JPH03177787A - Reduction of sintering nonuniformity of sintered ore - Google Patents
Reduction of sintering nonuniformity of sintered oreInfo
- Publication number
- JPH03177787A JPH03177787A JP31439789A JP31439789A JPH03177787A JP H03177787 A JPH03177787 A JP H03177787A JP 31439789 A JP31439789 A JP 31439789A JP 31439789 A JP31439789 A JP 31439789A JP H03177787 A JPH03177787 A JP H03177787A
- Authority
- JP
- Japan
- Prior art keywords
- layer thickness
- rows
- pallet
- value
- width direction
- 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.)
- Granted
Links
- 238000005245 sintering Methods 0.000 title claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 19
- 238000000611 regression analysis Methods 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 2
- 239000002994 raw material Substances 0.000 description 6
- 238000010304 firing Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000003908 quality control method Methods 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野1゜
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。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application 1] The present invention relates to a method for reducing uneven burning of sintered ore in a Dwight Lloyd sintering machine.
[従来の技術1
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測端部で観
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、いわゆるむら焼は現象が見られるこ
とがある。[Prior art 1] In a Dwight Lloyd-type moving grid sintering machine, when the sintered state of the sintered ore packed bed on the pallet is observed at the sintering machine waste ore measuring end, it is found that the width direction of the packed bed on the pallet is There are parts where firing has progressed sufficiently and parts where firing has not progressed sufficiently (unfired parts), and a so-called uneven firing phenomenon may be observed.
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 of the sintered ore (falling strength, particle size, chemical composition, etc.) deteriorates and varies, and the rate of return ore generation increases. As a result, there are many negative effects on the production of sintered ore, 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ィン
ドボックス温度Tiまたは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51−23365号公報、特公昭60−10
096号公報などに開示されている。Therefore, it is necessary to measure the wind box temperature Ti in the pallet width direction in the sintering machine ore discharge section or the red zone cross section HzRi of the sinter cake in the ore discharge section, and adjust the feed rate of raw materials in the pallet width direction based on the results. is being carried out. For example, these are JP 50-40361, JP 51-23365, and JP 60-10.
This is disclosed in Publication No. 096 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 the main parts of the sintering machine.
第3図において、l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 an ore feeding hopper, 2 is a drum feeder for supplying raw materials, 3 is a main gate whose opening degree is set according to production volume, 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。また排鉱部のウィ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
fTV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 split operation type adjustment gate 5 is provided to finely adjust the feed amount in the width direction of the drum feeder 2, and this 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 with an ultrasonic level meter 7. In addition, the measured values of the wind box thermometer 8 in the ore discharge section and the observation data of the fTV camera 9 that measures the red zone cross section of the sinter cake in the ore discharge section are input to the upper process computer 10, and the output of the upper process computer 10 is The data is input to the lower-order microcomputer 11, and necessary control is performed.
従来技術では排鉱部ウィンドボックス温度Ti又は排鉱
部のシンターケーキの赤熱帯断面積H2Riを連続測定
し、プロセスコンピュータ10ではTi、H2Ri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H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 conventional technology, the wind box temperature Ti of the ore discharge section or the red zone cross section H2Ri of the sinter cake in the ore discharge section is continuously measured, and the process computer 10 measures the layer thickness deviation in the width direction △ to eliminate variations in Ti and H2Ri. Hisv
That is, the difference between the average layer thickness and the measured layer thickness is set at regular intervals. The microcomputer 11 calculates the indicated value △ from the process computer based on the measurement result of the layer thickness Hi.
The power cylinder 6 is driven to control the opening degree of the adjustment gate 5 so as to match Hisv. The average layer thickness H is managed so that the supply amount (discharge amount) is controlled by controlling the rotation speed of the drum feeder 2, and the set layer thickness is achieved.
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
がこの制御で最ち難しい点であった。Generally, the layer thickness ΔHisv is set for each width direction mainly in order to smooth the ore discharge part temperature Ti, but how to give this set value was the most difficult point in this control.
幅方向別の層厚Hiと排鉱部ウィンドボックス温度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。Layer thickness Hi by width direction and ore discharge part wind box temperature Ti
We investigated the relationship over four days, and this is shown in Figure 4.
As shown in Fig. 4, there is a negative correlation between the layer thickness Hi and the temperature Ti, so for rows with good ventilation and high temperature Ti, the layer thickness Hi can be increased, and for the opposite row, the layer thickness Hi can be lowered. , the relationship between the layer thickness Hi and the temperature Ti changes depending on the location and time. In FIG. 4, the measured values are entered for each of No. 1 to 5 gates, and the relationship therebetween is shown by five straight lines. In this way, the relationship between the layer thickness Hi and the temperature Ti changes depending on the location and time. Therefore, a system can be considered in which the correlation between the layer thickness Hi and the temperature Ti is determined for each column based on the data of the most recent several hours, and the action width □ of the layer thickness Hi is determined based on the slope of the straight line.
ところが、排鉱部ウィンドボックス温度Tiに影響を与
える因子としては5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, in addition to the five-layer thickness Hi, there are various factors that affect the wind box temperature Ti of the ore discharge section, such as the packing density of the sintering raw material on the pallet, particle size composition, moisture content, clogging of the pallet, air leakage, etc. Since factors are involved, a clear relational expression is rarely obtained even if the correlation between the layer thickness Hi and the temperature Ti is investigated using 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T
iとの関係を数時間毎に列毎に見直す必要がある。Therefore, at present, the temperature Ti for the amount of change in the layer thickness Hi is
It is assumed that the width of change in is constant, and the layer thickness deviation ΔHi is set and controlled for each width direction. In order to perform finer control to eliminate variations in the temperature Ti in the width direction, it is necessary to adjust the layer thickness Hi and the temperature T.
It is necessary to review the relationship with i for each column every few hours.
ところが、列毎に層厚の絶対値Hiと排鉱部ウィンドボ
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 if the relationship between the absolute value Hi of the layer thickness and the absolute value Ti of the wind box temperature at the ore discharge portion was determined 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と幅方向ウィン
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と排鉱部のウィンドボ
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 as much as possible the influence of factors other than Hi that affect Ti, the relationship between the widthwise layer thickness deviation ΔHi and the widthwise windbox temperature deviation ΔTi was determined. An example is shown in FIG. 2, and there was a very good correlation between ΔHi and ΔTi. The data is for the last 4 hours, and the data here is 30
Minute average value. Furthermore, the layer thickness Hi and the wind box temperature Ti of the ore discharge portion are made to correspond with each other with a time delay of about 30 minutes in consideration of the traveling time.
このように幅方向層厚偏差△Hiと幅方向排鉱部ウィン
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
焼は管理ができることを知見し本発明を完成した。In this way, since there is always a good correlation between the width direction layer thickness deviation △Hi and the width direction windbox temperature deviation △Ti, a system that uses the slope Ki of this regression equation to determine the layer thickness action amount can be used. For example, the present invention was completed based on the finding that more fine-grained uneven firing in the width direction can be controlled.
本発明は、ドワイトロイド式焼結機の操業方法に当り、
排鉱側ウィンドボックスにおけるパレット幅方向の温度
分布を測定し、この温度の平均温度からの偏差△Tiの
分布を求め、一方給鉱側のパレット幅方向の充填層の層
厚の分布を測定し、この層厚の平均値からの偏差△Hf
の分布を求め、対応する幅方向位置の△Hiの変化量に
対する△Tiの変化幅を推定し、その推定値を基にパレ
ット幅方向の層厚の目標値に合わせて層厚分布を制御す
ることを特徴とする焼結鉱の焼けむら減少方法である。The present invention relates to a method of operating a Dwight Lloyd sintering machine,
The temperature distribution in the pallet width direction in the ore discharge side wind box was measured, and the distribution of the deviation △Ti from the average temperature of this temperature was determined, while the layer thickness distribution of the packed bed in the pallet width direction on the ore feeding side was measured. , the deviation of this layer thickness from the average value △Hf
The width of change in △Ti with respect to the amount of change in △Hi at the corresponding position in the width direction is estimated, and the layer thickness distribution is controlled based on the estimated value in accordance with the target value of the layer thickness in the width direction of the pallet. This is a method for reducing unevenness in sintered ore.
〔作用]
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。[Operation] The system configuration itself used to implement the present invention is the same as the conventional technology shown in FIG. The present invention is a method for setting layer thickness deviation ΔHisv in a process computer,
A schematic flowchart is shown in FIG.
第1図はパレット幅方向5力、所の排鉱部ウィンドボッ
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 wind box temperature Ti of the ore discharge section uniform at five forces 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、排鉱部のウィンドボックス温度T i 、j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Hi、Tiを求
める。さらに全列のの平均値からの偏差△Hi、△Ti
を列毎に計算する。△H1,ΔTfデータはファイル内
に保存される。In order to match the data, the layer thickness Hi for each column for each pallet
j, sample the wind box temperature T i,j of the ore discharge section. When the data for the specified number of pallets n is accumulated, average values Hi and Ti are calculated for each pallet width direction (for each column). Furthermore, the deviations from the average value of all columns △Hi, △Ti
Calculate column by column. ΔH1 and ΔTf data are saved within 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
70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 for each pallet width direction (for each row) using data for the most recent four hours. If the correlation coefficient γi of the obtained regression line is equal to or greater than the reference value 70, Ki is updated from the previous Ki using the slope of the regression line.
KLは列毎に定義されている(i=1〜5)。KL is defined for each column (i=1 to 5).
このKiと直近の列毎排鉱部ウィンドボックス温度偏差
△Ti、列毎層厚平均値HL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KLと直近の△T
i、HiからHisvが計算される。The next layer thickness setting value Hisv is calculated for each row using this Ki, the most recent ore discharge section windbox temperature deviation ΔTi for each row, and the average layer thickness value HL for each row. If the learning cycle (about every 2 hours) has not been reached, the KL before update and the latest △T
Hisv is calculated from i and Hi.
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、H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、操業制約条件のチエツクを行い、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△His
vになるように、各列のサブゲート開度をPID制御す
る。Although it is controlled by the rotation speed of the feeder 2, in this system, since the deviation from H is the control target, the layer thickness deviation set value ΔHisv is calculated in the pallet width direction. △Hisv for each column
The operating constraints are checked and instructions are given to the lower-level microcomputer. In the microcomputer, △His
The sub-gate opening degree of each column is PID controlled so that the opening degree of the sub-gate of each column is set to v.
上記制御フローはパー110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 par 110 passes. n
can be set arbitrarily.
「実施例]
磯長58m、パレット幅3.5m、ウィンドボックス1
5個のDL式焼結機を用いて、項生産量8500 t/
日、層厚630〜6’60 mm、パレットスピード1
.8〜2.2 m 7分の操業条件で本発明を実施した
。"Example" Rock length 58m, pallet width 3.5m, wind box 1
Using 5 DL type sintering machines, the production capacity is 8500 t/
day, layer thickness 630-6'60 mm, pallet speed 1
.. The invention was carried out under operating conditions of 8-2.2 m 7 minutes.
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 conducted 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 degree of the adjustment gate 5 is constant, and ventilation adjustment is performed only by changing the pallet speed and average layer thickness.
(2)m整ゲート制御あり(従来法)
胤14ウィンドボックス(15個のウィンドボックス中
の第14番目のウィンドボックス)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△Hf5vを設定する。(2) With m adjustment gate control (conventional method) In order to smooth the gas temperature in the width direction of the pallet in the wind box 14 (the 14th wind box among 15 wind boxes), the opening of the adjustment gate 5 is control. The layer thickness deviation ΔHf5v is set assuming that the change in Ti with respect to the amount of change in the layer thickness Hi in the width direction is constant.
(3)Fl整ゲート制御あり(本発明方法)No、14
ウインドボツクス内のパレット幅方向の温度(Ti)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 Fl adjustment gate control (method of the present invention) No. 14
In order to smooth the temperature (Ti) in the width direction of the pallet inside the window box, the adjustment gate is controlled according to the flow shown in 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 operations (1) to (3) above were carried out for one week each, 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、ウィ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。By performing adjustment gate control, uneven baking in the pallet width direction was reduced, and the widthwise variation in wind box temperature was reduced.As a result, the average layer thickness and shutter strength were improved, and the return generation rate was reduced.
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。Even with the conventional control method, the reduction is 0.9 compared to the case without control.
Although the % return ore generation rate has decreased, the method of the present invention has further reduced the return ore generation rate by 0.7%, and the control method according to the present invention has enabled more fine-grained management of burnt unevenness. Furthermore, the strength of the product shutter was improved by approximately 0.3% compared to the conventional method due to the reduction in brittle sinter cake.
「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。"Effects of the Invention" In the Dwight Lloyd sintering machine, the uneven burning method of the present invention enables quality control in the width direction of the pallet, which was difficult with conventional methods, and fine-grained pallets that take into account the influence of changes in raw material conditions over time. It becomes possible to control firing in the width direction, which has a great effect on improving the yield of sintered lumps and improving the strength of sintered ore.
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と幅方向ウィンドボック
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とウィンド
ボックス温度Tiの関係を示すグラフである。
l・・・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・・・排鉱部ウィ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
出
代
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川崎製鉄株式会社FIG. 1 is a flowchart for controlling uneven burning according to the method of the present invention.
Figure 2 shows the relationship between the layer thickness deviation ΔHi in the width direction and the windbox temperature deviation ΔTi in the width direction, Figure 3 is a block diagram showing the configuration of the uneven baking control system, and Figure 4 shows the relationship between the layer thickness Hi and the windbox temperature Ti. It is a graph showing a relationship. l...Ore supply hopper 2...Drum feeder 3...Main gate 4...Pallet 5...Adjustment gate 6...Power cylinder 7...Ultrasonic level meter 8...Ore discharge Wind box thermometer 9...ITV
Camera 10...Process computer 11...Microcomputer Kawasaki Steel Corporation
Claims (1)
ンドボックスにおけるパレット幅方向の温度分布を測定
し、該温度の平均温度からの偏差△Tiの分布を求め、
一方給鉱側のパレット幅方向の充填層の層厚の分布を測
定し、該層厚の平均値からの偏差△Hiの分布を求め、
対応する幅方向位置の△Hiの変化量に対する△Tiの
変化幅を推定し、その推定値を基にパレット幅方向の層
厚の目標値に合わせて層厚分布を制御することを特徴と
する焼結鉱の焼けむら減少方法。1. When operating the Dwight Lloyd sintering machine, measure the temperature distribution in the pallet width direction in the ore discharge side wind box, determine the distribution of deviation ΔTi from the average temperature of the temperature,
On the other hand, measure the layer thickness distribution of the packed layer in the pallet width direction on the ore feeding side, and determine the distribution of the deviation ΔHi from the average value of the layer thickness,
It is characterized by estimating the change range of △Ti with respect to the change amount of △Hi at the corresponding width direction position, and controlling the layer thickness distribution in accordance with the target value of the layer thickness in the pallet width direction based on the estimated value. Method for reducing unevenness in sintered ore.
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 true JPH03177787A (en) | 1991-08-01 |
| JPH0772670B2 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) |
Cited By (4)
| 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 |
| JP2014034686A (en) * | 2012-08-07 | 2014-02-24 | Nippon Steel & Sumitomo Metal | Production method of sintered ore using pallet position recognition device of sintering machine |
| JP2017057481A (en) * | 2015-09-18 | 2017-03-23 | Jfeスチール株式会社 | Method for producing sintered ore |
| JP2021085078A (en) * | 2019-11-28 | 2021-06-03 | Jfeスチール株式会社 | Method of manufacturing sintered ore |
-
1989
- 1989-12-05 JP JP31439789A patent/JPH0772670B2/en not_active Expired - Fee Related
Cited By (4)
| 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 |
| JP2014034686A (en) * | 2012-08-07 | 2014-02-24 | Nippon Steel & Sumitomo Metal | Production method of sintered ore using pallet position recognition device of sintering machine |
| JP2017057481A (en) * | 2015-09-18 | 2017-03-23 | Jfeスチール株式会社 | Method for producing sintered ore |
| JP2021085078A (en) * | 2019-11-28 | 2021-06-03 | Jfeスチール株式会社 | Method of manufacturing sintered ore |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0772670B2 (en) | 1995-08-02 |
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