JPH0455768B2 - - Google Patents
Info
- Publication number
- JPH0455768B2 JPH0455768B2 JP32326987A JP32326987A JPH0455768B2 JP H0455768 B2 JPH0455768 B2 JP H0455768B2 JP 32326987 A JP32326987 A JP 32326987A JP 32326987 A JP32326987 A JP 32326987A JP H0455768 B2 JPH0455768 B2 JP H0455768B2
- Authority
- JP
- Japan
- Prior art keywords
- molten metal
- stopper rod
- pouring
- tundish
- control
- 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
- 239000002184 metal Substances 0.000 claims description 69
- 238000000034 method Methods 0.000 claims description 26
- 238000002844 melting Methods 0.000 claims description 16
- 230000008018 melting Effects 0.000 claims description 16
- 230000001276 controlling effect Effects 0.000 claims description 14
- 238000005266 casting Methods 0.000 claims description 9
- 238000001816 cooling Methods 0.000 claims description 9
- 230000001105 regulatory effect Effects 0.000 claims description 2
- 238000003466 welding Methods 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000010349 pulsation Effects 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 229910008423 Si—B Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910000808 amorphous metal alloy Inorganic materials 0.000 description 1
- 238000007630 basic procedure Methods 0.000 description 1
- 238000009749 continuous casting Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 239000004576 sand Substances 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
- B22D11/06—Continuous casting of metals, i.e. casting in indefinite lengths into moulds with travelling walls, e.g. with rolls, plates, belts, caterpillars
- B22D11/0637—Accessories therefor
- B22D11/064—Accessories therefor for supplying molten metal
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Continuous Casting (AREA)
- Casting Support Devices, Ladles, And Melt Control Thereby (AREA)
Description
本発明は、薄板鋳造における溶湯流量の制御方
法に係り、特に、冷却ロールに溶融金属(溶湯)
を注いで凝固させ、直接的に板を製造する急冷薄
帯プロセス等、比較的微量の溶融金属を連続的に
供給する必要のある設備に用いるに好適な、溶融
金属を、連続的に冷却体に供給する際の安定且つ
正確な流量制御方法に関する。
The present invention relates to a method for controlling the flow rate of molten metal in thin plate casting, and in particular, the present invention relates to a method for controlling the flow rate of molten metal in thin plate casting.
This method is suitable for use in equipment that requires a continuous supply of a relatively small amount of molten metal, such as the quenched ribbon process that directly manufactures plates by pouring and solidifying molten metal. This invention relates to a stable and accurate flow rate control method when supplying water.
薄板の連続鋳造、例えば冷却ロール等の連続的
に移動する冷却体に溶融金属を注いで凝固させ、
直接的に板を製造する急冷薄帯プロセス等におい
て、注湯ノズルより供給する溶湯流量を正確に制
御することは、製品板厚を一定に保つために不可
欠の技術である。
従つて、例えば溶解炉等の溶湯保持設備より注
湯ノズルを具備したタンデイツシユに溶湯を供給
し、タンデイツシユの重量が一定になるように供
給量を制御することによつて注湯速度を一定に保
つ方法等によつて板厚を一定に保持する方法が開
発されている。
しかしながら、特に10Kg/s以下程度の比較的
少流量の場合には正確な制御を行うことが困難で
あるという問題点を有していた。
又、溶湯の供給を制御する他の方法として、炉
等の溶湯保持装置自体を傾動させて注湯する方法
や、スライデイングノズルから注湯する方法等も
用いられている。
しかしながら、前者は、注湯量の脈動が注湯口
での一部凝固のために正確な制御が困難であると
いう問題点を有し、後者も、設備が大規模で高価
であるばかりでなく、ノズル詰まり防止のためノ
ズル孔内に砂込めが必要となり、このような介在
物のタンデイツシユ内の混入が、微量注湯系では
注湯ノズルの詰まりや製板への妨害等の悪影響を
無視できない等の問題点を有しており、その利用
が制限されてきた。
又、特開昭61−296942及び特開昭61−296943に
おいては、タンデイツシユ又はタンデイツシユか
らのノズルが貫通する箱体を気密構造にすると共
に、該タンデイツシユの注湯ノズルにタンデイツ
シユストツパ棒を設け、タンデイツシユ内又は箱
体内の圧力調整とタンデイツシユストツパ棒の開
度調整の組合わせ、即ち、溶鋼レベルの比較的速
い変動を圧力調整によつて低減し、比較的遅い変
動はタンデイツシユストツパ棒の開度調整によつ
て低減する方法が開示されている。
Continuous casting of thin sheets, for example, by pouring molten metal onto a continuously moving cooling body such as a cooling roll and solidifying it.
Accurately controlling the flow rate of molten metal supplied from a pouring nozzle in the quenched ribbon process that directly manufactures plates is an essential technology for keeping the thickness of the product plate constant. Therefore, for example, by supplying molten metal from molten metal holding equipment such as a melting furnace to a tundish equipped with a pouring nozzle and controlling the supply amount so that the weight of the tundish remains constant, the pouring speed can be kept constant. Methods have been developed to maintain the plate thickness constant. However, there has been a problem in that it is difficult to perform accurate control, especially when the flow rate is relatively small, such as 10 kg/s or less. Other methods for controlling the supply of molten metal include a method of pouring the molten metal by tilting the molten metal holding device itself such as a furnace, and a method of pouring the molten metal from a sliding nozzle. However, the former method has the problem that it is difficult to accurately control the pulsation of the pouring amount due to partial solidification at the pouring port, and the latter method not only requires large-scale and expensive equipment, but also has the problem that the nozzle It is necessary to fill the nozzle hole with sand to prevent clogging, and if such inclusions enter the tundish, the negative effects such as clogging of the pouring nozzle and interference with plate making cannot be ignored in the micro-pouring system. It has problems and its use has been limited. In addition, in JP-A-61-296942 and JP-A-61-296943, the tundish or the box through which the nozzle from the tundish runs through is made airtight, and a tundish stopper rod is attached to the pouring nozzle of the tundish. This is a combination of pressure adjustment inside the tundish or box body and adjustment of the opening of the tundish stopper rod.In other words, relatively fast fluctuations in the molten steel level are reduced by pressure adjustment, and relatively slow fluctuations are reduced by the tundish stopper rod. A method of reducing this by adjusting the opening degree of a lever stopper is disclosed.
しかしながら、比較的狭い領域に設置されたタ
ンデイツシユにストツパ棒を設けることは設備上
の困難を伴い、又、タンデイツシユ内や箱体内を
加減圧するには、高温融体を含むタンデイツシユ
や箱体を完全な気密構造にしなければならず、大
掛りな設備が必要となつて、構造が複雑になると
いう問題点を有していた。
従つて、比較的設備上の制約が少いストツパ棒
方式による注湯方式において、高精度の注湯制御
を行うために、溶解炉等の溶湯保持装置より直接
冷却体に注湯したり、注湯ノズルを取付けたタン
デイツシユに溶湯を供給し、タンデイツシユより
注湯する場合に安定した正確な制御を行うことが
重要になるが、従来は、ストツパ棒のオンオフ制
御により断続的な注湯を行う流量調節は行われて
いるものの、湯面レベルの変化やストツパ棒の揺
れ等により制御性が低いため、微少流量の正確な
制御には用いることができなかつた。
なお、特開昭58−58964には本発明と類似の構
成が開示されているが、本願発明のように薄板鋳
造に関するものではなく、具体的な構成も異なる
ものであつた。
However, installing a stopper rod in a tundish installed in a relatively narrow area is difficult in terms of equipment, and in order to pressurize and depressurize the inside of the tundish or box, it is necessary to completely remove the tundish or box containing high-temperature melt. The problem was that the structure had to be airtight, requiring large-scale equipment, and making the structure complicated. Therefore, in the pouring method using the stopper rod method, which has relatively few restrictions on equipment, in order to perform high-precision pouring control, it is necessary to pour the molten metal directly into the cooling body from a molten metal holding device such as a melting furnace. When supplying molten metal to a tundish with a hot water nozzle attached, it is important to perform stable and accurate control when pouring from the tundish. Conventionally, the flow rate was controlled intermittently by on/off control of a stopper rod. Although adjustments have been made, the controllability is poor due to changes in the hot water level and swinging of the stopper rod, so it could not be used to accurately control minute flow rates. Incidentally, Japanese Patent Application Laid-Open No. 58-58964 discloses a structure similar to the present invention, but unlike the present invention, it does not relate to thin plate casting and the specific structure is different.
本発明は、前記従来の問題点を解消するべくな
されたもので、ストツパ棒の溶着を防止し、設備
上の制約が少いストツパ棒方式によつて、微少流
量を安定して正確に制御することが可能な薄板鋳
造における溶湯流量の制御方法を提供することを
目的とする。
The present invention was made to solve the above-mentioned conventional problems, and it prevents welding of the stopper rod and stably and accurately controls minute flow rates using a stopper rod method with fewer restrictions on equipment. The purpose of the present invention is to provide a method for controlling the flow rate of molten metal in thin plate casting.
本発明は、溶湯を冷却体表面上に供給する注湯
ノズルと、該注湯ノズルへの溶湯供給量を制御す
るストツパ棒を有する溶湯保持装置とを少なくと
も備えた注湯設備を用いて薄板を鋳造する際に、
第1図にその要旨を示す如く、注湯量又はその変
化速度をオンラインで測定し、該測定値と目標値
との偏差を基に、前記ストツパ棒の位置又は移動
速度を制御し、更に、前記ストツパ棒の位置が少
なくとも次式
dmin≧50/√・・・ ……(1)
ここで、
ρ:溶湯の密度(g/cm3)
C:溶湯の比熱(cal/g)
ΔT:溶湯温度とその融点との差(℃)(10≦ΔT
≦500)
h:注湯穴上面から溶湯表面までの高さ(mm)
(30≦h≦2000)
で示される最小開度dmin以下とならないように
規制することによつて、前記目的を達成したもの
である。
The present invention provides a method for forming a thin plate using pouring equipment that includes at least a pouring nozzle that supplies molten metal onto the surface of a cooling body, and a molten metal holding device that has a stopper rod that controls the amount of molten metal supplied to the pouring nozzle. When casting,
As shown in FIG. 1, the pouring amount or the rate of change thereof is measured online, the position or moving speed of the stopper rod is controlled based on the deviation between the measured value and the target value, and the The position of the stopper rod is determined by the following formula: dmin≧50/√... (1) Where, ρ: Density of the molten metal (g/cm 3 ) C: Specific heat of the molten metal (cal/g) ΔT: Temperature of the molten metal Difference from its melting point (℃) (10≦ΔT
≦500) h: Height from the top of the pouring hole to the surface of the molten metal (mm)
(30≦h≦2000) The above objective is achieved by regulating the opening degree so that it does not become less than the minimum opening degree dmin shown by the following formula.
本発明は、一般的には耐火物で作られる炉底開
口部とストツパ棒先端との間〓を厳密に調節する
ことが困難であるため、比較的大きな脈動も許容
できる大流量注湯系には採用できても、微少流量
を安定して正確に制御する必要がある微量注湯系
には適しないと従来考えられていたストツパ棒方
式を更に詳細に検討することによつてなされたも
のである。
溶解炉等の溶湯保持装置よりストツパ棒を上下
させて溶湯を供給する場合に、注湯量が一定にな
るようにストツパ棒の位置を制御することになる
が、ストツパ棒の溶着を防ぐために開度に下限を
設け、又、必要に応じて制御性を高めるためにス
トツパ棒の開度に上限を設けることにより、安定
性と高制御性を実現することができる。
以下、非晶質合金の製造等に用いる単ロール法
に本発明を適用した場合を例にとつて、本発明の
具体的構成を説明する。
第2図は、前記単ロール法の例を模式的に示し
たもので、タンデイツシユ12への溶湯10の供
給量を制御するストツパ棒14を溶湯保持装置で
ある溶解炉16に設け、該溶解炉16に、例えば
DCサーボモータのような制御が容易な駆動部を
用いたストツパ棒駆動装置18を取付ける。又、
下方のタンデイツシユ12に、例えばロードセル
20を取付け、前記タンデイツシユ12と共に内
部の溶湯重量を測定できるようにする。
図において、22は注湯ノズル、24は制御装
置、26は冷却ロール、28は薄帯である。
鋳造に際しては、目標とするタンデイツシユ内
湯面レベルに対応した重量になるように、ストツ
パ棒14の位置を制御装置24によつて例えば
PID制御する。即ち、例えば測定された重量と目
標重量との偏差を基にP(比例)制御によつてス
トツパ棒14の開度を指示する。P制御のみでは
定常偏差が生じるので、その値が大きい場合等に
は、I(積分)制御を加えて偏差を低減し、必要
に応じて更にD(微分)制御を加えることによつ
て速やかに偏差を極めて小さくすることが可能と
なる。
ここで問題となるのは、ストツパ棒14の開度
が非常に小さくなつた場合に、ストツパ棒14と
ストツパ座16A(炉底開口部周囲の、溶湯の供
給停止時にストツパ棒14と接触する部分)との
間に溶湯が一時的に滞留して温度低下により凝固
し、ストツパ棒14がストツパ座16Aに溶着し
てしまう可能性のあることである。例えば、P制
御の場合のゲインのような、PID定数の設定によ
つては、特に制御開始初期において、このような
状況が考えられるため、本発明においては、スト
ツパ開度に下限値dminを設けることによつてス
トツパ棒の溶着を回避し、操業の安定性を向上し
ている。なお、短時間で溶着が起こる際の流量は
ほとんど零であるので、下限値dminを設けても
制御性を著しく損うことはない。
この下限値dminの決定方法について、注湯穴
の面積、ストツパ棒14の先端形状、注湯の組成
等を変化させて検討した結果、下限値dminは、
注湯の密度ρ、比熱C、溶湯温度と凝固温度(融
点)との差ΔT、注湯穴上面(ストツパ棒14を
閉じた時の先端の接触位置)から溶湯表面までの
高さhに依存することが分つた。
第3図に、密度ρが6.5g/cm2で比熱Cが
0.15cal/gの溶湯金属について、いくつかのス
トパ開度について溶着を起す際の溶湯温度と注湯
穴から溶湯表面までの高さhの関係を調べた結果
の例を示す。例えばストツパ開度が0.5mmで溶湯
金属の温度とその融点との差ΔTが60℃の場合、
溶湯高さhが160mmで溶着を起しているように、
第3図の1点鎖線より下の領域では溶着を起す可
能性があるが、前出(1)式を満足する、1点鎖線よ
り上の領域では溶着が生じることはない。つま
り、(1)式で表される開度に設定しておくと溶着を
起こさない。
又、第4図に、直径が50mmで先端の半球状のス
トツパ棒14を用いて、注湯穴の半径を変えた場
合のストツパ開度と注湯速度との関係を示した
が、ストツパ棒制御の場合、ストツパ開度と溶湯
の供給速度の関係は単純な比例関係ではなく、ス
トツパ開度が大きくなると溶湯流量は注湯穴の断
面積により律速されるため、供給速度が飽和す
る。例えばP制御においてゲインが比較的大きい
場合等、PID定数の設定によつては、特に制御開
始初期において、このような飽和した状態もしく
はストツパ開度の増加に対する供給速度の増加が
極めて小さな状態になつても、ストツパの開度
dmaxを更に大きくするような無駄な操作をさせ
る場合があるが、ストツパ棒の移動速度に制約が
あるため、制御性が低下してしまうことがある。
このような場合には、ストツパ棒の開度に上限値
dmaxを設けることで、前記のような制御性の低
下を避けることが可能となる。
この上限値dmaxについては、流体力学の理論
によれば溶湯の動粘性係数等にも依存することが
考えられるが、実験の結果、ストツパ棒の位置を
PID制御したり、ストツパ棒の速度をP制御した
りする場合には、事実上注湯穴の断面積S(mm2)
に依存することが分つた。つまり制御理論によつ
て多少ばらつくが、次式に記載したような値に設
定することが適当である。
0.3√≦dmax≦0.8√ ……(2)
実際の制御にあたつては、例えばタンデイツシ
ユ12の目標重量と実測重量との偏差を制御装置
24のマイクロプロセツサに取込み、予め設定し
ておいたPID定数に従つて、ストツパ棒14の開
度を計算して例えば位置の指令を出す方法によつ
て、比較的簡単な制御論理で安定した正確な流量
制御を行うことができる。
なお、注湯中にストツパ棒先端が大きく破損し
た場合等は、ストツパ開度を小さくしても注湯量
が多くてタンデイツシユ12の重量が目標値を超
えてしまうという状況がある。このような場合に
は、一時的にストツパ棒14を移動可能な最下限
まで下げて、溶湯の供給を一時中断し、タンデイ
ツシユ重量等が目標値近くまで減少してから再び
制御を開始する方法によつて、鋳造を続行するこ
とができる。
なお、前記の説明では、タンデイツシユ内の溶
融金属量をロードセル20によつて測定していた
が、溶融金属量の測定方法はこれに限定されず、
ロードセル以外の荷重計を用いたり、あるいは、
湯面レベルを光学的に測定するレーザ液面計等を
用いることもできる。
又、前記の説明では、溶解炉16とタンデイツ
シユ12を備えた注湯設備で、タンデイツシユ1
2内の溶湯量が目標値となるようにストツパ棒1
4の位置を制御する場合を例にとつて本発明を説
明していたが、本発明の適用対象は、これに限定
されず、同じくタンデイツシユ12内の溶湯量が
目標値となるようにストツパ棒14の移動速度を
制御する場合(特願昭62−192336)、タンデイツ
シユ12からの注湯速度(溶湯量の変化速度)が
目標値となるようにストツパ棒14の位置(特願
昭62−205720)又は移動速度(特願昭62−
275108)を制御する場合、溶解炉16から直接冷
却ロール26に注湯する設備で、溶解炉重量(溶
湯量)の変化速度が目標値となるようにストツパ
棒14の位置(特願昭62−209907)又は移動速度
(特願昭62−275109)を制御する場合等にも、本
発明が同様に適用できることは明らかである。
Since it is difficult to precisely adjust the distance between the bottom opening of the furnace and the tip of the stopper rod, which is generally made of refractory material, the present invention aims to develop a high-flow pouring system that can tolerate relatively large pulsations. This was achieved through a more detailed study of the stopper rod method, which was previously thought to be unsuitable for micro-pouring systems that require stable and accurate control of minute flow rates, even if it could be adopted. be. When supplying molten metal by moving a stopper rod up and down from a molten metal holding device such as a melting furnace, the position of the stopper rod is controlled so that the amount of poured metal is constant. Stability and high controllability can be achieved by setting a lower limit on the opening degree of the stopper rod and, if necessary, setting an upper limit on the opening degree of the stopper rod in order to improve controllability. Hereinafter, the specific structure of the present invention will be explained by taking as an example the case where the present invention is applied to a single roll method used for manufacturing an amorphous alloy. FIG. 2 schematically shows an example of the single roll method, in which a stopper rod 14 for controlling the amount of molten metal 10 supplied to the tundish 12 is provided in the melting furnace 16, which is a molten metal holding device, and the melting furnace is 16, for example
A stopper rod drive device 18 using a drive unit that is easy to control, such as a DC servo motor, is installed. or,
For example, a load cell 20 is attached to the lower tundish 12 so that the weight of the molten metal inside can be measured together with the tundish 12. In the figure, 22 is a pouring nozzle, 24 is a control device, 26 is a cooling roll, and 28 is a ribbon. During casting, the position of the stopper rod 14 is controlled by the control device 24, for example, so that the weight corresponds to the target level of the molten metal in the tundish.
PID control. That is, for example, the opening degree of the stopper rod 14 is instructed by P (proportional) control based on the deviation between the measured weight and the target weight. P control alone will cause a steady-state deviation, so if the value is large, add I (integral) control to reduce the deviation, and if necessary, add D (differential) control to quickly correct the deviation. It becomes possible to make the deviation extremely small. The problem here is that when the opening degree of the stopper rod 14 becomes very small, the stopper rod 14 and the stopper seat 16A (the part around the furnace bottom opening that comes into contact with the stopper rod 14 when the supply of molten metal is stopped) ), there is a possibility that the molten metal will temporarily stay there and solidify due to the temperature drop, resulting in the stopper rod 14 being welded to the stopper seat 16A. For example, depending on the setting of the PID constant, such as the gain in the case of P control, such a situation is possible, especially at the beginning of control, so in the present invention, a lower limit value dmin is set for the stopper opening degree. This avoids welding of the stopper rod and improves operational stability. Note that since the flow rate when welding occurs in a short time is almost zero, even if a lower limit value dmin is provided, controllability will not be significantly impaired. Regarding the method of determining this lower limit value dmin, as a result of examining the area of the pouring hole, the tip shape of the stopper rod 14, the composition of the pouring metal, etc., the lower limit value dmin was determined as follows.
Depends on the density ρ of the pouring metal, the specific heat C, the difference ΔT between the molten metal temperature and the solidification temperature (melting point), and the height h from the top surface of the pouring hole (the contact position of the tip when the stopper rod 14 is closed) to the molten metal surface. I found out what to do. Figure 3 shows that the density ρ is 6.5 g/cm 2 and the specific heat C is
An example of the results of investigating the relationship between the molten metal temperature at which welding occurs and the height h from the pouring hole to the molten metal surface for several stopper openings for 0.15 cal/g molten metal is shown below. For example, if the stopper opening is 0.5 mm and the difference ΔT between the temperature of the molten metal and its melting point is 60°C,
As welding occurs when the molten metal height h is 160mm,
Although there is a possibility that welding will occur in the region below the dashed-dotted line in FIG. 3, welding will not occur in the region above the dashed-dotted line that satisfies the above-mentioned formula (1). In other words, welding will not occur if the opening is set to the opening expressed by equation (1). In addition, Fig. 4 shows the relationship between the stopper opening degree and the pouring speed when the radius of the pouring hole is changed using a stopper rod 14 with a diameter of 50 mm and a hemispherical tip. In the case of control, the relationship between the stopper opening and the molten metal supply rate is not a simple proportional relationship; as the stopper opening increases, the molten metal flow rate is controlled by the cross-sectional area of the pouring hole, so the supply rate becomes saturated. For example, when the gain is relatively large in P control, depending on the setting of the PID constant, especially at the beginning of control, the increase in supply speed with respect to the increase in the stopper opening may become saturated or extremely small. Even if the stopper opening is
This may cause unnecessary operations such as further increasing dmax, but since there are restrictions on the moving speed of the stopper rod, controllability may deteriorate.
In such a case, the upper limit value for the opening degree of the stopper rod should be set.
By providing dmax, it is possible to avoid the aforementioned deterioration in controllability. According to fluid mechanics theory, this upper limit value dmax may depend on the kinematic viscosity coefficient of the molten metal, but as a result of experiments, we found that the position of the stopper rod
When performing PID control or controlling the speed of the stopper rod by P, the cross-sectional area of the pouring hole S (mm 2 )
It was found that it depends on In other words, although it varies somewhat depending on the control theory, it is appropriate to set the value as shown in the following equation. 0.3√≦dmax≦0.8√ ...(2) In actual control, for example, the deviation between the target weight and the measured weight of the tundish 12 is input into the microprocessor of the control device 24 and set in advance. By calculating the opening degree of the stopper rod 14 according to the PID constant and issuing, for example, a position command, stable and accurate flow control can be performed with relatively simple control logic. If the tip of the stopper rod is severely damaged during pouring, even if the stopper opening degree is reduced, the amount of poured metal will be large and the weight of the tundish 12 will exceed the target value. In such a case, there is a method of temporarily lowering the stopper rod 14 to the lowest movable limit, temporarily interrupting the supply of molten metal, and restarting control after the tundish weight, etc. has decreased to near the target value. Casting can then be continued. In the above description, the amount of molten metal in the tundish was measured using the load cell 20, but the method for measuring the amount of molten metal is not limited to this.
Using a load cell other than a load cell, or
A laser level gauge or the like that optically measures the hot water level can also be used. Furthermore, in the above description, in the pouring equipment equipped with the melting furnace 16 and the tundish 12, the tundish 1
Hold the stopper rod 1 so that the amount of molten metal in 2 reaches the target value.
Although the present invention has been described taking as an example the case where the position of the stopper rod is controlled, the application of the present invention is not limited to this. When controlling the moving speed of the stopper rod 14 (Japanese Patent Application No. 62-192336), the position of the stopper rod 14 is adjusted so that the pouring speed (change rate of the amount of molten metal) from the tundish 12 becomes the target value (Japanese Patent Application No. 62-205720). ) or movement speed (patent application 1982-
275108), when controlling the position of the stopper rod 14 (Japanese Patent Application No. 1983-1996), in a device that pours melt directly from the melting furnace 16 to the cooling roll 26, so that the rate of change of the melting furnace weight (molten metal amount) reaches the target value. It is clear that the present invention can be similarly applied to the case of controlling the moving speed (Japanese Patent Application No. 62-275109).
第2図に示したように、溶湯保持装置として、
DCモータによつて駆動するストツパ棒14を取
付けた溶解炉16(使用溶湯表面高さ30〜500mm)
を用い、ストツパ棒14を上昇させることによつ
て、溶解炉下部のノズルより、注湯ノズル22を
取付けたタンデイツシユ12に溶湯を供給する装
置に、本発明の制御方法を適用した。
即ち、Fe−Si−B系合金の溶湯(凝固点1180
℃)を前記溶解炉16で1300℃に保持し、先端が
半球状で、直径が50mmのストツパ棒14を用い
て、直径が15mmの注湯穴より、下方のタンデイツ
シユ12に平均0.8Kg/sの速度で注湯した。
タンデイツシユ12に取付けたロードセル20
からのタンデイツシユ重量信号を、制御装置24
のマイクロプロセツサに送り、予め書込んだプロ
グラムに従つて、タンデイツシユ重量が目標値と
なるようにDCモータの電流を制御することによ
つて、ストツパ棒14の位置を制御した。
位置制御によるストツパ棒開度の制御におい
て、開度に制限を設けない場合、本発明により下
限値dminのみ設けた場合、上下限値dmax、
dminを共に設けた場合について実験したところ、
ストツパ棒の溶着の有無と制御時の注湯速度のば
らつきは下記第1表に示す如くであつた。
第1表から明らかなように、下限値dminを設
けない場合(実験番号1〜3)は溶着を起す場合
があるが、下限値dminを設定すると(実験番号
4〜7)、溶着が起らず、又、制御性も改善され
た。更に上限値dmaxを設けると(実験番号6、
7)、制御性が一層改善されることが分かる。
As shown in Figure 2, as a molten metal holding device,
Melting furnace 16 equipped with a stopper rod 14 driven by a DC motor (molten metal surface height used: 30 to 500 mm)
The control method of the present invention was applied to a device that supplies molten metal from a nozzle in the lower part of a melting furnace to a tundish 12 equipped with a pouring nozzle 22 by raising the stopper rod 14 using a molten metal. That is, molten metal of Fe-Si-B alloy (solidification point 1180
℃) is maintained at 1300℃ in the melting furnace 16, and using a stopper rod 14 with a hemispherical tip and a diameter of 50mm, an average of 0.8Kg/s is applied to the lower tundish 12 from the pouring hole with a diameter of 15mm. The water was poured at a speed of . Load cell 20 attached to tandem tray 12
The tundish weight signal from the control device 24
The position of the stopper rod 14 was controlled by controlling the current of the DC motor so that the tundish weight reached a target value according to a program sent to a microprocessor and written in advance. In controlling the opening degree of the stopper rod by position control, if there is no limit on the opening degree, and if only the lower limit value dmin is provided according to the present invention, the upper and lower limits dmax,
When I experimented with the case where dmin was also set up, I found that
The presence or absence of welding on the stopper rod and the variation in pouring speed during control were as shown in Table 1 below. As is clear from Table 1, welding may occur when the lower limit value dmin is not set (experiment numbers 1 to 3), but when the lower limit value dmin is set (experiment numbers 4 to 7), welding does not occur. Furthermore, controllability has also been improved. Furthermore, if an upper limit value dmax is set (experiment number 6,
7), it can be seen that the controllability is further improved.
【表】
なお、前記実施例においては、本発明が単一の
冷却ロールを備えた連続薄板製造設備に適用され
ていたが、本発明の適用範囲はこれに限定されな
い。[Table] Note that in the above embodiments, the present invention was applied to continuous thin plate manufacturing equipment equipped with a single cooling roll, but the scope of application of the present invention is not limited thereto.
以上説明した通り、本発明によれば、薄板連続
注湯設備において、ストツパ棒の溶着を防止する
ことができ、ストツパ棒の移動という比較的簡単
な方法で、安定した正確な注湯量制御が可能とな
る。従つて、板厚が均一になり、表面性状も改善
されるという優れた効果を有する。
As explained above, according to the present invention, it is possible to prevent welding of the stopper rod in thin plate continuous pouring equipment, and it is possible to stably and accurately control the pouring amount by the relatively simple method of moving the stopper rod. becomes. Therefore, it has the excellent effect of making the plate thickness uniform and improving the surface quality.
第1図は、本発明に係る溶湯流量制御方法の基
本的な手順を示す流れ図、第2図は、本発明が適
用された連続注湯装置の一例の構成を示す断面
図、第3図は、本発明の原理を発明するための、
ノズル詰りを起す際の溶湯温度と注湯穴から溶湯
表面までの高さの関係を示す線図、第4図は、同
じく注湯穴の半径を変えた場合のストツパ開度と
注湯速度との関係を示す線図である。
10……溶湯、12……タンデイツシユ、14
……ストツパ棒、16……溶解炉、18……スト
ツパ棒駆動装置、20……ロードセル、22……
注湯ノズル、24……制御装置、26……冷却ロ
ール、28……薄帯。
FIG. 1 is a flowchart showing the basic procedure of the molten metal flow rate control method according to the present invention, FIG. 2 is a sectional view showing the configuration of an example of a continuous pouring device to which the present invention is applied, and FIG. , for inventing the principles of the present invention,
Figure 4 is a diagram showing the relationship between the molten metal temperature and the height from the pouring hole to the molten metal surface when nozzle clogging occurs, and also shows the stopper opening degree and pouring speed when the radius of the pouring hole is changed. FIG. 10... Molten metal, 12... Tundishyu, 14
... Stopper rod, 16 ... Melting furnace, 18 ... Stopper rod drive device, 20 ... Load cell, 22 ...
Pouring nozzle, 24... control device, 26... cooling roll, 28... ribbon.
Claims (1)
と、該注湯ノズルへの溶湯供給量を制御するスト
ツパ棒を有する溶湯保持装置とを少なくとも備え
た注湯設備を用いて薄板を鋳造する際に、 溶湯量又はその変化速度をオンラインで測定
し、 該測定値と目標値との偏差を基に、前記ストツ
パ棒の位置又は移動速度を制御し、 更に、前記ストツパ棒の位置が少なくとも次式 dmin≧50/√・・・ ここで、 ρ:溶湯の密度(g/cm3) C:溶湯の比熱(cal/g) ΔT:溶湯温度とその融点との差(℃)(10≦ΔT
≦500) h:注湯穴上面から溶湯表面までの高さ(mm)
(30≦h≦2000) で示される最小開度dmin以下とならないように
規制することを特徴とする薄板鋳造における溶湯
流量の制御方法。[Scope of Claims] 1. Using pouring equipment that includes at least a pouring nozzle that supplies molten metal onto the surface of a cooling body, and a molten metal holding device that has a stopper rod that controls the amount of molten metal supplied to the pouring nozzle. When casting a thin plate, the amount of molten metal or its rate of change is measured online, the position or moving speed of the stopper rod is controlled based on the deviation between the measured value and the target value, and the stopper rod is The position of dmin≧50/√...where, ρ: Density of molten metal (g/cm 3 ) C: Specific heat of molten metal (cal/g) ΔT: Difference between molten metal temperature and its melting point (°C) ) (10≦ΔT
≦500) h: Height from the top of the pouring hole to the surface of the molten metal (mm)
(30≦h≦2000) A method for controlling the flow rate of molten metal in thin plate casting, characterized by regulating the flow rate so that it does not become less than the minimum opening dmin expressed by (30≦h≦2000).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32326987A JPH01166861A (en) | 1987-12-21 | 1987-12-21 | Control method for molten metal flow in casting thin strip |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32326987A JPH01166861A (en) | 1987-12-21 | 1987-12-21 | Control method for molten metal flow in casting thin strip |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01166861A JPH01166861A (en) | 1989-06-30 |
| JPH0455768B2 true JPH0455768B2 (en) | 1992-09-04 |
Family
ID=18152902
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP32326987A Granted JPH01166861A (en) | 1987-12-21 | 1987-12-21 | Control method for molten metal flow in casting thin strip |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01166861A (en) |
-
1987
- 1987-12-21 JP JP32326987A patent/JPH01166861A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01166861A (en) | 1989-06-30 |
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