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JPH0772670B2 - Method for reducing uneven burning of sinter - Google Patents
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JPH0772670B2 - Method for reducing uneven burning of sinter - Google Patents

Method for reducing uneven burning of sinter

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Publication number
JPH0772670B2
JPH0772670B2 JP31439789A JP31439789A JPH0772670B2 JP H0772670 B2 JPH0772670 B2 JP H0772670B2 JP 31439789 A JP31439789 A JP 31439789A JP 31439789 A JP31439789 A JP 31439789A JP H0772670 B2 JPH0772670 B2 JP H0772670B2
Authority
JP
Japan
Prior art keywords
width direction
layer thickness
pallet
temperature
column
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
Application number
JP31439789A
Other languages
Japanese (ja)
Other versions
JPH03177787A (en
Inventor
仁志 田辺
Original Assignee
川崎製鉄株式会社
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Application filed by 川崎製鉄株式会社 filed Critical 川崎製鉄株式会社
Priority to JP31439789A priority Critical patent/JPH0772670B2/en
Publication of JPH03177787A publication Critical patent/JPH03177787A/en
Publication of JPH0772670B2 publication Critical patent/JPH0772670B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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〕 本発明はドワイトロイド式焼結機における焼結鉱の焼け
むら減少方法に関する。
TECHNICAL FIELD The present invention relates to a method for reducing uneven burn of sinter in a Dwightroid type sintering machine.

〔従来の技術〕[Conventional technology]

ドワイトロイド型の移動格子式焼結機において、パレッ
ト上の焼結鉱充填層の焼結状態を焼結機排鉱側端部で観
察すると、パレット上の充填層の幅方向に焼成の充分進
行した部分と、焼成の充分進行していない部分(未焼成
部分)とが存在し、いわゆるむら焼け現象が見られるこ
とがある。
In the Dwightroid type moving grid type sintering machine, observing the sintering state of the sinter ore packed bed on the pallet at the end of the sinter of the sinter machine, the sintering progressed sufficiently in the width direction of the packed bed on the pallet. In some cases, a so-called uneven burning phenomenon may be observed due to the presence of a burnt portion and a portion in which firing has not progressed sufficiently (non-fired portion).

このような幅方向のむら焼けが生ずると、焼結鉱の品質
(落下強度、粒度、化学成分等)の劣化やばらつきを招
来し、返鉱発生率が増加する。その結果、生産量が減少
するなど焼結鉱の生産にもたらす弊害は多大である。
When such uneven burning in the width direction occurs, the quality (falling strength, particle size, chemical composition, etc.) of the sintered ore is deteriorated or varied, and the occurrence rate of returned ore increases. As a result, there are many adverse effects on the production of sinter, such as a decrease in production.

そこで、焼結機排鉱部におけるパレット幅方向のウイン
ドボックス温度Tiまた排鉱部のシンターケーキの赤熱帯
断面積HZRiを測定し、その結果に基づきパレット幅方向
における原料の供給量を調整することが行われている。
例えば、これらは特公昭50−40361号公報、特公昭51−2
3365号公報、特公昭60−10096号公報などに開示されて
いる。
Therefore, the wind box temperature Ti in the pallet width direction in the sinter machine mine or the red tropical cross-section HZRi of the sinter cake in the mine mine should be measured, and the raw material supply in the pallet width direction should be adjusted based on the results. Is being done.
For example, these are Japanese Examined Patent Publication No. 40-40361 and Japanese Examined Patent Publication No. 51-2.
It is disclosed in Japanese Patent No. 3365, Japanese Patent Publication No. 6010096, and the like.

第3図はこのことを説明する模式図であって、焼結機の
要部の斜視図に測定、制御系統を加えた説明図である。
FIG. 3 is a schematic diagram for explaining this, and is an explanatory diagram in which a measurement and control system is added to a perspective view of a main part of the sintering machine.

第3図において、1は給鉱ホッパ、2は原料供給用ドラ
ムフィーダ、3は生産量に応じ開度を設定した主ゲー
ト、4はパレットである。
In FIG. 3, 1 is a feed hopper, 2 is a raw material supply drum feeder, 3 is a main gate whose opening is set according to the production amount, and 4 is a pallet.

ドラムフィーダ2の幅方向の供給量を微調整するために
分割操作式の調整ゲート5が設けられており、この調整
ゲート5はパワーシリンダ6によって駆動される。パレ
ット上の原料層Aの層厚Hiは超音波レベル計7で測定さ
れる。また排鉱部のウインドボックス温度計8の測定値
や、排鉱部シンターケーキの赤熱帯断面積を測定するIT
Vカメラ9の観察データは上位プロセスコンピュータ10
に入力され、上位プロセスコンピュータ10の出力は下位
マイクロコンピュータ11に入力され、必要な制御が行わ
れる。
A division operation type adjustment gate 5 is provided for finely adjusting the widthwise supply amount of the drum feeder 2. The adjustment gate 5 is driven by a power cylinder 6. The layer thickness Hi of the raw material layer A on the pallet is measured by the ultrasonic level meter 7. IT that measures the measured value of the windbox thermometer 8 in the mine ore and the red tropical cross section of the sinter cake in the mine ore
The observation data of the V camera 9 is the upper process computer 10
, And the output of the upper process computer 10 is input to the lower microcomputer 11 to perform necessary control.

従来技術では排鉱部ウインドボックス温度Ti又は排鉱部
のシンターケーキの赤熱帯断面積HZRiを連続測定し、プ
ロセスコンピュータ10ではTi、HZRiのばらつきをなくす
るように、幅方向の層厚偏差△Hisvすなわち平均層厚と
測定層厚との差が一定時間毎に設定される。マイクロコ
ンピュータ11では、層厚Hiの測定結果をもとに、プロセ
スコンピュータよりの指示値△Hisvに一致するようにパ
ワーシリンダー6を駆動させ調整ゲート5の開度を制御
する。平均層厚はドラムフィーダー2の回転数制御に
より供給量(排出量)が制御され、設定層厚になるよう
に管理される。
In the prior art, the exhaust box windbox temperature Ti or the red tropical cross-sectional area HZRi of the sinter cake in the exhaust section is continuously measured, and the process computer 10 eliminates variations in Ti and HZRi so that the layer thickness deviation in the width direction Δ Hisv, that is, the difference between the average layer thickness and the measured layer thickness is set at regular intervals. In the microcomputer 11, the power cylinder 6 is driven to control the opening degree of the adjustment gate 5 so as to match the instruction value ΔHisv from the process computer based on the measurement result of the layer thickness Hi. The average layer thickness is controlled so that the supply amount (discharging amount) is controlled by controlling the number of rotations of the drum feeder 2 and the set layer thickness is obtained.

一般には、主に排鉱部温度Tiを平滑にすべく、幅方向別
に層厚△Hisvを設定するが、この設定値の与え方がこの
制御で最も難しい点であった。
Generally, the layer thickness ΔHisv is set in each width direction mainly to smooth the temperature Ti of the mine ore, but the method of giving this set value was the most difficult point in this control.

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

幅方向別の層厚Hiと排鉱部ウインドボックス温度Tiの関
係を4日間に亘って調査し、これを第4図に示す。第4
図に示すように層厚Hiと温度Tiは負の相関があるので、
通気がよくて温度Tiが高い列は層厚Hiを上げ、逆の列は
層厚Hiを下げればよい。ところが、この層厚Hiと温度Ti
の関係は場所によりまた時間により変化する。第4図に
はNo.1〜5ゲートのそれぞれについて測定値を記入し、
その関係を5本の直線で示している。このように、層厚
Hiと温度Tiの関係は場所、時間により変る。そのため、
直近数時間のデータを基に層厚Hiと温度Tiの相関を列毎
に求め、その直線の傾きを基に層厚Hiのアクション幅を
決定するシステムが考えられる。
The relationship between the bed thickness Hi in each width direction and the windbox temperature Ti of the mine ore was investigated over 4 days and is shown in Fig. 4. Fourth
As shown in the figure, since the layer thickness Hi and the temperature Ti have a negative correlation,
The layer thickness Hi should be increased in the rows with good ventilation and high temperature Ti, and the layer thickness Hi should be decreased in the opposite row. However, this layer thickness Hi and temperature Ti
The relationship of changes with place and with time. In Fig. 4, enter the measured values for each of No. 1 to 5 gates,
The relationship is shown by five straight lines. Thus, the layer thickness
The relationship between Hi and temperature Ti changes depending on the place and time. for that reason,
A system is conceivable in which the correlation between the layer thickness Hi and the temperature Ti is obtained for each column based on the data of the last few hours, and the action width of the layer thickness Hi is determined based on the slope of the straight line.

ところが、排鉱部ウインドボックス温度Tiに影響を与え
る因子としては、層厚Hiのほかにパレット上の焼結原料
の充填密度、粒度構成、水分含有量またはパレットの目
詰まり、漏風等の種々の因子が関与するため、数時間の
データで層厚Hiと温度Tiの相関関係を調べても明確な関
係式が得られることはほとんどない。
However, as factors affecting the exhaust box wind box temperature Ti, in addition to the layer thickness Hi, there are various factors such as the packing density of the sintering raw material on the pallet, the grain size composition, the water content or the clogging of the pallet, and the leakage of air. Since a factor is involved, a clear relational expression is rarely obtained even if the correlation between the layer thickness Hi and the temperature Ti is investigated with data of several hours.

そのため、現状では層厚Hiの変更量に対する温度Tiの変
化幅は一定と仮定し、幅方向別に層厚偏差△Hiを設定し
制御している。よりきめ細く温度Tiの幅方向バラツキを
なくす制御を行うためには、層厚Hiと温度Tiとの関係を
数時間毎に列毎に見直す必要がある。
Therefore, under the present circumstances, it is assumed that the variation width of the temperature Ti with respect to the variation amount of the layer thickness Hi is constant, and the layer thickness deviation ΔHi is set and controlled in each width direction. In order to perform finer control to eliminate the variation in the temperature Ti in the width direction, it is necessary to review the relationship between the layer thickness Hi and the temperature Ti every several hours for each column.

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

ところが、列毎に層厚の絶対値Hiと排鉱部ウインドボッ
クス温度の絶対値Tiとの関係を求めても、他の因子の影
響でなかなかよい相関は得られなかった。
However, even when the relationship between the absolute value Hi of the bed thickness and the absolute value Ti of the windbox temperature of the mine ore was obtained for each row, a good correlation could not be obtained due to the influence of other factors.

そこで、Tiに影響するHi以外の因子の影響をなるべく排
除するため、幅方向層厚偏差△Hiと幅方向ウインドボッ
クス温度偏差△Tiの関係を求めてみた。第2図に一例を
示すが△Hiと△Tiとは非常によい相関があった。データ
は真近4時間であり、ここのデータは30分平均値であ
る。また、層厚Hiと排鉱部のウインドボックス温度Tiと
はトラベリング時間を考え約30分の時間遅れをもって対
応させている。
Therefore, in order to eliminate the influence of factors other than Hi that affect Ti as much as possible, the relationship between the widthwise layer thickness deviation ΔHi and the widthwise windbox temperature deviation ΔTi was sought. An example is shown in Fig. 2, but there was a very good correlation between ΔHi and ΔTi. The data is for the last 4 hours and the data here is a 30 minute average. In addition, the layer thickness Hi and the windbox temperature Ti of the mine ore are correlated with a time delay of about 30 minutes considering the traveling time.

このように幅方向層厚偏差△Hiと幅方向排鉱部ウインド
ボックス温度偏差△Tiは常によい相関関係があるので、
この回帰式の傾きKiを用いて層厚アクション量を決定す
るシステムとすれば、よりきめ細かい幅方向むら焼け管
理ができることを知見し本発明を完成した。
In this way, there is always a good correlation between the widthwise layer thickness deviation ΔHi and the widthwise ore discharge part windbox temperature deviation ΔTi.
The present inventors have completed the present invention by finding that a system for determining the layer thickness action amount using the slope Ki of this regression equation enables more fine-grained uneven burn management in the width direction.

本発明は、ドワイトロイド式焼結機の操業に当り、排鉱
側ウインドボックスにおけるパレット幅方向複数列につ
いて第i列の複数個のパレットの平均温度とパレット幅
方向平均温度との偏差△Tiを求め、一方給鉱側のパレッ
ト幅方向複数列についての充填層の層厚の第i列の複数
個のパレットの平均層厚とパレット幅方向平均層厚との
偏差△Hiを求め、対応する幅方向複数列の各△Hiの変化
量に対応する各△Tiの回帰分析を行って第i列の層厚の
修正量を推定し、その推定修正量に基いてパレット幅方
向各列の層厚を調整し焼けむらを防止することを特徴と
する焼結鉱の焼けむら減少方法である。
In the operation of the Dwightroid-type sintering machine, the present invention calculates the deviation ΔTi between the average temperature of a plurality of pallets in the i-th row and the average temperature in the pallet width direction for a plurality of rows in the pallet width direction in the mine side windbox. On the other hand, the deviation ΔHi between the average layer thickness of the plurality of pallets in the i-th row and the average layer thickness in the pallet width direction of the packing thickness of the plurality of columns in the pallet width direction on the mine side is calculated, and the corresponding width is calculated. Direction of each ΔHi corresponding to the change amount of each ΔHi is performed regression analysis to estimate the correction amount of the layer thickness of the i-th column, and the layer thickness of each column in the pallet width direction is estimated based on the estimated correction amount. Is a method for reducing uneven burn of sintered ore, which is characterized by adjusting unevenness.

〔作用〕[Action]

本発明の実施に用いるシステム構成自体は第3図に示す
従来の技術と同じである。本発明はプロセスコンピュー
タにおいて層厚偏差△Hisvを設定する方法であり、その
概略フローを第1図に示す。
The system configuration itself used for implementing the present invention is the same as the conventional technique shown in FIG. The present invention is a method for setting the layer thickness deviation ΔHisv in a process computer, and its schematic flow is shown in FIG.

第1図はパレット幅方向5カ所の排鉱部ウインドボック
ス温度Tiを均一にするための制御システムを示す。
FIG. 1 shows a control system for making the exhaust box wind box temperature Ti uniform at five locations in the pallet width direction.

データの対応をとるためにパレット毎に列毎の層厚Hi
j、排鉱部のウインドボックス温度Tijをサンプリングす
る。指定したパレット数n個のデータがたまるとパレッ
ト幅方向別(列毎)に平均値▲▼、▲▼を求め
る。さらに全列の平均値 を求め、全列の平均値からの偏差△Hi、△Tiを列毎に計
算する。△Hi、△Tiデータはファイル内に保存される。
Layer thickness Hi for each row for each pallet to ensure data correspondence
j, Windbox temperature Tij of the mine is sampled. When the data of the specified number of pallets n is accumulated, average values ▲ ▼ and ▲ ▼ are obtained for each pallet width direction (each column). Furthermore, the average value of all columns And the deviations ΔHi and ΔTi from the average value of all columns are calculated for each column. The ΔHi and ΔTi data are saved in the file.

学習周期に達すると、パレット幅方向別(列毎)に、直
近4時間分程度のデータを用い、△Tiと△Hiの回帰分析
を行う。得られた回帰直線の相関係数γiが基準値γo
以上ならば、回帰線直線の傾きをもってKiを前のKiから
更新する。
When the learning cycle is reached, a regression analysis of ΔTi and ΔHi is performed using the data for the last 4 hours or so for each pallet width direction (each column). The correlation coefficient γi of the obtained regression line is the reference value γo
In the above case, Ki is updated from the previous Ki with the slope of the regression line.

Kiは列毎に定義されている(i=1〜5)。Ki is defined for each column (i = 1 to 5).

このKiと直近の列毎排鉱部ウインドボックス温度偏差△
Ti、列毎層厚平均値▲▼を用いて、次回の層厚設定
値Hisvが列毎に計算される。学習周期(2時間毎程度)
に達していない場合は、更新前のKiと直近の△Ti、▲
▼からHisvが計算される。
This Ki and the latest row box exhaust box temperature deviation of each line △
The next layer thickness setting value Hisv is calculated for each column using Ti and the average layer thickness value for each column. Learning cycle (about every 2 hours)
If not reached, Ki before update and latest △ Ti, ▲
Hisv is calculated from ▼.

はドラムフィーダ2の回転数により制御されるが、本シ
ステムでは、からの偏差が制御対象なのでパレット幅
方向に層厚偏差設定値△Hisvを計算する。列毎の△Hisv
について、操業制約条件のチェックを行い、下位のマイ
クロコンピュータに指示される。マイコンでは△Hisvに
なるように、各列のサブゲート開度をPID制御する。
Is controlled by the number of rotations of the drum feeder 2, but in this system, the deviation from is to be controlled, so the layer thickness deviation set value ΔHisv is calculated in the pallet width direction. △ Hisv for each row
Regarding the above, the operation constraint condition is checked, and the subordinate microcomputer is instructed. In the microcomputer, PID control is performed on the sub-gate opening of each row so that ΔHisv is achieved.

上記制御フローはパレットn台通過毎に繰返される。n
は任意に設定できる。
The above control flow is repeated every time n pallets are passed. n
Can be set arbitrarily.

〔実施例〕〔Example〕

機長58m、パレット幅3.5m、ウインドボックス15個のDL
式焼結機を用いて、塊生産量8500t/日、層厚630〜660m
m、パレットスピード1.8〜2.2m/分の操業条件で本発明
を実施した。
Captain 58m, pallet width 3.5m, 15 windbox DLs
Using a sintering machine, mass production 8500t / day, layer thickness 630-660m
The present invention was carried out under the operating conditions of m and pallet speed of 1.8 to 2.2 m / min.

原料条件すべて同じで下記の3種類の操業を行った。The following three types of operations were performed under the same raw material conditions.

(1)調整ゲート制御なし 調整ゲート5の開度は一定で通気調整はパレットスピー
ド、平均層厚変更のみで行う。
(1) No adjustment gate control The opening of the adjustment gate 5 is constant, and ventilation is adjusted only by changing the pallet speed and average layer thickness.

(2)調整ゲート制御あり(従来法) No.14ウインドボックス(15個のウインドボックス中の
第14番目のウインドボックス)内のパレット幅方向のガ
ス温度を平滑化すべく、調整ゲート5の開度を制御す
る。幅方向層厚Hiの変更量に対するTiの変化は一定とし
て層厚偏差△Hisvを設定する。
(2) With adjustment gate control (conventional method) The opening of the adjustment gate 5 in order to smooth the gas temperature in the pallet width direction in the No. 14 wind box (14th wind box among 15 wind boxes). To control. The layer thickness deviation ΔHisv is set assuming that the change of Ti with respect to the change amount of the layer thickness Hi in the width direction is constant.

(3)調整ゲート制御あり(本発明方法) No.14ウインドボックス内のパレット幅方向の温度(T
i)を平滑化すべく、第1図のフローによって調整ゲー
トの制御を行う。
(3) With adjustment gate control (invention method) No.14 Temperature in pallet width direction in wind box (T
In order to smooth i), the adjustment gate is controlled by the flow of FIG.

上記(1)〜(3)の操業をそれぞれ一週間ずつ行い第
1表に示す結果を得た。
The above operations (1) to (3) were each performed for one week, and the results shown in Table 1 were obtained.

調整ゲート制御を行うことによりパレット幅方向の焼け
むらが減少し、ウインドボックス温度の幅方向のばらつ
きが低減し、その結果平均層厚、シャッタ強度が向上
し、返鉱発生率が低下した。従来法による制御方法でも
制御なしの場合に比べ0.9%返鉱発生率が低下している
が、本発明法によりさらに0.7%返鉱発生率が下がって
おり、本発明方法による制御方法によりさらにきめ細や
かな焼けむら管理が可能となった。また、製品シャッタ
強度も脆弱シンターケーキの減少により従来法に比べ約
0.3%向上した。
By adjusting gate control, uneven burning in the width direction of the pallet was reduced, variation in the wind box temperature in the width direction was reduced, and as a result, the average layer thickness and shutter strength were improved, and the occurrence rate of returned ore was reduced. Even with the control method by the conventional method, the occurrence rate of the returned ore of 0.9% is lower than that without the control, but the occurrence rate of the returned ore of 0.7% is further reduced by the method of the present invention. It is now possible to manage fine burn spots. In addition, the product shutter strength is also reduced compared to the conventional method due to the reduction of brittle sinter cake.
Improved by 0.3%.

〔発明の効果〕 ドワイトロイド式焼結機において、本発明による焼けむ
ら低減法により、従来法では困難であったパレット幅方
向の品質管理及び経時的な原料条件変動の影響を加味し
た、きめ細かいパレット幅方向の焼成管理が可能とな
り、焼結塊歩留り向上、焼結鉱強度向上に大きな効果が
ある。
[Advantages of the Invention] In the Dwightroid-type sintering machine, the method for reducing unevenness in burning according to the present invention takes into account the quality control in the pallet width direction and the influence of changes in raw material conditions over time, which were difficult with the conventional method, and a fine pallet. It becomes possible to control the firing in the width direction, which has a great effect on improving the yield of sintered mass and the strength of sinter.

【図面の簡単な説明】 第1図は本発明法による焼けむら制御フローチャート、
第2図は幅方向層厚偏差△Hiと幅方向ウインドボックス
温度偏差△Tiの関係、第3図は焼けむら制御システム構
成を示すブロック図、第4図は層厚Hiとウインドボック
ス温度Tiの関係を示すグラフである。 1……給鉱ホッパ 2……ドラムフィーダ 3……主ゲート 4……パレット 5……調整ゲート 6……パワーシリンダ 7……超音波レベル計 8……排鉱部ウインドボックス温度計 9……ITVカメラ 10……プロセスコンピュータ 11……マイクロコンピュータ
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a flowchart for uneven burn control according to the method of the present invention,
Fig. 2 shows the relationship between the widthwise layer thickness deviation ΔHi and the widthwise windbox temperature deviation ΔTi, Fig. 3 is a block diagram showing the burn unevenness control system configuration, and Fig. 4 is the layer thickness Hi and windbox temperature Ti. It is a graph which shows a relationship. 1 …… Mine feeding hopper 2 …… Drum feeder 3 …… Main gate 4 …… Pallet 5 …… Adjustment gate 6 …… Power cylinder 7 …… Ultrasonic wave level meter 8 …… Sinking section windbox thermometer 9 …… ITV camera 10 …… Process computer 11 …… Microcomputer

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ドワイトロイド式焼結機の操業に当り、排
鉱側ウインドボックスにおけるパレット幅方向複数列に
ついて第i列の複数個のパレットの平均温度とパレット
幅方向平均温度との偏差△Tiを求め、一方給鉱側のパレ
ット幅方向複数列についての充填層の層厚の第i列の複
数個のパレットの平均層厚とパレット幅方向平均層厚と
の偏差△Hiを求め、対応する幅方向複数列の各△Hiの変
化量に対応する各△Tiの回帰分析を行って第i列の層厚
の修正量を推定し、その推定修正量に基いてパレット幅
方向各列の層厚を調整し焼けむらを防止することを特徴
とする焼結鉱の焼けむら減少方法。
1. A deviation ΔTi between the average temperature of a plurality of pallets in the i-th row and the average temperature in the pallet width direction of a plurality of rows in the pallet width direction in the windbox on the mine ore side during the operation of the Dwightroid type sintering machine. On the other hand, the deviation ΔHi between the average layer thickness of the plurality of pallets in the i-th column and the average layer thickness in the pallet width direction of the plurality of columns in the pallet width direction on the mining side is calculated, and corresponding Regression analysis of each ΔTi corresponding to each ΔHi change amount in multiple columns in the width direction is performed to estimate the correction amount of the layer thickness in the i-th column, and the layers in each column in the pallet width direction are estimated based on the estimated correction amount. A method for reducing uneven burning of a sinter, which comprises adjusting thickness to prevent uneven burning.
JP31439789A 1989-12-05 1989-12-05 Method for reducing uneven burning of sinter Expired - Fee Related JPH0772670B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31439789A JPH0772670B2 (en) 1989-12-05 1989-12-05 Method for reducing uneven burning of sinter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31439789A JPH0772670B2 (en) 1989-12-05 1989-12-05 Method for reducing uneven burning of sinter

Publications (2)

Publication Number Publication Date
JPH03177787A JPH03177787A (en) 1991-08-01
JPH0772670B2 true JPH0772670B2 (en) 1995-08-02

Family

ID=18052856

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31439789A Expired - Fee Related JPH0772670B2 (en) 1989-12-05 1989-12-05 Method for reducing uneven burning of sinter

Country Status (1)

Country Link
JP (1) JPH0772670B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101694349B (en) 2009-03-03 2012-02-15 北京科技大学 Sinter bed off-loading device, sintering machine and sintering method using same
JP5842762B2 (en) * 2012-08-07 2016-01-13 新日鐵住金株式会社 Method for producing sintered ore using pallet position recognition device of sintering machine
JP6384438B2 (en) * 2015-09-18 2018-09-05 Jfeスチール株式会社 Method for producing sintered ore
JP7099433B2 (en) * 2019-11-28 2022-07-12 Jfeスチール株式会社 Sintered ore manufacturing method

Also Published As

Publication number Publication date
JPH03177787A (en) 1991-08-01

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