JP2587472B2 - Method and apparatus for controlling cooling water amount during production of granulated slag - Google Patents

Method and apparatus for controlling cooling water amount during production of granulated slag

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Publication number
JP2587472B2
JP2587472B2 JP22635388A JP22635388A JP2587472B2 JP 2587472 B2 JP2587472 B2 JP 2587472B2 JP 22635388 A JP22635388 A JP 22635388A JP 22635388 A JP22635388 A JP 22635388A JP 2587472 B2 JP2587472 B2 JP 2587472B2
Authority
JP
Japan
Prior art keywords
slag
cooling water
amount
granulated slag
granulated
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 - Lifetime
Application number
JP22635388A
Other languages
Japanese (ja)
Other versions
JPH0274544A (en
Inventor
富美男 柴岡
幹男 青木
正広 橋本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Steel Corp
JFE Mineral Co Ltd
Original Assignee
Kawatetsu Mining Co Ltd
Kawasaki Steel Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kawatetsu Mining Co Ltd, Kawasaki Steel Corp filed Critical Kawatetsu Mining Co Ltd
Priority to JP22635388A priority Critical patent/JP2587472B2/en
Publication of JPH0274544A publication Critical patent/JPH0274544A/en
Application granted granted Critical
Publication of JP2587472B2 publication Critical patent/JP2587472B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、水砕スラグ製造時の冷却水量制御方法およ
びその装置に関する。
Description: TECHNICAL FIELD The present invention relates to a method and an apparatus for controlling the amount of cooling water during the production of granulated slag.

〔従来の技術〕[Conventional technology]

水砕の品質向上を図るためには、スラグ量を常時把握
し、変動するスラグ量に応じて冷却水量を制御する必要
がある。
In order to improve the quality of water granulation, it is necessary to constantly grasp the amount of slag and control the amount of cooling water according to the fluctuating amount of slag.

スラグの量を計測する手段としては、直接溶融スラグ
の量を測定する方法、連続脱水装置の負荷量を測定し演
算により求める方法、脱水後の水砕スラグ輸送用コンベ
ヤーにロードセルを取付けて測定する方法等が種々提案
されている。
As a means for measuring the amount of slag, a method of directly measuring the amount of molten slag, a method of measuring the load of a continuous dewatering device and calculating the amount, and attaching a load cell to a conveyor for transporting granulated slag after dehydration and measuring. Various methods have been proposed.

例えば、特開昭56−26752号では、脱水装置に水砕重
量を測定する重量測定装置を設けると共に、搬出コンベ
ヤーに水砕の流量を測定する流量測定装置を設け、これ
らの測定値から炉から流出する溶滓の流量を算出してい
る。
For example, in Japanese Patent Application Laid-Open No. 56-26752, a dehydrator is provided with a weight measuring device for measuring the weight of granulated particles, and a carry-out conveyor is provided with a flow measuring device for measuring the flow rate of granulated particles. The flow rate of the slag flowing out is calculated.

水砕スラグの製造時の冷却水量制御置については、例
えば、特開昭61−270238号に開示され、この方法を好適
に実施する装置として、各吹製函を複数に分割し、それ
ぞれに調節弁を設けた冷却水量制御置が紹介されてい
る。
The cooling water amount control device at the time of manufacturing granulated slag is disclosed in, for example, Japanese Patent Application Laid-Open No. 61-270238. As a device for suitably implementing this method, each blow box is divided into a plurality of pieces, and each is separately adjusted. A cooling water flow control device equipped with a valve is introduced.

これは、各吹製函に設けられているノズルプレートを
複数に分割し、各分割部分にそれぞれ水量調節弁を設け
ると共に全分割部分に設けられた噴射孔の総開口面積を
常時一定に保持することにより、冷却水ポンプの圧力と
全供給水量を常時一定値を保持しており、従って、冷却
水ポンプの運転が安定し、溶融高炉滓の量に応じて各調
節弁を開または閉の位置に操作することにより各吹製函
への供給水量を適切な分配比に保持しようとしたもので
ある。
This means that the nozzle plate provided in each blow box is divided into a plurality of parts, a water flow control valve is provided in each divided part, and the total opening area of the injection holes provided in all divided parts is always kept constant. As a result, the pressure of the cooling water pump and the total amount of supplied water are always maintained at constant values, so that the operation of the cooling water pump is stabilized, and each control valve is opened or closed according to the amount of molten blast furnace slag. In this way, the amount of water supplied to each blow box was maintained at an appropriate distribution ratio.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

冷却水量制御方法に関しては、従来技術においては、
水砕スラグ量が含水量の影響を受け、その結果、いずれ
も測定精度が悪い等の理由で未だに工業的に活用されて
いる技術手段がなく、従って、変動するスラグ量に応じ
た適切な冷却水量の制御方法はないのが現状であった。
Regarding the cooling water amount control method, in the prior art,
The amount of granulated slag is affected by the water content, and as a result, there are no technical means that are still industrially used due to poor measurement accuracy, etc., and therefore, appropriate cooling according to the fluctuating slag amount At present, there is no method for controlling the amount of water.

また冷却水量制御置に関しては、前記特開昭61−2702
38号では次のような問題があった。すなわち、 溶融高炉滓量の変動に対応した冷却水の供給水量の分
配比が変動する。
Regarding the cooling water amount control device, see Japanese Patent Laid-Open No.
No. 38 had the following problems. That is, the distribution ratio of the supply amount of cooling water corresponding to the change in the amount of molten blast furnace slag changes.

各ノズルプレートに設けられた噴射孔が摩耗するの
で、これに伴い水量、水圧が変動する。
Since the injection holes provided in each nozzle plate are worn, the amount of water and the water pressure fluctuate accordingly.

上記の原因によって、水砕スラグの粒化冷却条件が変
化し製品品質が変動する。
Due to the above factors, the granulation and cooling conditions of the granulated slag change, and the product quality changes.

多段吹製函としたので装置が大型化し、経済性、保全
性の面で劣る。
The multi-stage blow box makes the equipment bulky, and is inferior in economics and maintainability.

スラグと水の分配比が必要以上となるので製造コスト
が高くなる。
Since the distribution ratio of slag and water becomes more than necessary, the production cost increases.

本発明は、上述の問題点を解決するために提案された
ものであり、含水量の影響を受けないで水砕スラグ量を
正確に求め、この水砕スラグ量を把握することにより、
よりきめの細かい制御を可能とする冷却水量制御方法、
および、出滓量が変動してもこれに即応してスラグと冷
却水の分配比および吹製圧力が一定となるように制御し
て、製品品質の安定化を図る水砕スラグの冷却水量制御
装置を提供することを課題とするものである。
The present invention has been proposed in order to solve the above-described problems, accurately determine the amount of granulated slag without being affected by the water content, by grasping the amount of granulated slag,
Cooling water amount control method that enables finer control,
In addition, even if the amount of slag fluctuates, the distribution ratio of slag and cooling water and the blowing pressure are controlled so as to be constant in response to the change, and the cooling water amount control of granulated slag to stabilize product quality It is an object to provide a device.

〔課題を解決するための手段〕[Means for solving the problem]

本発明は、冷却水を溶滓に噴射させて水砕スラグスラ
リーとなし、スラリーを重力式脱水槽において脱水して
水砕スラグを製造する際の冷却水量制御方法および制御
装置に適用され、次の技術手段を採った。すなわち、 本発明方法は、水砕スラグがスラリー状態にある脱水
槽でその重量と容積を計測し演算すれば、含水量の影響
を受けないで水砕スラグ量を正確に測定することができ
るという知見によるものであり、 脱水槽に脱水槽内の水砕スラグスラリーの重量を計測
する重量計測器を設けると共に水砕スラグスラリーの容
積を計測する容積計測器を設け、これらの計測値に基づ
き、次式により脱水槽に流入するスラグ量を求め、スラ
グ量に応じて溶滓に対する冷却水量および冷却水噴射圧
を制御する方法である。
The present invention is applied to a method and a control device for controlling the amount of cooling water when producing granulated slag by spraying cooling water onto a slag to form granulated slag slurry and dewatering the slurry in a gravity dewatering tank to produce granulated slag. The technical measures were taken. That is, according to the method of the present invention, if the weight and volume of the granulated slag are measured and calculated in a dewatering tank in a slurry state, the granulated slag amount can be accurately measured without being affected by the water content. Based on the knowledge, the dewatering tank is provided with a weight measuring device that measures the weight of the granulated slag slurry in the dewatering tank, and a volume measuring device that measures the volume of the granulated slag slurry is provided.Based on these measured values, In this method, the amount of slag flowing into the dewatering tank is obtained by the following equation, and the amount of cooling water and the cooling water injection pressure for the slag are controlled according to the amount of slag.

WS=γS(W−γWV)/(γS−γW) ただし、 WS:水砕スラグの重量 W:脱水槽内の水砕スラグスラリーの重量 V:脱水槽内の水砕スラグスラリーの容積 γS:水砕スラグの比重 γW:脱水槽内の水の比重 である。W S = γ S (W−γ W V) / (γ S −γ W ) where W S : Weight of granulated slag W: Weight of granulated slag slurry in dewatering tank V: Granulated in dewatering tank Volume of slag slurry γ S : Specific gravity of granulated slag γ W : Specific gravity of water in the dewatering tank.

本発明の装置は、 変動する出滓量に対応してスラグと冷却水の分配比お
よび吹製圧力が所定の設定値となるよう冷却水流量を演
算する演算装置と、 演算装置の出力信号と冷却水流量計の信号および吹製
圧力計の信号から冷却水の流量調整弁と吹製圧力調整装
置をそれぞれ制御する制御装置を備えてなり、 吹製圧力調整装置は、複数の楔形状の調節弁体と、調
節弁体に嵌合する噴出孔を設けたノズルプレートと、調
節弁体と噴出孔との間隙を調整し吹製圧力を調整する調
節弁体駆動機から構成した。
The apparatus of the present invention is a computing device that computes a cooling water flow rate such that a distribution ratio of slag and cooling water and a blowing pressure are set to predetermined values in accordance with a fluctuating amount of slag, and an output signal of the computing device. The cooling water flow meter is provided with a control device for controlling the cooling water flow control valve and the blowing pressure control device based on the signal of the blowing pressure gauge, respectively. A valve body, a nozzle plate provided with an ejection hole fitted to the control valve body, and a control valve body drive device for adjusting the gap between the control valve body and the ejection hole to adjust the blowing pressure.

〔作用〕[Action]

(1)本発明方法において、脱水槽内の水砕スラグスラ
リーの重量W、脱水槽内の水砕スラグスラリーの容積
V、水砕スラグの比重γS、脱水槽内の水の比重γWから
水砕スラグの重量WSが求められる理由を以下に説明す
る、 脱水槽内の水砕スラグスラリーの重量Wは、水砕スラ
グの重量WSと水の重量WWとの和で表わされる。すなわ
ち、 W=WW+WS ここに、 WW=γW(V−WS/γS) で表わされるから、 W=γW(V−WS/γS)+WS =γWV−γWWS/γS+WS 従って、 WS−γWWS/γS=W−γWV WS(1−γW/γS)=W−γWV WS=γS(W−γWV)/(γS−γW) すなわち、水砕スラグの重量WSが得られる。
(1) In the method of the present invention, from the weight W of the granulated slag slurry in the dewatering tank, the volume V of the granulated slag slurry in the dewatering tank, the specific gravity γ S of the granulated slag, and the specific gravity γ W of the water in the dewatering tank The reason why the weight W S of the granulated slag is required will be described below. The weight W of the granulated slag slurry in the dewatering tank is represented by the sum of the weight W S of the granulated slag and the weight W W of the water. That is, here W = W W + W S, because represented by W W = γ W (V- W S / γ S), W = γ W (V-W S / γ S) + W S = γ W V- γ W W S / γ S + W S Therefore, W S -γ W W S / γ S = W-γ W V W S (1-γ W / γ S) = W-γ W V W S = γ S ( W-γ W V) / ( γ S -γ W) that is, the weight W S of granulated slag is obtained.

この水砕スラグの重量WSによってよりきめの細かい冷
却水量の制御が可能となるので、水砕の品質向上を図る
ことができる。
Since the control of finer cooling water by weight W S of the water granulated slag becomes possible, it is possible to improve the quality of the water-granulated.

(2)本発明装置の作用を説明する。出滓量(出滓速
度)は1〜10ton/minの範囲で変化するが、製品品質、
製造コスト並びに安全対策上冷却水とスラグの分配比は
4〜10とする必要がある。本発明は上述のように構成し
たので、出滓量が変動してもこれに即応して、冷却水の
流量調節弁および吹製圧力調整装置の調節弁体を制御す
ることが可能となり、スラグと冷却水の分配比および吹
製圧力を一定に維持することができる。また、調節弁体
と噴出孔の摩耗による冷却水の水量、水圧の変動はな
い。
(2) The operation of the device of the present invention will be described. The amount of slag (slag speed) varies in the range of 1 to 10 ton / min.
The distribution ratio between the cooling water and the slag needs to be 4 to 10 in view of production cost and safety measures. Since the present invention is configured as described above, it is possible to control the flow rate control valve of the cooling water and the control valve element of the blowing pressure control device immediately in response to the change in the amount of slag, And the distribution ratio of the cooling water and the blowing pressure can be kept constant. In addition, there is no fluctuation in the amount and pressure of the cooling water due to wear of the control valve body and the ejection hole.

従って、製品品質の安定化並びに冷却水ポンプの運転
経費の節減を図ることができる。
Therefore, it is possible to stabilize the product quality and reduce the operation cost of the cooling water pump.

〔実施例〕〔Example〕

第1図に本発明の水砕スラグ製造時の冷却水量制御装
置並びに冷却水の系統図を示す。第2図は本発明の圧力
調整装置の一実施例の説明図、第3図は第2のA−A断
面図である。
FIG. 1 shows a system diagram of a cooling water amount control device and a cooling water system at the time of producing granulated slag of the present invention. FIG. 2 is an explanatory view of an embodiment of the pressure adjusting device of the present invention, and FIG. 3 is a sectional view taken along the line AA of FIG.

第1図に示すように、吹製函に流入した溶滓に圧力水
を噴射させて水砕スラグスラリーとなし、水砕スラグス
ラリーは撹拌槽13から水砕ポンプ14によって脱水槽20に
搬送される。この脱水槽20は槽下部に脱水スクリーン24
を備え、水砕スラグを沈降させ水砕スラグの濾過作用を
利用して脱水するいわゆる重量脱水を行なっている。オ
ーバーフロー配管16或は脱水配管15から流出した水は温
水槽17に貯留され、この水に含有される微細スラグを除
去した後、ポンプで冷却塔18に送られ、冷却塔18で冷却
され冷却槽19の貯留される。この水は冷却水ポンプ7に
よって冷却水配管6に供給され再び圧力水として循環使
用されように構成されている。
As shown in FIG. 1, pressurized water is injected into the slag flowing into the blowing box to form granulated slag slurry, and the granulated slag slurry is conveyed from the stirring tank 13 to the dewatering tank 20 by the granulation pump 14. You. This dewatering tank 20 has a dewatering screen 24 at the bottom of the tank.
So-called heavy dewatering is performed in which the granulated slag is settled and dewatered by utilizing the filtering action of the granulated slag. The water flowing out of the overflow pipe 16 or the dewatering pipe 15 is stored in a hot water tank 17, and after removing fine slag contained in the water, the water is sent to a cooling tower 18 by a pump, and cooled in the cooling tower 18 to be cooled. 19 are stored. This water is supplied to the cooling water pipe 6 by the cooling water pump 7 and is circulated and used again as pressure water.

第1図では、脱水槽20の下部に水砕スラグスラリー中
の水砕スラグ23が沈降している状態を示している。脱水
槽20内の水砕スラグスラリーの重量Wは脱水槽20に設け
たロードセル22によって計測することができる。この
際、予め脱水槽20内に水を注入することによって、ロー
ドセル22の校正が精度よく実施できるので、ロードセル
22による計測は正確に行うことができる。また、水砕ス
ラグスラリーの容積Vは脱水槽20に設けた水位計21によ
り正確に計測可能である。
FIG. 1 shows a state in which the granulated slag 23 in the granulated slag slurry is settled below the dewatering tank 20. The weight W of the granulated slag slurry in the dewatering tank 20 can be measured by a load cell 22 provided in the dewatering tank 20. At this time, by injecting water into the dewatering tank 20 in advance, the load cell 22 can be calibrated with high accuracy.
The measurement by 22 can be performed accurately. Further, the volume V of the granulated slag slurry can be accurately measured by a water level gauge 21 provided in the dewatering tank 20.

水砕スラグの比重γSは水中であるので真比重に近似
しており、また、脱水槽内の水の比重γWはその温度を
測定することにより容易に求めることができる。
Since the specific gravity γ S of the granulated slag is in water, it is close to the true specific gravity, and the specific gravity γ W of the water in the dewatering tank can be easily obtained by measuring the temperature.

水砕スラグの重量WSを経時的に計測すれば水砕スラグ
の生産量および生産速度(出滓速度ton/min)も容易に
得られる。この水砕スラグの重量WSによって冷却水量を
制御することができる。
If over time weighed W S of granulated slag production and production rate of the water granulated slag (tapping speed ton / min) it is also easily obtained. It is possible to control the amount of cooling water by the weight W S of the water granulated slag.

本発明の制御装置は第1図に示すように、冷却水ポン
プ7から冷却水が供給される冷却水配管6には流量計2
および流量調節弁3が、また、吹製函には圧力計4およ
び圧力調節弁体5が夫々備えられている。また、演算装
置11は変動する出滓量に対応してスラグと冷却水の分配
比が所定の設定値となるよう冷却水流量を演算する。制
御装置12はこの演算結果と冷却水流量計2および吹製圧
力計4の信号により流量調節弁3および圧力調整装置1
を制御するものである。
As shown in FIG. 1, the control device of the present invention includes a flow meter 2 in a cooling water pipe 6 to which cooling water is supplied from a cooling water pump 7.
And a flow control valve 3, and the blow box is provided with a pressure gauge 4 and a pressure control valve body 5, respectively. Further, the arithmetic unit 11 calculates the flow rate of the cooling water such that the distribution ratio of the slag and the cooling water becomes a predetermined set value according to the fluctuating amount of slag. The controller 12 uses the result of the calculation and signals from the cooling water flow meter 2 and the blowing pressure gauge 4 to control the flow regulating valve 3 and the pressure regulating device 1.
Is controlled.

本装置では、出滓量の変動は、演算装置11の演算結果
を入力しているが、溶融スラグ量や撹拌槽の水温の変化
等を自動検出して入力することも可能である。実用的に
は目測結果を入力しても差支えない。
In the present apparatus, the change in the amount of slag is input by the calculation result of the arithmetic unit 11, but it is also possible to automatically detect and input the amount of molten slag, the change in the water temperature of the stirring tank, and the like. In practice, it is acceptable to input the eye measurement results.

圧力調整装置1は第2図に示すように、2組の楔形状
の調節弁体5と、調節弁体5に嵌合する噴出孔9を設け
たノズルプレート10と、調節弁体5を駆動し吹製圧力を
調整する調節弁体駆動機8から構成されている。調節弁
体駆動機8は第1図に示す制御装置12によって制御され
吹製圧力を制御する。
As shown in FIG. 2, the pressure regulating device 1 drives two sets of wedge-shaped regulating valve bodies 5, a nozzle plate 10 provided with ejection holes 9 fitted to the regulating valve bodies 5, and the regulating valve body 5. It comprises a regulating valve drive 8 for adjusting the blowing pressure. The control valve drive 8 is controlled by the control device 12 shown in FIG. 1 to control the blowing pressure.

第4図は本発明の実施結果を示すグラフである。これ
は、冷却水ポンプ7を3台使用し、分配比を5として操
業した場合の出滓時間と給水量の関係を示している。従
来例では、出滓量を正確に把握できなかったため、安全
をとって給水量を早めに増量していた。本発明では分配
比が5以下になる直前に給水量を増量することができる
ので使用水量が節減でき電力コストを低減することが可
能になった。また、吹製函のノズルを多段にしなくても
よく、1段でよく設備規模の縮小を図ることができる。
FIG. 4 is a graph showing the results of the implementation of the present invention. This shows the relationship between the slag time and the water supply amount when three cooling water pumps 7 are used and the operation is performed with the distribution ratio set to 5. In the conventional example, since the amount of slag could not be accurately grasped, the amount of water supply was increased promptly for safety. In the present invention, since the amount of water supply can be increased immediately before the distribution ratio becomes 5 or less, the amount of water used can be reduced and the power cost can be reduced. In addition, the number of nozzles of the blow box need not be multi-stage, and the size of the equipment can be reduced with only one stage.

〔発明の効果〕〔The invention's effect〕

本発明は次のような極めて優れた効果を奏する。 The present invention has the following extremely excellent effects.

冶金炉の出滓量管理および冶金炉の制御技術の大幅な
改善を図ることが可能となり、生産性の向上に寄与する
ことができる。
It is possible to significantly improve the control of the amount of slag in the metallurgical furnace and the control technology of the metallurgical furnace, which can contribute to an improvement in productivity.

溶融スラグの量に応じて冷却水の分配比や吹製圧力を
一定に保つことが可能となるので、製品品質の安定化並
びに電力費の低減を図ることができる。
Since the distribution ratio of the cooling water and the blowing pressure can be kept constant according to the amount of the molten slag, the product quality can be stabilized and the power cost can be reduced.

冷却水の分配比や吹製圧力を任意に設定することがで
きるので性質の異なった水砕スラグを容易に製造するこ
とができる。
Since the distribution ratio of the cooling water and the blowing pressure can be arbitrarily set, granulated slags having different properties can be easily produced.

吹製函のノズルを1段として設備規模の縮小を図るこ
とができる。
The size of the equipment can be reduced by using one nozzle for the blow box.

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

第1図は本発明の冷却水量制御装置並びに冷却水の系統
図、第2図は本発明の圧力調整装置の一実施例の説明
図、第3図は第2図のA−A断面図、第4図は本発明の
実施結果を示すグラフである。 1…圧力調整装置 2…流量計 3…流量調節弁 4…圧力計 5…調節弁体 6…冷却水配管 7…ポンプ 8…調節弁体駆動機 9…噴出孔 10…ノズルプレート 11…演算装置 12…制御装置 20…脱水槽 21…水位計 22…ロードセル 23…水砕スラグ 24…脱水スクリーン
FIG. 1 is a system diagram of a cooling water amount control device and cooling water of the present invention, FIG. 2 is an explanatory diagram of an embodiment of a pressure adjusting device of the present invention, FIG. 3 is a cross-sectional view taken along line AA of FIG. FIG. 4 is a graph showing the results of the implementation of the present invention. DESCRIPTION OF SYMBOLS 1 ... Pressure adjustment device 2 ... Flow meter 3 ... Flow control valve 4 ... Pressure gauge 5 ... Control valve body 6 ... Cooling water piping 7 ... Pump 8 ... Control valve body driving machine 9 ... Injection hole 10 ... Nozzle plate 11 ... Calculation device 12 ... Control device 20 ... Dehydration tank 21 ... Water level gauge 22 ... Load cell 23 ... Granulated slag 24 ... Dehydration screen

フロントページの続き (72)発明者 橋本 正広 岡山県倉敷市水島川崎通1丁目(番地な し) 川鉄鉱業株式会社水島製造所内Continued on the front page (72) Inventor Masahiro Hashimoto 1-chome, Kawasaki-dori, Mizushima, Kurashiki-shi, Okayama Pref.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】冷却水を溶滓に噴射させて水砕スラグスラ
リーとなり、該スラリーを重力式脱水槽において脱水し
て水砕スラグを製造するにあたり、 前記脱水槽に該脱水槽内の水砕スラグスラリーの重量を
計測する重量計測器を設けると共に該水砕スラグスラリ
ーの容積を計測する容積計測器を設け、これらの計測値
に基づき、次式により該脱水槽に流入するスラグ量を求
め、該スラグ量に応じて前記溶滓に対する冷却水量およ
び冷却水噴射圧を制御することを特徴とする冷却水量制
御方法。 WS=γS(W−γWV)/(γS−γW) ただし、 WS:水砕スラグの重量 W:脱水槽内の水砕スラグスラリーの重量 V:脱水槽内の水砕スラグスラリーの容積 γS:水砕スラグの比重 γW:脱水槽内の水の比重 である。
1. A method for producing granulated slag by injecting cooling water into a slag to form granulated slag slurry and dewatering the slurry in a gravity dewatering tank to produce granulated slag. Provide a weight measuring device to measure the weight of the slag slurry and provide a volume measuring device to measure the volume of the granulated slag slurry, based on these measured values, determine the amount of slag flowing into the dewatering tank by the following equation, A method for controlling the amount of cooling water, wherein the amount of cooling water and the cooling water injection pressure for the slag are controlled according to the amount of slag. W S = γ S (W−γ W V) / (γ S −γ W ) where W S : Weight of granulated slag W: Weight of granulated slag slurry in dewatering tank V: Granulated in dewatering tank Volume of slag slurry γ S : Specific gravity of granulated slag γ W : Specific gravity of water in the dewatering tank.
【請求項2】変動する出滓量に対応してスラグと冷却水
の分配比および吹製圧力が所定の設定値となるよう冷却
水流量を演算する演算装置と、該演算装置の出力信号と
冷却水流量計の信号および吹製圧力計の信号から冷却水
の流量調整弁と吹製圧力調整装置をそれぞれ制御する制
御装置を備えてなり、前記吹製圧力調整装置は、複数の
楔形状の調節弁体と、該調節弁体に嵌合する噴出孔を設
けたノズルプレートと、該調節弁体と該噴出孔との間隙
を調整し吹製圧力を調整する調節弁体駆動機を備えた冷
却水量制御装置。
2. An arithmetic unit for calculating a cooling water flow rate such that a distribution ratio of slag and cooling water and a blowing pressure are set to predetermined values in accordance with a fluctuating amount of slag, and an output signal of the arithmetic unit. A cooling water flow meter signal and a blowing pressure gauge signal are used to control a cooling water flow regulating valve and a blowing pressure adjusting device, respectively.The blowing pressure adjusting device has a plurality of wedge-shaped A control valve body, a nozzle plate provided with an ejection hole to be fitted to the control valve body, and a control valve body drive device for adjusting a gap between the control valve body and the ejection hole to adjust blowing pressure. Cooling water amount control device.
JP22635388A 1988-09-12 1988-09-12 Method and apparatus for controlling cooling water amount during production of granulated slag Expired - Lifetime JP2587472B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22635388A JP2587472B2 (en) 1988-09-12 1988-09-12 Method and apparatus for controlling cooling water amount during production of granulated slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22635388A JP2587472B2 (en) 1988-09-12 1988-09-12 Method and apparatus for controlling cooling water amount during production of granulated slag

Publications (2)

Publication Number Publication Date
JPH0274544A JPH0274544A (en) 1990-03-14
JP2587472B2 true JP2587472B2 (en) 1997-03-05

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Application Number Title Priority Date Filing Date
JP22635388A Expired - Lifetime JP2587472B2 (en) 1988-09-12 1988-09-12 Method and apparatus for controlling cooling water amount during production of granulated slag

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Country Link
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109825657A (en) * 2019-04-03 2019-05-31 中冶赛迪工程技术股份有限公司 Blast furnace cinder slag discharge amount on-line measuring device and method

Also Published As

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JPH0274544A (en) 1990-03-14

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