JPS60211021A - Method for controlling sintering of ore to be sintered - Google Patents

Method for controlling sintering of ore to be sintered

Info

Publication number
JPS60211021A
JPS60211021A JP6520784A JP6520784A JPS60211021A JP S60211021 A JPS60211021 A JP S60211021A JP 6520784 A JP6520784 A JP 6520784A JP 6520784 A JP6520784 A JP 6520784A JP S60211021 A JPS60211021 A JP S60211021A
Authority
JP
Japan
Prior art keywords
raw material
size distribution
particle size
sintering
pallet
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.)
Pending
Application number
JP6520784A
Other languages
Japanese (ja)
Inventor
Hideomi Yanaka
谷中 秀臣
Hirohisa Hotta
堀田 裕久
Masanori Nagano
長野 誠規
Hidetoshi Noda
野田 英俊
Kazuhiro Furukawa
古川 和博
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 Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP6520784A priority Critical patent/JPS60211021A/en
Publication of JPS60211021A publication Critical patent/JPS60211021A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To make the quality of sintered ore uniform by detecting the grain size distribution of starting materials for sintering dropped onto a sintering pallet from a hopper and by regulating the degree of opening of the partition gate of the hopper and the angle of a shoot so as to make the grain size distribution uniform in the lateral direction. CONSTITUTION:Starting materials 4 for sintering dropped onto a pallet 3 from a surge hopper 2 through the partition gate 6 and a sloping shoot 7 have a varying grain size distribution in the vertical direction. This state is photographed with a high-speed TV camera, and the grain size distribution in the vertical and lateral directions is detected with a picture processor 9. The degree of opening of the gate 6 and the angle of the shoot 7 are regulated according to a signal from the processor 9 so as to make the grain size distribution of the dropped starting materials 4 uniform in the lateral direction and uniformly vary in the vertical direction. By this control the quality of sintered ore is made uniform.

Description

【発明の詳細な説明】 この発明は、焼結鉱の焼結制御方法に係り、詳しくは、
焼結鉱原料内の粒度分布を詳細にめて焼結鉱原料の焼結
制御を行なう焼結鉱の焼結制御方法に関するものである
[Detailed Description of the Invention] The present invention relates to a method for controlling sintering of sintered ore, and in detail,
The present invention relates to a sintering control method for sintered ore, which controls the sintering of sintered ore raw materials by finely determining the particle size distribution within the sintered ore raw materials.

焼結機により製鉄原料である焼結鉱を製造する場合、焼
結機のパレット内における原料の粒度分布は、焼結鉱成
品性状に影響を与えるファクターである。すなわち、原
料の粗粒分がパレット内原料層の下層へ、細粒分が上層
へ偏在する原料層高さ方向の粒度偏析は、原料内の通気
性に影響を与えて、原料の焼成過程の熱履歴を大きく左
右し、強度、還元粉化性、還元率といった焼結鉱品質を
支配する。また、原料の粗粒分、細粒分がA?レット内
幅方向に偏在する原料層幅方向の粒度偏析は、原料の焼
むらを生じ、焼結鉱品質一般を低下して歩留シを低下さ
せ、操業に悪影響を与える。
When producing sintered ore, which is a raw material for iron manufacturing, using a sintering machine, the particle size distribution of the raw material within the pallet of the sintering machine is a factor that affects the properties of the sintered ore product. In other words, particle size segregation in the height direction of the raw material layer, where the coarse particles of the raw material are unevenly distributed in the lower layer of the raw material layer in the pallet and the fine particles are unevenly distributed in the upper layer of the raw material layer, affects the air permeability within the raw material and the firing process of the raw material. It greatly influences the thermal history and controls the quality of sintered ore, such as strength, reduction pulverizability, and reduction rate. Also, is the coarse particle content and fine particle content of the raw material A? Particle size segregation in the width direction of the raw material layer, which is unevenly distributed in the width direction of the let, causes uneven firing of the raw material, lowers the general quality of sintered ore, lowers the yield rate, and has a negative impact on operations.

このようなことから、従来から、パレット内原料の粒度
分布を測定し、粒度偏析を調べて、焼結鉱の焼結制御を
行なうことが行なわれている。
For this reason, conventional methods have been to measure the particle size distribution of raw materials in pallets, examine particle size segregation, and control the sintering of sintered ore.

従来、この粒度分布は次のようにして測定されている。Conventionally, this particle size distribution has been measured as follows.

(1)焼結機を停止して、・ぐレットの進行および原料
の装入を止め、人が原料装入部へ入って・やレット内に
装入された原料をサンプリングし、その粒度を測定して
、粒度偏析を調べる。(2)パレットに原料が装入さn
る前にパレットにサンゾラーヲ載置して、パレットへの
原料装入時にサングラ−に原料を装入させ、次いで原料
装入部と点火炉の間で、クレーンでサンシラーをパレッ
トから引き上げて回収し、サングラ−内の原料の粒度を
測定して、原料層高さ方向での粒度偏析を調べる。
(1) Stop the sintering machine, stop the progress of the gret and the charging of raw materials, and have a person enter the raw material charging section and sample the raw material charged into the gret and check its particle size. Measure to determine particle size segregation. (2) Raw materials are loaded onto the pallet.
Before loading, the Sanzolar is placed on a pallet, and when the material is loaded onto the pallet, the Sanzolar is charged with the raw material.Then, between the raw material charging section and the ignition furnace, the Sanzolar is lifted up from the pallet and recovered by a crane. The particle size of the raw material in the sunglass is measured to examine particle size segregation in the height direction of the raw material layer.

しかし、(1)の方法は、(a)焼結機を停止するため
に操業が乱れ、製造効率が悪化する、伽)サンプリング
に人手を要す、(e)サンプリングした原料を乾燥し、
篩いで篩分けて粒度を測定するので、粒度の測定に手間
がかかり、1日に1回の割り合いでしか測定ができない
といった欠点がある。また、(2)の方法は、(a)原
料層のサンプリング箇所が少ない、(b)粒度の測定が
(1)の方法と同じなので、1日に1回の割り合いでし
か測定ができないといった欠点がある。
However, method (1) (a) stops the sintering machine, which disrupts operations and reduces production efficiency, (a) requires labor for sampling, and (e) requires drying of the sampled raw material.
Since the particle size is measured by separating the particles with a sieve, it takes time and effort to measure the particle size, and the disadvantage is that the particle size can only be measured once a day. In addition, method (2) has the following problems: (a) there are few sampling points in the raw material layer, and (b) particle size measurement is the same as method (1), so it can only be measured once a day. There are drawbacks.

従って、従来の焼結制御方法では、粒度分布が詳しくめ
られてないので、そのために、良好な焼結制御を行なう
ことが困難であった。
Therefore, in the conventional sintering control method, the particle size distribution is not considered in detail, which makes it difficult to perform good sintering control.

この発明は、上述の現状に鑑み、焼結鉱原料のノやレッ
ト内での粒度分布を詳しくめて焼結制御を行なう、焼結
鉱の焼結制御方法を提供するもので、サージホッパーか
ら焼結機のパレット内に装入される焼結鉱原料の装入過
程を、高速度テレビカメラによって撮像して、前記パレ
ット内における前記原料の粒度分布をめ、このようにし
てめられた粒度分布に基づいて、前記サージホッパー下
方の分割P−)の開度、前記サージホッパー下方のスロ
ーピングシュートの角度等の原料装入制御要素を変更し
て、前記パレット内における前記原料の粒度分布を調整
し、かくして、前記原料の焼結制御を行なうことに特徴
を有する。
In view of the above-mentioned current situation, the present invention provides a method for controlling sintering of sintered ore, which controls sintering by carefully determining the particle size distribution in the sintered ore raw materials. The charging process of the sintered ore raw material charged into the pallet of the sintering machine was imaged by a high-speed television camera, and the particle size distribution of the raw material within the pallet was measured. Based on the distribution, raw material charging control elements such as the opening degree of the division P-) below the surge hopper and the angle of the sloping chute below the surge hopper are changed to adjust the particle size distribution of the raw material within the pallet. Thus, the present invention is characterized in that the sintering of the raw material is controlled.

以下、この発明の実施例を図面に基づき詳述する。第1
図は、この発明の焼結鉱の焼結制御方法を説明するため
の説明図、第2図は、第1図のA−A線矢視図である。
Hereinafter, embodiments of the present invention will be described in detail based on the drawings. 1st
The figure is an explanatory diagram for explaining the sintering control method of sintered ore according to the present invention, and FIG. 2 is a view taken along the line A--A in FIG. 1.

第1〜2図において、1は焼結機のサージホッパー2か
ら切出されて/’Pツクレット3内入される焼結鉱原料
4の装入過程を撮像するための高速度テレビカメラで、
高速度テレビカメラlは、サージホッパ−2の手前にノ
4?レット3の幅方向に3台設置され、ツクレット3内
の原料層の幅方向側面を視野に収めている。
In FIGS. 1 and 2, 1 is a high-speed television camera for photographing the charging process of sintered ore raw material 4 cut out from the surge hopper 2 of the sintering machine and put into the /'P tuklet 3;
Is the high-speed television camera located in front of the surge hopper 2? Three units are installed in the width direction of the ret 3, and the widthwise side surfaces of the raw material layer inside the ret 3 are kept in view.

原料4は、ロールフィーダー5によってサージホラ・ぐ
−2下部の分割f −) 6から切出されて、スローピ
ングシュート7に沿って落下した後、矢視の向きに進行
するパレット3内の原料4の層の表面に沿って落下して
、パレット3内に堆積する。
The raw material 4 is cut out from the division f-) 6 at the bottom of the serge hollow groove 2 by the roll feeder 5, and falls along the sloping chute 7, after which the raw material 4 in the pallet 3 advances in the direction of the arrow. It falls along the surface of the layer and is deposited in the pallet 3.

原料4が原料層の表面に沿って落下するときにはずり落
ちるので、落下速度は遅くなるが、それでも0.2〜1
 m1sec程度の速度がある。そのために、原料層の
表面を落下する原料4を通常のテレビカメラで撮像して
も、原料4の粒子の形状、大きさまではわからない。従
って、ノ臂レット3内の原料層の表面に沿って落下する
原料4の装入過程を撮像して、パレット3内での原料4
の粒度分布を測定するためには、高速度テレビカメラ1
を用いることを要する。なお、第1図において8はパレ
ット3内に装入された原料4の上部をならすカットオフ
プレートである。
When the raw material 4 falls along the surface of the raw material layer, it slides down, so the falling speed becomes slower, but still 0.2 to 1
The speed is about m1sec. Therefore, even if an ordinary television camera images the raw material 4 falling on the surface of the raw material layer, the shape and size of the particles of the raw material 4 cannot be seen. Therefore, the charging process of the raw material 4 falling along the surface of the raw material layer in the pallet 3 is imaged, and the raw material 4 in the pallet 3 is
In order to measure the particle size distribution of
It is necessary to use In addition, in FIG. 1, 8 is a cut-off plate that smooths the upper part of the raw material 4 charged into the pallet 3.

高速度テレビカメラ1によって原料4の装入過程を撮像
した画像信号は、画像処理装置9によって画像処理され
、これにより、例えば第3図、(a) 。
An image signal obtained by imaging the charging process of the raw material 4 by the high-speed television camera 1 is image-processed by the image processing device 9, and thereby, for example, the image shown in FIG. 3 (a) is obtained.

(b)に示すような、パレット3内における原料4の粒
度分布がめられる。ここで、第3図(a)は、原料層高
さ方向の粒度分布をめたもので、a−dの分布帯は、原
料4の平均粒度(M、S、)がa:3簡以上、b=3〜
1■、c:1〜0.5W1d:o、5閣以下となってい
る。また、第3図(b)は、原料層高さ方向を3つに分
け、原料層幅方向を4つに分けて、原料層を15のブロ
ックとし、各ブロックの平均粒度XI ” xtsをめ
たものである。
The particle size distribution of the raw material 4 within the pallet 3 can be seen as shown in (b). Here, FIG. 3(a) shows the particle size distribution in the height direction of the raw material layer, and the distribution bands a to d indicate that the average particle size (M, S,) of the raw material 4 is a: 3 cm or more. , b=3~
1■, c: 1 to 0.5 W1d: o, 5 or less. In addition, in Fig. 3(b), the raw material layer is divided into 3 parts in the height direction and 4 parts in the width direction, and the raw material layer is made into 15 blocks, and the average particle size of each block is calculated as follows: It is something that

このような平均粒度X、〜XI5から、例えば原料上層
(XI + I4 y Xy + X+o 、X+s 
) 、原料中層(I2゜xs l xg j XIt 
+ XI4 ) s原料下層(I31 xa l Xl
l +XI2 s xlIl)毎に、平均値マ、偏析の
程度(標準偏差)σをめて、原料層幅方向の偏析を指数
化する。また、例えば上層、中層、下層の平均粒度XI
 lX2 lX3に対して、(Xs −XI )/x2
をめて、原料層高さ方向の偏析を指数化する。
From such an average particle size X, ~XI5, for example, the raw material upper layer (XI + I4 y Xy + X+o,
), raw material middle layer (I2゜xs l xg j XIt
+ XI4) s Raw material lower layer (I31 xa l Xl
l + Also, for example, the average particle size of the upper layer, middle layer, and lower layer XI
For lX2 lX3, (Xs - XI)/x2
and index the segregation in the height direction of the raw material layer.

以上のようにしてパレット内における原料の粒度分布が
められたならば、焼結鉱製造の操業解析によって得られ
た最適粒度分布と比較し、アクション手段(原料装入制
御要素)を変更して、原料がノやレット内に最適の粒度
分布で装入されるように調整することによって、焼結制
御をする。原料層高さ方向の粒度分布を調整するには、
スローピングシュートの角U、スローピングシューとロ
ールフィーダーとの相対的位置、ロールフィーダー回転
数などを変更する。原料層幅方向の粒度分布の調整は、
幅方向での偏析をなくす均一化制御となるが、これは、
分割ダートの開度の調整によって行なわれる。また、ス
ローピングシュートニ原料が固着すると幅方向の偏析の
原因となるので、スローピングシュートの清掃も有効で
ある。
Once the particle size distribution of the raw material in the pallet has been determined as described above, it is compared with the optimum particle size distribution obtained through operational analysis of sinter production, and the action means (raw material charging control elements) are changed. Sintering is controlled by adjusting the raw material to be charged into the slot with the optimum particle size distribution. To adjust the particle size distribution in the height direction of the raw material layer,
The angle U of the sloping chute, the relative position of the sloping shoe and the roll feeder, the rotation speed of the roll feeder, etc. are changed. To adjust the particle size distribution in the width direction of the raw material layer,
This is uniform control that eliminates segregation in the width direction, but this
This is done by adjusting the opening degree of the divided darts. In addition, cleaning the sloping chute is also effective because if the sloping chute raw material sticks, it causes segregation in the width direction.

なお、測定された粒度分布のデータは蓄積して、操業解
析によって最適の粒度分布をめるのに使用されることは
勿論である。
It goes without saying that the measured particle size distribution data is accumulated and used to determine the optimum particle size distribution through operational analysis.

との発明の焼結鉱の焼結制御方法は以上のように構成さ
れるので、次のような効果がある。(1)原料の装入過
程を高速度テレビカメラで撮像して、A?レット内での
原料の粒度分布をめるので、原料層高さ方向、幅方向の
全面に亘って詳しく粒度分布を識って、焼結制御ができ
る。(2)従来のように1日に1回程度でなく、数分間
に1回の割9合いで粒度分布をめられるので、サンプリ
ングによるバラツキをなくして、焼結制御ができる。(
3)時間の経過と共に偏析の状況がどのように変化して
いるかがわかるので、制御のアクションが即座にとれる
。(4)粒度分布をめるのに人手や手間がかからない。
The method for controlling sintering of sintered ore according to the invention is configured as described above, and therefore has the following effects. (1) The raw material charging process is imaged with a high-speed television camera, and A? Since the particle size distribution of the raw material within the let is determined, sintering can be controlled by knowing the particle size distribution in detail over the entire height and width directions of the raw material layer. (2) Since the particle size distribution can be measured once every few minutes instead of once a day as in the conventional method, sintering can be controlled without variations due to sampling. (
3) Since it is possible to see how the segregation situation is changing over time, control actions can be taken immediately. (4) It does not require manpower or effort to determine the particle size distribution.

(5)粒度分布を詳しくめて焼結制御するので、良好な
焼結制御ができる。
(5) Since the particle size distribution is finely tuned for sintering control, good sintering control can be achieved.

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

法で用いる高速度テレビカメラで得られた原料の粒度分
布を示す図である。図面において、l・・・高速度テレ
ビカメラ、 2・・・サーソホツノ+−,3・・・パレット、4・・
・i料、 5・・・ロールフィーダー、6・・・分割ケ
゛−ト、 7・・・スローピングシュート、 8・・・カットオフプレート、 9・・・画像処理装置。 出願人 日本鋼管株式会社 代理人 潮谷 奈津夫(他2名) 棄1図 第3図 (a) 輻夕向 (b) すi方nη
FIG. 2 is a diagram showing the particle size distribution of raw materials obtained with a high-speed television camera used in the method. In the drawings, l...High-speed television camera, 2...Thursohatsuno+-, 3...Pallet, 4...
・I material, 5... Roll feeder, 6... Division case, 7... Sloping chute, 8... Cutoff plate, 9... Image processing device. Applicant Nippon Steel Tube Co., Ltd. Agent Natsuo Shioya (and 2 others) Figure 1 Figure 3 (a) Direction (b) Direction nη

Claims (1)

【特許請求の範囲】[Claims] サージホッパーから焼結機のパレット内に装入される焼
結鉱原料の装入過程を、高速度テレビカメラによって撮
像して、前記/fレット内における前記原料の粒度分布
をめ、このようにしてめられた粒度分布に基づいて、前
記サージホッパー下部の分割ケ°−トの開度、前記サー
ジホッパー下方のスローピングシュートの角度等の原料
装入制御要素を変更して、前記A?レット内における前
記原料の粒度分布を調整し、かくして、前記原料の焼結
制御を行なうことを特徴とする焼結鉱の焼結制御方法。
The charging process of the sintered ore raw material charged from the surge hopper into the pallet of the sintering machine was imaged by a high-speed television camera, and the particle size distribution of the raw material in the /flet was measured. The A? A method for controlling the sintering of sintered ore, the method comprising adjusting the particle size distribution of the raw material in a sintered ore, and thus controlling the sintering of the raw material.
JP6520784A 1984-04-03 1984-04-03 Method for controlling sintering of ore to be sintered Pending JPS60211021A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6520784A JPS60211021A (en) 1984-04-03 1984-04-03 Method for controlling sintering of ore to be sintered

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6520784A JPS60211021A (en) 1984-04-03 1984-04-03 Method for controlling sintering of ore to be sintered

Publications (1)

Publication Number Publication Date
JPS60211021A true JPS60211021A (en) 1985-10-23

Family

ID=13280237

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6520784A Pending JPS60211021A (en) 1984-04-03 1984-04-03 Method for controlling sintering of ore to be sintered

Country Status (1)

Country Link
JP (1) JPS60211021A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0286381A2 (en) * 1987-04-06 1988-10-12 Nippon Steel Corporation Apparatus and method for feeding sintering raw mix
JPH0445541U (en) * 1990-08-20 1992-04-17
CN100441996C (en) * 2005-11-24 2008-12-10 广东韶钢松山股份有限公司 Sintering automatic distributing method
KR100929490B1 (en) * 2002-12-23 2009-12-03 주식회사 포스코 Sintering raw material charging control method of sintering machine

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0286381A2 (en) * 1987-04-06 1988-10-12 Nippon Steel Corporation Apparatus and method for feeding sintering raw mix
JPH0445541U (en) * 1990-08-20 1992-04-17
KR100929490B1 (en) * 2002-12-23 2009-12-03 주식회사 포스코 Sintering raw material charging control method of sintering machine
CN100441996C (en) * 2005-11-24 2008-12-10 广东韶钢松山股份有限公司 Sintering automatic distributing method

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