JPS58171533A - Operating method for sintering device - Google Patents

Operating method for sintering device

Info

Publication number
JPS58171533A
JPS58171533A JP5409082A JP5409082A JPS58171533A JP S58171533 A JPS58171533 A JP S58171533A JP 5409082 A JP5409082 A JP 5409082A JP 5409082 A JP5409082 A JP 5409082A JP S58171533 A JPS58171533 A JP S58171533A
Authority
JP
Japan
Prior art keywords
sintering
layer
heat insulating
raw material
index
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
JP5409082A
Other languages
Japanese (ja)
Inventor
Yasushi Tomisaka
富阪 泰
Yosuke Sawada
澤田 羊助
Sakae Ito
榮 伊藤
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP5409082A priority Critical patent/JPS58171533A/en
Publication of JPS58171533A publication Critical patent/JPS58171533A/en
Pending legal-status Critical Current

Links

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To obtain sintered ore having less variation in quality, by regulating the flow of wind according to the value calculated in accordance with the heat insulating index at the respective points in a sintering raw material layer and controlling the heat insulating index within a specified layer. CONSTITUTION:Sintering raw material layer 8 is formed in upper pallets 7 moving toward an ore discharge part by the bedding supplied from a bedding layer hopper 5 and the raw material sintering ore supplied from a raw material hopper 6. The layers 8 are ignited in a sintering part and upon completion of the sintering, the sintered material is discharged from an ore discharge part. During this time, air is sucked 10 and supplied through the wind boxes 9 disposed below the pallet 7 and the temp. is detected with temp. sensor 11 in a number of places inserted and disposed in the layer 8, then the signal thereof is oscillated. The signal is received 12, and the heat insulating index from the heat pattern of the layer 8 and the deviation between the heat insulating index and a set range of the heat insulating index is calculated by a calculator 13 for heat insulating index. The opening of the respective dampers 15 disposed in the box 9 is changed by a control device 14 for damper opening according to the calculated deviations to control the suction negative pressures in the lower part of the layer 8, whereby the heat insulating index is protected approximately constant.

Description

【発明の詳細な説明】 本発明は、層内各点での保熱指数にもとづいて算出した
値により風量を調整し、保熱指数を特定値に制御する焼
結装置の運転方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method of operating a sintering apparatus in which the air volume is adjusted based on a value calculated based on the heat retention index at each point within a layer, and the heat retention index is controlled to a specific value.

現在、鉱石の焼結は、ドワイトロイド式、グリナワルト
式などの焼結装置を用い粉鉄の塊状化法として広く工業
的に採用されている。
Currently, sintering of ore is widely used industrially as a method of agglomerating powdered iron using sintering equipment such as the Dwight Lloyd type or the Greenawalt type.

しかしながら、これら従来の焼結装置を用いて焼結を行
なった場合、焼結層の上層部(0〜150朋)において
は焼結鉱の品質が著しく悪く、上下層間の歩留に大きな
ムラがある。このような品質上のムラが生じるのは、吸
引負圧一定力式により鉱石の層内を通過する風量が調整
されており、上層部燃焼時には吸入空気による冷却のた
め熱量不足となって充分な焼結が行なわれないことによ
ると考えられる。
However, when sintering is performed using these conventional sintering devices, the quality of the sintered ore is extremely poor in the upper layer (0 to 150 mm) of the sintered layer, and the yield between the upper and lower layers is greatly uneven. be. The reason for this unevenness in quality is that the amount of air passing through the ore layer is adjusted using a constant suction negative pressure system, and when the upper layer is burned, the amount of heat is insufficient due to the cooling caused by the intake air. This is thought to be due to the fact that sintering is not performed.

ここで従来の吸引負圧一定力式による風量制御方法によ
り第1図に示す鍋試験装置を用いて焼結を行なった場合
の排ガス量および焼結原料層内温度を第2図に示す。鍋
試験に用いた装置は第1図に示すごとく、原料層(1)
410朋と床敷層(2) 40朋を有し、層上面よりT
□100間、T220o朋、T3300順、T4385
龍およびTa205朋の層内各点ならびに層上面より4
307f1mの1嫂床敷層内の地点に温度測定点が設け
られる。
FIG. 2 shows the amount of exhaust gas and the temperature in the sintering raw material bed when sintering was carried out using the ladle testing apparatus shown in FIG. The equipment used for the pot test is as shown in Figure 1, with the raw material layer (1)
410 mm and bedding layer (2) It has 40 mm and T from the top surface of the layer.
□100, T220o, T3300, T4385
4 from each point in the layer of Ryu and Ta205 and the top surface of the layer
Temperature measurement points are provided at points within the first bedding layer of 307 f1m.

第2図より明らかに、各測定点における最高温度はほぼ
同じであるがf層となるほど高温保持時間が長くなり、
一方風量は焼結後半まで徐々に減少しつづけ終了時に急
増する。
It is clear from Figure 2 that the maximum temperature at each measurement point is almost the same, but the higher the f layer, the longer the high temperature retention time.
On the other hand, the air flow rate continues to gradually decrease until the latter half of sintering, and increases rapidly at the end of sintering.

本発明者らは、前記知見にもとづき鋭意検討を行なった
結果、焼結原料層へ供給する風量を調整することにより
保熱指数が一定範囲内に制御されて品質ムラの少ない焼
結鉱が得られ、あわせて生産率を向上させうろことを見
出し本発明を完成すすなわち本発明は、焼結原料に送風
しつつ焼結/\ を行なう制御系において、層内上下各地点の温度をT(
0、該地点が1000℃を越えた時刻および1000℃
まで下降した時刻をそれぞれ麹、t2(m1n)、保熱
指数Q (”C・m1n)をとしたとき、焼結原料へ供
給する風量の調整を行なうことにより前記保熱指数Qの
値を300〜700℃・minに制御する焼結装置の運
転方法を提供するものである。
As a result of intensive studies based on the above knowledge, the present inventors have found that by adjusting the air flow rate supplied to the sintered raw material layer, the heat retention index can be controlled within a certain range and sintered ore with less uneven quality can be obtained. At the same time, they found a way to improve the production rate and completed the present invention.In other words, the present invention is based on a control system that performs sintering while blowing air to the sintering raw material.
0, Time when the point exceeded 1000℃ and 1000℃
When the time when the temperature drops to 100% is taken as koji, t2 (m1n), and heat retention index Q ("C・m1n), respectively, by adjusting the air volume supplied to the sintering raw material, the value of the heat retention index Q can be set to 300. The present invention provides a method for operating a sintering apparatus that controls the temperature at ~700°C/min.

と交わる点を時刻t1、t2(min)とした場合、〔
ただし、Tはヒートパターン各点の温度〕で定義される
もので、Qは温度1000°C以上での温度の時間積分
値となり、第3図における斜線部(4)の面積となる。
If the points that intersect with are times t1 and t2 (min), then [
However, T is defined as the temperature at each point in the heat pattern], and Q is the time integral value of the temperature at a temperature of 1000° C. or higher, and is the area of the shaded portion (4) in FIG. 3.

Qが300°O−minより小さいと焼結は充分でなく
、歩留(10市篩オン品)が低下し、一方Qが700″
C−m1nを越えると焼結が過剰であって、もはや歩留
、品質の向上がみられない。
If Q is less than 300°O-min, sintering will not be sufficient and the yield (10-sieve-on product) will decrease;
When C-m1n is exceeded, sintering is excessive and no improvement in yield or quality can be seen.

本発明方法によれば、保熱指数の因子である高熱保持時
間が風量によって制御され、保熱指数が一定範囲に保た
れる結果、品質ムラがなく生産歓の向上をはかりうる。
According to the method of the present invention, the high heat retention time, which is a factor of the heat retention index, is controlled by the air flow rate, and the heat retention index is maintained within a certain range, resulting in uniform quality and improved production.

、つぎに図面により本発明方法をさらに詳しく説明する
。第4図は本発明方法を実施するドワイトロイド式焼結
機の概略図である。床敷層ホラ”(5)より供給された
床敷およびついで原料ホラ”(6)より供給された原料
焼結鉱は、排鉱部(図中右方)に向は移動、する上方の
パレット(7)に焼結原料層(8)を形成する。焼結原
料層は給鉱部(図中左方)にて点火が行なわれ、焼結が
完了すると排鉱部より排出される。パレット(7)の下
方にはウィンドボックス(9)が配設され、吸引負圧一
定式の2基のプロワ(10)により吸引を行なってパレ
ット(7)上の原料焼結鉱層に空気を供給する。パレッ
ト(7)には上下に数ケ所(例えば5ケ所)焼結鉱層中
に挿入した温度センサ(11亦配設され、該センサ(1
1)に付設された発信器(図示せず)により検知された
温度信号が発信される。該センサ(1)からの信号は固
定された受信器(12)により受信され、保熱指数算出
装置(13)によって該信号に基づいて得た焼結原料層
各層のヒτドパターンから保熱指数および該保熱指数と
設定保熱指数範囲との偏差が算出され、該偏差に基づき
ダンパー開度制御装置(14)によりウィンドボックス
(9)に配設された各ダンパ(15)の開度が・、変更
され原料層下部の吸引負圧が調節される。
Next, the method of the present invention will be explained in more detail with reference to the drawings. FIG. 4 is a schematic diagram of a Dwight Lloyd sintering machine implementing the method of the present invention. The bedding supplied from the bedding layer conch (5) and the raw material sintered ore supplied from the raw material conduit (6) are moved toward the ore discharge section (right side in the figure), and are transported to the upper pallet. A sintering raw material layer (8) is formed on (7). The sintering raw material layer is ignited in the ore supply section (left side in the figure), and when sintering is completed, it is discharged from the ore discharge section. A wind box (9) is installed below the pallet (7), and two blowers (10) with constant suction negative pressure perform suction to supply air to the raw material sintered ore layer on the pallet (7). do. The pallet (7) is provided with temperature sensors (11) inserted into the sintered ore layer at several locations (for example, 5 locations) on the top and bottom.
A detected temperature signal is transmitted by a transmitter (not shown) attached to 1). The signal from the sensor (1) is received by a fixed receiver (12), and the heat retention index calculation device (13) calculates the heat retention from the hidden pattern of each layer of the sintered raw material layer obtained based on the signal. The index and the deviation between the heat retention index and the set heat retention index range are calculated, and based on the deviation, the damper opening control device (14) controls the opening of each damper (15) disposed in the wind box (9). is changed and the suction negative pressure at the bottom of the raw material layer is adjusted.

なお、プロワ−は−基としてもよいが、本具体例のごと
く焼結前半用(低吸引負圧用)と後半用(高吸引負圧用
)の二基とすれば操業範囲が広くなり、一層保熱指数の
管理が容易となる。さらにプロワ−を三基以上とするこ
とも可能である。本発明方法においては各ウィンドボッ
クスに設置したダンパ′−の開度を調整することによっ
て風量の制御が行なわれるので総風量は常に一定である
Note that the blower may be a two-base blower, but as in this example, if there are two blowers, one for the first half of sintering (for low suction and negative pressure) and one for the second half (for high suction and negative pressure), the operating range will be wider and the maintenance will be further improved. It becomes easier to manage the heat index. Furthermore, it is also possible to use three or more blowers. In the method of the present invention, the air volume is controlled by adjusting the opening degree of the damper installed in each wind box, so the total air volume is always constant.

なお、ダンパー開度制御は手動によってもよぐこの場合
は予め各ウィンドボックス風量と保熱指数との関係を得
ておき、保熱指数算出装置により得られた保熱指数に基
づき最適保熱指数を示すよう手動でダンパー開度を調節
し風量を調整する。
In addition, the damper opening degree can also be controlled manually. In this case, the relationship between the air volume of each wind box and the heat retention index is obtained in advance, and the optimum heat retention index is calculated based on the heat retention index obtained by the heat retention index calculation device. Adjust the air volume by manually adjusting the damper opening as indicated.

しかして本発明方法によれば、第5図および6図に示す
ごとく焼結の初期段階(焼結層上部が焼結)では従来法
に比較して風量が低減し、焼結帯(ヒート・フロント)
の下降速度が低下し、以後焼結の終了段階に近づくに従
がって風量が増加し、保熱指数がほぼ一定に保持される
However, according to the method of the present invention, as shown in FIGS. 5 and 6, in the initial stage of sintering (the upper part of the sintered layer is sintered), the air volume is reduced compared to the conventional method, and the sintered zone (heat front)
The rate of descent of sintering decreases, and as the end of sintering approaches, the air volume increases and the heat retention index is kept almost constant.

以上述べたごとく、本発明方法によれば風量の調整によ
り焼結の全過程にわたり保熱指数が最適値に保持される
ので、焼結層全体の品質にムラがなくなり、後半の風量
の上昇により全体の生産量が増大する。
As described above, according to the method of the present invention, the heat retention index is maintained at an optimal value throughout the sintering process by adjusting the air volume, so the quality of the entire sintered layer becomes uniform, and the increase in air volume in the latter half Overall production increases.

以下に本発明方法を実施例にもとづきさらに詳しく説明
する。
The method of the present invention will be explained in more detail below based on Examples.

実施例 第1図に示した鍋試験の装置(320wflx410朋
)を用い、吸引負圧を−30011Aqから段階的に一
250011LAqまで500111Aq毎に変化さ・
せて第5図のごとく風量を調整し焼結を行なった。
Example Using the pot test apparatus (320wfl x 410mm) shown in Figure 1, the suction negative pressure was changed stepwise from -30011Aq to -250011LAq in steps of 500111Aq.
Then, sintering was carried out by adjusting the air volume as shown in Fig. 5.

使用原料は、ハマスレH15%、ゴードワージ29チ、
リョドセ8 F 29.3%、砂鉄、スケール、石灰石
、ケイ石であり、これに対し返鉱を501さらにこれら
の合計に対してコークスプリーズ4チを加えた。得られ
た結果を第1表ならびに第6〜8図に従来法と比較して
示す。
Raw materials used are Hamasure H15%, Godwaji 29chi,
Ryodose 8 F 29.3%, iron sand, scale, limestone, silica stone, to which 501 liters of return ore was added, and 4 liters of coke please was added to the total. The results obtained are shown in Table 1 and Figures 6 to 8 in comparison with the conventional method.

第  1  表 第1表ならびに第6〜8図より明らかなごとく本発明方
法においては保熱指数が前半は上昇し、後半は低下して
平準化され、生産率が約16チ向上するとともに、回転
強度、還元粉化率の上層、下層における差が減少して品
質ムラが少なくなり歩留も向上した。
Table 1 As is clear from Table 1 and Figures 6 to 8, in the method of the present invention, the heat retention index increases in the first half, decreases and becomes flat in the second half, and the production rate improves by about 16 inches, and the rotation The difference in strength and reduction powdering rate between the upper and lower layers was reduced, resulting in less uneven quality and improved yield.

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

第1図は鍋試験装置の概略図、第2図は従来の焼結の状
況を示すグラフ、第3図は保熱指示の説明図、第4図は
本発明方法の一具体例を示す概略図、第5〜8図は本発
明方法の実施結果を従来法と比較して示したグラフであ
る。 図中の主な符号はつぎのとおりである。 8:焼結原料層、9:ウィンドボックス、11:温度セ
ンサ、15:ダンパ噛 第4図 第5図 −第6図 碕肉(劃り
Fig. 1 is a schematic diagram of the pot testing device, Fig. 2 is a graph showing the conventional sintering situation, Fig. 3 is an explanatory diagram of heat retention instructions, and Fig. 4 is a schematic diagram showing a specific example of the method of the present invention. 5 to 8 are graphs showing the results of the method of the present invention in comparison with the conventional method. The main symbols in the figure are as follows. 8: Sintering raw material layer, 9: Wind box, 11: Temperature sensor, 15: Damper mesh Fig. 4 Fig. 5 - Fig. 6

Claims (1)

【特許請求の範囲】[Claims] (1)積層された焼結原料に送風しつつ焼結を行なう制
御系において、層内上下各地点の温度をT(C)、該地
点が1000°Cを越えた時刻および1000°Cまで
下降した時刻をそれぞれt□、t、 (min) 、保
熱指数Q(”0・min )を としだとき、焼結原料へ供給する風量の調整を行なうこ
とにより前記保熱指数Qの値を300〜700”C−m
1nに制御することを特徴とする焼結装置の運転方法。
(1) In a control system that performs sintering while blowing air to the stacked sintering raw materials, the temperature at each point above and below the layer is set to T (C), the time when the point exceeds 1000°C, and the temperature is lowered to 1000°C. When the time t□, t, (min) and the heat retention index Q (0・min) are respectively determined, the value of the heat retention index Q is set to 300 by adjusting the air volume supplied to the sintering raw material. ~700”Cm
A method of operating a sintering apparatus characterized by controlling the sintering device to 1n.
JP5409082A 1982-03-31 1982-03-31 Operating method for sintering device Pending JPS58171533A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5409082A JPS58171533A (en) 1982-03-31 1982-03-31 Operating method for sintering device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5409082A JPS58171533A (en) 1982-03-31 1982-03-31 Operating method for sintering device

Publications (1)

Publication Number Publication Date
JPS58171533A true JPS58171533A (en) 1983-10-08

Family

ID=12960916

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5409082A Pending JPS58171533A (en) 1982-03-31 1982-03-31 Operating method for sintering device

Country Status (1)

Country Link
JP (1) JPS58171533A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5979261A (en) * 1996-09-23 1999-11-09 Mannesmann Sachs Ag Positioning device for shifting gears in a transmission having an output component capable of two types of motion
KR20040021253A (en) * 2002-09-03 2004-03-10 주식회사 포스코 Apparatus with means for inhaling air up and down in sintering machine

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58144433A (en) * 1982-02-23 1983-08-27 Kawasaki Steel Corp Estimation and control in sintering machine

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58144433A (en) * 1982-02-23 1983-08-27 Kawasaki Steel Corp Estimation and control in sintering machine

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5979261A (en) * 1996-09-23 1999-11-09 Mannesmann Sachs Ag Positioning device for shifting gears in a transmission having an output component capable of two types of motion
KR20040021253A (en) * 2002-09-03 2004-03-10 주식회사 포스코 Apparatus with means for inhaling air up and down in sintering machine

Similar Documents

Publication Publication Date Title
US4410355A (en) Process for controlling a pelletizing plant for fine-grained ores
JPS58171533A (en) Operating method for sintering device
JPH0339424A (en) Method for controlling air permeability of sintered raw material bed
JP2022039966A (en) Manufacturing method of sintered ore and production apparatus of sintered ore
JPS6210227A (en) Sintering operation method
KR100413821B1 (en) Method for manufacturing sintered ore by controlling the ventilation in the sintered layer
SU456129A1 (en) The method of automatic control of the firing process in fluidized bed furnaces
RU1836431C (en) Procedure of burden charging
JPH02194128A (en) Method for operating sintering machine
JPH0814007B2 (en) Agglomerated ore manufacturing method
JPS5814856B2 (en) Heating furnace control method
JPS57140836A (en) Controlling method for volume distribution of blast gas in sintering machine
JP2000320978A (en) Control method of charging sintered material
KR20000014613A (en) Sinter mineral manufacturing system
SU429094A1 (en) METHOD OF INCREASING THE GAS PERMEABILITY OF IRELORADO MATERIAL LAYER
JPH0873951A (en) Production of sintered ore
JPS5838496B2 (en) Sintering operation method
JPS63183133A (en) Method for controlling sintering point in sintering machine and said sintering machine
JPH05272872A (en) Control device for feed amount of sintering material
JPH06256862A (en) Method for controlling pallet velocity in sintering machine
JPS5457404A (en) D. l. sintering method
SU1736925A1 (en) Method of automatically controlling activation of granulated carbon-containing materials in rotary furnace
SU775157A1 (en) Method of control of pellet annealing process
JPH0914857A (en) Manufacture of sintered ore
JPS6360236A (en) Method for controlling pressure in ignition furnace of sintering machine