment shown in Patent Document 1 and Patent Document 2, it is necessary to dispose a draining roll or a second-stage scraper further upstream of the scraper disposed upstream of the injection nozzle. The equipment configuration becomes complicated. Also, the installation space for the descaling equipment is usually limited in relation to other equipment, and it is difficult to arrange the draining roll or the second-stage scraper in the limited space. Furthermore, when a plurality of rows of spray nozzles are used in the direction of the transport line, since the scattered water is not sufficiently collected by the first-stage scraper, the descaling efficiency due to the spray water from the upstream spray nozzle is low. There is a problem of lowering.

本発明は、上記の事情に鑑みてなされたものであり、被圧延材表面に発生するスケールを高圧水の噴射によって除去するデスケーリング設備において、被圧延材の表面に衝突した後の飛散水を、簡便な設備構成で、被圧延材に疵をつけることなく、的確に回収することができる熱間圧延におけるデスケーリング方法及びデスケーリング設備を提供することを目的とするものである。   The present invention has been made in view of the above circumstances, and in the descaling equipment that removes the scale generated on the surface of the material to be rolled by jetting high-pressure water, the scattered water after colliding with the surface of the material to be rolled is removed. An object of the present invention is to provide a descaling method and descaling equipment in hot rolling that can be accurately recovered with a simple equipment configuration without wrinkling the material to be rolled.

発明者等は、上記課題を解決するために鋭意検討した結果、適切なデスケーリング効果が得られるように、噴射ノズルから被圧延材搬送ライン上流側に向かって所定の噴射圧によって所定の噴射角度で被圧延材の表面に噴射された高圧水は、被圧延材の表面に衝突した後、搬送ライン上流側に向かって被圧延材の表面を流れるのではなく、表面より上方のある高さに大部分飛散していることを知見した。具体的には、大部分の高圧水は、被圧延材搬送ライン上流側に向かって水平方向から上方に0.8°以上の角度方向に飛散することが分かった。そして、このように大部分が被圧延材表面から離れて飛散する飛散水を回収できるようにスクレーパを設置すれば、スクレーパを被圧延材表面に接触させなくとも、飛散水を的確に回収することができることを見出した。   As a result of intensive studies to solve the above problems, the inventors have determined a predetermined injection angle by a predetermined injection pressure from the injection nozzle toward the upstream side of the material to be rolled to obtain an appropriate descaling effect. The high-pressure water sprayed on the surface of the material to be rolled in does not flow on the surface of the material to be rolled toward the upstream side of the conveyance line after colliding with the surface of the material to be rolled, but at a certain height above the surface. I found that it was mostly scattered. Specifically, it has been found that most high-pressure water scatters in the angular direction of 0.8 ° or more upward from the horizontal direction toward the upstream side of the material to be rolled. And if the scraper is installed so that most of the scattered water that scatters away from the surface of the material to be rolled can be collected in this way, it is possible to accurately collect the scattered water without bringing the scraper into contact with the surface of the material to be rolled. I found out that I can.

本発明は、上記のような着想に基づいてなされたものであり、前記課題を解決するために、以下の特徴を有している。   The present invention has been made based on the above idea, and has the following features in order to solve the above problems.

[1]噴射ノズルから噴射圧が10MPa以上の高圧水を噴射して被圧延材の表面に生成したスケールを除去し、前記噴射ノズルの被圧延材搬送ライン上流側に設置されるスクレーパによって前記高圧水を回収するデスケーリング方法であって、前記スクレーパ位置において被圧延材からの距離と前記高圧水が上方に飛散する量との関係を予め求めておき、その関係に基づいて前記高圧水の回収率が80%以上となるように前記スクレーパの下端と被圧延材の表面との隙間を調整することを特徴とするデスケーリング方法。   [1] The high pressure water having an injection pressure of 10 MPa or more is injected from the injection nozzle to remove the scale generated on the surface of the material to be rolled, and the high pressure is applied by a scraper installed on the material conveying line upstream of the injection nozzle. A descaling method for recovering water, wherein a relationship between a distance from a material to be rolled at the scraper position and an amount of the high-pressure water scattered upward is obtained in advance, and the high-pressure water is recovered based on the relationship A descaling method comprising adjusting a gap between the lower end of the scraper and the surface of the material to be rolled so that the rate becomes 80% or more.

[2]被圧延材の表面に生成したスケールを噴射圧が10MPa以上の高圧水の噴射によって除去するための噴射ノズルと、該噴射ノズルから噴射された水を回収するため、該噴射ノズルの被圧延材搬送ライン上流側に設置されるスクレーパとを備えたデスケーリング設備であって、前記スクレーパの下端と被圧延材の表面との間に隙間Sgを設けるとともに、前記噴射ノズルから噴射された高圧水が被圧延材の表面に衝突する位置と前記スクレーパの下端との被圧延材搬送方向の距離Lsと、前記隙間Sgとが下式を満足することを特徴とするデスケーリング設備。   [2] An injection nozzle for removing the scale formed on the surface of the material to be rolled by injection of high-pressure water having an injection pressure of 10 MPa or more, and a target of the injection nozzle for recovering water injected from the injection nozzle. It is a descaling equipment provided with a scraper installed on the upstream side of the rolling material conveyance line, and provides a gap Sg between the lower end of the scraper and the surface of the material to be rolled, and high pressure injected from the injection nozzle A descaling facility characterized in that the distance Ls in the direction of the material to be rolled between the position where water collides with the surface of the material to be rolled and the lower end of the scraper, and the gap Sg satisfy the following equation.

100mm≦Ls≦700mm
tan-1(Sg/Ls)≦0.8°
100mm ≦ Ls ≦ 700mm
tan −1 (Sg / Ls) ≦ 0.8 °

本発明においては、被圧延材表面に衝突した後の飛散水の飛散状態に対応して、スクレーパと被圧延材表面の間に適切な隙間を設けているので、簡便な設備構成で、被圧延材に疵をつけることなく、被圧延材表面に衝突した後の飛散水を的確に回収することができる。   In the present invention, since an appropriate gap is provided between the scraper and the surface of the material to be rolled, corresponding to the scattering state of the scattered water after colliding with the surface of the material to be rolled, The splashed water after colliding with the surface of the material to be rolled can be accurately collected without wrinkling the material.

本発明の一実施形態を、図面を参照しながら説明する。   An embodiment of the present invention will be described with reference to the drawings.

図1は、本発明の一実施形態に係る熱間圧延のデスケーリング設備の説明図である。図中、1は被圧延材、3は噴射ノズルヘッダー、4は被圧延材1に高圧水を噴射する噴射ノズル、5は噴射ノズル4から噴射された高圧水(噴射水)、5’は噴射水5が被圧延材1の表面に衝突した後の飛散水、6は飛散水5’を回収するために噴射ノズル4の被圧延材搬送ライン上流側に設けられたスクレーパ、20は搬送用テーブルローラである。   Drawing 1 is an explanatory view of the descaling equipment of hot rolling concerning one embodiment of the present invention. In the figure, 1 is a material to be rolled, 3 is an injection nozzle header, 4 is an injection nozzle for injecting high-pressure water onto the material to be rolled 1, 5 is high-pressure water (injection water) injected from the injection nozzle 4, and 5 'is injection Spattered water after the water 5 has collided with the surface of the material 1 to be rolled, 6 is a scraper provided upstream of the material to be rolled on the material transport line of the spray nozzle 4 to collect the scattered water 5 ', and 20 is a transport table. Laura.

噴射ノズル4は、被圧延材搬送ラインの下流側から上流側に向けて斜めに噴射されるように、垂直下方から上流側に向けて所定の角度αだけ傾けられているとともに、噴射ノズル4からの噴射水5が被圧延材1の表面に衝突する位置Aから被圧延材搬送方向に距離Ls離れた位置の上方に、被圧延材1の表面から隙間Sgを設けて、スクレーパ6の下端Bが位置している。すなわち、噴射水5の衝突点Aとスクレーパ6の下端Bとを結ぶ線が水平方向となす角度をβとすると、β=tan-1(Sg/Ls)となっている。 The injection nozzle 4 is inclined by a predetermined angle α from the vertically lower side to the upstream side so as to be injected obliquely from the downstream side to the upstream side of the material to be rolled, and from the injection nozzle 4. A gap Sg is provided from the surface of the material to be rolled 1 above a position separated by a distance Ls from the position A where the jet water 5 collides with the surface of the material to be rolled 1 in the conveying direction of the material to be rolled, and the lower end B of the scraper 6 Is located. That is, β = tan −1 (Sg / Ls) where β is an angle formed by a line connecting the collision point A of the jet water 5 and the lower end B of the scraper 6 with the horizontal direction.

そして、この実施形態においては、噴射水5の衝突点Aからスクレーパ6の下端Bへの水平方向距離Lsと、噴射水5の衝突点Aからスクレーパ6の下端Bへ向けての角度βが下式を満足するようになっている。   In this embodiment, the horizontal distance Ls from the collision point A of the jet water 5 to the lower end B of the scraper 6 and the angle β from the collision point A of the jet water 5 to the lower end B of the scraper 6 are reduced. The expression is satisfied.

100mm≦Ls≦700mm
0.5°≦β≦0.8°
ここで、距離Lsを100mm以上としたのは、それより近づけると飛散水5’の勢いが強いためにスクレーパ6を相当強固な構造にする必要があるからである。一方、700mm以下としたのは、それより離すと設備スペースが広くなり過ぎるからである。
100mm ≦ Ls ≦ 700mm
0.5 ° ≦ β ≦ 0.8 °
Here, the reason why the distance Ls is set to 100 mm or more is that since the momentum of the scattered water 5 ′ is strong when the distance Ls is closer, the scraper 6 needs to have a considerably strong structure. On the other hand, the reason why it is set to 700 mm or less is that if it is further away, the facility space becomes too wide.

また、角度βを0.8°以下としたのは、後述するように、大部分の飛散水5’が被圧延材搬送ライン上流側に向かって水平方向から上方に0.8°以上の角度で飛散するので、角度βが0.8°以下になるようにスクレーパ6の下端Bの位置を下げておけば、大部分の飛散水5’を回収できるからである。一方、角度βを0.5°以上としたのは、スクレーパ6の下端Bを下げ過ぎると、搬送中の被圧延材1の表面に接触する可能性があるので、ある程度の間隔を確保するためである。   Further, the angle β is set to 0.8 ° or less, as will be described later, most of the splashed water 5 ′ is 0.8 ° or more upward from the horizontal direction toward the upstream side of the material to be rolled. This is because most of the scattered water 5 ′ can be recovered by lowering the position of the lower end B of the scraper 6 so that the angle β is 0.8 ° or less. On the other hand, the reason why the angle β is set to 0.5 ° or more is that if the lower end B of the scraper 6 is lowered too much, there is a possibility of coming into contact with the surface of the material to be rolled 1 being conveyed. It is.

そして、被圧延材1の表面とスクレーパ6の下端Bとの隙間Sgは、Sg=Ls・tanβで表されるので、例えば、Ls=300mmとして、0.5°≦β≦0.8°とすると、Sg=2.6mm〜4.2mmとなる。   And since the clearance gap Sg between the surface of the to-be-rolled material 1 and the lower end B of the scraper 6 is represented by Sg = Ls · tanβ, for example, assuming that Ls = 300 mm, 0.5 ° ≦ β ≦ 0.8 ° Then, Sg = 2.6 mm to 4.2 mm.

ここで、前述したように、被圧延材1の表面に衝突した後の飛散水5’の飛散状態を測定した結果を図2に示す。図2においては、衝突点Aから被圧延材搬送ライン上流側に向かって水平方向から上方へ飛散する角度θを横軸にして、その角度θ以上の角度方向に飛散した飛散水5’の合計流量Qθと飛散水5’の全体流量QTとの流量比Qθ/QTを縦軸にとって、両者の関係を示している。これによると、飛散方向角度θ=0.8°では、流量比Qθ/QT=80%となっている。すなわち、飛散方向角度θが0.8°以上となる角度方向に飛散水5’全体の80%が飛散していることが分かる。 Here, as described above, the result of measuring the scattering state of the scattered water 5 ′ after colliding with the surface of the material 1 to be rolled is shown in FIG. In FIG. 2, the total of the scattered water 5 ′ scattered in the angle direction equal to or greater than the angle θ, with the horizontal axis being the angle θ that scatters upward from the horizontal direction from the collision point A toward the upstream side of the workpiece conveyance line. The relationship between the flow rate Qθ and the flow rate ratio Qθ / Q T between the total flow rate Q T of the scattered water 5 ′ is shown on the vertical axis. According to this, at the scattering direction angle θ = 0.8 °, the flow rate ratio Qθ / Q T = 80%. That is, it can be seen that 80% of the entire scattered water 5 ′ is scattered in the angular direction in which the scattering direction angle θ is 0.8 ° or more.

したがって、噴射水5の衝突点Aからスクレーパ6の下端Bへ向けての角度βが0.8°となるようにスクレーパ6を設置すれば、飛散水5’ 全体の80%を回収することができ、さらに、角度βが0.8°以下になるようにスクレーパ6の下端Bの位置を下げておけば、飛散水5’全体の80%以上を回収することができる。   Therefore, if the scraper 6 is installed such that the angle β from the collision point A of the jet water 5 toward the lower end B of the scraper 6 is 0.8 °, 80% of the entire scattered water 5 ′ can be recovered. Further, if the position of the lower end B of the scraper 6 is lowered so that the angle β is 0.8 ° or less, 80% or more of the entire scattered water 5 ′ can be recovered.

なお、通常のデスケーリング設備では、適切なデスケーリング効果が得られるように、噴射ノズル4の向い角αを10°〜15°、噴射圧を10MPa以上にして高圧水を噴射するのが一般的であるが、その範囲では、飛散水5’の飛散状態は図2に示したものと変わらなかった。   In normal descaling equipment, in order to obtain an appropriate descaling effect, it is common to inject high-pressure water with an angle α of the injection nozzle 4 of 10 ° to 15 ° and an injection pressure of 10 MPa or more. However, in that range, the scattered state of the scattered water 5 ′ was not different from that shown in FIG.

したがって、前記のような位置にスクレーパ6の下端Bを位置させることによって、通常のデスケーリングにおいては、スクレーパ6を被圧延材1の表面に接触させなくとも、飛散水全体の80%以上の飛散水を回収することができる。   Therefore, by disposing the lower end B of the scraper 6 at the position as described above, in normal descaling, even if the scraper 6 is not brought into contact with the surface of the material 1 to be rolled, 80% or more of the scattered water is scattered. Water can be recovered.

そして、飛散水5’の回収率を変化させて、被圧延材1の温度低下等について観測した結果、飛散水5’全体の少なくとも80%を回収すれば、飛散水5’による被圧延材1の温度低下や設備侵食の問題が解消されるとともに、搬送ライン方向に複数列の噴射ノズルが用いられている場合に、下流側の噴射ノズルからの飛散水と上流側の噴射ノズルからの噴射水との干渉によってデスケーリング効率が低下するといった問題も解消され、スクレーパに求められる機能を充分に果たすことができることが確認された。   As a result of changing the recovery rate of the splashed water 5 ′ and observing the temperature drop of the material 1 to be rolled, if at least 80% of the entire splashed water 5 ′ is collected, the material 1 to be rolled by the splashed water 5 ′. In the case where multiple rows of spray nozzles are used in the transport line direction, the scattered water from the downstream spray nozzle and the spray water from the upstream spray nozzle are eliminated. It has been confirmed that the problem that the descaling efficiency is reduced due to the interference with the above can be solved, and the function required for the scraper can be sufficiently achieved.

なお、この実施形態において、角度βを0.5°以上としたのは、被圧延材1の板厚変動等によって、スクレーパ6の下端Bが搬送中の被圧延材1の表面に接触することがないように、ある程度の間隔を確保するためである。ここでは、被圧延材1の板厚変動や、先後端非定常部の反りやうねり、さらには搬送中の被圧延材の振動等を考慮して、距離Ls=240mmとした場合に、被圧延材1とスクレーパ6の下端Bとの距離が±1mm変動しても、スクレーパ6の下端Bが搬送中の被圧延材1の表面に接触しないようにしたものである。ただし、設備配置(距離Ls)及び板厚精度(板厚変動)から、スクレーパ6の下端Bが搬送中の被圧延材1の表面に接触しないようであれば、その接触しない範囲で、角度βを0.5°未満にしてもよい。それによって、さらに回収率を向上させることができる。   In this embodiment, the reason that the angle β is 0.5 ° or more is that the lower end B of the scraper 6 is in contact with the surface of the material to be rolled 1 being conveyed due to the thickness variation of the material 1 to be rolled. This is to ensure a certain interval so that there is no occurrence. Here, when the distance Ls is set to 240 mm in consideration of fluctuations in the thickness of the material 1 to be rolled, warping and undulation of the leading and trailing end unsteady portions, vibration of the material being rolled, etc. Even if the distance between the material 1 and the lower end B of the scraper 6 varies by ± 1 mm, the lower end B of the scraper 6 is prevented from coming into contact with the surface of the material 1 being conveyed. However, if the lower end B of the scraper 6 does not come into contact with the surface of the material to be rolled 1 being conveyed from the equipment arrangement (distance Ls) and the plate thickness accuracy (plate thickness fluctuation), the angle β May be less than 0.5 °. Thereby, the recovery rate can be further improved.

このようにして、この実施形態においては、被圧延材1表面に衝突した後の飛散水5’の飛散範囲に対応して、スクレーパ6と被圧延材1表面の間に適切な隙間Sgを設けているので、1段のスクレーパのみの簡便な設備構成で、被圧延材1に疵をつけることのなく、飛散水5’を的確に回収することができる。   Thus, in this embodiment, an appropriate gap Sg is provided between the scraper 6 and the surface of the material to be rolled 1 in correspondence with the scattering range of the scattered water 5 ′ after colliding with the surface of the material to be rolled 1. Therefore, the scattered water 5 ′ can be accurately collected with a simple equipment configuration having only one stage of scraper without wrinkling the material 1 to be rolled.

また、上記の考え方をベースにして、スクレーパ6の位置において被圧延材1からの距離と高圧水5が上方に飛散する量との関係を予め求めておき(例えば、図2)、その関係に基づいて飛散水5’の回収率が80%以上となるようにスクレーパ6の下端Bと被圧延材1の表面との隙間Sgを調整するようにすることで、簡便な設備構成で、被圧延材に疵をつけることのなく、被圧延材表面に衝突した後の飛散水を的確に回収することができる。   Further, based on the above concept, a relationship between the distance from the material to be rolled 1 and the amount of high-pressure water 5 scattered upward at the position of the scraper 6 is obtained in advance (for example, FIG. 2). The clearance Sg between the lower end B of the scraper 6 and the surface of the material 1 to be rolled is adjusted so that the recovery rate of the scattered water 5 ′ is 80% or more based on the simple equipment configuration. Splashing water after colliding with the surface of the material to be rolled can be accurately collected without causing wrinkles on the material.

上記の実施形態の効果を確認するために、搬送ライン方向に複数列の噴射ノズルが配置されている場合について、噴射水5の衝突点Aとスクレーパ6の下端Bとを結ぶ線が水平方向となす角度βを変化させて、その場合の飛散水5’の回収率と、スケール性欠陥(デスケーリング不良)及びスクレーパによるスリ疵の発生状況を調査した。その際、噴射水5の衝突点Aとスクレーパ6の下端Bとの被圧延材搬送方向の距離Lsは240mmとし、角度βは、0.4°、0.5°、0.8°、1.2°の4水準とした。ちなみに、被圧延材1の表面とスクレーパ6の下端Bとの隙間Sgは、Sg=240tanβ(mm)となる。   In order to confirm the effect of the above embodiment, the line connecting the collision point A of the jet water 5 and the lower end B of the scraper 6 is the horizontal direction when a plurality of rows of jet nozzles are arranged in the transport line direction. The angle β formed was changed, and the recovery rate of the scattered water 5 ′ in that case, the scale defect (de-scaling failure), and the generation state of the soot due to the scraper were investigated. At that time, the distance Ls between the collision point A of the jet water 5 and the lower end B of the scraper 6 in the conveyance direction of the material to be rolled is 240 mm, and the angle β is 0.4 °, 0.5 °, 0.8 °, 1 .4 levels of 2 °. Incidentally, the gap Sg between the surface of the material to be rolled 1 and the lower end B of the scraper 6 is Sg = 240 tan β (mm).

その調査結果を表1に示すように、角度βが0.5°と0.8°の場合は、飛散水5’の回収率が80%以上になり、下流側の噴射ノズルからの飛散水と上流側の噴射ノズルからの噴射水との干渉が回避されて、良好なデスケーリング効率が得られることから、デスケーリング不良によるスケール性欠陥の発生が抑止されている。また、隙間Sgが、被圧延材の板厚変動、反り、振動等(±1.0mm)があっても、スクレーパ6の下端Bが被圧延材に接触しない値になっているので、スクレーパによるスリ疵の発生も見られない。   As shown in Table 1, when the angle β is 0.5 ° and 0.8 °, the recovery rate of the scattered water 5 ′ is 80% or more, and the scattered water from the downstream injection nozzles. And the jet water from the upstream jet nozzle are avoided, and a good descaling efficiency is obtained, so that the occurrence of the scale defect due to the descaling failure is suppressed. In addition, even if the gap Sg has a thickness variation, warpage, vibration, etc. (± 1.0 mm) of the material to be rolled, the lower end B of the scraper 6 is a value that does not contact the material to be rolled. There is no occurrence of a pickpocket.

これに対して、角度βが0.4°の場合は、飛散水5’の回収率が88%となり、デスケーリング不良によるスケール性欠陥の発生が抑止されているが、隙間Sgが被圧延材の板厚変動、反り、振動等(±1.0mm)に対して充分でなく、スクレーパによるスリ疵の発生が見られる。   On the other hand, when the angle β is 0.4 °, the recovery rate of the scattered water 5 ′ is 88%, and the occurrence of the scale defect due to the descaling failure is suppressed, but the gap Sg is the material to be rolled. It is not sufficient with respect to fluctuations in plate thickness, warpage, vibration, etc. (± 1.0 mm), and generation of scratches by a scraper is observed.

また、角度βが1.2°の場合は、飛散水5’の回収率が80%未満であり、下流側の噴射ノズルからの飛散水と上流側の噴射ノズルからの噴射水との干渉のために、デスケーリング効率が低下して、デスケーリング不良によるスケール性欠陥が抑止されていない。   Further, when the angle β is 1.2 °, the recovery rate of the scattered water 5 ′ is less than 80%, and the interference between the scattered water from the downstream injection nozzle and the injection water from the upstream injection nozzle is caused. Therefore, the descaling efficiency is lowered, and the scale defect due to the descaling failure is not suppressed.

以上の結果から、前記の実施形態の効果を確認することができた。   From the above results, the effect of the above embodiment could be confirmed.

Figure 0004370996
Figure 0004370996

本発明の一実施形態に係る熱間圧延のデスケーリング設備の説明図である。It is explanatory drawing of the descaling equipment of the hot rolling which concerns on one Embodiment of this invention. 飛散水の飛散状態を示す図である。It is a figure which shows the scattering state of scattered water.

符号の説明Explanation of symbols

1 被圧延材
3 噴射ノズルヘッダー
4 噴射ノズル
5 噴射水
5’飛散水
6 スクレーパ
20 搬送用テーブルローラ
DESCRIPTION OF SYMBOLS 1 Rolled material 3 Injection nozzle header 4 Injection nozzle 5 Injection water 5 'splash water 6 Scraper 20 Conveyance table roller

Claims (2)

噴射ノズルから噴射圧が10MPa以上の高圧水を噴射して被圧延材の表面に生成したスケールを除去し、前記噴射ノズルの被圧延材搬送ライン上流側に設置されるスクレーパによって前記高圧水を回収するデスケーリング方法であって、前記スクレーパ位置において被圧延材からの距離と前記高圧水が上方に飛散する量との関係を予め求めておき、その関係に基づいて前記高圧水の回収率が80%以上となるように前記スクレーパの下端と被圧延材の表面との隙間を調整することを特徴とするデスケーリング方法。   The high pressure water with an injection pressure of 10 MPa or more is injected from the injection nozzle to remove the scale generated on the surface of the material to be rolled, and the high pressure water is recovered by a scraper installed on the material conveying line upstream of the injection nozzle. In this descaling method, a relationship between the distance from the material to be rolled at the scraper position and the amount of the high-pressure water scattered upward is obtained in advance, and the recovery rate of the high-pressure water is 80 based on the relationship. %. The descaling method characterized by adjusting the clearance gap between the lower end of the scraper and the surface of the material to be rolled so as to be at least%. 被圧延材の表面に生成したスケールを噴射圧が10MPa以上の高圧水の噴射によって除去するための噴射ノズルと、該噴射ノズルから噴射された水を回収するため、該噴射ノズルの被圧延材搬送ライン上流側に設置されるスクレーパとを備えたデスケーリング設備であって、前記スクレーパの下端と被圧延材の表面との間に隙間Sgを設けるとともに、前記噴射ノズルから噴射された高圧水が被圧延材の表面に衝突する位置と前記スクレーパの下端との被圧延材搬送方向の距離Lsと、前記隙間Sgとが下式を満足することを特徴とするデスケーリング設備。
100mm≦Ls≦700mm
tan-1(Sg/Ls)≦0.8°
An injection nozzle for removing the scale generated on the surface of the material to be rolled by jetting high-pressure water having an injection pressure of 10 MPa or more, and the material to be rolled of the jet nozzle for recovering the water jetted from the nozzle. A descaling facility including a scraper installed on the upstream side of the line, wherein a gap Sg is provided between a lower end of the scraper and the surface of the material to be rolled, and high-pressure water sprayed from the spray nozzle is covered with A descaling facility characterized in that the distance Ls in the direction of the material to be rolled between the position of the rolled material that collides with the surface of the rolled material and the lower end of the scraper, and the gap Sg satisfy the following equation.
100mm ≦ Ls ≦ 700mm
tan −1 (Sg / Ls) ≦ 0.8 °
JP2004219450A 2004-07-28 2004-07-28 Descaling method and descaling equipment in hot rolling Expired - Fee Related JP4370996B2 (en)

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JP2011230144A (en) * 2010-04-26 2011-11-17 Nippon Steel Corp Flashing device and flashing method for descaling injection water
KR101225710B1 (en) 2010-10-27 2013-01-23 현대제철 주식회사 Apparatus for removing remained water from hot coil
JP5974749B2 (en) * 2012-09-12 2016-08-23 Jfeスチール株式会社 Descaling equipment and descaling method
CN109201759A (en) * 2018-09-19 2019-01-15 陕西龙门钢铁有限责任公司 A kind of steel billet is come out of the stove dephosphorization apparatus and phosphorus removing method before rolling

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