JPH04110410A - Pre-reduction furnace in smelting reduction equipment for iron ore - Google Patents

Pre-reduction furnace in smelting reduction equipment for iron ore

Info

Publication number
JPH04110410A
JPH04110410A JP23016190A JP23016190A JPH04110410A JP H04110410 A JPH04110410 A JP H04110410A JP 23016190 A JP23016190 A JP 23016190A JP 23016190 A JP23016190 A JP 23016190A JP H04110410 A JPH04110410 A JP H04110410A
Authority
JP
Japan
Prior art keywords
dispersion plate
reduction
reduction furnace
dust
fluidized bed
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
JP23016190A
Other languages
Japanese (ja)
Inventor
Tatsuro Ariyama
達郎 有山
Shinichi Isozaki
進市 磯崎
Hitoshi Kawada
仁 川田
Sakae Arakawa
荒川 栄
Haruto Tsuboi
坪井 晴人
Yoshiyuki Kitano
北野 良幸
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP23016190A priority Critical patent/JPH04110410A/en
Publication of JPH04110410A publication Critical patent/JPH04110410A/en
Pending legal-status Critical Current

Links

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  • Crucibles And Fluidized-Bed Furnaces (AREA)
  • Manufacture Of Iron (AREA)

Abstract

PURPOSE:To effectively prevent stickiness and growth of dust to a dispersion plate by constituting the dispersion plate in a fluidized bed type pre-reduction furnace with plural rotatable bar-like bodies parallelly arranged at the suitable interval. CONSTITUTION:The pre-reduction chamber 6 in upper part of the dispersion plate 8 for partitioning inner part of the pre-reduction furnace body 5 and a gas blowing chamber 7 in lower part, are constituted, respectively. The above dispersion plate 8 is constituted of plural rotatable bar-like bodies 9 parallelly arranged at the suitable interval 10. The exhaust gas from a smelting reduction furnace guided in the gas blowing chamber 7 is blown into the pre-reduction chamber 6 through gap 10 of each bar-like body 9 to form the fluidized bed. The above bar-like body 9 is periodically rotated and the lower face side sticking the dust is turned to the fluidized bed side. By this method, the stuck material is quickly detached and removed from the bar-like body 9 by contact with fluidized ore particles.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、鉄鉱石の溶融還元設備にJ:、8ける予備
還元炉の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] This invention relates to an improvement of a pre-reduction furnace used in iron ore smelting and reduction equipment.

〔従来の技術〕[Conventional technology]

鉄鉱石の溶融還元では、設備を溶融還元炉と流動層式の
予備還元炉とから構成し、溶融還元炉で発生ずるt+1
ガスを予備還元炉流動層の流動化、還元ガスどして利用
する方法が経済上好ましい。そして、この流動層として
は、技術的完成度が高く、しかも鉱石の予熱、還元に伴
う粉化を抑制できるという点から、バブリング流動層が
特に有利である。
In the smelting reduction of iron ore, the equipment consists of a smelting reduction furnace and a fluidized bed pre-reduction furnace.
A method in which the gas is used to fluidize the fluidized bed of the pre-reducing furnace and as a reducing gas is economically preferable. As this fluidized bed, a bubbling fluidized bed is particularly advantageous because it has a high degree of technical perfection and can suppress powdering caused by preheating and reduction of the ore.

この予備還元炉は、その内部にガス噴出用の多数のノズ
ル孔(ガス通孔)を有する分散板を備えており、この分
散板の上方に形成される予備還元室に鉄鉱石が装入され
、分散板下方のカス吹込室(風箱)に溶融還元炉からの
排ガス(′a元ガス)が導入される。この排カスは、分
散板のノズル孔を通じて」三方の予備還元室に吹き出さ
れ、これにより流動層が形成され、鉄鉱石の予備還元と
予熱がなされる。
This pre-reduction furnace is equipped with a dispersion plate having a large number of nozzle holes (gas holes) for ejecting gas therein, and iron ore is charged into a pre-reduction chamber formed above the dispersion plate. The exhaust gas ('a original gas) from the melting reduction furnace is introduced into the waste blowing chamber (wind box) below the dispersion plate. This waste is blown out through the nozzle holes of the dispersion plate into the pre-reduction chambers on three sides, thereby forming a fluidized bed and pre-reducing and preheating the iron ore.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

このような予備還元炉では、排ガス中に含まれるダスト
の分散板への付着が大きな問題となる。
In such a preliminary reduction furnace, adhesion of dust contained in the exhaust gas to the dispersion plate poses a major problem.

すなわち、溶融還元炉から発生する排ガスには多量のダ
ス1−が含まれており、このうち]Oμn1以下の微粒
ダス1−は、多くの場合サイクロン等の除塵装置では除
去できず、このような微粒ダス]−を含む排ガスがその
まま予備還元炉に導入されてしまう。
In other words, the exhaust gas generated from the smelting reduction furnace contains a large amount of dust 1-, of which fine dust 1- of ]0 μn1 or less cannot be removed by dust removal equipment such as cyclones in many cases. The exhaust gas containing fine dust] is directly introduced into the preliminary reduction furnace.

上記ダストはSやNa、 K%のアルカリ土類金属多く
含んでいるため、900℃を超えるような温度の排ガス
中では粘着性を持ち、このため予備還元炉しこ導入され
ノーダス1〜は分散板下面やノズル孔内面に付着するこ
とになる。特に、ガス吹込室に導入された排ガスはノズ
ル孔を通過する際に縮流され、ノズル孔内のガス流速は
極めて高く(流速:約100 m/see程度)なるた
め、ノズル孔内面ではダス)・が特に強固に付着し易い
。このようなダストによる付着物は次第に成長し、遂に
は還元ガスの円滑な流れを妨げ、適正な療動層を形成で
きなくなる。第8図はこのような状況を示すもので、]
−は流動層、2は分散板、3は分散板下方のガス吹込室
、4は付着、成長したダストである。
Since the above-mentioned dust contains a large amount of alkaline earth metals such as S, Na, and K%, it becomes sticky in the exhaust gas at a temperature exceeding 900°C. It will adhere to the bottom surface of the plate and the inner surface of the nozzle hole. In particular, the exhaust gas introduced into the gas blowing chamber is contracted when passing through the nozzle hole, and the gas flow velocity inside the nozzle hole is extremely high (flow velocity: about 100 m/see), so the inner surface of the nozzle hole has a small amount of water.・Especially tends to adhere firmly. Such deposits due to dust gradually grow and eventually impede the smooth flow of the reducing gas, making it impossible to form a proper therapeutic layer. Figure 8 shows this situation.]
- is a fluidized bed, 2 is a dispersion plate, 3 is a gas blowing chamber below the dispersion plate, and 4 is attached and grown dust.

本発明は、このような従来の問題に鑑みなされたもので
、分散板に対するダストの付着、成長を効果的に防止で
きる予備還元炉の提供をその目的とする。[課題を解決
するための手段〕このため本発明は、分散板を、適当な
(■隙をおいて平行に配される回転可能な複数の棒状体
により構成したことをその特徴とする。
The present invention was made in view of such conventional problems, and an object of the present invention is to provide a pre-reduction furnace that can effectively prevent dust from adhering to and growing on a dispersion plate. [Means for Solving the Problems] Therefore, the present invention is characterized in that the dispersion plate is constituted by a plurality of rotatable rod-shaped bodies arranged in parallel with an appropriate gap.

〔作用〕[Effect]

従来用いられている予備還元炉の分散板においても、そ
の上面やノズル孔の出口では、ダスl−が付着しても流
動化した鉱石粒子の激しい運動により簡単に剥離し、し
たがって、ノズル孔内面や分散板下面のようなゲス1〜
付着、成長のおそれはほとんどない。本発明はこのよう
な事実に着目し、分散板を平行に配される複数の棒状体
により構成し、各棒状体を周期的に回転させることによ
り、ダストが付着した棒状体下面側を上方、すなわち流
tlJ側に向けさせ、仁着したダストを流動化した鉱石
粒子によって剥離させるようにしたものである。
Even on the dispersion plate of conventional pre-reduction furnaces, even if das l- adheres to the upper surface or the outlet of the nozzle hole, it easily peels off due to the violent movement of the fluidized ore particles, and therefore the inner surface of the nozzle hole Gesture 1 like the bottom surface of the dispersion plate
There is almost no risk of adhesion or growth. The present invention has focused on this fact, and consists of a dispersion plate made up of a plurality of rod-shaped bodies arranged in parallel, and by rotating each rod-shaped body periodically, the lower surface side of the rod-shaped bodies on which dust is attached is directed upward, That is, it is directed toward the flow tlJ side, and the deposited dust is peeled off by the fluidized ore particles.

ガス吹込室に導入された排ガスは、分散板を構成する各
棒状体間の間隙を通して予備還元室に吹き込まれる。各
棒状体は、周期的に適当な回転角(例えば、180°)
だけ回転する。これにより、ダス1〜が付着した棒状体
の下面側が流動層側に向けられ、ダストは流動化した鉱
石粒子の接触により棒状体から速やかに剥離、除去され
る。しだがって、このような棒状体の回転を周期的に繰
り返すことしこより、分散板しこ対するダストの付着、
成長が適切に防止できる。
The exhaust gas introduced into the gas blowing chamber is blown into the pre-reduction chamber through the gaps between the rod-like bodies constituting the distribution plate. Each rod-shaped body is periodically rotated through an appropriate rotation angle (for example, 180°).
only rotates. As a result, the lower surface of the rod to which the dust 1~ is attached is directed toward the fluidized bed, and the dust is quickly peeled off and removed from the rod by contact with the fluidized ore particles. Therefore, by periodically repeating the rotation of the rod-like body, dust may adhere to the dispersion plate.
Growth can be appropriately prevented.

なお、棒状体の回転は適当な時間的間隔をおいて行えば
十分であるが、場合によっては、常時回転させておくこ
ともできる。
Note that it is sufficient to rotate the rod-shaped body at appropriate time intervals, but depending on the situation, it is also possible to rotate the rod-shaped body all the time.

〔実施例〕〔Example〕

第1図および第2図は本発明の一実施例を示すもので、
5は予備還元炉本体、8は炉内部を仕切る分散板であり
、この分散板8の上部が予備還元室6を、また、下部が
ガス吹込室7をそれぞれ構成している。このガス吹込室
7にはガス吹込口(図示せず)が設けられ、これに溶融
還元炉からのガス導管が接続されている。
1 and 2 show an embodiment of the present invention,
Reference numeral 5 denotes a main body of the preliminary reduction furnace, and 8 denotes a distribution plate that partitions the inside of the furnace.The upper part of this distribution plate 8 constitutes a preliminary reduction chamber 6, and the lower part constitutes a gas blowing chamber 7. This gas blowing chamber 7 is provided with a gas blowing port (not shown), to which a gas conduit from the melting reduction furnace is connected.

前記分散板8は、適当な間隙1.0をおいて平行に配さ
れる回転可能な複数の棒状体9により構成されている。
The dispersion plate 8 is composed of a plurality of rotatable rod-shaped bodies 9 arranged in parallel with an appropriate gap of 1.0.

これらの棒状体9の両端は炉外において回転可能に支持
され、旺動装N11−により回転駆動できるようになっ
ている。
Both ends of these rod-shaped bodies 9 are rotatably supported outside the furnace, and can be rotationally driven by the moving device N11-.

ガス吹込室7内に導入された排ガスは、各棒状体9の間
隙10を通じて予備還元室6内に吹き込まれる。
The exhaust gas introduced into the gas blowing chamber 7 is blown into the preliminary reduction chamber 6 through the gaps 10 between the rod-like bodies 9 .

排ガスはガス吹込室内での温度が800 ℃以上あり、
このような高温状態での強度を確保するため、前記棒状
体9を中空構造とし、その内部に冷却媒体を流通させる
ようにすることが好ましい。
The exhaust gas has a temperature of 800°C or more in the gas blowing chamber,
In order to ensure strength under such high temperature conditions, it is preferable that the rod-shaped body 9 has a hollow structure and that a cooling medium is allowed to flow inside the rod-shaped body 9.

棒状体9の断面形状は任意であり、本実施例のように断
面丸形状のほか、第3図に示すような断面三角形状、或
いは断面多角形状等適宜なものとなし得る。
The cross-sectional shape of the rod-shaped body 9 is arbitrary, and in addition to the round cross-section as in this embodiment, it can be any suitable shape such as a triangular cross-section as shown in FIG. 3, or a polygonal cross-section.

また、棒状体9間の間隙10は、例えば、第4図ないし
第6図に示すように、棒状体9に長手方向で間隔を置い
て小径部12或いは溝部13を設けることにより、棒状
体9の長手方向に間隔的に形成させるようにしてもよい
。なお、第6図の例は、]本おきの棒状体9に小径部1
2を設けた例である。
Further, the gap 10 between the rod-shaped bodies 9 can be formed by providing small-diameter portions 12 or groove portions 13 at intervals in the longitudinal direction of the rod-shaped bodies 9, as shown in FIGS. 4 to 6, for example. They may be formed at intervals in the longitudinal direction. In addition, in the example shown in FIG.
This is an example in which 2 is provided.

以」二のような予備還元炉では、高温で且つ多量のダス
トを含む排ガスが長時間分散板を通過すると、分散板を
構成する各棒状体9の下面にダス1へによる付着物が構
成する。この状態で、第7図(イ)、(ロ)に示すよう
に棒状体9を回転させ、ダス1−が付着した棒状体の下
面側を流動層側に向ける。
In the pre-reducing furnace as described above, when high temperature exhaust gas containing a large amount of dust passes through the dispersion plate for a long time, deposits due to the dust 1 form on the lower surface of each rod-shaped body 9 constituting the dispersion plate. . In this state, the rod-shaped body 9 is rotated as shown in FIGS. 7(a) and 7(b), and the lower surface side of the rod-shaped body to which the dust 1- is attached is directed toward the fluidized bed side.

これにより付着物は流動化した鉱石粒子の接触1.コよ
り棒状体から速やかに剥離、除去される。特に付着物は
高温下で軟化した状態にあるため、このような除去は容
易になされる。したがって、このような棒状体の回転を
周期的しこ繰り返すことにより、分散板に対するダスト
の代著、成長が適切に防止される。
This causes the deposits to come into contact with the fluidized ore particles.1. It is quickly peeled off and removed from the rod-shaped body. In particular, since the deposits are in a softened state at high temperatures, such removal is easy. Therefore, by periodically repeating the rotation of such a rod-like body, it is possible to appropriately prevent dust from accumulating and growing on the dispersion plate.

〔発明の効果〕〔Effect of the invention〕

以」二述べた本発明によれば、分散板でのダストの付着
、成長が効果的に防止されるため、排ガスの流動層内へ
の吹き込みを安定して行わせることができる。
According to the present invention described above, since adhesion and growth of dust on the dispersion plate is effectively prevented, exhaust gas can be stably blown into the fluidized bed.

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

第1図および第2図は本発明の一実施例を示すもので、
第1図は縦断面図、第2図は第1図中■■線に沿う断面
図である。第3図は本発明の他の実施例を示す縦断面図
である。第4図ないし第6図は、それぞれ分散板を構成
する棒状体の構造例を示す平面図である。第7図(イ)
、(ロ)は本発明の予備還元炉の使用方法を示す説明図
である。第8図は従来の予備還元炉におけるダス1への
イ」着状況を示す説明図である。 図において、5は炉本体、6は予備還元室、7はガス吹
込室、8は分散板、9は棒状体、10は間隙である。 一
1 and 2 show an embodiment of the present invention,
FIG. 1 is a longitudinal cross-sectional view, and FIG. 2 is a cross-sectional view taken along the line ■■■ in FIG. FIG. 3 is a longitudinal sectional view showing another embodiment of the present invention. 4 to 6 are plan views showing structural examples of rod-shaped bodies constituting the dispersion plate, respectively. Figure 7 (a)
, (b) are explanatory diagrams showing how to use the preliminary reduction furnace of the present invention. FIG. 8 is an explanatory diagram showing the state of landing on dust 1 in a conventional preliminary reduction furnace. In the figure, 5 is a furnace main body, 6 is a preliminary reduction chamber, 7 is a gas blowing chamber, 8 is a dispersion plate, 9 is a rod-shaped body, and 10 is a gap. one

Claims (1)

【特許請求の範囲】[Claims] 流動層式の予備還元炉において、分散板を、適当な間隙
をおいて平行に配される回転可能な複数の棒状体により
構成したことを特徴とする鉄鉱石の溶融還元設備におけ
る予備還元炉。
1. A pre-reduction furnace for iron ore melting and reduction equipment, characterized in that the dispersion plate is constituted by a plurality of rotatable rod-shaped bodies arranged in parallel with appropriate gaps in the pre-reduction furnace of the fluidized bed type.
JP23016190A 1990-08-31 1990-08-31 Pre-reduction furnace in smelting reduction equipment for iron ore Pending JPH04110410A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23016190A JPH04110410A (en) 1990-08-31 1990-08-31 Pre-reduction furnace in smelting reduction equipment for iron ore

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23016190A JPH04110410A (en) 1990-08-31 1990-08-31 Pre-reduction furnace in smelting reduction equipment for iron ore

Publications (1)

Publication Number Publication Date
JPH04110410A true JPH04110410A (en) 1992-04-10

Family

ID=16903557

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23016190A Pending JPH04110410A (en) 1990-08-31 1990-08-31 Pre-reduction furnace in smelting reduction equipment for iron ore

Country Status (1)

Country Link
JP (1) JPH04110410A (en)

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