JPH03211241A - Operating method for sintering machine - Google Patents
Operating method for sintering machineInfo
- Publication number
- JPH03211241A JPH03211241A JP768090A JP768090A JPH03211241A JP H03211241 A JPH03211241 A JP H03211241A JP 768090 A JP768090 A JP 768090A JP 768090 A JP768090 A JP 768090A JP H03211241 A JPH03211241 A JP H03211241A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- exhaust gas
- sintering machine
- sintering
- temp
- 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 51
- 238000011017 operating method Methods 0.000 title description 2
- 238000000034 method Methods 0.000 claims description 14
- 230000002250 progressing effect Effects 0.000 abstract description 2
- 239000007789 gas Substances 0.000 abstract 4
- 238000004519 manufacturing process Methods 0.000 description 6
- 238000007796 conventional method Methods 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 230000007704 transition Effects 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] 本発明は、焼結機の操業方法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a method of operating a sintering machine.
[従来の技術]
DL式焼結機で焼結鉱を製造する際、焼結鉱の品質、成
品歩留の向上を計るための種々の操業技術が開発され、
実施されている。従来から、焼結機の機長方向の排ガス
温度を測定し、排鉱部側の温度分布に近似する2次曲線
式を求め、温度が極大値となる位置(焼結終了点)が所
定位、置になるように、パレットスピードを制御する方
法や、焼結機の排鉱部端における焼結層断面の残火層厚
が所定の厚さになるようにパレットスピードを制御する
方法が一般的に行われてきた。公開された特許文献とし
ては、焼結機機長方向の風箱の排ガス温度推移から幅方
向別に焼結終了点を検出し、幅方向平均焼成点を算出し
て、それが目標値となるようにパレットスピードを調整
する方法(特開昭60−13032号公報)がある。[Prior art] When producing sintered ore using a DL sintering machine, various operating techniques have been developed to improve the quality of the sintered ore and the product yield.
It has been implemented. Conventionally, the exhaust gas temperature in the longitudinal direction of the sintering machine is measured, a quadratic curve equation that approximates the temperature distribution on the ore discharge side is found, and the position where the temperature reaches the maximum value (sintering end point) is determined at a predetermined position. Generally, the pallet speed is controlled so that the thickness of the sinter layer at the end of the ore discharge section of the sintering machine reaches a predetermined thickness. It has been carried out in As a published patent document, the sintering end point is detected in each width direction from the exhaust gas temperature transition of the wind box in the longitudinal direction of the sintering machine, the average sintering point in the width direction is calculated, and this is set as the target value. There is a method of adjusting pallet speed (Japanese Patent Laid-Open No. 13032/1983).
[発明が解決しようとする課題]
しかしながら、従来の焼結終了点でパレットスピードを
制御する方法については以下のような問題点がある。排
鉱部に近づくにしたがって焼結層の収縮が増大し、この
結果、焼結層の割れに起因する漏風、サイドウオールと
焼結層間での漏風が増加する。これらの漏風および排鉱
部端からの漏風は時間的に一様でなく、漏風量の変化が
大きい、このため、排鉱部側の排ガス温度の変動が大き
い、すなわち、焼結層の焼成状態に変化が無くとも、見
掛けの排ガス温度が変化し、そのため、このような排ガ
ス温度に基づいて算出される焼結終了点が変化し、パレ
ットスピードを変化させてしまう、この結果、生産率の
低下および歩留りを悪化させるという問題点がある。[Problems to be Solved by the Invention] However, the conventional method of controlling the pallet speed at the sintering end point has the following problems. The shrinkage of the sintered layer increases as it approaches the ore discharge area, and as a result, air leakage due to cracks in the sintered layer and air leakage between the sidewall and the sintered layer increase. These air leaks and the air leakage from the end of the ore discharge section are not uniform over time, and the amount of air leakage changes greatly. Therefore, the fluctuation of the exhaust gas temperature on the ore discharge section side is large, that is, the firing state of the sintered layer Even if there is no change in , the apparent exhaust gas temperature changes, and therefore the sintering end point calculated based on such exhaust gas temperature changes, causing a change in pallet speed, resulting in a decrease in production rate. Also, there is a problem of deterioration of yield.
一方、排鉱部端の焼結層断面の残火の層厚を一定にする
方法は、残火層厚を検出するモニターカメラの感度が経
時的に変化すること、および排鉱部は発塵が著しく、測
定精度が悪いため正確なパレットスピード制御ができな
いという問題点がある。On the other hand, the method of keeping the layer thickness of the embers constant in the cross-section of the sintered layer at the end of the ore discharge section is difficult because the sensitivity of the monitor camera that detects the thickness of the ember layer changes over time, and the ore discharge section is dust-producing. There is a problem that accurate pallet speed control is not possible due to the extremely low measurement accuracy.
[課題を解決するための手段]
本発明は上記のような問題点を解決しようとするもので
、一つは焼結機の機長方向複数箇所の排ガス温度を測定
し、該測定温度から機長方向の排ガス温度曲線式な求め
、該温度曲線の温度上昇開始点から焼結終了点の間であ
って、所定温度になる位置を求め、該位置が設定位置に
なるように焼結機のパレットスピードを制御することを
特徴とする焼結機の操業方法であり、他のものは焼結機
の機長方向の複数列の排ガス温度曲線式を求め、各列の
排ガス温度曲線式について、該温度曲線の温度上昇開始
点から焼結終了点の間であって、所定温度になる位置を
求め、それらの位置の平均位置またはそれらの位置のう
ち点火箱から最も離れた位置が設定位置になるように焼
結機のパレットスピードを制御することを特徴とする焼
結機の操業方法である。そして、前記方法において、所
定温度は150〜300℃の範囲にするのが望ましい。[Means for Solving the Problems] The present invention attempts to solve the above-mentioned problems. One is to measure the exhaust gas temperature at multiple locations in the longitudinal direction of a sintering machine, and to calculate the temperature in the longitudinal direction from the measured temperature. Find the exhaust gas temperature curve formula, find the position on the temperature curve between the temperature rise start point and the sintering end point where the specified temperature is reached, and adjust the pallet speed of the sintering machine so that this position becomes the set position. Another method is to obtain exhaust gas temperature curve equations for multiple rows in the longitudinal direction of the sintering machine, and for each row of exhaust gas temperature curve equations, calculate the temperature curve. Find the position between the temperature rise start point and the sintering end point where the predetermined temperature is reached, and set the set position to be the average position of those positions or the position farthest from the ignition box among those positions. A method of operating a sintering machine characterized by controlling the pallet speed of the sintering machine. In the method, the predetermined temperature is preferably in the range of 150 to 300°C.
[作用コ
焼結機の機長方向(進行方向)の排ガス温度は、第3図
に示すように、排鉱部側、特に焼結終了点の前後で変動
(振れ)が大きいが、排ガス温度上昇開始点Aから焼結
終了点の間は変動が小さい。従って、所定温度を排ガス
温度上昇開始点Aから焼結終了点の間に設定すれば、パ
レットスピードの適正な制御ができ、生産率および歩留
りの向上を計ることができる。[Effectiveness] As shown in Figure 3, the exhaust gas temperature in the machine length direction (progressing direction) of the sintering machine fluctuates greatly on the ore discharge side, especially before and after the sintering end point, but the exhaust gas temperature rises. There is little variation between the starting point A and the sintering end point. Therefore, by setting the predetermined temperature between the exhaust gas temperature rise start point A and the sintering end point, the pallet speed can be appropriately controlled and the production rate and yield can be improved.
[実施例コ
本発明の実施例を以下に詳細に説明する。第1図は焼結
機の排ガス温度分布の例を示すグラフである。この例は
風箱数が23個ある焼結機の例である。焼結機の排ガス
温度は、装入された原料層の上面に点火された後、層中
に燃焼帯ができ、燃焼帯が降下してゆくにしたがって、
上昇するものであるが、有効機長の70%までは排ガス
温度は殆ど上昇せず、80〜90℃で推移する。この後
、排ガス温度は上昇し、有効機長の約95%位に温度の
最大点(焼結終了点、略記号BTPこの点の排ガス温度
は、通常350〜450℃である)が表れ、その後降下
する。第1図の例では風箱N017まで、80℃、N0
18で100℃に上昇し、その後曲線(2次−数)的に
上昇して最大400 ’Cになっている。[Example] Examples of the present invention will be described in detail below. FIG. 1 is a graph showing an example of exhaust gas temperature distribution of a sintering machine. This example is of a sintering machine with 23 wind boxes. The exhaust gas temperature of the sintering machine changes as the combustion zone is formed in the layer after it is ignited on the top surface of the charged raw material layer, and as the combustion zone descends,
However, up to 70% of the effective aircraft length, the exhaust gas temperature hardly rises and remains at 80 to 90°C. After this, the exhaust gas temperature rises, and a maximum temperature point (sintering end point, abbreviation BTP; the exhaust gas temperature at this point is usually 350 to 450°C) appears at about 95% of the effective length, and then decreases. do. In the example in Figure 1, up to wind box N017, the temperature is 80℃, N0
The temperature rises to 100°C at 18°C, and then rises in a curve (quadratic order) to a maximum of 400°C.
本発明の操業方法は、パレットスピードの制御指標値1
を排ガス温度変動の大きい焼結終了点を避け、排ガス温
度変動の小さい温度上昇開始点(A)から焼結終了点(
B)の間に目標温度を設け、その目標温度になる風箱位
置を求め、その位置が、生産率、成品歩留を考慮して定
めた位置になるようにパレットスピードを制御するもの
である。パレットスピード制御は、具体的には演算機を
使用して、次のように行う。演算機に、排ガス温度上昇
開始点以降の3箇所の風箱温度を入力し、(1)式の係
数A、B、Cを求めて、排ガス温度曲線式を確定し、該
排カス温度曲線式から目標温度になる風箱位置を演算し
て、これが設定位置になるようにパレットスピードを制
御する。The operating method of the present invention has a pallet speed control index value of 1
Avoid the sintering end point where the exhaust gas temperature fluctuation is large, and move from the temperature rise start point (A) where the exhaust gas temperature fluctuation is small to the sintering end point (
A target temperature is set between B), the wind box position at which the target temperature is achieved is determined, and the pallet speed is controlled so that the position is determined by taking into account the production rate and product yield. . Specifically, pallet speed control is performed using a computer as follows. Input the wind box temperatures at three locations after the exhaust gas temperature rise start point into the computer, determine the coefficients A, B, and C of equation (1), determine the exhaust gas temperature curve formula, and calculate the exhaust gas temperature curve formula. The wind box position at which the target temperature is achieved is calculated from , and the pallet speed is controlled so that this is the set position.
TI=A+ P+ +−131pl +C+ ・
(1)ここに、T1・風箱位置P+における排ガス温
度P+・・・風箱位置
At、B+、C区・・・それぞれ、2次項、1次項の係
数、定数
添字i・風箱の幅方向に排ガス温度計を複数設けた場合
の列数(第4図
参照)
排ガス温度の変動ができるだけ少いこと、および焼結速
度の変化を早く把握できることを考慮すれば、目標温度
は排ガス温度が150〜300℃の範囲内(第1図でC
〜Dの範囲)に決めることがより望ましい。TI=A+ P+ +-131pl +C+ ・
(1) Here, T1, exhaust gas temperature P+ at wind box position P+...Wind box position At, B+, C section...respectively, coefficients of quadratic term, linear term, constant subscript i, width direction of wind box Number of rows when multiple exhaust gas thermometers are installed (see Figure 4) Considering that fluctuations in the exhaust gas temperature are as small as possible and changes in the sintering speed can be ascertained quickly, the target temperature is the exhaust gas temperature of 150 ~300℃ (C in Figure 1)
It is more desirable to set it in the range of ~D).
排ガス温度を測定する温度センサーは、各風箱の中心で
機長方向に1列だけ設ける場合と、第4図のように、風
箱の幅方向に複数の温度センサを設けて、機長方向に複
数列設ける場合がある。Temperature sensors that measure the exhaust gas temperature can be installed in one row in the longitudinal direction of the aircraft at the center of each wind box, or as shown in Fig. There may be a row.
第2図は温度センサーを機長方向に3列(第4図参照)
設けて、各列毎の温度曲線を求め、目標温度250℃に
対応する風箱位置を求める様子をグラフに示したもので
ある。実際は演算機で(1)式のTI =250℃とし
、Plを求める。この場合、目標温度250°Cに対応
する風箱値Iは、生産率を重視するときはP 、、P
2.P 、の平均値とし、歩留りを重視するときは、P
、、P 2.P 3の最大値とする。Figure 2 shows three rows of temperature sensors in the direction of the pilot (see Figure 4).
The graph shows how the wind box position corresponding to the target temperature of 250° C. is determined by setting the temperature curve for each row. Actually, Pl is determined using a computer by setting TI = 250°C in equation (1). In this case, the wind box value I corresponding to the target temperature of 250°C is P, , P when emphasis is placed on the production rate.
2. When the yield is important, P is the average value of P.
,,P 2. Let it be the maximum value of P3.
なお、自動制御運転を行う場合、従来と同じように1次
の条件を入れて運転する。Note that when automatically controlled operation is performed, the primary conditions are entered as in the conventional case.
(1) 主ダクトの吸引負圧上限で、パレ・7トスピ
ドを低下する。(1) At the upper limit of the suction negative pressure of the main duct, reduce the Pare 7 tospid.
(2+ 主ダクト電気集塵機前の排ガス温度下限で、
パレットスピードを低下する。(2+ At the lower limit of the exhaust gas temperature before the main duct electrostatic precipitator,
Reduce pallet speed.
本発明の方法(条件:目標温度250℃、設定風箱位置
20.2>と従来方法の生産率を比較したものが第1表
である。ここで、従来法(1)は従来の焼結終了点でパ
レットスピードを制御する方法、従来法(2)は排鉱部
端の焼結層断面の残火の層厚を一定にする方法である0
本発明方法による方が0.05T/m”hの向上が得ら
れた。Table 1 compares the production rates of the method of the present invention (conditions: target temperature 250°C, set wind box position 20.2) and the conventional method. The conventional method (2), which is a method of controlling the pallet speed at the end point, is a method of keeping the layer thickness of the embers constant on the cross section of the sintered layer at the end of the ore discharge section.
An improvement of 0.05 T/m''h was obtained using the method of the present invention.
第 1 表
[発明の効果]
本発明は、排ガス温度の変動の少ない温度上昇開始点と
焼結終了点の間に目標温度を設定し、この温度に対応す
る位置を設定位置になるようにパレットスピードを制御
するようにしたから、従来方法に比較して、生産率、成
品歩留が向上するという効果がある。Table 1 [Effects of the Invention] In the present invention, a target temperature is set between a temperature rise start point and a sintering end point where there is little fluctuation in exhaust gas temperature, and the pallet is moved so that the position corresponding to this temperature becomes the set position. Since the speed is controlled, the production rate and product yield are improved compared to conventional methods.
第1図は焼結機の機長方向排ガス温度曲線の一例を示す
グラフ図、第2図は温度センサーを機長方向に3列設け
た場合の排ガス温度曲線を示すグラフ図、第3図は排ガ
ス温度曲線と風箱位置における排ガス温度の変動を示す
グラフ図、第4図は機長方向に温度センサーを複数列設
けたときの温度センサーの配置を示す図である。Figure 1 is a graph showing an example of the exhaust gas temperature curve in the machine length direction of a sintering machine, Figure 2 is a graph diagram showing the exhaust gas temperature curve when three rows of temperature sensors are installed in the machine length direction, and Figure 3 is the exhaust gas temperature curve. FIG. 4 is a graph showing the fluctuation of exhaust gas temperature at the curve and wind box position, and is a diagram showing the arrangement of temperature sensors when a plurality of rows of temperature sensors are provided in the longitudinal direction.
Claims (6)
、該測定温度から機長方向の排ガス温度曲線式を求め、
該温度曲線の温度上昇開始点から焼結終了点の間であっ
て、所定温度になる位置を求め、該位置が設定位置にな
るように焼結機のパレットスピードを制御することを特
徴とする焼結機の操業方法。(1) Measure the exhaust gas temperature at multiple locations in the longitudinal direction of the sintering machine, calculate the exhaust gas temperature curve formula in the longitudinal direction from the measured temperatures,
The method is characterized in that a position at which a predetermined temperature is reached between a temperature rise start point and a sintering end point on the temperature curve is determined, and the pallet speed of the sintering machine is controlled so that the position reaches a set position. How to operate a sintering machine.
の間の温度に設定する焼結機の操業方法。(2) In claim 1, the predetermined temperature is 150 to 300°C.
How to operate a sintering machine to set the temperature between.
求め、各列の排ガス温度曲線式について、該温度曲線の
温度上昇開始点から焼結終了点の間であつて、所定温度
になる位置を求め、それらの位置の平均位置が設定位置
になるように焼結機のパレットスピードを制御すること
を特徴とする焼結機の操業方法。(3) Find exhaust gas temperature curve equations for multiple rows in the machine length direction of the sintering machine, and for each row of exhaust gas temperature curve equations, determine the temperature at a predetermined temperature between the temperature rise start point and sintering end point of the temperature curve. 1. A method for operating a sintering machine, which comprises determining the position where the position is, and controlling the pallet speed of the sintering machine so that the average position of those positions becomes the set position.
の間の温度に設定する焼結機の操業方法。(4) In claim 3, the predetermined temperature is 150 to 300°C.
How to operate a sintering machine to set the temperature between.
求め、各列の排ガス温度曲線式について、該温度曲線の
温度上昇開始点から焼結終了点の間であって、所定温度
になる位置を求め、それらの位置のうち点火箱から最も
離れた位置が設定位置になるように焼結機のパレットス
ピードを制御することを特徴とする焼結機の操業方法。(5) Find exhaust gas temperature curve equations for multiple rows in the machine length direction of the sintering machine, and for each row of exhaust gas temperature curve equations, determine the temperature between the temperature rise start point and the sintering end point of the temperature curve. 1. A method for operating a sintering machine, which comprises determining the position where the ignition box is located, and controlling the pallet speed of the sintering machine so that the position farthest from the ignition box among those positions becomes the set position.
の間の温度に設定する焼結機の操業方法。(6) In claim 5, the predetermined temperature is 150 to 300°C.
How to operate a sintering machine to set the temperature between.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2007680A JPH0819488B2 (en) | 1990-01-17 | 1990-01-17 | How to operate the sintering machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2007680A JPH0819488B2 (en) | 1990-01-17 | 1990-01-17 | How to operate the sintering machine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03211241A true JPH03211241A (en) | 1991-09-17 |
JPH0819488B2 JPH0819488B2 (en) | 1996-02-28 |
Family
ID=11672506
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2007680A Expired - Fee Related JPH0819488B2 (en) | 1990-01-17 | 1990-01-17 | How to operate the sintering machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0819488B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006307259A (en) * | 2005-04-27 | 2006-11-09 | Jfe Steel Kk | Method for controlling pallet speed in sintering machine |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS552725A (en) * | 1978-06-21 | 1980-01-10 | Nippon Kokan Kk <Nkk> | Control method for dl sintering machine |
JPS6013032A (en) * | 1983-07-01 | 1985-01-23 | Sumitomo Metal Ind Ltd | Method for controlling calcination point with sintering machine |
-
1990
- 1990-01-17 JP JP2007680A patent/JPH0819488B2/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS552725A (en) * | 1978-06-21 | 1980-01-10 | Nippon Kokan Kk <Nkk> | Control method for dl sintering machine |
JPS6013032A (en) * | 1983-07-01 | 1985-01-23 | Sumitomo Metal Ind Ltd | Method for controlling calcination point with sintering machine |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006307259A (en) * | 2005-04-27 | 2006-11-09 | Jfe Steel Kk | Method for controlling pallet speed in sintering machine |
Also Published As
Publication number | Publication date |
---|---|
JPH0819488B2 (en) | 1996-02-28 |
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