JPS6312132B2 - - Google Patents

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Publication number
JPS6312132B2
JPS6312132B2 JP56032873A JP3287381A JPS6312132B2 JP S6312132 B2 JPS6312132 B2 JP S6312132B2 JP 56032873 A JP56032873 A JP 56032873A JP 3287381 A JP3287381 A JP 3287381A JP S6312132 B2 JPS6312132 B2 JP S6312132B2
Authority
JP
Japan
Prior art keywords
feo
sintered ore
amount
sintering
chute
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
Application number
JP56032873A
Other languages
Japanese (ja)
Other versions
JPS57149433A (en
Inventor
Tomya Fukuda
Masato Kono
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.)
Nippon Steel Nisshin Co Ltd
Original Assignee
Nisshin Steel Co Ltd
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 Nisshin Steel Co Ltd filed Critical Nisshin Steel Co Ltd
Priority to JP3287381A priority Critical patent/JPS57149433A/en
Publication of JPS57149433A publication Critical patent/JPS57149433A/en
Publication of JPS6312132B2 publication Critical patent/JPS6312132B2/ja
Granted legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】 この発明は、焼結鉱のFeO含有率の連続測定値
と最適FeO値との比較にもとづいて、焼結条件を
コントロールし、希望するFeO含有率の焼結鉱を
得る焼結方法及び同装置に関するものである。
[Detailed Description of the Invention] This invention controls sintering conditions based on a comparison between continuous measurement values of the FeO content of sintered ore and the optimum FeO value, and produces sintered ore with a desired FeO content. The present invention relates to a sintering method and apparatus for obtaining the same.

従来製鉄所の焼結設備で製造される焼結鉱は、
高炉原料用の鉄鉱石類の内で一般的に良好な原料
として評価されており、従つて高炉への装入割合
も鉄鉱石類の大半を占める状況にある。
Sintered ore, which is conventionally produced in sintering equipment at steel plants, is
It is generally regarded as a good raw material among iron ores used as raw material for blast furnaces, and therefore accounts for the majority of iron ores charged into blast furnaces.

また今日の省エネルギーあるいは省資源の観点
から、高炉設備においても低燃料比化が指向され
その検討結果も多く知られているところである。
Furthermore, from the point of view of energy conservation or resource conservation today, blast furnace equipment is also directed toward lower fuel ratios, and many of the results of this study are well known.

一方焼結鉱の性状は焼結の燃料比に関連するだ
けでなく、高炉操業の安定性やその燃料比に影響
を与えることが明らかにされており、そのため焼
結鉱の低温還元粉化性及び被還元性が特に重視さ
れているのが現状である。
On the other hand, it has been revealed that the properties of sintered ore are not only related to the fuel ratio of sintering, but also affect the stability of blast furnace operation and its fuel ratio, and therefore the properties of sintered ore are At present, particular emphasis is placed on reducibility and reducibility.

この低温還元粉化は高炉の300〜700℃の低温領
域(高炉のシヤフト上部)で焼結鉱が粉化する現
象であり、この性状が劣化すると高炉シヤフト部
のガス流れが悪化し、棚、スリツプなどを生ずる
不安定な炉況を誘発する因となる。
This low-temperature reduction pulverization is a phenomenon in which sintered ore is pulverized in the 300-700°C low-temperature region of the blast furnace (the upper part of the shaft of the blast furnace). When this property deteriorates, the gas flow in the shaft part of the blast furnace deteriorates, and the shelf, This can lead to unstable furnace conditions, such as slips.

また被還元性は焼結鉱が塊状状態でガスにより
還元される度合を表わすもので、この性状が向上
すると高炉のガス利用率が向上し、高炉燃料比は
低減すると考えられている。
Further, reducibility indicates the degree to which sintered ore is reduced by gas in a lumpy state, and it is thought that improving this property improves the gas utilization rate of the blast furnace and reduces the blast furnace fuel ratio.

これら還元性状は焼結鉱中のFeO量と関連し、
FeO量が多いほど低温還元粉化性は向上し、高炉
炉況は安定するものの被還元性は劣化するため、
高炉燃料比は逆に増大するという二律背反の関係
にあることが知られている。このように両還元性
状とFeO量の間には、焼結機や排風機の規模など
の違いにより異なる場合もあるがほぼ一定の関係
があることが周知されている。
These reduction properties are related to the amount of FeO in the sintered ore,
The higher the amount of FeO, the better the low-temperature reduction powdering property becomes, and the blast furnace condition becomes stable, but the reducibility deteriorates.
It is known that there is a trade-off relationship in which the blast furnace fuel ratio increases. In this way, it is well known that there is a nearly constant relationship between the two reduction properties and the amount of FeO, although this may vary depending on the size of the sintering machine and the exhaust fan.

以上の状況により、焼結鉱の性状さらには高炉
炉況のより一層の安定化を図るためには、焼結鉱
の最適FeO値を設定し、実際の焼結鉱のFeO含有
率の連続測定との比較制御による焼結操業管理を
行うことが不可欠と考えられる。
Under the above circumstances, in order to further stabilize the properties of sintered ore and the conditions of the blast furnace, it is necessary to set the optimum FeO value for sintered ore and continuously measure the FeO content of sintered ore. It is considered essential to manage sintering operations through comparative control.

これに対し現状の焼結操業では、焼結鉱の最適
FeO値は一定設定できるが、測定方法の制約から
測定に時間を要すると共に、測定のための連続し
た焼結鉱の供給や、焼結の性状安定化、焼結鉱成
品への寄与のための操業手段との連系などの方法
が十分に確立されていない状況にある。
On the other hand, in the current sintering operation, the optimum
Although the FeO value can be set at a constant value, it takes time to measure due to limitations in the measurement method, and it is necessary to continuously supply sinter for measurement, stabilize the properties of sinter, and contribute to sintered ore products. Methods such as interconnection with operational means have not been sufficiently established.

本発明は上記のような欠点を除去し、焼結鉱の
連続定量測定にもとづく制御管理により常に焼結
設備への焼結条件コントロールを行い、予め設定
したFeO値の焼結鉱を得る焼結方法及び同装置を
提供しようとするもので、以下の図面に基きこの
発明に係る実施例を説明する。
The present invention eliminates the above drawbacks, constantly controls the sintering conditions of the sintering equipment through control management based on continuous quantitative measurement of sintered ore, and enables sintering to obtain sintered ore with a preset FeO value. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In order to provide a method and an apparatus for the same, embodiments of the present invention will be described with reference to the following drawings.

第1図において垂直なパイプシユート6の外側
にはアウターパイプ7が同心状に配置されてお
り、パイプシユート6の外周には電磁コイル8が
配置されると共にアウターパイプ7の外周には磁
場付与用ソレノイド9が配置されている。パイプ
シユート6の上部は拡大して漏斗状になつてお
り、サンプリングを送り込む投入用シユート14
が臨ませてある。パイプシユート6の下端には適
当な空隙を保つて回転型テーブルフイーダー12
が配置されており、テーブルフイーダー12上に
近接して半径方向に対し角度を持つた水平状掻出
片13が静止状態に配置されており、掻出片13
の外端には移送用シユート15が接続してある。
以上によつて連続定量装置2が構成されている。
In FIG. 1, an outer pipe 7 is arranged concentrically outside the vertical pipe chute 6, an electromagnetic coil 8 is arranged around the outer periphery of the pipe chute 6, and a solenoid 9 for applying a magnetic field is arranged around the outer periphery of the outer pipe 7. is located. The upper part of the pipe chute 6 is enlarged to form a funnel shape, and is connected to an input chute 14 into which the sampling is sent.
is coming. A rotary table feeder 12 is provided at the lower end of the pipe chute 6 with an appropriate gap.
is arranged, and a horizontal scraping piece 13 having an angle with respect to the radial direction is placed in a stationary state close to the table feeder 12, and the scraping piece 13
A transfer chute 15 is connected to the outer end of the transfer chute 15 .
The continuous quantitative determination device 2 is configured as described above.

また、焼結機1からふるい分け装置28を経て
出された床敷用焼結鉱成品の一部は、サンプリン
グとして任意な手段によつて抽出され、投入用シ
ユート14に載せられるようになつている。
Further, a part of the sintered ore product for bedding discharged from the sintering machine 1 through the sieving device 28 is extracted by any means as a sampling, and placed on the input chute 14. .

制御装置3には電磁コイル8によつて得た測定
信号aと最適FeO値の信号bが入力されるように
なつており、制御装置3から出た制御出力信号c
は焼結条件コントロール装置4に入力されるよう
になつている。焼結条件コントロール装置4から
出た信号はコークス量を含む原料制御信号d、添
加水量に対する制御信号e及び焼結排風量に対す
る制御信号f等を出すようになつている。以上に
よつてFeO量検知制御手段17が構成されてい
る。
The control device 3 is configured to receive a measurement signal a obtained by the electromagnetic coil 8 and a signal b of the optimum FeO value, and a control output signal c output from the control device 3.
is input to the sintering condition control device 4. The signals output from the sintering condition control device 4 include a raw material control signal d including the amount of coke, a control signal e for the amount of added water, and a control signal f for the amount of sintering exhaust air. The FeO amount detection control means 17 is configured as described above.

焼結鉱5は、焼結鉱FeO含有率の連続定量2を
介して連続して上方から下方へと移動しながら、
外筒の磁場付与用電磁コイル9により適当な強さ
の磁界を与えられると共に、焼結鉱5のFeO量に
応じた磁気変化を内筒の電磁コイル8を介して電
圧として検出される。
The sintered ore 5 is continuously moved from the top to the bottom through the continuous determination 2 of the sintered ore FeO content, while
A magnetic field of appropriate strength is applied by the magnetic field applying electromagnetic coil 9 in the outer cylinder, and a magnetic change corresponding to the amount of FeO in the sintered ore 5 is detected as a voltage via the electromagnetic coil 8 in the inner cylinder.

この検出電圧はあらかじめ第2,3,4図で確
められている如く、検出電圧とFeO量との相関関
係は直線回帰できるデータにもとづき、焼結鉱
FeO量の含有率として連続測定され、該測定値を
入力信号aとして制御装置3にインプツトする。
As this detection voltage has been confirmed in advance in Figures 2, 3, and 4, the correlation between the detection voltage and the amount of FeO is based on data that can be linearly regressed.
The FeO content is continuously measured, and the measured value is input to the control device 3 as an input signal a.

そこで公知の検出手段により設定しておいた焼
結鉱5の最適FeO値bと比較した制御装置3の出
力信号cを、焼結条件コントロール装置4を介し
て焼結装置のFeO量制御に関係するコークス量を
含む原料制御信号d、添加水制御信号e、焼結排
風量制御信号f等を制御しつつ、できるだけ前記
測定値を最適FeO値に近づけるべく焼結操業条件
の十分な管理により、予め設定したFeO含有率の
成品焼結鉱を作るものである。
Therefore, the output signal c of the control device 3 compared with the optimum FeO value b of the sintered ore 5 set by a known detection means is sent to the control device 4 to control the amount of FeO in the sintering device. While controlling the raw material control signal d including the amount of coke to be added, the added water control signal e, the sintering exhaust air volume control signal f, etc., the sintering operating conditions are sufficiently managed to bring the measured value as close to the optimum FeO value as possible. This is to produce finished sintered ore with a preset FeO content.

第5図に示す如く前記焼結鉱FeO含有率の連続
定量装置2は、焼結鉱成品のうちの一定粒度の範
囲内の焼結鉱を連続投入する投入用シユート14
の直下に立設したパイプシユート6、その外周の
電磁コイル8を囲繞する耐振中間材10、さらに
その外側のアウターパイプ7、及び外周の磁場付
与用電磁ソレノイド9を囲む外套材11、ならび
にパイプシユート6の下方に配したテーブルフイ
ーダー12、掻出部13、移送用シユート15等
より構成されており、前述の制御装置3、焼結条
件コントロール装置4と共に、FeO量検知制御手
段17として焼結装置の一環を構成しているもの
である。
As shown in FIG. 5, the device 2 for continuously quantifying the FeO content of sintered ore includes a charging chute 14 into which sintered ore within a certain particle size range among the sintered ore products is continuously charged.
A pipe chute 6 erected directly below the pipe chute 6, a vibration-proof intermediate material 10 surrounding the electromagnetic coil 8 on its outer periphery, an outer pipe 7 on the outside thereof, a jacket material 11 surrounding the outer pipe 7 and the magnetic field applying electromagnetic solenoid 9 on the outer periphery, and the pipe chute 6. It is composed of a table feeder 12, a scraping part 13, a transfer chute 15, etc. arranged below, and is used as an FeO amount detection control means 17 of the sintering apparatus, together with the aforementioned control device 3 and sintering condition control device 4. It forms part of this.

第6図は公知の焼結工程図に本発明の手段の一
例を付加した状態を示す概要図で、貯鉱槽22に
送られた各種原料Aは一次ミキサー23、二次ミ
キサー24、原料装入ホツパー25、焼結機1、
クラツシヤー26、クーラー27、ふるい分け装
置28に送られる。ふるい分け装置28によつて
分けられた粒径不適な焼結鉱成品は返鉱移送手段
Bによつて貯鉱槽22へ戻される。ふるい分け装
置28によつて床敷用焼結鉱成品として床敷鉱受
入れ手段19に入つた焼結鉱成品の一部はサンプ
リング抽出手段16によつて前述のFeO検知制御
手段17に送られたのち戻入れ手段18に送られ
る。戻入れ手段18によつて送られる焼結鉱成品
とサンプリング抽出手段16をバイパスした焼結
鉱成品は床敷鉱として床敷鉱移送手段20によつ
て床敷ホツパー29へ送られる。床敷ホツパー2
9中の床敷鉱は前記焼結機1に送られる。
FIG. 6 is a schematic diagram showing an example of the means of the present invention added to a known sintering process diagram, in which various raw materials A sent to the ore storage tank 22 are transferred to the primary mixer 23, secondary mixer 24, Input hopper 25, sintering machine 1,
It is sent to a crusher 26, a cooler 27, and a sieving device 28. The sintered ore products having inappropriate particle sizes separated by the sieving device 28 are returned to the ore storage tank 22 by the return ore transfer means B. A part of the sintered ore product entered into the bedding ore receiving means 19 as a sintered ore product for bedding by the sieving device 28 is sent to the FeO detection control means 17 by the sampling extraction means 16, and then sent to the FeO detection control means 17 described above. It is sent to the return means 18. The sintered ore products sent by the return means 18 and the sintered ore products that have bypassed the sampling extraction means 16 are sent as bedding ore to the bedding hopper 29 by the bedding ore transfer means 20. Bedding hopper 2
The bedding ore in 9 is sent to the sintering machine 1.

FeO検知制御手段17から出たコークス量及び
原料調整を含む原料制御信号dは貯鉱槽22へ送
られ、コークスを含む焼結原料の比率を調整機構
Dによつて制御する。
A raw material control signal d including the amount of coke and raw material adjustment output from the FeO detection control means 17 is sent to the ore storage tank 22, and the ratio of the sintering raw material containing coke is controlled by the adjustment mechanism D.

また添加水量調整信号eは可変調整弁Eを調整
して二次ミキサー24に添加される水量を調整す
る。またFeO量検知制御手段から出た信号21は
焼結機1の層高処理装置Fに伝わり、またFeO量
検知制御手段から出た信号fは焼結機排風量調整
装置Gを制御して排風機30から煙突31へと抜
かれる風量を調整する。更にふるい分け装置28
から出た成品は高炉原料槽33を介して高炉34
へ送られる。
Further, the added water amount adjustment signal e adjusts the variable adjustment valve E to adjust the amount of water added to the secondary mixer 24. Further, the signal 21 output from the FeO amount detection control means is transmitted to the layer height processing device F of the sintering machine 1, and the signal f output from the FeO amount detection control means is discharged by controlling the sintering machine exhaust air volume adjustment device G. The amount of air discharged from the wind fan 30 to the chimney 31 is adjusted. Furthermore, the sieving device 28
The products discharged from the blast furnace are sent to the blast furnace 34 via the blast furnace raw material tank 33.
sent to.

上述した如く本発明に係る予め設定したFeO含
有率の焼結鉱を得る焼結方法は、FeO量の含有率
を連続して求める測定を行い、その連続測定値と
焼結鉱の最適FeO値とを比較し、最適FeO値に対
し連続測定値を可及的に近づける如く任意の制御
手段により少なくとも使用コークス量、添加水
量、排風量を変化させることを特徴とするもので
ある。
As described above, the sintering method for obtaining sintered ore with a preset FeO content according to the present invention involves continuously measuring the FeO content, and comparing the continuously measured value with the optimum FeO value of the sintered ore. The present invention is characterized in that at least the amount of coke used, the amount of added water, and the amount of discharged air are changed by an arbitrary control means so as to bring the continuously measured value as close as possible to the optimum FeO value.

また本発明に係る予め設定したFeO含有率の焼
結鉱を得る焼結装置は焼結鉱成品のうちの一定粒
度の焼結鉱を連続投入する投入用シユートを配置
し、同投入用シユート出口の直下に非磁性材製パ
イプシユートを立設し、該パイプシユート外周に
電磁コイルを配置し、該電磁コイルの外側に磁場
付与用ソレノイドを配置し、パイプシユート下方
に空隙を介してテーブルフイーダを設けて、焼結
鉱のFeO含有率の連続定量装置の測定信号を制御
装置に入力する如く構成し、最適FeO値と比較し
た制御装置の出力信号を、少なくとも使用コーク
ス量、添加水量、排風量のFeO量に関係する焼結
条件コントロール装置にインプツトする如く構成
したものである。
Further, the sintering apparatus for obtaining sintered ore with a preset FeO content according to the present invention is provided with a charging chute for continuously charging sintered ore of a certain particle size among the sintered ore products, A pipe chute made of non-magnetic material is erected directly under the pipe chute, an electromagnetic coil is arranged around the outer periphery of the pipe chute, a solenoid for applying a magnetic field is arranged outside the electromagnetic coil, and a table feeder is provided below the pipe chute with an air gap. , the measurement signal of the FeO content of the sintered ore from the continuous determination device is input to the control device, and the output signal of the control device compared with the optimum FeO value is calculated based on at least the amount of coke used, the amount of added water, and the amount of exhausted air. It is configured so as to be input to a sintering condition control device related to quantity.

このように焼結鉱FeO量を連続定量測定した測
定値をもとに焼結操業を十分に制御管理するた
め、予め設定したFeO含有率の焼結鉱の生産なら
びに供給が可能となり、高炉操業の安定化にも寄
与するなど利する所はきわめて大きい。
In this way, the sintering operation is sufficiently controlled and managed based on continuous quantitative measurements of the amount of FeO in the sintered ore, making it possible to produce and supply sintered ore with a preset FeO content, which improves blast furnace operation. The benefits are extremely large, such as contributing to the stabilization of the economy.

【図面の簡単な説明】[Brief explanation of the drawing]

図面はこの発明に係る予め設定したFeO含有率
の焼結鉱を得る焼結方法及び同装置の実施例につ
いてのもので、第1図は装置要部の垂直切断側面
図に一部の電気回路を模式的に記載し説明図を示
すものであり、第2図乃至第4図は焼結鉱の各塩
基度毎のFeO量と検出電圧との相関関係を示すも
ので、第2図は塩基度0.2〜0.8の場合、第3図は
同上1.0〜1.4の場合、第4図は同上1.5〜2.0の場
合を示すものである。第5図はFeO量連続定量装
置を垂直切断した概略正面図、第6図は焼結装置
の各工程説明図である。 1…焼結機、2…連続定量装置、3…制御装
置、4…焼結条件コントロール装置、5…焼結成
品、6…パイプシユート、7…アウターパイプ、
8…電磁コイル、9…磁場付与用ソレノイド、1
0…耐振中間材、11…外套材、12…テーブル
フイーダー、13…掻出片、14…投入用シユー
ト、15…移送用シユート、16…サンプリング
抽出手段、17…FeO量検知制御手段、18…戻
入れ手段、19…床敷鉱受入れ手段、20…床敷
鉱移送手段、21…信号、22…貯鉱槽、23…
一次ミキサー、24…二次ミキサー、25…原料
装入ホツパー、26…クラツシヤー、27…クー
ラー、28…ふるい分け装置、29…床敷ホツパ
ー、30…排風機、31…煙突、33…高炉原料
槽、34…高炉、A…原料、B…返還移送手段、
D…比率・原量制御信号、E…可変調整弁、F…
層高処理装置、G…焼結機排風量調節装置、a…
測定信号、b…最適FeO値の信号、c…制御出力
信号、d…原料制御信号、e…添加水量制御信
号、f…焼結排風量。
The drawings show an embodiment of the sintering method and apparatus for obtaining sintered ore with a preset FeO content according to the present invention. Figures 2 to 4 show the correlation between the amount of FeO and the detection voltage for each basicity of sintered ore; In the case of 0.2 to 0.8, FIG. 3 shows the case of 1.0 to 1.4 as above, and FIG. 4 shows the case of 1.5 to 2.0 as above. FIG. 5 is a vertically sectioned schematic front view of the device for continuously determining the amount of FeO, and FIG. 6 is an explanatory diagram of each step of the sintering device. 1... Sintering machine, 2... Continuous quantitative device, 3... Control device, 4... Sintering condition control device, 5... Sintered product, 6... Pipe chute, 7... Outer pipe,
8... Electromagnetic coil, 9... Solenoid for applying magnetic field, 1
0... Vibration-resistant intermediate material, 11... Mantle material, 12... Table feeder, 13... Scraping piece, 14... Input chute, 15... Transfer chute, 16... Sampling extraction means, 17... FeO amount detection control means, 18 ...Returning means, 19...Bed ore receiving means, 20...Bed ore transfer means, 21...Signal, 22...Ore storage tank, 23...
Primary mixer, 24... Secondary mixer, 25... Raw material charging hopper, 26... Crusher, 27... Cooler, 28... Sieving device, 29... Bedding hopper, 30... Exhaust fan, 31... Chimney, 33... Blast furnace raw material tank, 34...Blast furnace, A...Raw material, B...Return transfer means,
D...Ratio/quantity control signal, E...Variable adjustment valve, F...
Bed height processing device, G... Sintering machine exhaust air volume adjustment device, a...
Measurement signal, b... Optimum FeO value signal, c... Control output signal, d... Raw material control signal, e... Added water amount control signal, f... Sintering exhaust air volume.

Claims (1)

【特許請求の範囲】 1 FeO量の含有率を連続して求める測定を行
い、その連続測定値と焼結鉱の最適FeO値とを比
較し、最適FeO値に対し連続測定値を可及的に近
づける如く任意の制御手段により少なくとも使用
コークス量、添加水量、排風量を変化させること
を特徴とする予め設定したFeO含有率の焼結鉱を
得る焼結方法。 2 焼結鉱成品のうちの一定粒度の焼結鉱を連続
投入する投入用シユートを配置し、同投入用シユ
ート出口の直下に非磁性材製パイプシユートを立
設し、該パイプシユート外周に電磁コイルを配置
し、該電磁コイルの外側に磁場付与用ソレノイド
を配置し、パイプシユート下方に空隙を介してテ
ーブルフイーダを設けて、焼結鉱のFeO含有率の
連続定量装置の測定信号を制御装置に入力する如
く構成し、最適FeO値と比較した制御装置の出力
信号を、少なくとも使用コークス量、添加水量、
排風量のFeO量に関係する焼結条件コントロール
装置にインプツトする如く構成したことを特徴と
する予め設定したFeO含有率の焼結鉱を得る焼結
装置。
[Claims] 1. Measure the content of FeO continuously, compare the continuous measured values with the optimum FeO value of the sintered ore, and compare the continuous measured values with the optimum FeO value as much as possible. 1. A sintering method for obtaining sintered ore with a preset FeO content, characterized in that at least the amount of coke used, the amount of added water, and the amount of exhaust air are changed by arbitrary control means so as to approach the FeO content. 2 A charging chute for continuously charging sintered ore of a certain particle size among the sintered ore products is arranged, a pipe chute made of non-magnetic material is erected immediately below the exit of the charging chute, and an electromagnetic coil is installed around the outer circumference of the pipe chute. A solenoid for applying a magnetic field is placed outside the electromagnetic coil, a table feeder is provided below the pipe chute through a gap, and the measurement signal of the continuous quantitative device for determining the FeO content of sintered ore is input to the control device. The output signal of the control device compared with the optimum FeO value is configured such that at least the amount of coke used, the amount of added water,
1. A sintering device for obtaining sintered ore with a preset FeO content, characterized in that the information is input to a sintering condition control device related to the amount of FeO in the exhaust air volume.
JP3287381A 1981-03-07 1981-03-07 Method and device for preparing sintered ore having preset content of feo Granted JPS57149433A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3287381A JPS57149433A (en) 1981-03-07 1981-03-07 Method and device for preparing sintered ore having preset content of feo

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3287381A JPS57149433A (en) 1981-03-07 1981-03-07 Method and device for preparing sintered ore having preset content of feo

Publications (2)

Publication Number Publication Date
JPS57149433A JPS57149433A (en) 1982-09-16
JPS6312132B2 true JPS6312132B2 (en) 1988-03-17

Family

ID=12370980

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3287381A Granted JPS57149433A (en) 1981-03-07 1981-03-07 Method and device for preparing sintered ore having preset content of feo

Country Status (1)

Country Link
JP (1) JPS57149433A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5544784B2 (en) * 2009-08-17 2014-07-09 Jfeスチール株式会社 Sintering machine
EP3517632B1 (en) 2016-12-16 2021-11-24 JFE Steel Corporation Blast furnace operation method
EP3550037A4 (en) 2017-02-16 2020-01-08 JFE Steel Corporation Method for manufacturing sintered ore
JP6866856B2 (en) * 2018-01-30 2021-04-28 Jfeスチール株式会社 Sintered ore manufacturing method and blast furnace operation method
CN109371230B (en) * 2018-12-05 2020-03-03 江苏永钢集团有限公司 Method for adjusting solid fuel ratio in sintering ore raw material

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53118215A (en) * 1977-03-26 1978-10-16 Sumitomo Metal Ind Ltd Sintering method
JPS53130203A (en) * 1977-04-20 1978-11-14 Nippon Steel Corp Preliminary treating method for raw material to be sintered

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53118215A (en) * 1977-03-26 1978-10-16 Sumitomo Metal Ind Ltd Sintering method
JPS53130203A (en) * 1977-04-20 1978-11-14 Nippon Steel Corp Preliminary treating method for raw material to be sintered

Also Published As

Publication number Publication date
JPS57149433A (en) 1982-09-16

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