JPH089740B2 - Operating method of sintering machine - Google Patents

Operating method of sintering machine

Info

Publication number
JPH089740B2
JPH089740B2 JP1089390A JP1089390A JPH089740B2 JP H089740 B2 JPH089740 B2 JP H089740B2 JP 1089390 A JP1089390 A JP 1089390A JP 1089390 A JP1089390 A JP 1089390A JP H089740 B2 JPH089740 B2 JP H089740B2
Authority
JP
Japan
Prior art keywords
temperature
zone
exhaust gas
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.)
Expired - Fee Related
Application number
JP1089390A
Other languages
Japanese (ja)
Other versions
JPH03215630A (en
Inventor
龍一 中島
純幸 岸本
信一 黒沢
吉史 松永
寛 福与
和田  隆
Original Assignee
日本鋼管株式会社
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 日本鋼管株式会社 filed Critical 日本鋼管株式会社
Priority to JP1089390A priority Critical patent/JPH089740B2/en
Publication of JPH03215630A publication Critical patent/JPH03215630A/en
Publication of JPH089740B2 publication Critical patent/JPH089740B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、製鉄業における焼結機の操業方法に関する
ものである。
TECHNICAL FIELD The present invention relates to a method for operating a sintering machine in the iron manufacturing industry.

[従来技術] 従来焼結機の操業においては、被焼結帯の下面に流出
する排ガスの温度の、機長方向の温度分布を調査して焼
成完了点を求め、この点が、できるだけ排鉱部(焼結機
から焼成完了後の鉱が排出される場所)に近接した場所
に留まるように、ライン速度を調節している。第2図は
排ガス温度の機長方向分布のパターンを示すグラフであ
る。横軸機長方向の位置を、縦軸に排ガス温度をそれぞ
れ示す。図に示すように、排ガス温度は、当初は燃料帯
が被焼結帯の上面にあるため定温を保持し、燃焼帯が下
面に近づくとともに温度が上昇を開始して、燃焼帯が下
面に達した位置ですなわち、焼結が終了した場所で、最
高温度に到達し、以後自然放冷によって下降する。この
温度パターンは巾方向において異なり、例えば被焼結帯
の巾方向中央部の焼結終了点と巾方向端部の焼結終了点
とは必ずしも一致しない。特公昭54−11763号公報にお
いては、機長方向の特定位置において、巾方向に複数の
排ガス温度計を配して、その測定値と予め定めた設定値
とを比較して、原料供給における巾方向分布を調節し、
巾方向に均一な焼結を行っている。
[Prior Art] In the operation of a conventional sintering machine, the temperature distribution in the machine length direction of the temperature of the exhaust gas flowing out to the lower surface of the zone to be sintered is investigated to find the firing completion point. The line speed is adjusted so that it stays close to the place (where the ore after firing is completed is discharged from the sintering machine). FIG. 2 is a graph showing a pattern of exhaust gas temperature distribution in the machine length direction. The horizontal axis represents the machine length direction, and the vertical axis represents the exhaust gas temperature. As shown in the figure, the exhaust gas temperature keeps a constant temperature because the fuel zone is on the upper surface of the sintered zone at the beginning, and as the combustion zone approaches the lower surface, the temperature starts rising and the combustion zone reaches the lower surface. The maximum temperature is reached at the above-mentioned position, that is, at the place where the sintering is completed, and then the temperature is lowered by natural cooling. This temperature pattern differs in the width direction, and for example, the sintering end point at the widthwise center of the sintered band and the sintering end point at the widthwise end do not necessarily coincide. In Japanese Patent Publication No. 54-11763, at a specific position in the machine length direction, a plurality of exhaust gas thermometers are arranged in the width direction, and the measured value is compared with a predetermined set value, and the width direction in the raw material supply is measured. Adjust the distribution,
Uniform sintering is performed in the width direction.

[発明が解決しようとする課題] しかしながら、従来技術においては下記の問題点があ
る。すなわち、 従来技術においては、焼結機の機長方向の所定位置にお
いて排ガス温度の巾方向分布を測定しているが、第2図
に示すような温度パターンにおいては燃焼帯の発達状況
を誤認する可能性がある。第3図は巾方向中央部の温度
パターンqと、巾方向端部の温度パターンrを示すグラ
フである。今機長方向の位置Pにおいて、中央部の温度
Qを測定し、端部の温度Rを得たとする。点Rはグラフ
の最高点すなわち焼結終了点の右側にあるが、点Qは左
側にあるので、これらの値を比較することは、焼結終了
前の温度と終了後の温度を混同することになる。本発明
は上記の問題点を解決し、正確に焼結反応を制御できる
焼結機の操業方法を提供することをその目的とするもの
である。
[Problems to be Solved by the Invention] However, the prior art has the following problems. That is, in the conventional technique, the widthwise distribution of the exhaust gas temperature is measured at a predetermined position in the machine length direction of the sintering machine, but in the temperature pattern as shown in FIG. There is a nature. FIG. 3 is a graph showing a temperature pattern q at the center in the width direction and a temperature pattern r at the end in the width direction. It is assumed that the temperature Q at the central portion is measured at the position P in the machine length direction and the temperature R at the end portion is obtained. The point R is on the right side of the highest point of the graph, that is, the end point of sintering, but the point Q is on the left side. Therefore, comparing these values should be confused with the temperature before and after the sintering. become. SUMMARY OF THE INVENTION It is an object of the present invention to solve the above problems and provide a method of operating a sintering machine that can accurately control the sintering reaction.

[課題を解決するための手段] 上記課題を、機長方向かつ水平方向に移動しながら、
上面より下面に燃焼帯が移動する被燃焼帯を有し、かつ
該被焼結帯の上面から下面に空気を通過する手段を有す
る焼結機の操業方法において、被焼結帯下面の巾方向お
よび進行方向に複数個配設した排ガスの温度計によって
排ガス温度を計測し、該排ガス温度が一定に保持される
帯域の温度と最大値を示す点の温度との中間にある排ガ
ス温度を予め指定値として定め、この温度指定値を与え
る機長方向長さを各幅方向位置において各々算出し、こ
れらを基準長とし、さらにこれらの各基準長の平均値を
求めて、各巾方向位置における基準長と基準長の平均値
との偏差を求め、これらの偏差が予め定めた値になるよ
うに巾方向の分割装入ゲートを調節して原料の巾方向装
入量を変えることを特徴とする焼結機の操業方法によっ
て解決する。
[Means for Solving the Problem] While moving the above-mentioned problem in the machine length direction and the horizontal direction,
In a method for operating a sintering machine, which has a burned zone in which a combustion zone moves from an upper surface to a lower surface and has means for passing air from an upper surface to a lower surface of the sintered zone, in a width direction of a lower surface of the sintered zone. And a plurality of exhaust gas thermometers arranged in the traveling direction are used to measure the exhaust gas temperature, and an exhaust gas temperature intermediate between the temperature of the zone in which the exhaust gas temperature is kept constant and the temperature at the maximum value is designated in advance. The length in the machine length direction that gives this temperature specified value is calculated at each position in the width direction, these are used as reference lengths, and the average value of these reference lengths is calculated to obtain the reference length at each position in the width direction. And the average value of the reference length are obtained, and the widthwise charging amount of the raw material is changed by adjusting the dividing charging gates in the width direction so that these deviations become predetermined values. Solve by the operation method of the conclusion.

[作用] 被焼結帯下面の巾方向および進行方向に複数個配設し
た排ガスの温度計によって排ガス温度を計測し、該排ガ
ス温度が一定に保持される帯域(以下初期低温帯域)の
温度と最大値を示す点(以下焼結終了点)の温度との中
間にある排ガス温度を予め指定値として予め定め、該温
度指定値を与える各巾方向位置の基準長を求め、それら
の基準長の平均値を求めて、各巾方向位置における基準
長と基準長の平均値との偏差を求め、この偏差が予め定
めた値になるように巾方向の分割装入ゲートを調節して
原料の巾方向装入量を変えるので、焼結終了点を越え被
焼結帯が放冷状態に入った位置を誤認することがない。
[Operation] The exhaust gas temperature is measured by a plurality of exhaust gas thermometers arranged in the width direction and the advancing direction of the lower surface of the zone to be sintered, and the temperature of a zone where the exhaust gas temperature is kept constant (hereinafter, initial low temperature zone) is measured. The exhaust gas temperature in the middle of the temperature at the point showing the maximum value (hereinafter referred to as the sintering end point) is set in advance as a specified value, the reference length of each width direction position that gives the specified temperature value is determined, and the reference length Obtain the average value, find the deviation between the reference length and the average value of the reference length at each position in the width direction, and adjust the widthwise divided charging gate so that this deviation becomes a predetermined value. Since the direction charging amount is changed, the position where the zone to be sintered enters the cooling state is not mistakenly recognized beyond the sintering end point.

[実施例] 第1図(a)は本発明の一実施例を示す説明図であ
る。ホッパー1により排出された原料2は装入ゲート
3、31、32、33、34によってその量を制御され、カット
オフゲート4によって、被焼結帯5の厚さが定められ
る。被焼結帯はパレットコンベアー(図示せず)によっ
て移送されるので、その厚さが一定の場合は、装入量を
変えるとその密度が変化して移送量が変化する。装入量
はレベルメーター6によって測定される。被焼結帯は点
火装置7によって、その上面において点火され、その水
平方向の進行とともに焼結帯は上面から下面に発達し、
排鉱前に下面に達して焼結が終了する。この間空気は被
焼結帯を通過し、排ガスとなって風箱に導入される。風
箱の総数は23個である。これらの風箱のうち、18番目、
20番目、22番目の風箱Q1(i=18,20,22)には、温度計
Si,j(i=は機長方向風箱の番号、jは巾方向風箱の番
号を表す;たとえばi=18,20,22,j=1,2,3,4,5)が配
されている。第1図(b)は第1図(a)のA−A矢視
図である。図に示すように装入ゲートおよび温度計は巾
方向に5個配されている。第1図において、温度計の情
報は演算器8に入力され、この情報に基づいて制御器9
は装入ゲートを調節する。これら温度計の指定値をXi,j
(i=18,20,22,j=1,2,3,4,5)とし、温度の機長方向
の分布を二次曲線で近似すると、温度Xi,jと機長方向長
さLjの関係は(1)式の様に表すことができる。
[Embodiment] FIG. 1A is an explanatory view showing an embodiment of the present invention. The amount of the raw material 2 discharged by the hopper 1 is controlled by the charging gates 3, 31, 32, 33, 34, and the thickness of the zone 5 to be sintered is determined by the cutoff gate 4. Since the zone to be sintered is transferred by a pallet conveyor (not shown), if the thickness is constant, if the charging amount is changed, the density changes and the transfer amount changes. The charging amount is measured by the level meter 6. The zone to be sintered is ignited on its upper surface by the igniter 7, and the horizontal zone advances the sintered zone from the upper surface to the lower surface.
Before the mine is mined, the bottom surface is reached and sintering is completed. During this time, the air passes through the zone to be sintered, becomes exhaust gas, and is introduced into the wind box. The total number of wind boxes is 23. The 18th of these wind boxes,
The 20th and 22nd wind box Q 1 (i = 18,20,22) has a thermometer
S i, j (i = represents the captain direction wind box number, j represents the width direction wind box number; for example, i = 18,20,22, j = 1,2,3,4,5) ing. FIG. 1 (b) is a view on arrow AA of FIG. 1 (a). As shown in the figure, five charging gates and thermometers are arranged in the width direction. In FIG. 1, the information of the thermometer is input to the calculator 8, and the controller 9 is based on this information.
Adjust charging gate. Specify the specified values of these thermometers as X i, j
(I = 18,20,22, j = 1,2,3,4,5) and the temperature distribution in the machine length direction is approximated by a quadratic curve, the temperature X i, j and the length L j in the machine length direction are The relationship can be expressed as in equation (1).

Lj=Aj・Xi,j 2+Bj・Xi,j+Cj …(1) ただし、Aj,Bj,Cjは定数である。すなわち、各分割巾
に対応する、この定数が温度計の位置と温度指示値によ
って求められる。したがって、(1)式に温度指定値を
与えると各分割巾ごとに機長方向長さが計算でき、これ
を基準長とする。この基準等を各巾ごとに制御するのが
本発明の要点である。長さの単位としては、風箱の機長
方向長さを用いた。すなわち、風箱18、20、22における
機長方向長さは、は箱風の単位長を1とすると、それぞ
れ、18、20、22である。
L j = A j · X i , j 2 + B j · X i, j + C j ... (1) However, A j, B j, C j is a constant. That is, this constant corresponding to each division width is obtained from the position of the thermometer and the temperature indication value. Therefore, when the temperature designated value is given to the equation (1), the length in the machine length direction can be calculated for each division width, and this is used as the reference length. It is an essential point of the present invention to control this standard and the like for each width. As the unit of length, the length of the wind box in the machine length direction was used. That is, the lengths in the machine length direction of the wind boxes 18, 20, and 22 are 18, 20, and 22, respectively, when the unit length of the box wind is 1.

第1表はこのようにして求めた各分割巾に対応する基
準長である。この場合、温度の指定値は250℃である。
表において、各分割巾に対応する基準長を(1)式から
求め、その平均値からの偏差が得られる。制御の方針と
して、この偏差を零にするものであれば、零から各偏差
を差し引いたものが演算器より制御器に入力され、制御
器は装入ゲートを調節する。
Table 1 shows reference lengths corresponding to the respective division widths thus obtained. In this case, the specified temperature is 250 ° C.
In the table, the reference length corresponding to each division width is obtained from the equation (1), and the deviation from the average value is obtained. As a control policy, if this deviation is set to zero, a value obtained by subtracting each deviation from zero is input to the controller from the arithmetic unit, and the controller adjusts the charging gate.

第2表は、第1表における制御の効果を示すもので、
従来法に較べて本発明法においては、生産能率が向上
し、しかも焼結鉱の回転強度(JISM8712)、焼成歩留ま
り、において大差が無い。
Table 2 shows the effects of the control in Table 1,
In the method of the present invention, the production efficiency is improved as compared with the conventional method, and there is no great difference in the rotational strength (JIS M8712) of the sintered ore and the firing yield.

第3表は制御の方針として、排ガスからの熱回収を重
視した場合の制御目標値を表のように定めた場合で、こ
の値から基準長の巾方向偏差を差し引いたものが演算器
より制御器に入力され、それによって制御器は装入巾方
向の制御目標値を第3表のようにすれば、被焼結層の焼
成による収縮でサイドウオールと焼成層の間に隙間が生
じる巾方向両端部での焼結完了点位置を後方へ移動で
き、冷風の吸込み量を抑制できるので、排ガスの温度を
高温にすることができる。
Table 3 shows the case where the control target value when heat recovery from exhaust gas is prioritized is set as shown in the table as a control policy, and the value obtained by subtracting the widthwise deviation of the reference length from this value is controlled by the calculator. If the control target value in the charging width direction is set as shown in Table 3 by the controller, the shrinkage due to firing of the layer to be sintered causes a gap between the side wall and the firing layer in the width direction. Since the positions of the sintering completion points at both ends can be moved backward and the amount of sucked in cold air can be suppressed, the temperature of the exhaust gas can be raised to a high temperature.

第4表は、第3表における制御の効果を示すもので、
従来法に較べて、本発明法においては、排ガスの熱回収
によって発生した蒸気の回収量が向上している。
Table 4 shows the effects of the control in Table 3,
Compared with the conventional method, in the method of the present invention, the recovery amount of steam generated by heat recovery of exhaust gas is improved.

以上のように、本発明においては、制御の方針によっ
て巾方向の基準長の分布を変更することが可能である。
As described above, in the present invention, the distribution of the reference length in the width direction can be changed according to the control policy.

[発明の効果] 以上のように、本発明においては、巾方向の基準長分
布を制御することにより、焼結機の能率が向上し、品質
が確保され、熱回収が効率良く行われる効果がある。
[Effect of the Invention] As described above, in the present invention, by controlling the reference length distribution in the width direction, the efficiency of the sintering machine is improved, the quality is ensured, and the heat recovery is efficiently performed. is there.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の一実施例を示す説明図、第2図は排ガ
ス温度の機長方向分布のパターンを示すグラフ図、第3
図は巾方向中央部の温度パターンqと巾方向端部の温度
パターンrを示すグラフ図である。 1……ホッパー、2……原料、3、31、32、33、34……
装入ゲート、4……カットオフゲート、5……被焼結
帯、6……レベルメーター、7……点火装置、8……演
算器、9……制御器、Si,j(i=18,20,22,j=1,2,3,4,
5)……温度計、Qi(i=18,20,22)……風箱。
FIG. 1 is an explanatory view showing an embodiment of the present invention, FIG. 2 is a graph showing a pattern of exhaust gas temperature distribution in the machine length direction, and FIG.
The figure is a graph showing a temperature pattern q at the center in the width direction and a temperature pattern r at the ends in the width direction. 1 ... Hopper, 2 ... Raw material, 3, 31, 32, 33, 34 ...
Charge gate, 4 ... Cut-off gate, 5 ... Sintered zone, 6 ... Level meter, 7 ... Ignition device, 8 ... Computing unit, 9 ... Controller, S i, j (i = 18,20,22, j = 1,2,3,4,
5) ... thermometer, Q i (i = 18, 20, 22) ... wind box.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 福与 寛 東京都千代田区丸の内1丁目1番2号 日 本鋼管株式会社内 (72)発明者 和田 隆 東京都千代田区丸の内1丁目1番2号 日 本鋼管株式会社内 審査官 中村 朝幸 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Hiroshi Fukuyo 1-2-1 Marunouchi, Chiyoda-ku, Tokyo Nihon Kokan Co., Ltd. (72) Takashi Wada 1-2-1 Marunouchi, Chiyoda-ku, Tokyo Asahi Nakamura Examiner, Nihon Kokan Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】機長方向かつ水平方向に移動しながら、上
面より下面に燃焼帯が移動する被焼結帯を有し、かつ該
被焼結帯の上面から下面に空気を通風する手段を有する
焼結機の操業方法において、被焼結帯下面の巾方向およ
び進行方向に複数個配設した排ガスの温度計によって排
ガス温度を計測し、該排ガス温度が一定に保持される帯
域の温度と最大値を示す点の温度との中間にある排ガス
温度を予め指定値として定め、該温度指定値を与える機
長方向長さを各幅方向位置において各々算出し、これら
を基準長とし、さらに該各基準長の平均値を求めて、各
巾方向位置における基準長と基準長の平均値との偏差を
求め、該偏差が予め定めた値になるように巾方向の分割
装入ゲートを調節して原料の巾方向装入量を変えること
を特徴とする焼結機の操業方法。
1. A sintered zone in which a combustion zone moves from an upper surface to a lower surface while moving in the machine direction and a horizontal direction, and means for ventilating air from the upper surface to the lower surface of the sintered zone. In the operating method of the sintering machine, the exhaust gas temperature is measured by a plurality of exhaust gas thermometers arranged in the width direction and the traveling direction of the lower surface of the zone to be sintered, and the temperature of the zone where the exhaust gas temperature is kept constant and the maximum The exhaust gas temperature in the middle of the temperature at the point indicating the value is set in advance as a specified value, and the length in the machine length direction that gives the specified temperature value is calculated at each position in the width direction. Obtain the average value of the lengths, find the deviation between the reference length at each position in the width direction and the average value of the reference lengths, and adjust the widthwise divided charging gate so that the deviation becomes a predetermined value. Sintering characterized by changing the widthwise charging amount of The method of operation.
JP1089390A 1990-01-19 1990-01-19 Operating method of sintering machine Expired - Fee Related JPH089740B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1089390A JPH089740B2 (en) 1990-01-19 1990-01-19 Operating method of sintering machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1089390A JPH089740B2 (en) 1990-01-19 1990-01-19 Operating method of sintering machine

Publications (2)

Publication Number Publication Date
JPH03215630A JPH03215630A (en) 1991-09-20
JPH089740B2 true JPH089740B2 (en) 1996-01-31

Family

ID=11762995

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1089390A Expired - Fee Related JPH089740B2 (en) 1990-01-19 1990-01-19 Operating method of sintering machine

Country Status (1)

Country Link
JP (1) JPH089740B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006206972A (en) * 2005-01-28 2006-08-10 Jfe Steel Kk Method for controlling divided gate in sintering machine and method for producing sintered ore
JP5103820B2 (en) * 2006-08-08 2012-12-19 Jfeスチール株式会社 Method for producing sintered ore
JP5640876B2 (en) * 2011-04-13 2014-12-17 新日鐵住金株式会社 Method for monitoring sinter quality fluctuation in sinter production and method for producing sinter using the monitoring method

Also Published As

Publication number Publication date
JPH03215630A (en) 1991-09-20

Similar Documents

Publication Publication Date Title
US4389242A (en) Interior arrangement for direct reduction rotary kilns and method
JP5103820B2 (en) Method for producing sintered ore
JPH089740B2 (en) Operating method of sintering machine
US2441383A (en) Sintering apparatus
JPH0774397B2 (en) Method for controlling air permeability of sintering raw material layer
JPH055589A (en) Operating method for sintering machine
JP7568174B1 (en) Sintered ore manufacturing apparatus, sintered ore manufacturing method, and program
JPH07180972A (en) Method for operating sintering machine
JPH05195091A (en) Manufacture of sintered ore
JP3297796B2 (en) Operating method of sintering machine
US3265377A (en) Method of and apparatus for regulating the speed of sintering strands
JPH0499135A (en) Method for controlling sintering of calcined lump ore
JPS63183133A (en) Method for controlling sintering point in sintering machine and said sintering machine
JPH03211241A (en) Operating method for sintering machine
JPH01191751A (en) Operating method of sintering machine
JPH0949031A (en) Operation of sintering machine
JP2005350742A (en) Method for manufacturing sintered ore
JPH0288724A (en) Method for operating sintering machine
JPS6017007B2 (en) Method for detecting firing completion point in DL type sintering machine
SU1014944A1 (en) Method for roasting iron ore pellets
JPS6334213B2 (en)
JPS60194024A (en) Production of sintered ore
JPH02301525A (en) Method for charging raw material into sintering machine
KR20030055021A (en) Apparatus for manufacturing the sintered ore
JPH0873951A (en) Production of sintered ore

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees