JPS6316207B2 - - Google Patents
Info
- Publication number
- JPS6316207B2 JPS6316207B2 JP57156508A JP15650882A JPS6316207B2 JP S6316207 B2 JPS6316207 B2 JP S6316207B2 JP 57156508 A JP57156508 A JP 57156508A JP 15650882 A JP15650882 A JP 15650882A JP S6316207 B2 JPS6316207 B2 JP S6316207B2
- Authority
- JP
- Japan
- Prior art keywords
- descaling
- pressure
- width direction
- slurry
- pressure water
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B21—MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
- B21B—ROLLING OF METAL
- B21B45/00—Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills
- B21B45/04—Devices 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 de-scaling, e.g. by brushing
- B21B45/08—Devices 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 de-scaling, e.g. by brushing hydraulically
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
Description
【発明の詳細な説明】
本発明は鋼板の湿式ブラスト脱スケール法に関
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a wet blast descaling method for steel plates.
最近例えば砂鉄粒を混入したスラリーを高圧下
に投射するメカニカル脱スケール法(以下湿式ブ
ラスト脱スケール法という)が開発され、例えば
熱延鋼帯のスケール除去に適用されている。従
来、湿式ブラストデスケーリング設備に於て、板
巾方向に高圧水圧力を調節する装置は存在せず、
従つてヘツダーの巾方向の高圧水圧力はすべて一
定である。一方、デスケーリング設備に通板され
る原板は前工程に於ける製造条件、デスケーリン
グ設備に通板される前のコイルの仕掛り条件等に
より板巾方向の酸化膜厚み及び組成は必らずしも
同じではない。この様な巾方向で酸化膜条件の異
なる金属板を、巾方向で一定の高圧水圧力に保た
れた湿式ブラストデスケーリング設備で処理した
場合、当然巾方向のデスケーリングむらが発生す
ることとなる。 Recently, a mechanical descaling method (hereinafter referred to as a wet blast descaling method) in which a slurry containing iron sand particles is blasted under high pressure has been developed, and has been applied, for example, to remove scale from hot rolled steel strips. Conventionally, in wet blast descaling equipment, there was no device to adjust high pressure water pressure in the width direction of the board.
Therefore, the high pressure water pressure in the width direction of the header is all constant. On the other hand, the thickness and composition of the oxide film in the width direction of the original sheet passed through the descaling equipment may vary depending on the manufacturing conditions in the previous process, the conditions of the coil before being passed through the descaling equipment, etc. It's not the same either. If such a metal plate with different oxide film conditions in the width direction is processed using wet blast descaling equipment that maintains a constant high water pressure in the width direction, uneven descaling in the width direction will naturally occur. .
従来はこのむら防止のため、最もデスケーリン
グ状態の悪い部分に合せて、ヘツダー全体の高圧
水圧力を与える必要があり、これによつて巾方向
のデスケーリングされ易い部分はオーバデスケー
リング状態となつており、このためポンプモータ
の電力及び通板材のオーバデスケーリングによる
歩留面での損失を余儀なくされている。 Conventionally, in order to prevent this unevenness, it was necessary to apply high water pressure to the entire header according to the part with the worst descaling condition, and as a result, the part that is easily descaled in the width direction becomes over-descaled. As a result, losses are inevitable in terms of yield due to pump motor power and over-descaling of the threaded material.
一般に、熱延後の鋼板の酸化膜の脱スケール性
は、両端部が最も優れており、次いで中央部が良
く、残りの中央部と両端部にはさまれた50〜150
mm巾の部分が最も脱スケール性が悪い傾向にあ
る。この状況を第1図に示す。 In general, the descaling property of the oxide film on a steel sheet after hot rolling is the best at both ends, followed by the center, and the remaining 50 to 150
The mm-wide portion tends to have the worst descaling properties. This situation is shown in Figure 1.
図に於て1,2,3の順に脱スケール性は悪く
なつている。この様な材料をデスケーリングする
場合、従来高圧水の圧力設定は最も脱スケール性
の悪い3の部分のデスケーリング状況に合せて行
なわれるため、1及び2の部分に於てはオーバデ
スケーリングの状態となつており、高圧ポンプの
駆動モータの電力の有効利用及び1,2部分の地
鉄研削による通板歩留り低下、地鉄への砂鉄喰込
みによる成品々位の低下等の問題がある。 In the figure, descaling performance worsens in the order of 1, 2, and 3. When descaling such materials, the pressure of high-pressure water is conventionally set according to the descaling status of the 3 parts with the worst descaling properties, so in the 1 and 2 parts, there is no possibility of over-descaling. There are problems such as effective use of the electric power of the drive motor of the high-pressure pump, a decrease in the threading yield due to grinding of one or two sections of the base metal, and a decline in the quality of the finished product due to sand being eaten into the base metal.
一方従来の酸洗法による脱スケールは酸による
化学的脱スケールであり、脱スケールが完了する
と地鉄が露出して来るが、酸洗溶液中には抑制剤
が添加されており、これが地鉄表面に作用して地
鉄の酸蝕は進行せず、只スケールのみが溶解、剥
離するだけで上記の如き問題はない。 On the other hand, descaling by the conventional pickling method is chemical descaling using acid, and when descaling is completed, the bare steel is exposed, but an inhibitor is added to the pickling solution, which prevents the bare steel from being removed. The acid corrosion of the base iron does not proceed on the surface, and only the scale dissolves and peels off, so there is no problem as described above.
第2図は従来の巾方向高圧水圧力制御を行なわ
ない場合のノズルヘツダー部の略図、第3図は第
2図のa−a矢視図を示す。図に於て高圧水は1
より入り、高圧水室2より各ノズル3へ高圧水孔
を通して分配される。第3図に於てノズル3の高
圧水は、高圧水孔4よりノズル3の先端部に設け
られた高圧水噴出孔5に入つて噴射される。砂鉄
スラリーは導入管6より入りノズル中心部を通つ
て流出する。 FIG. 2 is a schematic diagram of a nozzle header section when conventional width direction high pressure water pressure control is not performed, and FIG. 3 is a view taken along the line aa in FIG. 2. In the figure, high pressure water is 1
The high-pressure water enters the high-pressure water chamber 2 and is distributed to each nozzle 3 through high-pressure water holes. In FIG. 3, high-pressure water from the nozzle 3 enters a high-pressure water jet hole 5 provided at the tip of the nozzle 3 through a high-pressure water hole 4 and is jetted. The iron sand slurry enters through the introduction pipe 6 and flows out through the center of the nozzle.
ヘツダーに流入する高圧水1は、ラインスピー
ド及び板巾に従つて圧力制御を行なわれるが、ヘ
ツダ内部で各ノズルに共通に導かれるため、巾方
向の圧力変更は行なえない構造となつている。即
ち研掃材を高圧水で加速して、金属材に投射して
表面酸化膜を除去する湿式ブラストデスケーリン
グ設備に於て、従来そのデスケーリング能力は高
圧水の圧力に依存しており、デスケーリング能力
は高圧水圧力変更により行なわれる。 The pressure of high-pressure water 1 flowing into the header is controlled according to the line speed and width of the plate, but since it is commonly guided to each nozzle inside the header, the pressure cannot be changed in the width direction. In other words, in wet blast descaling equipment that accelerates the abrasive material with high-pressure water and projects it onto the metal material to remove the surface oxide film, the descaling ability has conventionally depended on the pressure of the high-pressure water. Scaling capability is achieved by high pressure water pressure changes.
従来行なわれている高圧水圧力変更は、1ヘツ
ダー内の巾方向ノズルについて、個別に高圧水圧
力調節は行なわれていないため、金属板の巾方向
の酸化膜残りによるデスケーリングむらに対して
はコントロール不可能であつた。 The conventional high-pressure water pressure change is not performed individually for the width direction nozzles in one header, so it is difficult to deal with descaling unevenness due to oxide film remaining in the width direction of the metal plate. It was out of control.
本発明は、これらの問題点を解消するため、金
属板のデスケーリング状態に合せて、板巾方向の
高圧水圧力の制御を行うことを目的としたもので
ある。 In order to solve these problems, the present invention aims to control the high pressure water pressure in the width direction of the metal plate in accordance with the descaling state of the metal plate.
即ち本発明は金属板の製造過程において発生す
る巾方向酸化膜の厚み差や、酸化膜組織の違いに
よつて生ずる巾方向のデスケーリングむらを解消
するようヘツダーの巾方向に於ける脱スケール性
能の調整を行うことを特徴とするものである。 That is, the present invention improves the descaling performance in the width direction of the header in order to eliminate uneven descaling in the width direction caused by differences in the thickness of the oxide film in the width direction and differences in the structure of the oxide film that occur during the manufacturing process of the metal plate. It is characterized by making adjustments.
第4図は本発明の一実施例の説明図である。金
属板表面酸化膜のデスケーリング性パターンを示
す第1図に基づいて、板巾方向の高圧水圧力制御
が行えるよう、高圧水室2をブロツク分けし、各
ブロツク毎に高圧水を別系統より導くようにし、
各系統に圧力調節弁等により圧力制御機能を持た
せている。 FIG. 4 is an explanatory diagram of one embodiment of the present invention. Based on Figure 1 showing the descaling pattern of the oxide film on the surface of the metal plate, the high-pressure water chamber 2 is divided into blocks so that high-pressure water pressure can be controlled in the width direction of the plate, and high-pressure water is supplied to each block from a separate system. Let me guide you.
Each system has a pressure control function using pressure regulating valves, etc.
第4図に於て高圧水室2は隔壁a,b,c,d
により,,,,の各室に分離されてい
る。酸化膜のデスケーリングパターンによると
と、とはほぼ同じデスケーリング性を示す
ことにより、これらは連結して、最終的にはイ,
ロ,ハの3ブロツクに分離して、それぞれのブロ
ツクに圧力調節弁A,B,Cを設置して、ストリ
ツプの巾方向デスケーリング状況に合せて、個別
に高圧水圧力調整が行なえる。2−3は高圧水ノ
ズルへの流路を示す。 In Figure 4, the high-pressure water chamber 2 has partition walls a, b, c, and d.
It is separated into , , , chambers. According to the descaling pattern of the oxide film, by showing almost the same descaling property as , these are connected and eventually become i,
It is divided into three blocks (B and C), and pressure regulating valves A, B, and C are installed in each block, so that high-pressure water pressure can be adjusted individually according to the descaling situation of the strip in the width direction. 2-3 shows the flow path to the high pressure water nozzle.
制御を更に緻密に行うため、高圧水室2の分割
数を増加すること及び高圧水室と、との
連結を行なわず、各分割された小室ごとに圧力コ
ントロールを行うことも可能である。又圧力制御
は調節弁の開度コントロールによるものの他に各
ブロツク毎に高圧ポンプを設けてその回転数コン
トロールによる方法も可能である。 In order to perform more precise control, it is also possible to increase the number of divisions of the high-pressure water chamber 2 and to perform pressure control for each divided small chamber without connecting it to the high-pressure water chamber. In addition to controlling the opening of the control valve, the pressure can also be controlled by providing a high-pressure pump for each block and controlling its rotation speed.
各ブロツク毎の圧力制御は、ラインスピード及
び板巾により求まる圧力によつて得られるデスケ
ーリング後の板表面仕上り状況により、オペレー
タが手動介入により高圧水圧力の上げ、下げを行
う方法や、この他、デスケーリング後の板表面の
残留スケール検出器信号により自動的に巾方向及
び長手方向の圧力制御を行うこともできる。 Pressure control for each block involves manual intervention by the operator to increase or decrease the high-pressure water pressure, depending on the surface finish of the plate after descaling, which is determined by the line speed and the pressure determined by the plate width. It is also possible to automatically control the pressure in the width direction and longitudinal direction based on the residual scale detector signal on the plate surface after descaling.
本発明の他の実施例として第5図に示した両端
に仕切り壁のある金属円筒を挿入する方法(1)及び
ヘツダ自体を分割して製作した後、これらを連結
する方法(2)等がある。第5図1に於て,,
,,は分割された金属円筒2−1を示し、
これを第1図の高圧水室2へ順次、端部から押込
んでいくことを示している。又第5図2は複数の
高圧水室2−2を配設して一体化した構成を示し
ている。 Other embodiments of the present invention include a method (1) of inserting a metal cylinder with partition walls at both ends as shown in FIG. be. In Figure 5 1,
,, indicates the divided metal cylinder 2-1,
This is shown to be sequentially pushed into the high pressure water chamber 2 of FIG. 1 from the end. Further, FIG. 5 2 shows a structure in which a plurality of high pressure water chambers 2-2 are arranged and integrated.
なお脱スケールすべきほとんどの種類の鋼板
が、例えば第1図に示すような巾方向の脱スケー
ル性難度分布を有することを予測して、あらかじ
め各位置のノズルの能力設計において、例えば脱
スケール性の悪い部分のノズルはその流量などの
容量を大きくしておけば良い。 It should be noted that, in anticipation of the fact that most types of steel plates to be descaled have a descaling difficulty distribution in the width direction as shown in Fig. 1, for example, the descaling difficulty is The nozzles in the areas with poor performance should have a large capacity such as flow rate.
即ちデスケーリング能力の変更は、高圧水圧力
の変更による他、研掃材として与えられるスラリ
ーの流量又はスラリーの濃度によつても変更でき
ることが知られている。これは研掃材の多少によ
つて脱スケール能率が変化する現象である。この
ことを利用して前述したような高圧水圧力を鋼板
巾方向に変更する方法によらず、スラリーの流量
又はスラリーの濃度を巾方向変更する方法が可能
である。スラリーの流量、濃度の変更は高圧水圧
力の変更を行なう方法と比べればその効果は劣
る。 That is, it is known that the descaling ability can be changed not only by changing the high water pressure but also by changing the flow rate of the slurry applied as the abrasive material or the concentration of the slurry. This is a phenomenon in which the descaling efficiency changes depending on the amount of abrasive used. Utilizing this fact, it is possible to use a method of changing the slurry flow rate or slurry concentration in the width direction, instead of using the above-described method of changing the high water pressure in the width direction of the steel plate. Changing the slurry flow rate and concentration is less effective than changing the high water pressure.
即ち高圧水圧力の変更による方法では、オーバ
ーデスケーリングの防止により脱スケールに要す
る電力の節約をも図ることが可能であるのに対
し、スラリーの流量又は濃度の変更による方法で
は、オーバーデスケーリングによる通板歩留ロス
及びデスケーリングむら発生による成品品質低下
等は防止できるが、スラリーの流量、濃度にかか
わらず投射される高圧水の消費する脱スケール電
力の節約は期待できないためである。 In other words, with the method of changing high water pressure, it is possible to save the power required for descaling by preventing over-descaling, whereas with the method of changing the slurry flow rate or concentration, it is possible to save the power required for descaling by preventing over-descaling. This is because although it is possible to prevent product quality degradation due to sheet threading yield loss and descaling unevenness, it is not possible to save the descaling power consumed by the high-pressure water that is projected regardless of the flow rate or concentration of the slurry.
しかしながらスラリーの流量、濃度の変更は高
圧水の圧力変更に比べて、低圧系を取り扱うため
比較的簡便に行なうことができる利点がある。 However, compared to changing the pressure of high-pressure water, changing the flow rate and concentration of the slurry has the advantage that it can be done relatively easily because it deals with a low-pressure system.
スラリー流量を変更する装置の例を第6図に、
又スラリー濃度の変更を行なう装置の例を第7図
に示す。第6図において1〜3はスラリーの流量
を変更するための絞り弁、4〜10は噴射ノズル
を示している。各ノズルのブロツク毎の絞り弁は
鋼板のスケール分布又は脱スケール后の鋼板性状
により調整を行う。このようにスラリーの流量を
巾方向に変えうる装置により前述した目的が達成
できる。 Figure 6 shows an example of a device that changes the slurry flow rate.
FIG. 7 shows an example of an apparatus for changing the slurry concentration. In FIG. 6, reference numerals 1 to 3 indicate throttle valves for changing the flow rate of slurry, and reference numerals 4 to 10 indicate injection nozzles. The throttle valve for each block of each nozzle is adjusted depending on the scale distribution of the steel plate or the properties of the steel plate after descaling. The above-mentioned object can be achieved by a device that can change the flow rate of the slurry in the width direction.
第7図において1〜3は補給水濃度を変更する
ための絞り弁、4〜6はスラリー補給系統、7〜
9はスラリータンク、10〜12はスラリーのア
ジテータ、4〜10はノズルである。各ノズルの
ブロツク毎の絞り弁は鋼板のスケール分布又は脱
スケール后の鋼板性状により調整を行うが、この
絞り弁の調整により補給水量が変化し、従つてス
ラリータンク内のスラリーの希釈の程度が変化す
るので、これによりスラリー濃度が変化し、脱ス
ケール能力を巾方向に変化させることができる。 In Fig. 7, 1 to 3 are throttle valves for changing the makeup water concentration, 4 to 6 are slurry supply systems, and 7 to
9 is a slurry tank, 10 to 12 are slurry agitators, and 4 to 10 are nozzles. The throttle valve for each block of each nozzle is adjusted depending on the scale distribution of the steel plate or the properties of the steel plate after descaling, but the adjustment of this throttle valve changes the amount of replenishment water, and therefore the degree of dilution of the slurry in the slurry tank. This changes the slurry concentration and allows the descaling ability to vary across the width.
スラリーの濃度、流量の可変化を行なうには単
に第6図、第7図に示した例にとどまらずスラリ
ー生成機構に遡つて多重化した装置も適用でき
る。 In order to vary the concentration and flow rate of the slurry, it is possible to apply not only the examples shown in FIGS. 6 and 7 but also a device in which the slurry generation mechanism is multiplexed.
以上の通り本発明によるときは鋼板の巾方向の
高圧水圧力を制御して脱スケール性能を調整し、
デスケーリングのむらの発生を解消し得て、その
工業的効果は大きい。 As described above, according to the present invention, the descaling performance is adjusted by controlling the high pressure water pressure in the width direction of the steel plate,
It is possible to eliminate the occurrence of uneven descaling, and the industrial effects thereof are great.
第1図ほ脱スケール率の板巾分布のグラフ、第
2図は従来法の投射ノズル説明図、第3図は第2
図a−a矢視図、第4図は本発明の説明図、第5
図は本発明の他の例の説明図、第6図は本発明の
他の例の説明図、第7図は本発明の更に他の例の
説明図である。
1:高圧水、2:高圧水室、3:ノズル、4:
高圧水孔、A,B,C:圧力調節弁。
Figure 1 is a graph of the width distribution of the descaling rate, Figure 2 is an explanatory diagram of the conventional projection nozzle, and Figure 3 is the graph of the width distribution of the descaling rate.
Figure a-a arrow view, Figure 4 is an explanatory diagram of the present invention, Figure 5
The figures are explanatory diagrams of another example of the present invention, FIG. 6 is an explanatory diagram of another example of the present invention, and FIG. 7 is an explanatory diagram of still another example of the present invention. 1: High pressure water, 2: High pressure water chamber, 3: Nozzle, 4:
High pressure water hole, A, B, C: Pressure control valve.
Claims (1)
り脱スケールするにあたり、前記湿式ブラストノ
ズル群を、鋼板の巾方向に複数のブロツクに区画
して、鋼板巾方向の脱スケール状況に応じて、そ
れぞれのブロツク系統の高圧水圧力、スラリー
量、スラリー濃度の少なくとも一つを鋼板の巾方
向に調整することを特徴とする鋼板の脱スケール
方法。1. When descaling a continuously running steel plate by wet blasting, the wet blast nozzle group is divided into a plurality of blocks in the width direction of the steel plate, and each block is descaled according to the descaling situation in the width direction of the steel plate. A method for descaling a steel plate, comprising adjusting at least one of the high water pressure of a block system, the amount of slurry, and the concentration of slurry in the width direction of the steel plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15650882A JPS5947013A (en) | 1982-09-10 | 1982-09-10 | Descaling method of steel plate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15650882A JPS5947013A (en) | 1982-09-10 | 1982-09-10 | Descaling method of steel plate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5947013A JPS5947013A (en) | 1984-03-16 |
| JPS6316207B2 true JPS6316207B2 (en) | 1988-04-07 |
Family
ID=15629292
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15650882A Granted JPS5947013A (en) | 1982-09-10 | 1982-09-10 | Descaling method of steel plate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5947013A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5979143A (en) * | 1982-10-28 | 1984-05-08 | Toyota Motor Corp | Measuring and detecting method of wear quantity of grindstone |
| JPS62127430A (en) * | 1985-11-26 | 1987-06-09 | Sumitomo Metal Mining Co Ltd | How to recover cadmium |
| JPS62188734A (en) * | 1986-02-14 | 1987-08-18 | Sumitomo Metal Mining Co Ltd | Method for recovering high-purity cement cadmium from acidic aqueous solution containing thallium and cadmium sulfate |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5195938A (en) * | 1975-02-20 | 1976-08-23 | HYOMENSHORISOCHI | |
| JPS54176727U (en) * | 1978-06-02 | 1979-12-13 | ||
| JPS5660517U (en) * | 1979-10-09 | 1981-05-23 |
-
1982
- 1982-09-10 JP JP15650882A patent/JPS5947013A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5947013A (en) | 1984-03-16 |
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