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JPS6124456B2 - - Google Patents
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JPS6124456B2 - - Google Patents

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Publication number
JPS6124456B2
JPS6124456B2 JP13349981A JP13349981A JPS6124456B2 JP S6124456 B2 JPS6124456 B2 JP S6124456B2 JP 13349981 A JP13349981 A JP 13349981A JP 13349981 A JP13349981 A JP 13349981A JP S6124456 B2 JPS6124456 B2 JP S6124456B2
Authority
JP
Japan
Prior art keywords
melting
rate
ore
raw material
firing
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
JP13349981A
Other languages
Japanese (ja)
Other versions
JPS5837132A (en
Inventor
Takazo Kawaguchi
Minoru Ichidate
Shun Sato
Kazumasa Kato
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 Corp
Original Assignee
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP13349981A priority Critical patent/JPS5837132A/en
Publication of JPS5837132A publication Critical patent/JPS5837132A/en
Publication of JPS6124456B2 publication Critical patent/JPS6124456B2/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】[Detailed description of the invention]

本発明は、製鉄用焼結鉱製造における焼結操業
方法に関するものである。 焼結鉱は、製鉄用溶鉱炉原料として広く用いら
れている。焼結鉱の品質を判断する基準として
は、化学成分、粒度分布、冷間強度、還元粉化性
等がある。これらは溶鉱炉操業にあたつてきわめ
て重要な因子となるので、不断の管理が行われて
いる。 焼結鉱は、粉鉱石を溶融させ、これを結合ボン
ドとして接着結合させて製造させる。したがつ
て、この結合ボンドが多い(すなわち、未溶融残
留物が少ない)方が、焼結鉱の常温強度は高くな
る。 一方、還元粉化の主原因は一度溶融して凝固し
たヘマタイト(以下、第2ヘマタイトという。)
の量によつて定まり、あまり溶融させすぎると、
2次ヘマタイト量が増加し、還元粉化性を悪化さ
せることになる。また、多く溶融させるには、焼
成時間を長くとるか、燃料消費量を多くする必要
がある。溶融量が少なければ、冷間強度が低下す
る。これらの傾向を第1図に示す。実際には、焼
結鉱の品質、生産性、燃料原単位等の各観点か
ら、適性な溶融率が決定される(例えば、第1図
の斜線範囲)。 ここで、溶融率とは、後に詳述するが、一般に
焼結鉱製造過程中で溶融した履歴をもつものの焼
結ケーキ中の体積比率と定義する。 焼結鉱の製造においては、その原料は種々雑多
な鉱石を用いており、その溶融に関する性質も異
なるところから、同じ操業条件でも原料配合が変
れば、異なつた溶融率を示す。 従来における原料鉱石の配合は、これら溶融率
の測定が多大な工数を要することから、溶融率を
把握せずに、直接製造した成品の品質試験を実施
し、満足する品質を得るまで配合変更を繰り返さ
なければならなかつた。したがつて、適正な原料
配合条件をつかむまでに多大な時間を必要とし、
無駄な原料配合および焼結鉱の製造を行わなけれ
ばならなかつた。 本発明の目的は、焼結原料の諸物性値と実測焼
成速度から事前に焼結炉中の溶融率を予測し、こ
れが目標値になるように焼成速度を設定し、無駄
な焼結鉱の製造をなくし、焼結鉱の品質を安定さ
せ、諸原単位の低減を図ることにある。 本発明の操業方法は、焼結鉱の製造過程におい
て、焼成速度の実測値と予め算出した各原料鉱石
の物性から配合原料の溶融率を算出し、該算出値
が目標溶融率になるように焼成速度を制御するこ
とを特徴としている。 焼結鉱の製造においては、極めて多種類の原料
鉱石が用いられているが、これら原料の溶融に関
する性質はすべて異なつており、同一温度履歴で
も異なつた値を示す。 本発明者等は、実験の結果、焼結鉱製造中の鉱
石粒子の溶融現象は1100℃以上になると、原料中
のCaOが反応を起し、カルシウム・フエライトを
形成し、初期溶融液をつくり、この溶融液が逐次
鉱石粒子の外周から内側に向かつて侵食するよう
に溶融を進行させる反応であることを見い出し
た。 したがつて、100℃以上の保持時間tと配合原
料の溶融率Qとは次の(1)式で表される。さらに、
1100℃以上で保持時間6分間の場合における配合
原料の溶融率は、各単味鉱石銘柄別の溶融率qj
(1100℃以上6分間)を加重平均することによつ
て(2)式のように表される。 Q=・(t/6)n ……(1) ただし、 t :1100℃以上保持時間(分) n :定数 j :原料の各種銘柄を示すインデツクス qj:鉱石銘柄jにおける溶融率(気孔、空隙部
を除く) wj:配合原料中の鉱石銘柄jの体積配合率 単味鉱石銘柄別の1100℃以上で保持時間6分の
場合の溶融率qjは原料入荷時に実験室で試験的に
求めることができる。その測定結果の一例を第1
表に示す。
The present invention relates to a sintering operation method for producing sintered ore for iron manufacturing. Sintered ore is widely used as a raw material for blast furnaces for iron manufacturing. Criteria for determining the quality of sintered ore include chemical composition, particle size distribution, cold strength, reduction pulverizability, etc. These are extremely important factors when operating a blast furnace, so they are constantly managed. Sintered ore is produced by melting fine ore and adhesively bonding it together as a bond. Therefore, the room temperature strength of the sintered ore increases as the number of bond bonds increases (that is, the amount of unmelted residue decreases). On the other hand, the main cause of reduction powdering is hematite that has once been melted and solidified (hereinafter referred to as secondary hematite).
It is determined by the amount of
The amount of secondary hematite increases, which worsens reduction powdering properties. Furthermore, in order to melt a large amount, it is necessary to take a longer firing time or to increase fuel consumption. If the amount of melting is small, the cold strength will decrease. These trends are shown in Figure 1. In reality, an appropriate melting rate is determined from various viewpoints such as quality of sintered ore, productivity, fuel consumption rate, etc. (for example, the shaded range in FIG. 1). Here, the melting rate will be described in detail later, but is generally defined as the volume ratio in the sintered cake of something that has a history of melting during the sintered ore manufacturing process. In the production of sintered ore, a variety of miscellaneous ores are used as raw materials, and their melting properties vary, so even under the same operating conditions, if the raw material composition is changed, the melting rate will vary. In the conventional blending of raw material ores, measuring the melting rate requires a large amount of man-hours, so quality tests are conducted on directly manufactured products without knowing the melting rate, and the blending is changed until a satisfactory quality is obtained. I had to repeat it. Therefore, it takes a lot of time to find the appropriate raw material blending conditions.
This resulted in unnecessary mixing of raw materials and production of sintered ore. The purpose of the present invention is to predict the melting rate in the sintering furnace in advance from the physical property values of the sintering raw material and the measured firing rate, set the firing rate so that this becomes the target value, and eliminate unnecessary sintered ore. The aim is to eliminate manufacturing, stabilize the quality of sintered ore, and reduce various basic units. The operating method of the present invention calculates the melting rate of the blended raw materials from the actual value of the sintering rate and the physical properties of each raw material ore calculated in advance in the process of manufacturing sintered ore, and adjusts the melting rate so that the calculated value becomes the target melting rate. It is characterized by controlling the firing speed. In the production of sintered ore, a wide variety of raw material ores are used, but the melting properties of these raw materials are all different and exhibit different values even under the same temperature history. As a result of experiments, the present inventors have found that during the production of sintered ore, the phenomenon of melting of ore particles occurs when the temperature exceeds 1100℃, CaO in the raw material reacts, forms calcium ferrite, and creates an initial molten liquid. It was discovered that this reaction progresses melting so that the molten liquid gradually erodes from the outer periphery of the ore particles toward the inside. Therefore, the holding time t at 100° C. or higher and the melting rate Q of the blended raw materials are expressed by the following equation (1). moreover,
The melting rate of the blended raw materials when held at 1100℃ or higher for 6 minutes is the melting rate qj of each single ore brand.
(1100℃ or more for 6 minutes) is expressed as equation (2) by taking a weighted average. Q=・(t/6)n...(1) However, t: Holding time over 1100℃ (minutes) n: Constant j: Index indicating various brands of raw materials qj: Melt rate of ore brand j (excluding pores and voids) wj: Melting rate of ore brand j in the blended raw materials Volumetric ratio The melting rate qj of each single ore brand when held at 1100°C or higher for 6 minutes can be experimentally determined in the laboratory when raw materials are received. An example of the measurement results is shown in the first section.
Shown in the table.

【表】 測定溶融率を、1100℃以上の保持時間を6分間
としたときのものにした理由は、焼結操業時の層
内温度履歴では1100℃以上の平均保持時間が6分
間となつているからである。以下、ある鉱石銘柄
の1100℃以上の保持時間が6分間の場合の溶融率
を鉱石銘柄の溶融度指数という。異なる溶融度指
数を適当に組合せることによつて配合原料の溶融
率を変えることができる。この場合、鉱石の銘柄
を変えるか、または同じ銘柄で粒度を調整するこ
とによつても配合原料の溶融率を変えることがで
きる。例えば、SFハマスレーの場合には、平均
径が3、2、1mmをとき、溶融度指数がそれぞれ
79.0、84.0、98.0Vo1%となる。 さて、この保持時間tは焼成速度vと密接な関
係があり、この関係を第2図に示す。また式で表
示すると(3)式で示される。第2図は、焼成速度v
を種々変化させながら1100℃以上の保持時間tを
調べたものである。 t=av2+bv+c ……(3) ただし、 v:焼成速度(mm/分) a、b、c:定数 焼成速度vは、種々の計測方法があるが、最も
簡単な方法は、第3図に示すように、焼結機1に
おいて最終前段のウインド・ボツクス3aにおけ
る焼結排ガス温度のピーク時をもつて焼結完了と
みなし、焼結時間(T)を計測し、このときの配
合原料の層高(H)からv=H/Tを求めること
ができる。 焼成速度vは、第4図に示すように、焼結機1
において焼成ブロワ2の回転数、ウインド・ボツ
クス3のダンパ31の開度、パレツト4内の原料
層高、原料充填密度、原料造粒ミキサ5への原料
添加水分量および造粒度等を調整することによつ
て制御される。これらの諸因子を変化させた時の
焼成速度vへの影響の一例を第5図に示す。 以上のようにして求めた鉱石銘柄ごとの溶融度
指数qjおよびその体積配合率wjと焼成速度vと
を前述の(1)〜(3)式に代入することによつて溶融率
を算出し、これを目標品質に応じた溶融率に合せ
るように原料配合または焼成速度を制御する。 <実施例> DL型焼結後に本発明の操業方法を実施した。
第2表に示す異なる溶融度指数を有する鉱石銘柄
A〜Hを用いて配合原料の溶融率が一定となるよ
うにDL型焼結機を制御した。
[Table] The reason why the measured melting rate was determined when the holding time at 1100°C or higher was 6 minutes was because the average holding time at 1100°C or higher was 6 minutes based on the temperature history in the layer during sintering operation. Because there is. Hereinafter, the melting rate of a certain ore brand when the holding time at 1100°C or higher is 6 minutes is referred to as the melting index of the ore brand. By suitably combining different melting indexes, the melting rate of the compounded raw materials can be varied. In this case, the melting rate of the raw materials can be changed by changing the brand of ore or by adjusting the particle size of the same brand. For example, in the case of SF Hammersley, when the average diameter is 3, 2, and 1 mm, the melting index is
79.0, 84.0, 98.0Vo1%. Now, this holding time t has a close relationship with the firing speed v, and this relationship is shown in FIG. 2. Also, when expressed as an equation, it is shown as equation (3). Figure 2 shows the firing speed v
The holding time t at 1100°C or higher was investigated while varying the temperature. t=av 2 +bv+c...(3) where, v: Firing speed (mm/min) a, b, c: constants There are various ways to measure the firing speed v, but the simplest method is as shown in Figure 3. As shown in , in the sintering machine 1, sintering is considered to be completed when the temperature of the sintering exhaust gas in the window box 3a at the front stage reaches its peak, the sintering time (T) is measured, and the amount of the raw materials mixed at this time is determined. v=H/T can be determined from the layer height (H). The firing speed v is determined by the sintering machine 1 as shown in FIG.
In this step, the rotation speed of the firing blower 2, the opening degree of the damper 31 of the wind box 3, the height of the raw material layer in the pallet 4, the raw material packing density, the amount of moisture added to the raw material granulation mixer 5, the granulation degree, etc. are adjusted. controlled by FIG. 5 shows an example of the effect on the firing rate v when these factors are changed. The melting rate is calculated by substituting the melting index qj for each ore brand, its volume mixing ratio wj, and firing speed v found in the above manner into equations (1) to (3), The raw material blend or firing rate is controlled to match the melting rate to the target quality. <Example> The operating method of the present invention was carried out after DL type sintering.
Using ore brands A to H having different melting indexes shown in Table 2, a DL type sintering machine was controlled so that the melting rate of the blended raw materials was constant.

【表】 第4図に示すDL型焼結機1において、原料鉱
石の配合率が変更されるたびに、焼成速度が一定
であるとすれば、配合原料の溶融率が変ることに
なる。焼成速度vは、前述したように、ウイン
ド・ボツクス3内に設けた温度計32によつて焼
結排ガス温度のピーク時(すなわち、焼結時間
T)を検出し、また、原料カツトオフ・プレート
6の設定高さからパレツト4内原料層高Hを検出
することによつて算出した(v=H/T)。 そのときの原料鉱石の設定体積配合率と、各原
料鉱石の溶融度指数から配合原料の溶融率Qが一
定となる焼成速度を算出し、この焼成速度を保持
するように焼成ブロワ2の回転数、ウインド・ボ
ツクス3のダンプ31の開度、カツトオフ・プレ
ート6の設定高さ、ミキサ注水管51から原料造
粒ミキサ5への注水量をそれぞれ調整して操業し
た(第6図)。 参考として、また逆に、生産量を確保するため
に、焼成速度vを一定にし、配合原料の溶融度指
数qが一定となるように、原料鉱石の体積配合率
wjを調整して操業した(第7図)。 本発明法にもとづく実施例と従来法との比較例
を第3表に示す。第3表からわかるように、本発
明法によれば焼結鉱の品質が安定すると同時に焼
結鉱品質向上、コークス原単位の低減を図ること
ができた。
[Table] In the DL type sintering machine 1 shown in FIG. 4, each time the blending ratio of the raw material ore is changed, the melting rate of the blended raw materials will change if the firing rate is constant. As described above, the firing speed v is determined by detecting the peak time of the sintering exhaust gas temperature (that is, the sintering time T) by the thermometer 32 installed in the window box 3, and by detecting the peak time of the sintering exhaust gas temperature (that is, the sintering time T). It was calculated by detecting the height H of the raw material layer in the pallet 4 from the set height (v=H/T). Calculate the firing speed at which the melting rate Q of the mixed raw materials is constant from the set volume blending ratio of the raw material ores and the melting index of each raw material ore at that time, and set the rotation speed of the firing blower 2 to maintain this firing speed. The operation was carried out by adjusting the opening degree of the dumper 31 of the wind box 3, the set height of the cut-off plate 6, and the amount of water injected from the mixer water injection pipe 51 to the raw material granulation mixer 5 (Fig. 6). For reference and conversely, in order to ensure the production volume, the volume blending ratio of the raw material ore is set so that the firing speed v is constant and the melting index q of the blended raw material is constant.
The operation was carried out by adjusting wj (Fig. 7). Table 3 shows comparative examples between examples based on the method of the present invention and the conventional method. As can be seen from Table 3, according to the method of the present invention, the quality of the sintered ore was stabilized, and at the same time, it was possible to improve the quality of the sintered ore and reduce the coke consumption rate.

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

第1図は溶融率と焼結鉱の品質との関係を示す
グラフ。第2図は焼成速度と溶融層内温度1100℃
以上保持時間との関係を示すグラフ。第3図は各
ウインド・ボツクスにおける焼結排ガス温度を示
すグラフ。第4図は本発明の方法が適用される
DL型焼結機の概略構成図。第5図は焼成速度と
各条件との関係の傾向の一例を示すグラフ。第6
図は本発明の方法にもとづいて焼成速度を制御し
たときの実施例を説明するグラフ。第7図は参考
として配合原料の配合率を制御したときの実施例
を説明するグラフ。 1:焼結機、2:焼成ブロワ、3:ウインド・
ボツクス、4:パレツト、5:原料造粒ミキサ、
6:カツトオフ・プレート、31:ダンパ、3
2:温度計、51:注水管。
Figure 1 is a graph showing the relationship between the melting rate and the quality of sintered ore. Figure 2 shows the firing speed and temperature inside the molten layer, 1100℃.
The above is a graph showing the relationship with the retention time. FIG. 3 is a graph showing the sintering exhaust gas temperature in each wind box. Figure 4 shows the method of the present invention being applied.
Schematic diagram of the DL type sintering machine. FIG. 5 is a graph showing an example of the tendency of the relationship between firing speed and each condition. 6th
The figure is a graph explaining an example when the firing rate is controlled based on the method of the present invention. FIG. 7 is a graph illustrating an example when the blending ratio of blended raw materials is controlled for reference. 1: Sintering machine, 2: Sintering blower, 3: Window
box, 4: pallet, 5: raw material granulation mixer,
6: Cut-off plate, 31: Damper, 3
2: Thermometer, 51: Water injection pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 焼結鉱の製造過程において、実測焼成速度
と、予め算出した各原料鉱石の諸物性とから配合
原料の溶融率を算出し、該算出値が目標値になる
ように、焼成速度を調整することを特徴とした焼
成操業方法。
1. In the process of manufacturing sintered ore, the melting rate of the blended raw materials is calculated from the measured firing rate and the various physical properties of each raw material ore calculated in advance, and the firing rate is adjusted so that the calculated value becomes the target value. A firing operation method characterized by:
JP13349981A 1981-08-26 1981-08-26 Sintering operating method Granted JPS5837132A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13349981A JPS5837132A (en) 1981-08-26 1981-08-26 Sintering operating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13349981A JPS5837132A (en) 1981-08-26 1981-08-26 Sintering operating method

Publications (2)

Publication Number Publication Date
JPS5837132A JPS5837132A (en) 1983-03-04
JPS6124456B2 true JPS6124456B2 (en) 1986-06-11

Family

ID=15106195

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13349981A Granted JPS5837132A (en) 1981-08-26 1981-08-26 Sintering operating method

Country Status (1)

Country Link
JP (1) JPS5837132A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59153845A (en) * 1983-02-21 1984-09-01 Nippon Kokan Kk <Nkk> Mixing control method for sintering raw material ore
JP4877994B2 (en) * 2007-03-14 2012-02-15 日立エーアイシー株式会社 Electrolytic capacitor
JP6763412B2 (en) * 2018-01-30 2020-09-30 Jfeスチール株式会社 Sintered ore manufacturing method

Also Published As

Publication number Publication date
JPS5837132A (en) 1983-03-04

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