JP3439059B2 - Reduced iron production equipment - Google Patents
Reduced iron production equipmentInfo
- Publication number
- JP3439059B2 JP3439059B2 JP00905497A JP905497A JP3439059B2 JP 3439059 B2 JP3439059 B2 JP 3439059B2 JP 00905497 A JP00905497 A JP 00905497A JP 905497 A JP905497 A JP 905497A JP 3439059 B2 JP3439059 B2 JP 3439059B2
- Authority
- JP
- Japan
- Prior art keywords
- rotary hearth
- hearth
- processed
- combustion
- reduced iron
- 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
Links
Landscapes
- Manufacture Of Iron (AREA)
- Tunnel Furnaces (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、サーキュラ型の回
転炉床上に石炭を含む鉄鉱石粉から成る被処理体を載置
し、該被処理体を高温雰囲気中にて還元させる還元鉄製
造装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for producing reduced iron, in which a target object made of iron ore powder containing coal is placed on a circular type rotary hearth and the target object is reduced in a high temperature atmosphere. .
【0002】[0002]
【従来の技術】従来の還元鉄製造装置の一例を図5〜7
に示す。図5は還元鉄製造装置の概念図、図6は還元鉄
製造装置の概略平面図、図7は図6のVII-VII矢視断面
図である。2. Description of the Related Art An example of a conventional reduced iron manufacturing apparatus is shown in FIGS.
Shown in. 5 is a conceptual diagram of the reduced iron manufacturing apparatus, FIG. 6 is a schematic plan view of the reduced iron manufacturing apparatus, and FIG. 7 is a sectional view taken along the line VII-VII of FIG.
【0003】同図に示すように、円形状の還元炉1の炉
壁6内に環状の回転炉床2が旋回自在に配置されると共
にその回転炉床2の上に被処理体10が載置され、この
被処理体10が加熱され還元処理されるようになってい
る。即ち、回転炉床2の下方には、駆動輪5が配設され
ると共にこの駆動輪5にレール4を介して回転炉床2が
支持され、回転炉床2は駆動輪5によって図6の点線矢
印の方向に2〜10rphのゆっくりした速度で旋回す
る。As shown in the figure, an annular rotary hearth 2 is rotatably arranged in a furnace wall 6 of a circular reduction furnace 1, and an object 10 is placed on the rotary hearth 2. The object 10 to be processed is heated and reduced. That is, drive wheels 5 are arranged below the rotary hearth 2 and the rotary hearth 2 is supported by the drive wheels 5 via rails 4. The rotary hearth 2 is driven by the drive wheels 5 as shown in FIG. Turn in the direction of the dotted arrow at a slow speed of 2-10 rph.
【0004】還元炉1の上部には投入口11が設けら
れ、この投入口11から投入されたペレット状の被処理
体10が炉壁6内の回転炉床2上に複数層(1〜3層)
に敷詰められる。被処理体10は、粉状又は粒状の鉄鉱
石に石炭が加えられ、バインダーとを混合して直径10
〜20mmのペレット状に固められたものであり、別途
設けられた乾燥機12によって予め乾燥されている。A charging port 11 is provided in the upper part of the reduction furnace 1, and the pellet-shaped object to be processed 10 charged from the charging port 11 is formed in a plurality of layers (1 to 3) on the rotary hearth 2 in the furnace wall 6. layer)
Be spread over. The object 10 to be treated has a diameter of 10 or less obtained by adding coal to powdery or granular iron ore and mixing it with a binder.
The pellets are hardened into pellets of about 20 mm and dried in advance by a dryer 12 provided separately.
【0005】還元炉1の炉壁6内周面には、燃焼バーナ
3が複数箇所取り付けられ、燃焼バーナ3より発生した
高温ガスの輻射熱によって、被処理体10が加熱され還
元反応が生じる。尚、回転炉床2の側壁側には、高温ガ
スに対するシール装置7が設けられている。更に、還元
炉1のある箇所には排出機8が設けられており、還元反
応した被処理体10は約1回転後に排出機8より排出さ
れることとなる。A plurality of combustion burners 3 are attached to the inner peripheral surface of the furnace wall 6 of the reduction furnace 1, and the radiant heat of the high-temperature gas generated by the combustion burners 3 heats the object to be treated 10 to cause a reduction reaction. A sealing device 7 for high temperature gas is provided on the side wall of the rotary hearth 2. Further, an ejector 8 is provided at a certain location of the reducing furnace 1, and the object 10 to be subjected to the reduction reaction is ejected from the ejector 8 after about one rotation.
【0006】上記のような還元鉄製造装置においては、
別途設置されている乾燥機12によって被処理体10を
乾燥した後、乾燥した被処理体10を投入口11から連
続的に投入することにより、回転炉床2上で被処理体1
0をゆっくり旋回しながら、加熱し、還元するまで昇温
されているので、被処理体10を乾燥させる為の熱エネ
ルギー及び昇温させるための熱エネルギーが別々に必要
であり熱効率が良くなかった。In the reduced iron manufacturing apparatus as described above,
After the object to be processed 10 is dried by the dryer 12 separately installed, the object to be processed 1 is placed on the rotary hearth 2 by continuously charging the dried object 10 from the charging port 11.
Since 0 is slowly swirled and the temperature is raised until it is heated and reduced, the thermal energy for drying the object 10 and the thermal energy for raising the temperature are separately required, and the thermal efficiency is not good. .
【0007】[0007]
【発明が解決しようとする課題】上記のような従来の還
元鉄製造装置では、次のような問題点があった。
(1)還元炉1が1段式ハースの場合では、乾燥機12
が還元炉1とは別に設置されているため、乾燥機用の熱
エネルギーが必要となっていた。
(2)乾燥機12が還元炉1と独立して設置されている
と、乾燥機12によって乾燥・予熱された被処理体10
が搬送経路を通過する間に冷却されるので、還元炉1に
投入された後昇温する必要があり、この熱エネルギーが
ロスしていた。The conventional reduced iron manufacturing apparatus as described above has the following problems. (1) When the reduction furnace 1 is a single-stage hearth, the dryer 12
However, since it is installed separately from the reduction furnace 1, heat energy for the dryer is required. (2) When the dryer 12 is installed independently of the reduction furnace 1, the object to be processed 10 that has been dried and preheated by the dryer 12
Since it is cooled while passing through the transport path, it is necessary to raise the temperature after it has been charged into the reduction furnace 1, and this thermal energy has been lost.
【0008】本発明は、従来の還元鉄製造装置における
不具合点を解消し、還元炉内を上下2段に構成すること
によって、下段での加熱排ガスを上段へ導き乾燥・予熱
に利用し、装置全体がコンパクトで熱効率の良い還元鉄
製造装置を提供することを目的としている。The present invention solves the problems in the conventional reduced iron production apparatus and constructs the inside of the reduction furnace into the upper and lower stages, so that the heating exhaust gas in the lower stage is guided to the upper stage and utilized for drying and preheating. It is an object of the present invention to provide a reduced iron manufacturing apparatus which is compact as a whole and has good thermal efficiency.
【0009】[0009]
【課題を解決するための手段】この目的を達成するた
め、本発明においては、円形状の還元炉内を旋回する回
転炉床上に石炭を含む鉄鉱石粉から成る被処理体を載置
し、該被処理体を高温雰囲気中にて加熱、還元し鉄を得
る還元鉄製造装置において、前記回転炉床を上下2段に
積み重ねて構成すると共に上段の回転炉床を下段の回転
炉床よりも小型形状で高速回転させ、上段の回転炉床に
は被処理体を投入する投入口及び下段の回転炉床へ搬送
する搬送手段を設け、更に、下段の回転炉床には前記被
処理体を炉外に排出する排出機及び前記被処理体を加熱
する燃焼装置を設け、下段の回転炉床で発生した燃焼ガ
スを上段の回転炉床へ導入することによって、上段の回
転炉床上の被処理体を乾燥することを特徴とする。In order to achieve this object, in the present invention, an object to be treated made of iron ore powder containing coal is placed on a rotary hearth that swirls in a circular reduction furnace. In a reduced iron manufacturing apparatus for heating and reducing an object to be processed in a high temperature atmosphere to obtain iron, the rotary hearths are constructed by stacking the upper and lower rotary hearths in two stages, and the upper rotary hearths are smaller than the lower rotary hearths. It is rotated at a high speed in a shape, and the upper rotary hearth is provided with an inlet for introducing the object to be processed and a transfer means for transferring the object to the lower rotary hearth, and the lower rotary hearth is provided with the object to be processed. An object to be processed on the upper rotary hearth is provided by providing a discharger for discharging outside and a combustion device for heating the object to be processed, and introducing the combustion gas generated in the lower rotary hearth to the upper rotary hearth. Is dried.
【0010】更に、下段の回転炉床より上段の回転炉床
へ燃焼ガスを導く燃焼ガス流路に、多孔材の輻射熱変換
体或いは該輻射熱変換体に触媒をコーティングした燃焼
触媒体を介装したことをも特徴とする。Further, a radiant heat conversion body of a porous material or a combustion catalyst body obtained by coating a catalyst on the radiant heat conversion body is interposed in a combustion gas flow passage for guiding combustion gas from a lower rotary hearth to an upper rotary hearth. It is also characterized.
【0011】〔作用〕本発明の還元鉄製造装置によれ
ば、円形状の還元炉内を旋回する回転炉床が、上下2段
に積み重ねて構成されており、まず、被処理体が上段の
投入口から小型形状の回転炉床上に投入されると、被処
理体を載せた回転炉床が高速で旋回しながら加熱ガスに
よって乾燥・予熱され、略1回転した位置から下段へ搬
送される。[Operation] According to the reduced iron manufacturing apparatus of the present invention, the rotary hearths that swirl in the circular reduction furnace are configured by stacking the upper and lower two stages. When charged into the small-sized rotary hearth from the charging port, the rotary hearth on which the object to be processed is swirled at a high speed is dried and preheated by the heating gas, and is conveyed from the position where it is rotated about once to the lower stage.
【0012】次に、下段に搬送された回転炉床上の被処
理体は、低速でゆっくり旋回しながら高温ガス雰囲気中
で輻射熱を受けて還元反応を完結させた後、略1回転し
た位置から搬送機によって被処理体が系外へ排出され
る。また、下段に設けられた燃焼装置からの高温ガスの
輻射熱によって下段の被処理体を加熱し、還元反応を起
こさせる。そして、この下段で使用され排気される高温
の排ガスは、下段から上段へ導入され、上段の被処理体
を乾燥・予熱することによって熱エネルギーを有効に利
用し熱効率を高めることができる。Next, the object to be treated on the rotary hearth, which has been conveyed to the lower stage, receives radiant heat in a high-temperature gas atmosphere while slowly rotating at a low speed to complete the reduction reaction, and then is conveyed from a position where it has rotated approximately once. The object to be processed is discharged to the outside of the system by the machine. Further, the object to be treated in the lower stage is heated by the radiant heat of the high temperature gas from the combustion device provided in the lower stage to cause a reduction reaction. Then, the high-temperature exhaust gas used and exhausted in the lower stage is introduced from the lower stage to the upper stage, and by drying and preheating the object to be treated in the upper stage, the thermal energy can be effectively utilized and the thermal efficiency can be improved.
【0013】更に、下段の回転炉床より上段の回転炉床
へ燃焼ガスを導く燃焼ガス流路に、多孔材の輻射熱変換
体或いは燃焼触媒体を介装したので、下段から排気され
る可燃分を有する高温ガスは、輻射熱変換体或いは燃焼
触媒体を通過することによって輻射熱変換或いは燃焼を
行ない、熱エネルギーを効率よく被処理体へ供給するこ
とができる。Further, since the radiant heat converter of the porous material or the combustion catalyst is interposed in the combustion gas passage for guiding the combustion gas from the lower rotary hearth to the upper rotary hearth, the combustible components exhausted from the lower rotary hearth are disposed. The high-temperature gas having the above-mentioned properties can be converted into radiant heat or burned by passing through the radiant heat converter or the combustion catalyst, and heat energy can be efficiently supplied to the object to be processed.
【0014】[0014]
〔構成〕本発明の一実施例につき図1〜4により説明す
る。図1は還元鉄製造装置の縦断面図、図2は図1の平
面図、図3は還元鉄製造装置の作用説明図、図4は図1
の要部説明図である。従来例の図5〜7と同一部分には
同一符号を付し、重複する説明は省略する。[Structure] An embodiment of the present invention will be described with reference to FIGS. 1 is a vertical cross-sectional view of the reduced iron manufacturing apparatus, FIG. 2 is a plan view of FIG. 1, FIG. 3 is an operation explanatory view of the reduced iron manufacturing apparatus, and FIG.
FIG. The same parts as those in the conventional example shown in FIGS.
【0015】本実施例の還元鉄製造装置は、従来の乾燥
機12を廃止し、還元炉内の回転炉床(グレード)を上
下2段にて構成し、上段グレード22で乾燥・予熱を行
なう小型形状の上段ハース31と、下段グレード24で
加熱・還元を行なう大型形状の下段ハース32を積み重
ねて構成したもので、下段ハース32に設けられた燃焼
バーナ3からの高温燃焼ガスによって被処理体10を加
熱、還元反応に使用し、その高温の排気ガスを上段ハー
ス31に導入して乾燥・予熱に利用できるようにしたも
のである。In the reduced iron producing apparatus of this embodiment, the conventional dryer 12 is abolished, the rotary hearth (grade) in the reduction furnace is composed of two upper and lower stages, and the upper grade 22 is used for drying and preheating. It is configured by stacking a small-sized upper stage hearth 31 and a large-sized lower stage hearth 32 that heats and reduces with a lower stage grade 24. The high temperature combustion gas from the combustion burner 3 provided in the lower stage hearth 32 is used to process the object. 10 is used for heating and reduction reactions, and its high temperature exhaust gas is introduced into the upper stage hearth 31 so that it can be used for drying and preheating.
【0016】なお、本実施例で用いる被処理体10とし
ては、例えば、粉状又は粒状の鉄鉱石に石炭が加えら
れ、バインダーとを混合して直径10〜20mmのペレ
ット状に固めたものである。図1〜2に示すように、還
元炉20の上段ハース31内には、上段グレード22が
旋回自在に配置されると共に被処理体10を載せて上段
ハース31内を高速で旋回できるようになっている。The object 10 to be used in this embodiment is, for example, powdery or granular iron ore to which coal is added, mixed with a binder, and solidified into pellets having a diameter of 10 to 20 mm. is there. As shown in FIGS. 1-2, the upper grade 22 is rotatably arranged in the upper hearth 31 of the reduction furnace 20, and the object 10 to be processed is placed on the upper hearth 31 so that the upper grade 22 can swirl at a high speed. ing.
【0017】即ち、上段グレード22の下部には支持材
25が取り付けられると共にこの支持材25の両端部に
旋回用のレール4が回動可能に固定される一方、このレ
ール4の下側には駆動輪5が配置され、この駆動輪5に
レール4が乗って旋回できるようになっている。上段グ
レード22は、分割受皿が連続した形状の回転炉床であ
り、多孔板或いは金網で形成されていて、燃焼ガスの通
過可能なものである。分割受皿は、支持材25の回動に
よってそれぞれ傾斜可能である。上段グレード22は、
後述するように燃焼バーナ3の上部に位置するものであ
り、燃焼バーナ3から導かれた高温の排気ガスにより被
処理体10を乾燥・予熱できるようになっている。That is, a supporting member 25 is attached to the lower portion of the upper grade 22, and turning rails 4 are rotatably fixed to both ends of the supporting member 25, while below the rail 4. Drive wheels 5 are arranged, and the rails 4 can ride on the drive wheels 5 and turn. The upper grade 22 is a rotary hearth having a continuous divided pan, is formed of a perforated plate or a wire mesh, and is capable of passing combustion gas. Each of the divided trays can be tilted by rotating the support member 25. The upper grade 22 is
As will be described later, it is located above the combustion burner 3, and the object 10 to be processed can be dried and preheated by the high-temperature exhaust gas introduced from the combustion burner 3.
【0018】上段ハース31の天井部には被処理体10
の投入口21が設けられると共に排気ダクト9が設けら
れている。上段ハース31の下部には床板23が配置さ
れ、この床板23には下方から加熱ガスを導く導入孔2
7が多数設けられている。導入孔27には、網目状、ハ
ニカム状等の多孔材から成る輻射熱変換体或いは同輻射
熱変換体に白金等の触媒をコーティングした燃焼触媒体
が介装されている。On the ceiling of the upper hearth 31, the object to be processed 10 is placed.
And an exhaust duct 9 are provided. A floor plate 23 is disposed below the upper hearth 31, and an introduction hole 2 for guiding the heating gas from below is provided in the floor plate 23.
Many 7 are provided. Into the introduction hole 27, a radiant heat converter made of a mesh-like or honeycomb-like porous material or a combustion catalyst body obtained by coating the radiant heat converter with a catalyst such as platinum is interposed.
【0019】本実施例では、燃焼ガス流路である導入孔
27に輻射熱変換体或いは燃焼触媒体が介装されている
が、これに限るものではなく、多孔材の輻射熱変換体に
より燃焼ガス流路を形成してもよく、また、多孔材の輻
射熱変換体を流路表面に張り付けても良い。上段グレー
ド22の床板23は一部が傾斜して、被処理体10を下
段グレード24へ搬送する下降シュート26として形成
されている。In the present embodiment, the radiant heat converter or the combustion catalyst is provided in the introduction hole 27, which is a combustion gas flow path, but the invention is not limited to this. A passage may be formed, or a radiant heat converter made of a porous material may be attached to the surface of the passage. The floor plate 23 of the upper grade 22 is partially inclined and is formed as a descending chute 26 that conveys the object 10 to the lower grade 24.
【0020】還元炉20の下段ハース32内に下段グレ
ード24が旋回自在に配置されると共に下段グレード2
4には被処理体10が載せられ、下段グレード24の下
部にはレール4が設置され、レール4の下側には駆動輪
5が配置されている。従って、この駆動輪5にレール4
が乗って、下段グレード24が下段ハース32内で低速
のゆっくりした速度で旋回できるようになっている。下
段ハース32の炉壁には燃焼バーナ3が複数個所に設置
されると共に下段グレード24には排出機8が設けられ
て、還元反応が完結した被処理体10を装置外のホッパ
ー28を経て次工程へ排出するようになっている。The lower grade 24 is rotatably arranged in the lower hearth 32 of the reduction furnace 20 and the lower grade 2 is used.
An object to be processed 10 is placed on the rail 4, a rail 4 is installed under the lower grade 24, and drive wheels 5 are arranged below the rail 4. Therefore, the rail 4 is attached to the drive wheel 5.
The lower grade 24 can turn in the lower hearth 32 at a low and slow speed. Combustion burners 3 are installed at a plurality of locations on the furnace wall of the lower stage hearth 32, and an exhauster 8 is provided at the lower stage grade 24, and the object 10 to which the reduction reaction is completed is passed through a hopper 28 outside the apparatus to the next stage. It is designed to be discharged into the process.
【0021】従って、下段ハース32の側壁に設けられ
た燃焼バーナ3からの高温ガスは、低速で旋回する下段
グレード24で加熱、還元反応に利用された後、高速で
旋回する上段グレード22へ導入され被処理体10を乾
燥・予熱し、上段ハース31の上部から排気ダクト9へ
吸引されて、系外へ排気されている。Therefore, the high temperature gas from the combustion burner 3 provided on the side wall of the lower stage hearth 32 is used for heating and reduction reaction in the lower stage grade 24 rotating at a low speed and then introduced into the upper stage grade 22 rotating in a high speed. Then, the object 10 to be processed is dried and preheated, sucked from the upper part of the upper hearth 31 to the exhaust duct 9, and discharged to the outside of the system.
【0022】上段グレード22及び下段グレード24に
載せられ加熱される被処理体10の状態を図4に示す。
同図に示すように、下段グレード24には被処理体10
が略1層に並ベられ、燃焼バーナ3からの輻射熱が十分
伝わるように配慮されており、上段グレード22には被
処理体10が多層に並べられ、下方からの排ガスが床板
23の導入孔27を通過して上段グレード22の被処理
体10を乾燥・予熱している。FIG. 4 shows the condition of the object to be processed 10 placed on the upper grade 22 and the lower grade 24 and heated.
As shown in FIG.
Are arranged in almost one layer so that the radiant heat from the combustion burner 3 is sufficiently transmitted, the objects 10 to be treated are arranged in multiple layers on the upper grade 22, and the exhaust gas from below is introduced into the floor plate 23. After passing through 27, the upper grade 22 object 10 to be processed is dried and preheated.
【0023】〔実験例〕実験条件を次に示す。 2段式サーキュラーグレード;上段グレード径D=10m、幅W=1.2m 下段グレード径D=50m、幅W=5m グレードの回転数 ;上段25rph、下段6.8rph。 被処理体の投入速度 ;80ton/h(還元体換算)。 被処理体 ;鉄鉱石粉77%、石炭18%、Ca(OH)2 3.6% バインダー1.4 %から成る直径15mmの球体。 燃焼バーナ ;微粉炭焚きバーナを下段の側壁に複数個所設置。 炉内雰囲気温度 ;上段300℃、下段1300℃。Experimental Example The experimental conditions are shown below. Two-stage circular grade; upper grade diameter D = 10 m, width W = 1.2 m Lower grade diameter D = 50 m, width W = 5 m Grade rotation speed; upper stage 25 rph, lower stage 6.8 rph. Input speed of the object to be treated: 80 ton / h (reduced substance conversion). Object to be treated: A sphere with a diameter of 15 mm consisting of iron ore powder 77%, coal 18%, Ca (OH) 2 3.6% and binder 1.4%. Combustion burner: Multiple pulverized coal burning burners are installed on the lower side wall. Furnace atmosphere temperature: upper 300 ° C, lower 1300 ° C.
【0024】この条件での実験によると、上段の投入口
から投入された被処理体は、上段にて乾燥・予熱され、
下段にて加熱、還元反応された後排出されると、還元率
90%以上になったペレットとして取り出され、経済性
の高い還元鉄製造装置であることが確認された。According to the experiment under these conditions, the object to be treated, which was charged from the charging port in the upper stage, was dried and preheated in the upper stage,
When the product was heated and reduced in the lower stage and then discharged, it was taken out as pellets with a reduction rate of 90% or more, and it was confirmed that this is a highly economical reduced iron production apparatus.
【0025】〔作用・効果〕上記のような還元鉄製造装
置によれば、小型形状の上段ハース31と大型形状の下
段ハース32が、上下2段に積み重ねて構成されてお
り、先ず、ペレット状の被処理体10が上段ハース31
の投入口21から上段グレード22上に投入されると、
被処理体10を載せた上段グレード22が、例えば20
〜30rphの高速で旋回しながら被処理体10が下段
から上昇してきた加熱排ガスによって乾燥され、略1回
転した位置までくると、支持材25の回動による分割受
皿の傾斜により滑り落ち、下降シュート26から下段グ
レード24へ搬送される。[Operation / Effect] According to the reduced iron manufacturing apparatus as described above, the small-sized upper stage hearth 31 and the large-sized lower stage hearth 32 are configured by being stacked in two upper and lower stages. The object 10 to be processed is the upper hearth 31
When it is thrown into the upper grade 22 from the charging port 21 of
The upper grade 22 on which the object 10 is placed is, for example, 20
The object to be processed 10 is dried by the heated exhaust gas rising from the lower stage while turning at a high speed of ˜30 rph, and when it reaches a position where it is rotated about once, it slides down due to the inclination of the divided pan due to the rotation of the support member 25, and the descending shoot It is conveyed from 26 to the lower grade 24.
【0026】そして、下段グレード24上の被処理体1
0は、例えば2〜10rphの低速でゆっくり旋回しな
がら燃焼バーナ3からの高温ガス(例えば1300℃)
による輻射熱を受けて加熱され、還元反応を起こさせた
後、略1回転した位置から搬出機8によって排出され
る。また、この下段ハース32で使用された後、上段へ
導かれる加熱排ガスは、床板23に設けられた排ガスの
導入孔27から上段へ上昇し、図4で示すように被処理
体10を乾燥・予熱することによって熱エネルギーを有
効に利用し熱効率を高めている。Then, the object 1 to be processed on the lower grade 24
0 is a high temperature gas (for example, 1300 ° C.) from the combustion burner 3 while slowly turning at a low speed of 2 to 10 rph.
After being heated by receiving the radiant heat from the sheet and causing a reduction reaction, the sheet is discharged by the carry-out machine 8 from a position where it is rotated approximately once. Further, the heated exhaust gas, which is used in the lower stage hearth 32 and then guided to the upper stage, rises to the upper stage from the exhaust gas introduction hole 27 provided in the floor plate 23, and as shown in FIG. By preheating, the thermal energy is effectively used and the thermal efficiency is increased.
【0027】また、導入孔27には多孔材の輻射熱変換
体或いは燃焼触媒体が介装されているので、下段から上
昇してきた可燃分を有する高温ガスが通過することによ
って、輻射熱変換或いは燃焼を行ない、熱エネルギーを
効率よく被処理体10へ供給することができる。Further, since the radiant heat converter or the combustion catalyst which is a porous material is interposed in the introduction hole 27, the radiant heat conversion or combustion is carried out by the passage of the high temperature gas having the combustible component rising from the lower stage. The heat energy can be efficiently supplied to the object to be processed 10.
【0028】上記のような還元鉄製造装置によれば、還
元炉内のグレードを上下2段に配置し、上段を小型で高
速回転させ、下段を大型で低速回転させるように構成し
たので、従来の装置に比べて装置がコンパクトになり、
設置面積を小さくすることができる。また、下段の高温
排ガスを上段へ導き乾燥・予熱に利用するので、熱エネ
ルギーの排出ロスが少なくなり装置の熱効率が高くな
る。According to the apparatus for producing reduced iron as described above, the grades in the reduction furnace are arranged in upper and lower two stages, the upper stage is small and rotates at high speed, and the lower stage is large and rotates at low speed. The device is more compact than that of
The installation area can be reduced. Further, since the high-temperature exhaust gas in the lower stage is guided to the upper stage and used for drying and preheating, the exhaust loss of thermal energy is reduced and the thermal efficiency of the device is increased.
【0029】[0029]
【発明の効果】以上、実施例に基づいて具体的に説明し
たように、本発明の還元鉄製造装置によれば、円形状の
還元炉内を旋回する回転炉床上に石炭を含む鉄鉱石粉か
ら成る被処理体を載置し、該被処理体を高温雰囲気中に
て加熱、還元し鉄分を得る還元鉄製造装置であって、前
記回転炉床を上下2段に積み重ねて構成すると共に上段
の回転炉床を下段の回転炉床よりも小型形状で高速回転
させ、上段の回転炉床には被処理体を投入する投入口と
下段の回転炉床へ搬送する搬送手段を設け、下段の回転
炉床には被処理体を排出する排出機を設けると共に被処
理体を加熱する燃焼装置を設け、下段の回転炉床で発生
した燃焼ガスを上段の回転炉床に導入することによって
上段の被処理体を乾燥させるように構成したので、装置
がコンパクトになり、上段の小型化によって放熱面積か
小さく熱損失が少なくなり、且つ、下段で発生した高温
の排ガスの熱エネルギーを、上段にて乾燥・予熱に有効
利用し熱効率を高めることができる。As described above in detail with reference to the embodiments, according to the reduced iron manufacturing apparatus of the present invention, the iron ore powder containing coal is removed from the rotary hearth rotating in the circular reduction furnace. An apparatus for producing reduced iron, in which an object to be treated is placed, and the object is heated and reduced in a high-temperature atmosphere to obtain iron content, which is configured by stacking the rotary hearths in two upper and lower stages and The rotary hearth is rotated at a higher speed with a smaller shape than the lower rotary hearth, and the upper rotary hearth is provided with an inlet for introducing the object to be processed and a transport means for transporting the lower rotary hearth to the lower rotary hearth. The hearth is provided with a discharger for discharging the object to be processed and a combustion device for heating the object to be processed, and the combustion gas generated in the lower rotary hearth is introduced into the upper rotary hearth to allow the upper object Since the processing body is configured to dry, the device can be made compact. , Small heat loss or heat dissipation area by miniaturization of the upper is reduced, and the thermal energy of the hot exhaust gas generated in the lower, it is possible to increase the effective use heat efficiency drying and preheating at upper.
【0030】更に、下段の回転炉床より上段の回転炉床
へ燃焼排ガスを導入する燃焼ガス流路に、多孔材の輻射
熱変換体或いは該輻射熱変換体に触媒をコーティングし
た燃焼触媒体を介装して構成したので、下段から排気さ
れる可燃分を有する高温ガスは、輻射熱変換体或いは燃
焼触媒体を通過することによって輻射熱変換或いは燃焼
を行ない、熱エネルギーを効率よく被処理体へ供給する
ことができる。上記のように、本発明は装置全体がコン
パクトになり、熱エネルギーを効率よく利用できるの
で、経済性の良い還元鉄製造装置を提供することができ
る。Further, in the combustion gas passage for introducing the combustion exhaust gas from the lower rotary hearth to the upper rotary hearth, a radiant heat converter made of a porous material or a combustion catalyst body obtained by coating the radiant heat converter with a catalyst is interposed. Since the high temperature gas having a combustible component exhausted from the lower stage passes through the radiant heat converter or the combustion catalyst, radiant heat conversion or combustion is performed, and heat energy is efficiently supplied to the object to be processed. You can As described above, according to the present invention, the entire apparatus becomes compact and heat energy can be used efficiently, so that it is possible to provide a reduced iron manufacturing apparatus with good economical efficiency.
【図1】本発明の一実施例に係る還元鉄製造装置の縦断
面図である。FIG. 1 is a vertical cross-sectional view of a reduced iron manufacturing apparatus according to an embodiment of the present invention.
【図2】図1の平面図である。FIG. 2 is a plan view of FIG.
【図3】本発明の一実施例に係る還元鉄製造装置の作用
説明図である。FIG. 3 is an operation explanatory view of the reduced iron manufacturing apparatus according to the embodiment of the present invention.
【図4】図1の要部説明図である。FIG. 4 is an explanatory view of a main part of FIG.
【図5】従来の還元鉄製造装置の概念を示す説明図であ
る。FIG. 5 is an explanatory diagram showing the concept of a conventional reduced iron manufacturing apparatus.
【図6】従来の還元鉄製造装置の概略平面図である。FIG. 6 is a schematic plan view of a conventional reduced iron manufacturing apparatus.
【図7】図6のVII-VII 矢視断面図である。7 is a sectional view taken along the line VII-VII of FIG.
3 燃焼バーナ 4 レール 5 駆動輪 8 排出機 9 排気ダクト 10 被処理体 20 還元炉 21 投入口 22 上段グレード 23 床板 24 下段グレード 25 支持材 26 下降シュート 27 導入孔 31 上段ハース 32 下段ハース 3 combustion burner 4 rails 5 drive wheels 8 ejector 9 exhaust duct 10 Processing object 20 Reduction furnace 21 Input port 22 Upper grade 23 Floorboard 24 Lower grade 25 Support material 26 down shoot 27 introduction hole 31 Upper Hearth 32 Lower Haas
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平10−204514(JP,A) 特開 平1−152225(JP,A) 特開 昭47−4251(JP,A) 特開 昭58−207307(JP,A) 特開 平10−30106(JP,A) 特開 昭58−153088(JP,A) 特開 昭62−26487(JP,A) (58)調査した分野(Int.Cl.7,DB名) C21B 13/08 F27B 9/16 F27B 17/00 F27D 17/00 101 ─────────────────────────────────────────────────── --- Continuation of the front page (56) References JP 10-204514 (JP, A) JP 1-152225 (JP, A) JP 47-4251 (JP, A) JP 58- 207307 (JP, A) JP 10-30106 (JP, A) JP 58-153088 (JP, A) JP 62-26487 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) C21B 13/08 F27B 9/16 F27B 17/00 F27D 17/00 101
Claims (2)
に石炭を含む鉄鉱石粉から成る被処理体を載置し、該被
処理体を高温雰囲気中にて加熱、還元し鉄を得る還元鉄
製造装置において、前記回転炉床を上下2段に積み重ね
て構成すると共に上段の回転炉床を下段の回転炉床より
も小型形状で高速回転させ、上段の回転炉床には被処理
体を投入する投入口及び下段の回転炉床へ搬送する搬送
手段を設け、更に、下段の回転炉床には前記被処理体を
炉外に排出する排出機及び前記被処理体を加熱する燃焼
装置を設け、下段の回転炉床で発生した燃焼ガスを上段
の回転炉床へ導入することによって、上段の回転炉床上
の被処理体を乾燥することを特徴とする還元鉄製造装
置。1. An object to be treated made of iron ore powder containing coal is placed on a rotary hearth rotating in a circular reduction furnace, and the object is heated and reduced in a high temperature atmosphere to obtain iron. In the reduced iron manufacturing apparatus, the rotary hearths are stacked in two layers, and the upper rotary hearth is rotated in a smaller shape and at a higher speed than the lower rotary hearth, and the upper rotary hearth has an object to be treated. A charging means for charging and a transporting means for transporting to the lower rotary hearth are provided, and further, in the lower rotary hearth, an ejector for discharging the object to be processed out of the furnace and a combustion device for heating the object to be processed. And a combustion gas generated in the lower rotary hearth to be introduced into the upper rotary hearth to dry the object to be processed on the upper rotary hearth.
焼ガスを導入する燃焼ガス流路に、多孔材の輻射熱変換
体或いは該輻射熱変換体に触媒をコーティングした燃焼
触媒体を介装したことを特徴とする請求項1記載の還元
鉄製造装置。2. A radiant heat converter of a porous material or a combustion catalyst body obtained by coating the radiant heat converter with a catalyst is provided in a combustion gas passage for introducing combustion gas from a lower rotary hearth to an upper rotary hearth. The reduced iron manufacturing apparatus according to claim 1, wherein
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP00905497A JP3439059B2 (en) | 1997-01-22 | 1997-01-22 | Reduced iron production equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP00905497A JP3439059B2 (en) | 1997-01-22 | 1997-01-22 | Reduced iron production equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10204515A JPH10204515A (en) | 1998-08-04 |
JP3439059B2 true JP3439059B2 (en) | 2003-08-25 |
Family
ID=11709928
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP00905497A Expired - Fee Related JP3439059B2 (en) | 1997-01-22 | 1997-01-22 | Reduced iron production equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3439059B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8518146B2 (en) | 2009-06-29 | 2013-08-27 | Gb Group Holdings Limited | Metal reduction processes, metallurgical processes and products and apparatus |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1439236B1 (en) * | 2001-09-27 | 2012-12-05 | Nippon Steel Corporation | Method for drying molding containing oxidized metal, method for reducing oxidized metal and rotary hearth type metal reduction furnace |
CN102071275A (en) * | 2011-01-29 | 2011-05-25 | 沈阳博联特熔融还原科技有限公司 | Kiln device used for directly reducing iron |
-
1997
- 1997-01-22 JP JP00905497A patent/JP3439059B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8518146B2 (en) | 2009-06-29 | 2013-08-27 | Gb Group Holdings Limited | Metal reduction processes, metallurgical processes and products and apparatus |
Also Published As
Publication number | Publication date |
---|---|
JPH10204515A (en) | 1998-08-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4676741A (en) | Radiantly heated furnace | |
US2925336A (en) | Process for the production of hard burned agglomerates | |
CN101660866A (en) | Rotary hearth furnace for treating metal oxide materials | |
CN113604662B (en) | Pellet roasting system and method based on sintering machine | |
US6221127B1 (en) | Method of pyroprocessing mineral ore material for reducing combustion NOx | |
US2532335A (en) | Process for heat-treating solids | |
JP3439059B2 (en) | Reduced iron production equipment | |
CN108048613A (en) | A kind of rotary hearth furnace and deep bed sintering restoring method | |
US3594286A (en) | Carbonizing multiple layers of material by maintaining reducing atmosphere in bed and oxidizing atmosphere above bed | |
US8377371B2 (en) | System and method for producing metallic iron | |
US3732062A (en) | Method of and apparatus for reducing air pollution in the thermal processing of ores and other materials | |
JP2002539415A (en) | Method and apparatus for reducing feedstock in a rotary hearth furnace | |
US3766663A (en) | Preheater for lime kiln | |
JP3272605B2 (en) | Method and apparatus for reducing coal-containing iron ore pellets | |
US3531095A (en) | Annular rotary reactor | |
JPH10204514A (en) | Apparatus for producing reduced iron | |
CN211346241U (en) | Bottom blowing type drying device | |
JP3745271B2 (en) | Smelting reduction method and smelting reduction apparatus | |
US5248330A (en) | Method of pyroprocessing mineral ore material | |
US2210479A (en) | Process and apparatus for oxidizing sulphide ores | |
CA2343212A1 (en) | Method for producing directly reduced metal in a multi-tiered furnace | |
JPH10204516A (en) | Production of reduced iron and apparatus thereof | |
CN216668313U (en) | Pellet roasting system based on sintering machine | |
JPH0420786A (en) | Bulk matter calcining furnace | |
JPS6213296B2 (en) |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20030513 |
|
LAPS | Cancellation because of no payment of annual fees |