JP2598418B2 - Sintering method and apparatus for sintering compounding raw materials - Google Patents

Sintering method and apparatus for sintering compounding raw materials

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Publication number
JP2598418B2
JP2598418B2 JP62208150A JP20815087A JP2598418B2 JP 2598418 B2 JP2598418 B2 JP 2598418B2 JP 62208150 A JP62208150 A JP 62208150A JP 20815087 A JP20815087 A JP 20815087A JP 2598418 B2 JP2598418 B2 JP 2598418B2
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JP
Japan
Prior art keywords
sintering
carbon material
service tank
carbonaceous material
hopper
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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 - Lifetime
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JP62208150A
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Japanese (ja)
Other versions
JPS6452029A (en
Inventor
昭二 新田
信司 小島
Original Assignee
川崎製鉄株式会社
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Priority to JP62208150A priority Critical patent/JP2598418B2/en
Publication of JPS6452029A publication Critical patent/JPS6452029A/en
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Description

【発明の詳細な説明】 <産業上の利用分野> 本発明は焼結配合原料の焼結方法に係り、特に、パレ
ットの両サイドウォールから中央方向に少なくとも150m
m以上離れた部分から500mmに至る部分で焼結された焼結
鉱の品質を中央部の品質並みに向上することができる焼
結配合原料の焼結方法および装置に関するものである。
The present invention relates to a sintering method for a sintering compound material, and in particular, at least 150 m from both sidewalls of a pallet in a central direction.
The present invention relates to a sintering method and apparatus for a sintering compound raw material, which can improve the quality of a sintered ore sintered in a portion ranging from a portion separated by more than m to 500 mm to the same quality as a central portion.

<従来の技術およびその問題点> 従来焼結鉱は、第3図に示すような焼結プロセスによ
り製造されていた。すなわち複数の配合槽1に1次配合
原料A,粉コークスB,石灰石C,副原料D(蛇文岩,硅石)
等の一次配合原料を装入し、各配合槽1に貯えた一次配
合原料を槽下のコンスタントフィーダ2で定量切出し、
ベルトコンベヤ2′上で多層配合され、ミキサ3内で水
分添加,混合,造粒された後、2次配合原料として給鉱
ホッパ4に貯蔵される。そして2次配合原料は給鉱ホッ
パ4,ドラムフィーダ5,シュート6を経由して焼結機7上
のパレット8に装入される。その後、パレット8に装入
された配合原料層11はカットゲート9にて平坦化され、
点火炉10により配合原料層11の表層の炭材に点火された
後、主排風機12により下向きに吸気することによって配
合原料層11内の焼結反応が上層部から下層部へと連続的
に進行して行き、約15〜20分で焼結反応が終了し焼結鉱
が製造される方式である。
<Conventional technology and its problems> Conventionally, sintered ores have been manufactured by a sintering process as shown in FIG. That is, the primary compounding raw material A, the coke breeze B, the limestone C, and the auxiliary raw material D (the serpentine rock and the silica stone) are stored in the plural mixing tanks 1.
, Etc., and the primary blended raw material stored in each blending tank 1 is quantitatively cut out by a constant feeder 2 below the tank.
After being multi-layer compounded on the belt conveyor 2 ′, added with water, mixed and granulated in the mixer 3, it is stored in the feed hopper 4 as a secondary compounding material. Then, the secondary compounding raw material is charged into a pallet 8 on a sintering machine 7 via a feed hopper 4, a drum feeder 5, and a chute 6. Thereafter, the compounding material layer 11 charged in the pallet 8 is flattened by the cut gate 9,
After being ignited by the ignition furnace 10 on the carbon material on the surface of the blended material layer 11, the sintering reaction in the blended material layer 11 is continuously performed from the upper layer to the lower layer by suctioning downward by the main exhaust fan 12. This is a method in which the sintering reaction is completed in about 15 to 20 minutes and sinter is produced.

焼結鉱の品質は、その焼結過程で配合原料が受ける昇
温,冷却温度パターンによって左右される。
The quality of the sinter depends on the temperature rise and cooling pattern experienced by the blended raw materials during the sintering process.

しかるに、パレットサイドウォール近傍部の焼結鉱
は、装入初期の段階から配合原料とウォールとの接触
面がパレット幅中央部と比較して通気性が大きいこと、
焼結過程では、焼結鉱の収縮を伴う焼きじまりによっ
てサイドウォールと焼結鉱端部との間に間隙が生じ過剰
空気が侵入すること、サイドウォールから放熱がある
こと、などによりパレットサイドウォール近傍部の焼結
鉱は通風量過多の状態で焼結されるため、熱不足に至
る。
However, the sintered ore in the vicinity of the pallet sidewall has a large air permeability at the contact surface between the compounding material and the wall from the initial stage of charging as compared with the center of the pallet width,
In the sintering process, a gap between the side wall and the end of the sinter occurs due to burning-in accompanied by shrinkage of the sinter, and excess air enters, and heat is radiated from the side wall. Since the sintered ore near the wall is sintered in a state of excessive ventilation, heat shortage occurs.

この点、第4図に示すように焼結機パレットの幅方向
におけるコークス燃焼熱に着目すると、サイドウォール
近傍は、中央部に比較して、サイドウォールからの熱放
散があって、配合原料層中の鉱石を十分溶融するだけの
燃焼熱が不足するため融体生成量が少なく、従って中央
部の焼結鉱のようなシャッター強度が得られず、返鉱発
生の一つの要因となっている。
In this regard, focusing on the coke combustion heat in the width direction of the sintering machine pallet as shown in FIG. 4, the vicinity of the side wall has more heat dissipation from the side wall than the central portion, and the The amount of melt generated is small due to the lack of combustion heat enough to sufficiently melt the ore inside, so shutter strength like that of the sinter in the center cannot be obtained, which is one factor in the occurrence of returned ore .

さて、前述,の問題に対する通気抑制のためにと
られる手段としては、特開昭48−11204号に開示されて
いる焼結原料層上に返鉱を散布して焼結を行う方法があ
る。しかしながら、この方法は前述の問題の解決には
なりえず、また前述,のための通気抑制が焼結原料
全体としての通気性の悪化をもたらし好ましくない。
As a measure taken to suppress the ventilation for the above-mentioned problem, there is a method of performing sintering by sprinkling return ore on a sintering raw material layer disclosed in Japanese Patent Application Laid-Open No. 48-11204. However, this method cannot solve the above-mentioned problem, and the suppression of the air flow for the above-mentioned method is not preferable because the air permeability of the whole sintering raw material is deteriorated.

さらに、前述,,の問題を同時に満足する技術
として、特開昭58−31040号が開示されているが、サイ
ドウォールに沿って返鉱を介在させる手段が複雑となる
ばかりでなく、実操業において返鉱と焼結原料間を仕切
る仕切板の寿命が短く、保守が困難である。
Further, Japanese Patent Application Laid-Open No. 58-31040 is disclosed as a technique that simultaneously satisfies the above-mentioned problems. However, not only is the means for intervening return ore along the sidewall complicated, but also in actual operation. The life of the partition plate separating the returned ore and the sintering raw material is short, and maintenance is difficult.

<問題点を解決するための手段> 本発明は、前述の問題を解決し、焼結機パレットの幅
方向におけるコークス燃焼熱の偏析を防止し、特にパレ
ットの両サイドウォールから中央方向に少なくとも150m
m以上離れた部分から500mmに至る部分の熱不足を改善し
て、以て、幅方向の焼結原料層の均一な焼結を行い、返
鉱発生量の低減化を目的としてなされたものである。
<Means for Solving the Problems> The present invention solves the above-mentioned problems, prevents segregation of coke combustion heat in the width direction of the sintering machine pallet, and in particular, at least 150 m in the center direction from both sidewalls of the pallet.
The purpose is to improve the heat deficiency in the part from a distance of more than m to 500 mm from the part that is more than m apart, to perform uniform sintering of the sintering material layer in the width direction, and to reduce the amount of returned ore. is there.

本発明の焼結配合原料の焼結方法は、焼結機の給鉱ホ
ッパと点火炉間におけるパレット幅方向の両端部上方
に、それぞれ配設した焼結用炭材添加装置から、パレッ
トの両サイドウォールから中央方向に少なくとも150mm
離れた部分から500mmに至る部分の焼結配合原料層上に
焼結用炭材を追加して添加しつつ焼結することを特徴と
するものであり、また本発明の焼結原料添加装置は、焼
結機の給鉱ホッパと点火炉間におけるパレット幅方向の
両端部上方にそれぞれ配設され、上部に炭材分離用フィ
ルタを内蔵したサービスタンクを有すると共に下部に炭
材供給ホッパを有する炭材供給装置と、炭材搬送用のタ
ンクローリ車と上記サービスタンク間を連結し、途上に
遮断弁を有する炭材気送管と、上記サービスタンクと焼
結機ウインドレッグ間を連結し途上に遮断弁を有する吸
気管と、上記サービスタンクと上記炭材供給ホッパ間に
配設された遮断弁と、上記炭材供給ホッパの下部に配設
された炭材切出し装置とからなり、上記焼結機の主排風
機の吸引圧力によって上記タンクローリ車から炭材を上
記サービスタンクに受入れるように構成してなることを
特徴とするものである。
The sintering method of the sintering compounded raw material of the present invention comprises a sintering carbon material addition device disposed above both ends of a sintering machine between a feed hopper and an ignition furnace in a pallet width direction. At least 150mm in the middle direction from the sidewall
It is characterized by sintering while additionally adding a sintering carbon material on the sintering blended raw material layer of the part from the distant part to 500 mm, and the sintering raw material addition device of the present invention A charcoal having a service tank with a built-in filter for separating carbonaceous materials at the upper part and a carbonaceous material supply hopper at the lower part, which are respectively disposed above both ends in the pallet width direction between the feeder hopper of the sintering machine and the ignition furnace. The material supply device is connected between the tank truck for transporting the carbon material and the above-mentioned service tank, and the pneumatic pipe having a shutoff valve on the way is connected between the service tank and the wind leg of the sintering machine, and is shut off on the way. An intake pipe having a valve, a shutoff valve disposed between the service tank and the carbonaceous material supply hopper, and a carbonaceous material cutting device disposed below the carbonaceous material supply hopper; Depending on the suction pressure of the main exhaust fan The carbonaceous material from the tank lorry vehicle is characterized in that become configured to receive the said service tank.

<実施例> 次に本発明の実施例を図面に基づいて説明する。<Example> Next, an example of the present invention will be described with reference to the drawings.

第1図は、焼結機給鉱ホッパ4と点火炉10との間に焼
結用炭材添加装置13を配設した本発明の実施例を示す全
体側面図を示し、第2図は第1図のA−A矢視断面図を
示している。第4図に示すようにサイドウォールから中
央方向に少なくとも150mm以上離れた部分から500mmに至
る部分のコークス燃焼熱を中央部と同程度に改善するた
め第1図および第2図に示すように焼結機の給鉱ホッパ
4と点火炉10との間に、パレット8のサイドウォール内
壁面8′から中央方向に少なくとも150mm以上離れた部
分から500mmに至る部分の配合原料の表面に5〜10kg/t
・sの炭材を添加する焼結用炭材添加装置13を配設す
る。
FIG. 1 is an overall side view showing an embodiment of the present invention in which a sintering carbon material addition device 13 is disposed between a sintering machine feed hopper 4 and an ignition furnace 10, and FIG. 1 shows a cross-sectional view taken along the line AA of FIG. As shown in FIGS. 4 and 5, in order to improve the coke combustion heat in a portion extending from the portion at least 150 mm in the center direction from the sidewall to at least 500 mm from the side wall to the same extent as in the center portion, as shown in FIGS. Between the feeder hopper 4 and the ignition furnace 10 of the kneading machine, 5 to 10 kg / t
A sintering carbon material addition device 13 for adding s carbon material is provided.

第4図においてコークス燃焼熱の不足部分はハッチン
グ部分であり、第4図中Aの値が500mmに相当する。従
って、ウォール内壁面から中央方向に少なくとも150mm
以上離れた部分から500mmに至る部分の熱不足を補うた
め、炭材を添加するものである。第4図に示すようにウ
ォール内壁面において熱放散が急激であるが、少なくと
も内壁面より150mm以上離れた部分から、500mmに至る部
分に炭材を添加する必要がある。その理由は150mm未満
のサイズウォール道近部分は、炭材を添加しても熱不足
が殆ど解消されず、また500mmを超える範囲は熱不足が
生ぜず添加不要だからである。
In FIG. 4, the insufficient portion of the coke combustion heat is a hatched portion, and the value of A in FIG. 4 corresponds to 500 mm. Therefore, at least 150mm from the inner wall surface toward the center
Carbon material is added to compensate for the lack of heat in the part from the distant part to 500 mm. As shown in FIG. 4, heat is rapidly dissipated on the inner wall surface of the wall, but it is necessary to add carbonaceous material to at least a portion that is at least 150 mm away from the inner wall surface and reaches 500 mm. The reason is that, in the portion near the size wall road less than 150 mm, the heat deficiency hardly disappears even if the carbon material is added, and in the range exceeding 500 mm, the heat deficiency does not occur and the addition is unnecessary.

また、添加量は5〜10kg/t・sの範囲で行い、5kg/t
・s未満では加える炭材量が少なく効果はなく、かつ、
10kg/t・sを超えると場合によってはウォール面の焼損
が発生する危険があり、さらに炭材の原単位上昇に伴う
経済的不利が生じるからである。本発明によればハッチ
ング部分(ウォール内壁面から中央方向に150mm未満の
部分を除く)の熱不足がなくなり、幅方向に亘り均一に
焼結されるる。
In addition, the addition amount is in the range of 5 to 10 kg / t · s, and 5 kg / t
・ If it is less than s, the amount of carbon material added is small and there is no effect.
If it exceeds 10 kg / t · s, there is a danger that the wall surface may be burned in some cases, and furthermore, there is an economic disadvantage associated with an increase in the basic unit of carbonaceous material. According to the present invention, the lack of heat in the hatched portion (excluding the portion less than 150 mm in the center direction from the inner wall surface of the wall) is eliminated, and sintering is performed uniformly in the width direction.

ところで前記添加装置13は、第2図に示すように地上
のタンクローリ車14内の炭材をサービスタンク15まで空
気輸送するための炭材気送管16,該サービスタンク15の
下部に設けた遮断弁17を介し、炭材供給ホッパ18を設け
た該炭材供給ホッ18の下部には炭材を定量フィードする
ためのロータリーバルブ19が設置されている。さらに、
地上のタンクローリ車14内の炭材を空気輸送するための
動力源として、主排風機12の吸引圧力を利用すべく、吸
気管20が、前記サービスタンク15とウィンドレッグ21間
を連結している。なお、前記炭材気送管16および吸気管
20には切換え用の遮断弁22,23が設けてあり、またサー
ビスタンク15内には炭材を分離するためのフィルタ24が
取付けられている。
Meanwhile, as shown in FIG. 2, the addition device 13 includes a carbon material pneumatic pipe 16 for pneumatically transporting the carbon material in the tank truck 14 on the ground to the service tank 15, and a shutoff provided at a lower portion of the service tank 15. A rotary valve 19 for feeding a constant amount of carbon material is provided below the carbon material supply hopper 18 provided with a carbon material supply hopper 18 via a valve 17. further,
As a power source for pneumatically transporting the carbon material in the tank truck 14 on the ground, an intake pipe 20 connects the service tank 15 and the wind leg 21 so as to use the suction pressure of the main exhaust fan 12. . The carbon material pneumatic pipe 16 and the intake pipe
Switching valves 22 and 23 for switching are provided on 20, and a filter 24 for separating the carbon material is mounted in the service tank 15.

次に炭材を追加して添加するための手順について述べ
る。
Next, a procedure for additionally adding a carbon material will be described.

まず、焼結用炭材には一般に−3mmの粉コークスおよ
び微粉炭が使用されるが、ハンドリング上の発塵が問題
となるため通常タンクローリ車14にて持込まれることが
多い。このタンクローリ14の後部排出口に炭材気送管16
をジョイントし、サービスタンク15の下部に設けた遮断
弁17を全閉および吸気管20の遮断弁23,炭材気送管16の
遮断弁22を全開にすると、ウィンドレッグ21内の吸気負
圧(−1500〜−1900mm H2O)により、タンクローリ車14
内の炭材は炭材気送管16を経由してサービスタンク15内
に導かれ、該サービスタンク15内に設けたフィルタ24に
より分離回収される。タンクローリ車14内の炭材全量を
サービスタンク15内に装入し終わったら、遮断弁23を全
閉し、遮断弁17を全開して、炭材供給ホッパ18へサービ
スタンク15内の炭材が装入される。炭材供給ホッパ18内
の炭材はロータリバルブ19によって切り出され、パレッ
ト8のサイドウォール8′の内壁面から中央に少なくと
も150mm以上離れた部分から500mmに至る範囲における原
料表面に炭材が適当量づつ添加される。このようにする
ことによって焼結機パレットの幅方向におけるコークス
燃焼熱の偏析が防止される。
First, -3 mm coke breeze and pulverized coal are generally used as the sintering carbon material. However, dust generation during handling is a problem, and the sintering carbon material is often brought into the tank truck 14 in many cases. The carbon material pneumatic pipe 16
When the shut-off valve 17 provided at the lower part of the service tank 15 is fully closed and the shut-off valve 23 of the intake pipe 20 and the shut-off valve 22 of the carbonaceous air feeding pipe 16 are fully opened, the intake negative pressure in the wind leg 21 is reduced. the (-1500~-1900mm H 2 O) , the tank lorry vehicles 14
The carbonaceous material therein is led into the service tank 15 via the carbonaceous material feeding pipe 16 and separated and collected by the filter 24 provided in the service tank 15. When the entire amount of the carbon material in the tank truck 14 has been charged into the service tank 15, the shutoff valve 23 is fully closed, the shutoff valve 17 is fully opened, and the carbon material in the service tank 15 is supplied to the carbon material supply hopper 18. Be charged. The carbon material in the carbon material supply hopper 18 is cut out by a rotary valve 19, and an appropriate amount of carbon material is applied to the surface of the raw material in a range from the inner wall surface of the side wall 8 'of the pallet 8 at least 150mm in the center to 500mm. It is added one by one. By doing so, segregation of coke combustion heat in the width direction of the sintering machine pallet is prevented.

<発明の効果> パレット幅方向のコークス燃焼熱の偏析を防止し、配
合原料の均一焼結が可能となる。従って、従来コークス
燃焼熱不足により脆弱な焼結鉱となり返鉱発生の原因の
一つとなっていたサイドウォールから中央方向に少なく
とも150mm以上離れた部分から500mmに至る部分の焼結鉱
のシャッター強度が向上し、返鉱発生量の低減が達成で
きる。
<Effects of the Invention> Segregation of coke combustion heat in the width direction of the pallet is prevented, and uniform sintering of the blended raw material is enabled. Therefore, the shutter strength of the sintered ore from the part at least 150 mm in the center direction away from the sidewall to 500 mm from the side wall, which has become a fragile sinter due to the lack of coke combustion heat and which has been one of the causes of the occurrence of ore return, It is possible to improve and reduce the amount of returned ore.

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

第1図は本発明の実施例を示す全体側面図、第2図は第
1図のA−A矢視断面図、第3図は従来例を示す全体側
面図、第4図はパレット幅方向のコークス燃焼熱分布を
示すグラフである。 1……配合槽、3……ミキサ、 4……給鉱ホッパ、7……焼結機、 8……パレット、9……カットゲート、 10……点火炉、11……配合原料層、 12……主排風機、13……焼結用炭材添加装置、 14……タンクローリ車、15……サービスタンク、 16……炭材気送管、18……炭材供給ホッパ、 19……ロータリーバルブ、20……吸気管、 21……ウィンドレッグ、22,23……遮断弁。
1 is an overall side view showing an embodiment of the present invention, FIG. 2 is a sectional view taken along the line AA of FIG. 1, FIG. 3 is an overall side view showing a conventional example, and FIG. 3 is a graph showing a coke combustion heat distribution of FIG. DESCRIPTION OF SYMBOLS 1 ... Mixing tank, 3 ... Mixer, 4 ... Mining hopper, 7 ... Sintering machine, 8 ... Pallet, 9 ... Cut gate, 10 ... Ignition furnace, 11 ... Mixing raw material layer, 12 … Main exhaust fan, 13… Carbon material addition device for sintering, 14 …… Tank truck, 15… Service tank, 16 …… Carbon air supply pipe, 18 …… Carbon supply hopper, 19… Rotary Valve, 20 ... intake pipe, 21 ... wind leg, 22, 23 ... shut-off valve.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】焼結機の給鉱ホッパと点火炉間におけるパ
レット幅方向の両端部上方に、それぞれ配設した焼結用
炭材添加装置から、パレットの両サイドウォールから中
央方向に少なくとも150mm以上離れた部分から500mmに至
る部分の焼結配合原料層上に焼結用炭材を追加して添加
しつつ焼結することを特徴とする焼結配合原料の焼結方
法。
1. A sintering carbon material adding device disposed above both ends of a pallet width direction between a feeder hopper and an ignition furnace of a sintering machine. A sintering method for a sintering mixture raw material, characterized in that sintering is performed while additionally adding a carbon material for sintering to a portion of the sintering mixture raw material layer extending from the above-mentioned separated portion to 500 mm.
【請求項2】焼結機の給鉱ホッパと点火炉間におけるパ
レット幅方向の両端部上方にそれぞれ配設され、上部に
炭材分離用フィルタを内蔵したサービスタンクを有する
と共に下部に炭材供給ホッパを有する焼結用炭材供給装
置と、炭材搬送用のタンクローリ車と上記サービスタン
ク間を連結し、途上に遮断弁を有する炭材気送管と、上
記サービスタンクと焼結機ウィンドレッグ間を連結し途
上に遮断弁を有する吸気管と、上記サービスタンクと上
記炭材供給ホッパ間に配設された遮断弁と、上記炭材供
給ホッパの下部に配設された炭材切出し装置とからな
り、上記焼結機の主排風機の吸引圧力によって上記タン
クローリ車から炭材を上記サービスタンクに受入れるよ
うに構成してなることを特徴とする焼結配合原料添加装
置。
2. A service tank, which is disposed above both ends in the pallet width direction between a feed hopper and an ignition furnace of a sintering machine, has a built-in filter for separating carbon material, and supplies carbon material to a lower portion. A sintering carbonaceous material supply device having a hopper, a carbonaceous material pneumatic pipe having a shutoff valve on the way connecting a tanker truck for carbonaceous material transportation with the service tank, a service tank and a sintering machine wind leg An intake pipe connecting between them and having a shut-off valve on the way, a shut-off valve arranged between the service tank and the carbonaceous material supply hopper, and a carbonaceous material cutting device arranged below the carbonaceous material supply hopper. A sintering compound raw material adding apparatus, wherein carbon material is received from the tank truck into the service tank by suction pressure of a main exhaust fan of the sintering machine.
JP62208150A 1987-08-24 1987-08-24 Sintering method and apparatus for sintering compounding raw materials Expired - Lifetime JP2598418B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62208150A JP2598418B2 (en) 1987-08-24 1987-08-24 Sintering method and apparatus for sintering compounding raw materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62208150A JP2598418B2 (en) 1987-08-24 1987-08-24 Sintering method and apparatus for sintering compounding raw materials

Publications (2)

Publication Number Publication Date
JPS6452029A JPS6452029A (en) 1989-02-28
JP2598418B2 true JP2598418B2 (en) 1997-04-09

Family

ID=16551469

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2598418B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101300366B (en) * 2005-10-31 2011-01-05 杰富意钢铁株式会社 Method for producing sintered ore and sintering machine therefor

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5862872B2 (en) * 2011-12-22 2016-02-16 Jfeスチール株式会社 Sintering machine and gaseous fuel supply method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6148538A (en) * 1984-08-13 1986-03-10 Kawasaki Steel Corp Manufacture of sintered ore

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101300366B (en) * 2005-10-31 2011-01-05 杰富意钢铁株式会社 Method for producing sintered ore and sintering machine therefor

Also Published As

Publication number Publication date
JPS6452029A (en) 1989-02-28

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