JPS6013032A - Method for controlling calcination point with sintering machine - Google Patents

Method for controlling calcination point with sintering machine

Info

Publication number
JPS6013032A
JPS6013032A JP12044383A JP12044383A JPS6013032A JP S6013032 A JPS6013032 A JP S6013032A JP 12044383 A JP12044383 A JP 12044383A JP 12044383 A JP12044383 A JP 12044383A JP S6013032 A JPS6013032 A JP S6013032A
Authority
JP
Japan
Prior art keywords
calcination
point
raw material
sintering machine
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
JP12044383A
Other languages
Japanese (ja)
Inventor
Masanari Hamada
浜田 勝成
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 JP12044383A priority Critical patent/JPS6013032A/en
Publication of JPS6013032A publication Critical patent/JPS6013032A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To control adequately the calcination point of a sintering machine in the stage of producing sintered ore with a DL type sintering machine by detecting the calcination point by each transverse direction from the transition of the waste wind temp. of the wind box in the advancing direction of the sintering raw material, calculating the average calcination point in the transverse direction and regulating pallet speed until the target value thereof is attained. CONSTITUTION:A sintering raw material 17 is fed out on the grate 1 of the pallet of a DL type sintering machine from a hopper 2 to form a raw material layer 18. The layer 18 is ignited by an ignition furnace 5 and as the layer advances toward the right, combustion front lines 13-1, 13-2 descend and the layer arrives at the grate 1 at calcination points 14-1, 14-2. The above-mentioned calcination points are detected and the average calcination distance in the transverse direction is calculated by a calculator 25 and is inputted to a control device 26 for the calcination point which determines the set speed of a pallet speed from the pallet speed inputted from a device 27 for detecting and adjusting the pallet speed and the target value of the calcination distance inputted from a manual setter 28 and commands the device 27 to control adequate the calcination points.

Description

【発明の詳細な説明】 この発明は、DL式焼結機における原料充填層の巾方向
平均の焼成点の制御方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the average firing point in the width direction of a raw material packed bed in a DL type sintering machine.

焼結操業において、基本的な操業指標である焼成点の制
御は、焼結操業の安定化をはかる上で重要である。この
焼成点の制御方法としては、焼結機の巾方向平均の排風
温度推移から、その立上り点を焼成点として検出し、該
検出値に基づいて巾方向平均の焼成点を制御するという
方法がとられている。すなわち、従来は巾方向平均の排
風温度推移から検出した焼成点に基づいて、焼成点を制
御している。しかし、このような方法では、巾方向に焼
むらがある場合焼成点を誤検出し、焼成点制御の制御性
を悪くするという欠点がある。
In sintering operations, controlling the firing point, which is a basic operating index, is important for stabilizing sintering operations. The method for controlling this firing point is to detect the rising point as the firing point from the average exhaust air temperature change in the width direction of the sintering machine, and to control the average firing point in the width direction based on the detected value. is taken. That is, conventionally, the firing point is controlled based on the firing point detected from the widthwise average exhaust air temperature transition. However, such a method has the disadvantage that if there is uneven baking in the width direction, the baking point may be detected incorrectly, resulting in poor controllability of baking point control.

すなわち、排風温度を巾方向で検出した後の機長方向温
度推移からその立上り点を焼成点として検出する方法で
は、第1図に示すごと<[IJ力方向焼むらがある場合
、その立上り点は燃焼前線が最も早くグレードに到達し
た部分の位置となり、巾方向の平均値とならないため、
制御の安定性は良好と言い難い。
In other words, in the method of detecting the exhaust air temperature in the width direction and then detecting the rising point as the firing point from the temperature transition in the machine length direction, as shown in Fig. 1, if there is uneven firing in the IJ force direction, the rising point is the position of the part where the combustion front reached the grade earliest, and is not the average value in the width direction, so
It is difficult to say that the control stability is good.

この発明は、従来の前記問題を解決するためになされた
ものであって、その要旨は、原料の移動に従い巾方向別
に測定された各風箱の排風温度推移により、巾方向別に
焼成点を検出し、該検出値より巾方向平均焼成点を算出
し、該算出値が所定の目標値となるよう、パレット速度
を調整することを特徴とする焼結操業方法にある。
This invention was made in order to solve the above-mentioned conventional problems, and its gist is to determine the firing point in each width direction based on the change in exhaust air temperature of each wind box measured in each width direction as the raw material moves. The sintering operation method is characterized by detecting the firing point, calculating the average firing point in the width direction from the detected value, and adjusting the pallet speed so that the calculated value becomes a predetermined target value.

すなわち、この発明は、各風箱の排風温度推移からその
立上り点を焼成点として巾方向別に検出し、ついで巾方
向別に検出したいくつかの焼成点を加算平均し、その値
を巾方向平均焼成点とすることにより、巾方向に焼むら
がある場合の焼成点の誤検出を防止する方法である。
That is, in this invention, the rising point of each wind box is detected as a firing point from the change in exhaust air temperature for each width direction, and then several firing points detected for each width direction are added and averaged, and the values are averaged in the width direction. This method prevents erroneous detection of the firing point when there is uneven firing in the width direction by setting the firing point as the firing point.

以下、この発明に係る焼成点制御法を第2図に基づいて
説明する。
Hereinafter, the firing point control method according to the present invention will be explained based on FIG. 2.

第2図はDL式焼結機における焼成点と各風箱の排風温
度との関係を示す説明図であり、原料装入かさ高計(4
)の測定値が所定の値となるように、サージホッパー(
2)からロールフィーダ(3)によって連続的に給鉱さ
れた原料0ηは、パレットのグレード+1j上に充填層
幀を形成しながらパレットの移動によって排鉱部へ搬送
され、この間に点火炉(5)で充填層(18Nの表面に
点火される。一方、各風箱(8)は燃焼ガスを主排風機
flo)により強制的に充填層0!9の下方から吸引し
ている。この吸引力は主排風管(9)に設けられている
ダンパー(lI)の開度により調整する。排風温度は各
風箱(8)に設けられた熱電対(I匂によって測定され
ているが、燃焼前線α3−1) (13−2)がグレー
ド(1)に到達するまでは、排風温度はほぼ一定であり
、グレード到達位置すなわち焼成点(14−1) (1
4−2) と相前後して排風温度は上昇し始める。
Figure 2 is an explanatory diagram showing the relationship between the firing point and the exhaust air temperature of each wind box in a DL type sintering machine.
) so that the measured value of the surge hopper (
The raw material 0η continuously fed from 2) by the roll feeder (3) is transported to the ore discharge section by the movement of the pallet while forming a packed bed on grade +1j of the pallet. ), the surface of the packed bed (18N) is ignited. On the other hand, each wind box (8) forcibly sucks the combustion gas from below the packed bed 0 to 9 by the main exhaust fan flo. This suction force is adjusted by the opening degree of a damper (lI) provided in the main exhaust pipe (9). The exhaust air temperature is measured by a thermocouple (I) installed in each wind box (8), but the exhaust air temperature is measured until the combustion front α3-1 (13-2) reaches grade (1). The temperature is almost constant, and the grade reaching position, that is, the firing point (14-1) (1
4-2) The exhaust air temperature begins to rise around the same time.

すなわち、原料の移動に従い巾方向別に測定された各風
箱の排風温度推移(15−1) (15−2)によって
その立上り点(16−1) (16−2)を巾方向それ
ぞれの部分における焼成点とみなすことができる。これ
により、巾方向平均の焼成点距離(点火炉から焼成点ま
での距離)は、下記(1)式によりめられる。なお、(
I)式の右辺第2項は巾方向の排風温度測定を2点しか
測定していないことにより生じる誤差を補正する項であ
る。
In other words, the rise points (16-1) (16-2) are calculated for each width direction by the exhaust air temperature transition (15-1) (15-2) of each wind box measured in each width direction as the raw material moves. It can be regarded as the firing point at As a result, the average firing point distance in the width direction (distance from the ignition furnace to the firing point) can be determined by the following equation (1). In addition,(
The second term on the right side of equation I) is a term that corrects the error caused by measuring the exhaust air temperature in the width direction at only two points.

・・・・・・(I) ただし、 l rrp は巾方向平均の焼成側lIF、
(−)、NFrP+ e 1rFPHはそれぞれ排風温
度推移(15−t)(15−2)により検出された焼成
点からめ゛た焼成距離(N)、αは補正係数(−)であ
る。
・・・・・・(I) However, l rrp is the firing side lIF averaged in the width direction,
(-) and NFrP+ e 1rFPH are the firing distances (N) from the firing point detected by the exhaust air temperature transition (15-t) and (15-2), respectively, and α is the correction coefficient (-).

よって、焼成点を制御するために目標の焼成距離が与え
られると、パレット速度設定値は例えば下記(1)式の
ごとく与えられ、調整される。
Therefore, when a target firing distance is given to control the firing point, the pallet speed setting value is given and adjusted as shown in equation (1) below, for example.

ただし、Pμ3.P8 はそれぞれパレット速度の設定
値と測定値(m/m1n)、1hvp は焼成距離目標
値(m)、tは時間(min)、TI は積分時開(m
in)である。
However, Pμ3. P8 is the set value and measured value of pallet speed (m/m1n), 1hvp is the firing distance target value (m), t is the time (min), and TI is the opening during integration (m/m1n).
in).

次に、この発明の一実施例を第3図に基づいて説明する
Next, one embodiment of the present invention will be described based on FIG.

各原料槽(イ))から切出された焼結原料は、まずメリ
ック(21)により全体の切出し社が計測され、ミキサ
レタで水分が添加混和されてサージポツパー(2)へ投
入される。サージホッパー(2)内の原料07)は、該
ホッパー内に設置された水分針(至)により原料中水分
が測定された後、装入かさ高計(4)の計測値が所定の
値となるようロールフィーダ(3)により切出され、給
鉱シュートHを介してパレットのグレードftl上に連
続的に給鉱される。グレード0)上に給鉱された原料は
、充填層α樽を形成しながらパレットの移動によって排
鉱部へ搬送される。充填IQ8)の層厚は所定値になる
よう、給鉱シュート(24)の角度、高さが調整される
。充填層0綽は点火炉(6)で表面に点火さ、れ、排鉱
部へ搬送されるに従い各風箱(8)に設けられた熱電対
(I2)により排風温度が測定される。
The sintered raw material cut out from each raw material tank (a) is first measured by a merrick (21), water is added and mixed in a mixer, and the sintered raw material is fed into a surge potper (2). After the moisture content of the raw material 07) in the surge hopper (2) is measured by the moisture needle (to) installed in the hopper, the measured value of the charging bulk meter (4) is determined to be a predetermined value. The ore is cut out by the roll feeder (3) so that the ore becomes the same, and is continuously fed onto the pallet grade ftl via the ore feed chute H. The raw material fed onto the grade 0) is transported to the ore discharge section by moving pallets while forming packed bed α barrels. The angle and height of the ore feeding chute (24) are adjusted so that the layer thickness of the filling IQ8) becomes a predetermined value. The surface of the packed bed is ignited in an ignition furnace (6), and as it is transported to the ore discharge section, the exhaust air temperature is measured by a thermocouple (I2) provided in each wind box (8).

そして、各風箱の排風温度推移により、燃焼前線(13
−1)(13−2) のグレード到達位置、すなわち焼
成点(14−1) (14−2)が検出され、焼成距離
演算装置(至)により前記(1)式の演算を行ない、そ
の結果を焼成点制御装置E6)に出力する。焼成点制御
装置−は、焼成点演算装置(2四より入力したl]方向
平均の焼成距離と、パレット速度検出・調節装置いηか
ら入力したパレット速度と、手動設定器(ハ)より入力
した焼成距離目標値とから、前記(1)式によりパレッ
ト速度設定値をめ、これをパレット速度検出・調節装置
しηへ指令し、パレット速度を調節する。
The combustion front (13
-1) (13-2), that is, the firing points (14-1) (14-2) are detected, and the firing distance calculation device (to) calculates the above formula (1), and the result is is output to the firing point control device E6). The firing point control device uses the average firing distance in the direction L input from the firing point calculation device (24), the pallet speed input from the pallet speed detection/adjustment device η, and the input from the manual setting device (c). The pallet speed setting value is determined from the firing distance target value using the above equation (1), and this is sent to the pallet speed detection/adjustment device to be commanded to η to adjust the pallet speed.

この発明は上記のごとく、原料の進行に従い測定され1
こ各風箱の排風湿度推移より巾方向別に焼成点を検出し
、この巾方向別に検出した焼成点より巾方向平均の焼成
点を算出し、該算出値が所定の目標値となるよう、パL
ノット速度を調整して焼成点を制御する方法であるから
、巾方向に焼きむらがある温合でも焼成点を的確に検出
して安定制御することができ、焼結操業の安定化に多大
なる効果を発揮するものである。
As mentioned above, this invention measures according to the progress of the raw material.
The firing point is detected in each width direction from the change in exhaust air humidity of each wind box, and the average firing point in the width direction is calculated from the firing points detected in each width direction, so that the calculated value becomes a predetermined target value. Pa L
Since this method controls the firing point by adjusting the knot speed, it is possible to accurately detect and stably control the firing point even when heating is uneven in the width direction, which greatly contributes to stabilizing the sintering operation. It is effective.

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

第1図は従来の焼成点検出方法を示す説明図、第2図は
この発明に係るDL式焼結機の焼成点と各風箱の関係を
示す説明図、第3図はこの発明の一実施例における填成
点制御方法を示す説明図である。 1・・・グレード、2・・・サージホッパー、3・・・
ロールフィーダ、4・・・装入かさ高畦、5・・・点火
炉、8・・・風箱、9・・・主排風管、10・・主排風
機、12・・・熱電対、13−1.13−2・・・燃焼
前線、14−1゜14−2・・・焼成点、15−]、、
 15−2・・・各風箱の排風温度推移、−16−1,
16−2・・・立上り点、17・・・原料、18・・・
充填層、20・・・原料槽、25・・・焼成距離演算装
置、26・・・焼成点制御装置、27・・・パレット速
度検出・調節装置、28・・・手動設定器。 出願人 住友金属工業株式会社 代理人 押 1) 良 久しゲ↓j::1’i□ !
FIG. 1 is an explanatory diagram showing a conventional firing point detection method, FIG. 2 is an explanatory diagram showing the relationship between the firing point and each wind box of the DL type sintering machine according to the present invention, and FIG. It is an explanatory view showing a filling point control method in an example. 1...Grade, 2...Surge hopper, 3...
Roll feeder, 4... Charging height ridge, 5... Ignition furnace, 8... Wind box, 9... Main exhaust pipe, 10... Main exhaust fan, 12... Thermocouple, 13 -1.13-2... Combustion front, 14-1°14-2... Firing point, 15-],
15-2...Change in exhaust air temperature of each wind box, -16-1,
16-2...Rise point, 17...Raw material, 18...
Filled bed, 20... Raw material tank, 25... Firing distance calculation device, 26... Firing point control device, 27... Pallet speed detection/adjustment device, 28... Manual setting device. Applicant Sumitomo Metal Industries Co., Ltd. Agent Press 1) Good for a long time↓j::1'i□!

Claims (1)

【特許請求の範囲】[Claims] 各風箱に排風温度測定装置を備えた焼結機において、原
料の移動に従い巾方向別に測定された各風箱の排風温度
推移により、巾方向別に焼成点を検出し、該検出値より
巾方向平均焼成点を算出し、該算出値が所定の目標値と
なるよう、パレット速度を調整することを特徴とする焼
結機における焼成点制御法。
In a sintering machine equipped with an exhaust air temperature measuring device in each wind box, the firing point is detected in each width direction based on the change in the exhaust air temperature of each wind box measured in each width direction as the raw material moves, and based on the detected value. A method for controlling a firing point in a sintering machine, comprising calculating a widthwise average firing point and adjusting a pallet speed so that the calculated value becomes a predetermined target value.
JP12044383A 1983-07-01 1983-07-01 Method for controlling calcination point with sintering machine Pending JPS6013032A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12044383A JPS6013032A (en) 1983-07-01 1983-07-01 Method for controlling calcination point with sintering machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12044383A JPS6013032A (en) 1983-07-01 1983-07-01 Method for controlling calcination point with sintering machine

Publications (1)

Publication Number Publication Date
JPS6013032A true JPS6013032A (en) 1985-01-23

Family

ID=14786328

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12044383A Pending JPS6013032A (en) 1983-07-01 1983-07-01 Method for controlling calcination point with sintering machine

Country Status (1)

Country Link
JP (1) JPS6013032A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03211241A (en) * 1990-01-17 1991-09-17 Nkk Corp Operating method for sintering machine

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03211241A (en) * 1990-01-17 1991-09-17 Nkk Corp Operating method for sintering machine

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