JPH07100217B2 - Thin plate manufacturing equipment - Google Patents
Thin plate manufacturing equipmentInfo
- Publication number
- JPH07100217B2 JPH07100217B2 JP24477087A JP24477087A JPH07100217B2 JP H07100217 B2 JPH07100217 B2 JP H07100217B2 JP 24477087 A JP24477087 A JP 24477087A JP 24477087 A JP24477087 A JP 24477087A JP H07100217 B2 JPH07100217 B2 JP H07100217B2
- Authority
- JP
- Japan
- Prior art keywords
- stirrer
- semi
- stirring
- temperature
- thin plate
- 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 - Fee Related
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 14
- 238000003756 stirring Methods 0.000 claims description 49
- 239000002002 slurry Substances 0.000 claims description 40
- 239000002184 metal Substances 0.000 claims description 27
- 238000005096 rolling process Methods 0.000 claims description 14
- 239000007790 solid phase Substances 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 7
- 238000001816 cooling Methods 0.000 description 17
- 239000007787 solid Substances 0.000 description 15
- 239000013078 crystal Substances 0.000 description 9
- 210000004027 cell Anatomy 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000002826 coolant Substances 0.000 description 3
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 210000001787 dendrite Anatomy 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/10—Supplying or treating molten metal
- B22D11/11—Treating the molten metal
- B22D11/112—Treating the molten metal by accelerated cooling
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Continuous Casting (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、薄板製造装置に関するものである。The present invention relates to a thin plate manufacturing apparatus.
[従来の技術] 従来の薄板製造装置を第6図により説明すると、内部冷
却されている二つのロール1,2を水平に配設し、該ロー
ル1,2上にバレルシール板とサイドシール板で囲まれた
容器3を設け、容器3内に溶湯4を供給すると共にロー
ル1,2を図中矢印bで示すように互いに対向部を下向き
に回転し、溶湯4をロール1,2で冷却してロール1,2表面
に凝固殻5を形成し、表面に凝固殻5を形成しつつある
溶湯4をロール1,2の回転によりロール1,2間から引出し
その後徐々に凝固殻5を成長させて薄板6を製造してい
た。[Prior Art] Referring to FIG. 6, a conventional thin plate manufacturing apparatus will be described. Two internally cooled rolls 1 and 2 are horizontally arranged, and a barrel seal plate and a side seal plate are provided on the rolls 1 and 2. The container 3 surrounded by is provided, the molten metal 4 is supplied into the container 3, and the rolls 1 and 2 are rotated so that their facing portions face downward as shown by an arrow b in the figure, and the molten metal 4 is cooled by the rolls 1 and 2. Then, the solidified shell 5 is formed on the surface of the rolls 1 and 2, and the molten metal 4 which is forming the solidified shell 5 on the surface is pulled out from between the rolls 1 and 2 by the rotation of the rolls 1 and 2 and thereafter the solidified shell 5 is gradually grown. Then, the thin plate 6 was manufactured.
しかし上記の薄板製造装置では、溶湯4は、粘性が低い
ためロール1,2と容器3の間aに入り込み、外部へ漏れ
たり、或いはロール1,2と容器3の間aに入り込んだ溶
湯4が凝固してできたバリがはがれてロール1,2間の凝
固殻5を形成しつつある溶湯4内に入り込み、凝固殻5
の生長を悪化し且つ不均一にさせて、凝固殻5が途中で
切れてしまういわゆるブレイクアウトを起こしたり、或
いは製造された薄板6の強度が弱くなる原因となってい
た。However, in the thin plate manufacturing apparatus described above, the molten metal 4 has a low viscosity and enters the space a between the rolls 1 and 2 and the container 3 and leaks to the outside, or the molten metal 4 that enters the space a between the rolls 1 and 2 and the container 3. The burr formed by the solidification of the ash peels off and enters the molten metal 4 that is forming the solidified shell 5 between the rolls 1 and 2, and the solidified shell 5
Of the coagulation shell 5 is deteriorated and made non-uniform, causing a so-called breakout in which the solidified shell 5 is cut in the middle, or the strength of the manufactured thin plate 6 is weakened.
又、ロール1,2と容器3の間に溶湯4が入り込むことに
より容器3の損傷を引起していた。Further, the molten metal 4 entered between the rolls 1 and 2 and the container 3, causing damage to the container 3.
そこで斯かる問題点を解決するために近年、第7図に示
すように、容器3内部にロール1,2の軸線方向に延びる
内部冷却可能な多角形状の攪拌棒7を図示しない駆動装
置によって回転自在に設け、容器3の外側を囲むように
冷却媒体を流通させる冷却管から成る冷却装置8を配設
して、容器3内に供給された溶湯を冷却装置8を用いて
固液共存温度域まで冷却し、次に攪拌棒7を回転させ固
液共存温度域まで冷却された溶湯に機械的攪拌を与えて
微細結晶粒を含む、粘性の高い半凝固スラリーを形成し
た後、該半凝固スラリーを前記と同様にロール1,2間で
冷却し薄板6を製造するようにして、粘性の高い半凝固
スラリーが容器3とロール1,2の間に入り込むことを防
止し、外部への半凝固スラリーのもれをなくし、又強度
が高く良質な薄板6を製造すると共に、容器3の破損等
を防止し得る薄板製造装置が提案されている。Therefore, in order to solve such a problem, in recent years, as shown in FIG. 7, an internally-coolable polygonal stirring rod 7 extending in the axial direction of the rolls 1 and 2 inside the container 3 is rotated by a driving device (not shown). A cooling device 8 including a cooling pipe that freely provides and surrounds the outside of the container 3 to circulate a cooling medium is provided, and the molten metal supplied into the container 3 is used by the cooling device 8 in a solid-liquid coexisting temperature range. After that, the stirring rod 7 is rotated and mechanical stirring is applied to the molten metal cooled to the solid-liquid coexistence temperature range to form a highly viscous semi-solidified slurry containing fine crystal grains. In the same manner as above, the thin plate 6 is manufactured by cooling between the rolls 1 and 2 to prevent the highly viscous semi-solidified slurry from entering between the container 3 and the rolls 1 and 2, and to semi-solidify to the outside. Produces a thin plate 6 with high strength and high strength that eliminates leakage of slurry While, the thin plate manufacturing apparatus has been proposed which can prevent the breakage of the container 3.
[発明が解決しようとする問題点] しかしながら、上記した薄板製造装置では、例えば、溶
湯を固液共存温度域まで冷却するのに容器3の外側に冷
却装置8を設けているため、溶湯は容器3の外側に近い
程冷却が早く進行し、攪拌される溶湯の温度即ち攪拌温
度は常に容器3の外側に近い程低くなるので溶湯4全体
の攪拌温度が安定しない。このように攪拌温度が安定し
ないまま半凝固スラリーを形成すると、例えば攪拌温度
が低い場合には、形成される半凝固スラリー中の微細結
晶粒の固相率が増大し半凝固スラリーの粘性が高くなり
すぎて流動性が著しく悪化し、反対に攪拌温度が高い場
合には半凝固スラリーの固相率が減少し粘性が低く流動
性が良好になる等半凝固スラリーの粘性が一定しないた
め、ロール1,2間には半凝固スラリーが安定して供給さ
れにくくなり、ロール1,2間から引出された薄板6の形
状が悪化してしまうという問題があった。[Problems to be Solved by the Invention] However, in the above-described thin plate manufacturing apparatus, for example, since the cooling device 8 is provided outside the container 3 to cool the molten metal to the solid-liquid coexistence temperature range, the molten metal is stored in the container. The closer the temperature is to the outside of the container 3, the faster the cooling progresses, and the temperature of the molten metal to be stirred, that is, the stirring temperature, is always lower to the outside of the container 3, so that the stirring temperature of the entire molten metal 4 is not stable. When the semi-solidified slurry is formed without the stirring temperature being stable in this way, for example, when the stirring temperature is low, the solid phase ratio of the fine crystal grains in the formed semi-solidified slurry increases and the viscosity of the semi-solidified slurry becomes high. When the stirring temperature is high, the solid fraction of the semi-solidified slurry decreases and the viscosity becomes low and the fluidity becomes good. There is a problem that it becomes difficult to stably supply the semi-solidified slurry between the rolls 1 and 2, and the shape of the thin plate 6 drawn out from between the rolls 1 and 2 deteriorates.
本発明は、上述の実情に鑑み、冷却装置を容器の外側に
設けた場合でも良好な形状の薄板を製造し得るようにし
た薄板製造装置を提供することを目的とするものであ
る。In view of the above situation, it is an object of the present invention to provide a thin plate manufacturing apparatus capable of manufacturing a thin plate having a good shape even when the cooling device is provided outside the container.
[問題点を解決するための手段] 本発明は、溶湯の流入量調節装置を備えた攪拌装置に、
該攪拌装置内部の固液共存温度域まで冷却された溶湯を
機械的に攪拌して半凝固スラリーを形成する回転自在な
撹攪棒を取付け、前記攪拌装置の下流に内部冷却し得る
ようにした一対の無端状の移動鋳型を配設し、又、前記
攪拌装置に攪拌装置内部の温度を検出する温度検出器を
設け、前記攪拌棒に回転数検出器を取付け、前記移動鋳
型に圧延荷重を検出する荷重計を或いは前記移動鋳型又
は攪拌棒の一方に駆動電流を検出する電流計を接続し、
更に前記荷重計或いは電流計からの圧延荷重或いは駆動
電流と温度検出器からの温度を入力して半凝固スラリー
の固相率を求める第1の演算器と、該演算器からの固相
率と前記回転数検出器からの攪拌棒の回転数を入力して
注湯量を求め前記流入量調節装置に指令を送る第2の演
算器を設け、薄板製造装置としたものである。[Means for Solving the Problems] The present invention provides a stirring device equipped with a device for adjusting the inflow amount of molten metal,
A rotatable stirring bar that mechanically stirs the molten metal cooled to the solid-liquid coexisting temperature range inside the stirrer to form a semi-solidified slurry was provided so that internal cooling could be performed downstream of the stirrer. A pair of endless moving molds are arranged, a temperature detector for detecting the temperature inside the stirring device is provided in the stirring device, a rotation speed detector is attached to the stirring rod, and a rolling load is applied to the moving mold. Connect a load cell to detect or connect an ammeter to detect the drive current to one of the moving mold or the stirring rod,
Furthermore, a first calculator for determining the solid phase ratio of the semi-solidified slurry by inputting the rolling load or drive current from the load meter or ammeter and the temperature from the temperature detector, and the solid phase ratio from the calculator. A thin plate manufacturing apparatus is provided with a second arithmetic unit for inputting the rotation speed of the stirring rod from the rotation speed detector to obtain the pouring amount and sending a command to the inflow amount adjusting device.
[作用] 従って、本発明では、第1の演算器は荷重計からの圧延
荷重或いは電流計からの駆動電流と温度検出器からの攪
拌装置内部の温度を入力して半凝固スラリーの固相率を
求め、第2の演算器は第1の演算器からの固相率と回転
数検出器からの攪拌棒の回転数を入力し注湯量を求め流
入量調節装置に指令を送り、流入量調節装置は第2の演
算器からの指令を受けると開度が変わり半凝固スラリー
の固相率及び攪拌棒の回転数に応じた最適な注湯量にし
て半凝固スラリーの粘性を適正化するので、移動鋳型間
には半凝固スラリーが安定して供給され、良好な形状の
薄板が製造される。[Operation] Therefore, in the present invention, the first computing unit inputs the rolling load from the load meter or the driving current from the ammeter and the temperature inside the stirrer from the temperature detector to obtain the solid fraction of the semi-solidified slurry. The second calculator inputs the solid phase ratio from the first calculator and the rotation speed of the stirring rod from the rotation speed detector to obtain the pouring amount and sends a command to the inflow amount adjusting device to adjust the inflow amount. When the apparatus receives a command from the second computing unit, the opening changes and the viscosity of the semi-solidified slurry is optimized by setting the optimum pouring amount according to the solid fraction of the semi-solidified slurry and the rotation speed of the stirring rod. The semi-solidified slurry is stably supplied between the moving molds, and a thin plate having a good shape is manufactured.
[実 施 例] 以下、本発明の実施例を図面を参照して説明する。[Examples] Examples of the present invention will be described below with reference to the drawings.
第1図乃至第3図は本発明の一実施例の説明図である。1 to 3 are explanatory views of an embodiment of the present invention.
タンディッシュ9の下流に攪拌装置10を設け、タンディ
ッシュ9と攪拌装置10を真空チャンバ11内に収納すると
共に、攪拌装置10の下流に内部冷却可能な一対の無端状
の移動鋳型、例えばロール1,2を水平に配設する。A stirrer 10 is provided downstream of the tundish 9, the tundish 9 and the stirrer 10 are housed in a vacuum chamber 11, and a pair of endless movable molds that can be internally cooled downstream of the stirrer 10, for example, a roll 1 , 2 are arranged horizontally.
前記タンディッシュ9は真空チャンバ11に取付けたシリ
ンダ50及び該シリンダ50先端に取付けた弁体49から成る
流入量調節装置を備えており攪拌装置10への溶湯4の供
給量(注湯量)を調節し得るようになっている。The tundish 9 is provided with an inflow amount adjusting device including a cylinder 50 attached to the vacuum chamber 11 and a valve body 49 attached to the tip of the cylinder 50, and adjusts the supply amount (the pouring amount) of the molten metal 4 to the stirring device 10. Is ready to go.
前記攪拌装置10は、水平に二つの円筒状の攪拌室12,13
を形成するケーシング14を有し、該ケーシング14の攪拌
室12,13のそれぞれに攪拌室12,13の軸線方向に延びる内
部冷却可能な攪拌棒15,16を後述するように回転自在に
設け、攪拌室12,13の下流中間部に仕切板18及び熱電対
等の非接触式の温度検出器48を設け、ケーシング14の外
側に冷却媒体を流通させる冷却管から成る冷却装置17を
配設している。(第1図) 前記攪拌棒15,16は、軸部19,20を軸受21,22を介して薄
板製造装置のハウジング或いは真空チャンバ11の外壁に
回転自在に支承すると共に、攪拌装置10と軸部19,20と
の貫通部をシール24,25により溶湯もれをシールし、
又、軸部19,20の一端をカップリング26,27を介して減速
器28に接続する。該減速器28にカップリング29を介して
モータ30等の駆動装置を接続し、軸部20の他端にパルス
ジェネレータ等の回転数検出器51を取付ける。(第2
図) 又前記ロール1は、軸部31を軸受32を用いて回転自在に
支承し、該軸受32を真空チャンバ11と一体のハウジング
23に取付け、ガタ殺し用のスプリング33で固定する。The stirrer 10 comprises two cylindrical stirring chambers 12 and 13 horizontally.
Having a casing 14 that forms a stirrer chamber 12, 13 of the casing 14, each stirrer rod 15, 16 that can be internally cooled extending in the axial direction of the stirrer chamber 12, 13 is rotatably provided as described later, A non-contact type temperature detector 48 such as a partition plate 18 and a thermocouple is provided in the downstream intermediate portion of the stirring chambers 12 and 13, and a cooling device 17 including a cooling pipe for circulating a cooling medium is provided outside the casing 14. There is. (FIG. 1) The stirring rods 15 and 16 rotatably support the shaft portions 19 and 20 via bearings 21 and 22 on the housing of the thin plate manufacturing apparatus or the outer wall of the vacuum chamber 11, and the stirring device 10 and the shafts. Sealing the penetrations with parts 19 and 20 by sealing 24 and 25,
Further, one ends of the shaft portions 19, 20 are connected to the speed reducer 28 via the couplings 26, 27. A drive device such as a motor 30 is connected to the decelerator 28 via a coupling 29, and a rotation speed detector 51 such as a pulse generator is attached to the other end of the shaft portion 20. (Second
(Fig.) In the roll 1, a shaft 31 is rotatably supported by a bearing 32, and the bearing 32 is integrated with the vacuum chamber 11 in a housing.
Attach it to 23 and secure it with spring 33 for killing backlash.
前記ロール2は軸部34を軸受35を用いて回転自在に支承
し、該軸受35を前記ハウジング23に形成した水平方向に
延びる長穴36にスライド可能に取付け、軸受35のロール
1と反対側に荷重計37a,37b(荷重計に代えて電流計を
後述の駆動装置或いは攪拌棒15,16の駆動装置に設ける
ようにしても良いが、以後荷重計として説明する)を取
付け、該荷重計37a,37bと軸受35をロッドが水平方向に
延びるシリンダ38でロール1と反対側から押さえ付ける
と共にロール1側からガタ殺し用のスプリング39で固定
する。The roll 2 rotatably supports a shaft portion 34 by means of a bearing 35, and the bearing 35 is slidably mounted in an elongated hole 36 formed in the housing 23 and extending in the horizontal direction. A load meter 37a, 37b (instead of the load meter, an ammeter may be provided in the driving device described later or in the driving device of the stirring bars 15, 16 will be described as a load meter hereinafter) is attached to the load meter. The cylinders 38 having rods extending in the horizontal direction press the 37a, 37b and the bearing 35 from the side opposite to the roll 1, and the springs 39 for slashing play are fixed from the roll 1 side.
前記ロール1,2は固定しない駆動装置に接続し回転駆動
されるようになっている。(第3図) 更に、前記荷重計37a,37bが検出したロール2に掛かる
荷重P1,P2を入力して両者を加算し或いは平均値を取っ
て圧延荷重を求める加算器40を設け、加算器40からの圧
延装置と前記温度検出器48からの攪拌装置10内温度を入
力して両者から固相率を求める第1の演算器41を設け、
演算器41からの固相率と前記回転数検出器51からの攪拌
棒15,16の回転数を入力して両者から攪拌装置10へ注湯
量を求める第2の演算器42を設け、演算器42からの注湯
量と設定器43からの注湯量の設定値を入力して両者の偏
差を取って該偏差分だけ前記設定値を修正した回転数を
信号として、シリンダ50のサーボ弁52に指令する減算器
44を設ける。(第1図) 尚、45はタンディッシュ9に溶湯4を供給するため真空
チャンバ11内に搬入し得るようにしたレードル、46は微
細結晶粒、47は半凝固スラリーである。The rolls 1 and 2 are connected to a drive device that is not fixed and are driven to rotate. (FIG. 3) Further, an adder 40 is provided which inputs the loads P 1 and P 2 applied to the roll 2 detected by the load cells 37a and 37b and adds them, or takes an average value to obtain a rolling load, A first calculator 41 is provided, which inputs the rolling device from the adder 40 and the temperature inside the stirrer 10 from the temperature detector 48 to obtain the solid fraction from both.
A second calculator 42 is provided, which inputs the solid phase rate from the calculator 41 and the rotation speeds of the stirring rods 15 and 16 from the rotation speed detector 51 to determine the pouring amount from the both to the stirring device 10. Input the set amount of pouring amount from 42 and the set amount of pouring amount from the setting device 43, take the deviation between the two, and command the servo valve 52 of the cylinder 50 as a signal with the rotation speed corrected by the deviation. Subtractor
Provide 44. (FIG. 1) Reference numeral 45 is a ladle that can be carried into the vacuum chamber 11 for supplying the molten metal 4 to the tundish 9, 46 is a fine crystal grain, and 47 is a semi-solidified slurry.
薄板6を製造する場合には、真空チャンバ11内を真空排
気した後、レードル45からタンディッシュ9に溶湯4を
供給し、又、撹拌棒15,16を内部冷却しつつ図中矢印c
で示すように互いに対向部を上向きに回転し且つ冷却装
置17の冷却管に冷却媒体を供給して撹拌室12,13内部を
溶湯4が固液共存する温度域まで徐々に冷却するように
し、更にロール1,2を内部冷却しつつ図中矢印dで示す
ように互いに対向部を下向きに回転する。When the thin plate 6 is manufactured, after the vacuum chamber 11 is evacuated, the molten metal 4 is supplied from the ladle 45 to the tundish 9 and the stirring rods 15 and 16 are internally cooled while the arrow c in the figure is used.
As shown in FIG. 3, the opposing portions are rotated upward and a cooling medium is supplied to the cooling pipe of the cooling device 17 to gradually cool the insides of the stirring chambers 12 and 13 to a temperature range in which the molten metal 4 coexists with solid and liquid, Further, while internally cooling the rolls 1 and 2, the facing portions are rotated downward as shown by an arrow d in the figure.
レードル45からタンディッシュ9に供給された溶湯4は
後述するようにタンディッシュ9内に一部が滞溜すると
共に弁体49を通って攪拌装置10に供給される。攪拌装置
10に供給された溶湯4は攪拌棒15,16の回転により図中
矢印eで示すように攪拌室12,13内部に導かれて徐々に
固液共存温度域まで冷却されて固体結晶のほぼ規則的な
骨組構造からなるデンドライト形態となり、更に攪拌棒
15,16で機械的に攪拌されることによりデンドライト形
態が破壊されて均質変形の可能な微細結晶粒46を含む粘
性及び表面張力の大きい半凝固スラリー47となりその後
仕切り板18により導かれてロール1,2間に供給される。
ロール1,2間に供給された半凝固スラリー47はロール1,2
により冷却されてロール1,2表面に凝固殻5を形成し、
表面に凝固殻5を形成した半凝固スラリー47はロール1,
2の回転によりロール1,2間から引出され、その後均一に
凝固殻5を生長して行き、又、微細結晶粒46を中心に内
部からも凝固して行き強度が高く均質な薄板6となる。The molten metal 4 supplied from the ladle 45 to the tundish 9 is partially retained in the tundish 9 and also supplied to the stirring device 10 through the valve body 49 as described later. Stirrer
The molten metal 4 supplied to 10 is guided into the stirring chambers 12 and 13 by the rotation of the stirring rods 15 and 16 and gradually cooled to the solid-liquid coexisting temperature range as shown by the arrow e in the figure, so that the solid crystals are almost ruled. It has a dendrite shape with a typical skeleton structure.
When mechanically stirred by 15, 16 the dendrite morphology is destroyed to become a semi-solidified slurry 47 containing fine crystal grains 46 capable of uniform deformation and having high viscosity and surface tension, and then guided by a partition plate 18 to roll 1. It is supplied between the two.
The semi-solidified slurry 47 supplied between the rolls 1 and 2 is the rolls 1 and 2.
It is cooled by and forms solidified shell 5 on the surface of rolls 1 and 2,
The semi-solidified slurry 47 with the solidified shell 5 formed on the surface is roll 1,
It is pulled out from between the rolls 1 and 2 by the rotation of 2, and thereafter the solidified shell 5 grows uniformly, and also solidifies from the inside centering on the fine crystal grains 46 to form a thin plate 6 with high strength and homogeneity. .
又、真空チャンバ11を設けてタンディッシュ9及び攪拌
装置10を空気から隔離することにより、薄板6内に酸素
が溶存せず、より高品質で強度の高い薄板6を製造し得
る。Further, by providing the vacuum chamber 11 and isolating the tundish 9 and the stirring device 10 from the air, oxygen is not dissolved in the thin plate 6, and the thin plate 6 having higher quality and higher strength can be manufactured.
このように、溶湯4を半凝固スラリー47にして薄板6を
製造すると、高強度の薄板6が得られることが確認され
ている。Thus, it has been confirmed that when the molten metal 4 is made into the semi-solidified slurry 47 to produce the thin plate 6, the thin plate 6 having high strength can be obtained.
このとき、容器3内では、容器3の外側に設けた冷却装
置17により容器3の外側に近い程冷却が早く進行し、攪
拌される溶湯4の温度即ち攪拌温度は常に容器3の外側
に近い程低くなるので溶湯4全体の攪拌温度が安定しな
い。該攪拌温度が安定しないまま半凝固スラリー47を形
成すると、攪拌温度が低い場合には、形成される半凝固
スラリー47中の微細結晶粒46の固相率が増大し、半凝固
スラリー47の粘性が高くなりすぎて流動性が著しく悪化
し、反対に攪拌温度が高い場合には半凝固スラリー47の
固相率が減少し粘性が低く流動性が良好になるため、ロ
ール1,2間には半凝固スラリー47が安定して供給されに
くくなり、ロール1,2間から引出された薄板6の形状が
悪化してしまう。At this time, in the container 3, cooling proceeds faster by the cooling device 17 provided on the outside of the container 3 closer to the outside of the container 3, and the temperature of the molten metal 4 to be stirred, that is, the stirring temperature is always closer to the outside of the container 3. Since it becomes so low, the stirring temperature of the entire molten metal 4 is not stable. When the semi-solidified slurry 47 is formed while the stirring temperature is not stable, when the stirring temperature is low, the solid phase ratio of the fine crystal grains 46 in the formed semi-solidified slurry 47 increases, and the viscosity of the semi-solidified slurry 47 increases. Is too high and the fluidity is significantly deteriorated.On the contrary, when the stirring temperature is high, the solid fraction of the semi-solidified slurry 47 decreases and the viscosity becomes low and the fluidity becomes good. It becomes difficult to stably supply the semi-solidified slurry 47, and the shape of the thin plate 6 pulled out between the rolls 1 and 2 deteriorates.
上記のような薄板6の形状の悪化を防止するため攪拌装
置10への注湯量を次のように制御する。In order to prevent the deterioration of the shape of the thin plate 6 as described above, the pouring amount to the stirring device 10 is controlled as follows.
即ち、薄板製造装置の起動時には、設定器43に運転状況
に応じた注湯量を設定値として入力して該設定値の信号
を減算器44を介してサーボ弁52に入力することによりシ
リンダ50の伸縮を行い弁体49の開度を調節して設定値ど
うりの注湯量にする。That is, at the time of starting the thin plate manufacturing apparatus, the pouring amount according to the operating condition is input as a set value to the setter 43, and a signal of the set value is input to the servo valve 52 via the subtractor 44, whereby the cylinder 50 By expanding and contracting, the opening of the valve element 49 is adjusted to obtain the pouring amount according to the set value.
それ以降は、半凝固スラリー47中の微細結晶粒46の固相
率が増大すると、半凝固スラリー47の粘性が高くなり流
動性が悪化してロール1,2間の圧延荷重が増大し、反対
に前記固相率が減少すると、半凝固スラリー47の粘性が
低くなり流動性が良好となってロール1,2間の圧延荷重
が減少することを利用し、荷重計37a,37bで検出したロ
ール2に掛る荷重P1,P2を加算器40に送り、加算器40はP
1,P2から圧延荷重を計算して演算器41に送り、演算器41
は加算器40からの圧延荷重と温度検出器48からの攪拌装
置10内の温度を入力して第4図のT1,T2,T3等の各温度に
応じた圧延荷重と固相率との関係を表わす線図に示され
るデータ等に基いて固相率を求め、演算器42は演算器41
からの固相率と回転数検出器51からの攪拌棒15,16の回
転数(固相率が同一でも攪拌速度が異なると半凝固スラ
リーの粘度は変化する)を入力して第5図のN1,N2,N3等
の各回転数に応じた固相率と注湯量との関係を表わす線
図に示されるデータ等に基いて注湯量を求め、減算器44
は演算器42からの注湯量と設定器43からの注湯量の設定
値を入力して両者の偏差を取り該偏差分だけ前記設定値
を修正した注湯量を信号としてサーボ弁52に指令を送
り、サーボ弁52は該指令を受けてシリンダ50の伸長量を
変更し弁体49の開度を調節して注湯量を変更する。After that, when the solid fraction of the fine crystal grains 46 in the semi-solidified slurry 47 increases, the viscosity of the semi-solidified slurry 47 increases and the fluidity deteriorates, the rolling load between the rolls 1 and 2 increases, and the opposite. When the solid fraction is reduced to, the viscosity of the semi-solidified slurry 47 becomes low and the fluidity becomes good, and the rolling load between the rolls 1 and 2 is reduced, and the rolls detected by the load cells 37a and 37b are used. The loads P 1 and P 2 on 2 are sent to the adder 40, and the adder 40
The rolling load is calculated from 1 and P 2 and sent to the calculator 41.
Is the rolling load from the adder 40 and the temperature in the stirrer 10 from the temperature detector 48, and the rolling load and solid fraction according to each temperature of T 1 , T 2 and T 3 in FIG. Based on the data and the like shown in the diagram showing the relationship with
5 and the rotation speed of the stirring rods 15 and 16 from the rotation speed detector 51 (the viscosity of the semi-solidified slurry changes when the stirring speed is different even if the solid proportion is the same). Subtractor 44 calculates the pouring amount based on the data and the like shown in the diagram showing the relationship between the solid fraction and the pouring amount corresponding to the respective rotation speeds of N 1 , N 2 , N 3 etc.
Inputs the set value of the pouring amount from the calculator 42 and the set amount of pouring amount from the setter 43, takes the deviation between the two, and sends a command to the servo valve 52 with the pouring amount corrected by the deviation as a signal. In response to the command, the servo valve 52 changes the expansion amount of the cylinder 50 and adjusts the opening degree of the valve body 49 to change the pouring amount.
このように注湯量を制御することにより、攪拌棒15,16
の回転数が少く形成された半凝固スラリー47の固相率が
大きい場合には注湯量を多くして半凝固スラリー47の粘
性を下げ、反対に攪拌棒15,16の回転数が多く形成され
た半凝固スラリー47の固相率が小さい場合には注湯量を
少くして半凝固スラリー47の粘性を上げることができる
ので、ロール1,2間には半凝固スラリー47が安定して供
給され、従って形状の良好な薄板6が製造できる。By controlling the pouring amount in this way, the stirring rods 15,16
When the solidification rate of the semi-solidified slurry 47 formed with a small number of revolutions is large, the pouring amount is increased to reduce the viscosity of the semi-solidified slurry 47, and conversely, the number of revolutions of the stirring rods 15 and 16 is increased. When the solid fraction of the semi-solidified slurry 47 is small, the pouring amount can be reduced to increase the viscosity of the semi-solidified slurry 47, so that the semi-solidified slurry 47 is stably supplied between the rolls 1 and 2. Therefore, the thin plate 6 having a good shape can be manufactured.
尚、本発明は上述の実施例に限定されるものではなく、
攪拌装置は必ずしもタンディッシュと別個に設ける必要
はなくタンディッシュ或いはバレルシール板とサイドシ
ール板から成る容器内に攪拌棒及び冷却装置を設け攪拌
装置を兼ねるようにしても良いこと、ロールに代えて無
端状に連ねたブロック鋳型及びスチールベルトからなる
移動鋳型を使用し得ること、前記した如く固相率は荷重
計を設けてロールに掛る圧延荷重を基に求めるようにす
る代りに電流計を設けてロールに掛る回転抵抗即ちロー
ルの駆動電流を基に求めるように或いは同様の理由から
攪拌棒の駆動電流を基に求めるようにし得ること、その
他本発明の要旨を逸脱しない範囲内で種々変更を加え得
ることは勿論である。The present invention is not limited to the above-mentioned embodiment,
The stirrer does not necessarily have to be provided separately from the tundish, and the stirrer and the cooling device may be provided in the tundish or the container composed of the barrel seal plate and the side seal plate so as to also serve as the stirrer, instead of the roll. It is possible to use a moving mold consisting of an endless block mold and a steel belt. As mentioned above, the solid phase ratio is provided with a load meter, and instead of being determined based on the rolling load applied to the roll, an ammeter is provided. It is possible to obtain the rotational resistance applied to the roll, that is, the drive current of the roll, or for the same reason, to obtain the drive current of the stirring rod, and other various changes may be made within the scope of the present invention. Of course, it can be added.
[発明の効果] 上記したように、本発明の薄板製造装置によれば、形成
された半凝固スラリーの固相率及び攪拌速度に応じた最
適な注湯量を求めて流入量調節装置を作動させ、半凝固
スラリーの粘性を適正化するようにしたので移動鋳型間
には半凝固スラリーが安定して供給され形状の良好な薄
板を製造し得る等の優れた効果を奏し得る。[Effects of the Invention] As described above, according to the thin plate manufacturing apparatus of the present invention, the inflow controller is operated by obtaining the optimum pouring amount according to the solid phase ratio and the stirring speed of the formed semi-solidified slurry. Since the viscosity of the semi-solidified slurry is optimized, the semi-solidified slurry is stably supplied between the moving molds, and excellent effects such as the production of a thin plate having a good shape can be achieved.
第1図は本発明の一実施例の説明図、第2図は第1図の
II−II矢視図、第3図は第1図のIII−III矢視図、第4
図は温度に応じた圧延荷重と固相率の関係を表わす線
図、第5図は攪拌棒の回転数に応じた固相率と注湯量の
関係を表わす線図、第6図は従来例の説明図、第7図は
他の従来例の説明図である。 図中1,2はロール、4は溶湯、5は凝固殻、6は薄板、
9はタンディッシュ、10は攪拌装置、15,16は攪拌棒、1
7は冷却装置、30は駆動装置、37a,37bは荷重計、40は加
算器、41,42は演算器、43は設定器、44は減算器、46は
微細結晶粒、47は半凝固スラリー、48は温度検出器、49
は弁体、50はシリンダ、51は回転数検出器、52はサーボ
弁を示す。FIG. 1 is an explanatory view of an embodiment of the present invention, and FIG. 2 is a view of FIG.
II-II arrow view, FIG. 3 is a III-III arrow view of FIG. 1, 4
FIG. 5 is a diagram showing the relationship between rolling load and solid fraction depending on temperature, FIG. 5 is a diagram showing the relationship between solid fraction and pouring amount according to the rotation speed of the stirring rod, and FIG. 6 is a conventional example. FIG. 7 is an explanatory view of another conventional example. In the figure, 1 and 2 are rolls, 4 is a molten metal, 5 is a solidified shell, 6 is a thin plate,
9 is a tundish, 10 is a stirrer, 15 and 16 are stirring rods, 1
7 is a cooling device, 30 is a driving device, 37a and 37b are load cells, 40 is an adder, 41 and 42 are calculators, 43 is a setting device, 44 is a subtractor, 46 is a fine crystal grain, and 47 is a semi-solidified slurry. , 48 is a temperature detector, 49
Is a valve body, 50 is a cylinder, 51 is a rotation speed detector, and 52 is a servo valve.
Claims (1)
に、該攪拌装置内部の固液共存温度域まで冷却された溶
湯を機械的に攪拌して半凝固スラリーを形成する回転自
在な攪拌棒を取付け、前記攪拌装置の下流に内部冷却し
得るようにした一対の無端状の移動鋳型を配設し、又、
前記攪拌装置に攪拌装置内部の温度を検出する温度検出
器を設け、前記攪拌棒に回転数検出器を取付け、前記移
動鋳型に圧延荷重を検出する荷重計を或いは前記移動鋳
型又は攪拌棒の一方に駆動電流を検出する電流計を接続
し、更に前記荷重計或いは電流計からの圧延荷重或いは
駆動電流と温度検出器からの温度を入力して半凝固スラ
リーの固相率を求める第1の演算器と、該演算器からの
固相率と前記回転数検出器からの攪拌棒の回転数を入力
して注湯量を求め前記流入量調節装置に指令を送る第2
の演算器を設けたことを特徴とする半凝固スラリーから
の薄板製造装置。1. A rotatable stirrer for mechanically stirring a molten metal cooled to a solid-liquid coexisting temperature range inside the stirrer with a stirrer equipped with a device for controlling the inflow amount of the molten metal to form a semi-solidified slurry. A rod is attached, and a pair of endless moving molds that can cool the inside of the stirring device are arranged downstream of the stirring device.
The stirrer is provided with a temperature detector for detecting the temperature inside the stirrer, the stirrer is equipped with a rotation speed detector, and the moving mold is equipped with a load meter for detecting a rolling load or one of the moving mold and the stirrer. A first operation for connecting a current meter for detecting a driving current to the above, and further inputting a rolling load or a driving current from the load meter or the ammeter and a temperature from a temperature detector to obtain a solid phase ratio of the semi-solidified slurry. And a solid phase ratio from the calculator and the rotation speed of the stirring rod from the rotation speed detector to determine the pouring amount and send a command to the inflow amount adjusting device.
An apparatus for manufacturing a thin plate from a semi-solidified slurry, which is provided with an arithmetic unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24477087A JPH07100217B2 (en) | 1987-09-29 | 1987-09-29 | Thin plate manufacturing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24477087A JPH07100217B2 (en) | 1987-09-29 | 1987-09-29 | Thin plate manufacturing equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6487042A JPS6487042A (en) | 1989-03-31 |
| JPH07100217B2 true JPH07100217B2 (en) | 1995-11-01 |
Family
ID=17123649
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24477087A Expired - Fee Related JPH07100217B2 (en) | 1987-09-29 | 1987-09-29 | Thin plate manufacturing equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07100217B2 (en) |
-
1987
- 1987-09-29 JP JP24477087A patent/JPH07100217B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6487042A (en) | 1989-03-31 |
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