JPH04116113A - Prereducing furnace for iron ore smelting reduction equipment - Google Patents

Prereducing furnace for iron ore smelting reduction equipment

Info

Publication number
JPH04116113A
JPH04116113A JP23625890A JP23625890A JPH04116113A JP H04116113 A JPH04116113 A JP H04116113A JP 23625890 A JP23625890 A JP 23625890A JP 23625890 A JP23625890 A JP 23625890A JP H04116113 A JPH04116113 A JP H04116113A
Authority
JP
Japan
Prior art keywords
nozzle hole
hole
furnace
ball
dust
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
JP23625890A
Other languages
Japanese (ja)
Inventor
Haruto Tsuboi
坪井 晴人
Shinichi Isozaki
進市 磯崎
Jiro Mase
間瀬 二郎
Yoshiyuki Kitano
北野 良幸
Sakae Arakawa
荒川 栄
Tatsuro Ariyama
達郎 有山
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 JP23625890A priority Critical patent/JPH04116113A/en
Publication of JPH04116113A publication Critical patent/JPH04116113A/en
Pending legal-status Critical Current

Links

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  • Manufacture Of Iron (AREA)

Abstract

PURPOSE:To prevent the deposition and growth of dust on the inner surface of a nozzle hole by providing a spiral groove on the inner surface of a diffuser plate partitioning the inside of the furnace and moving a ball along the groove. CONSTITUTION:A nozzle hole 6 consisting of a metallic tube 8 is provided to a diffuser plate 5 vertically partitioning the inside of a prereducing furnace. A spiral groove 9 having a semicircular cross section is furnished on the inner surface of the hole 6 from the lower to upper ends. When dust deposits on the inner surface of the hole 6, a solid ball 12 is force-fed to the inside of the inlet of the hole 6 by a gas through a ball feed passage 10. The ball 12 is spirally moved toward the outlet along the groove 9. Consequently, the deposit on the inner surface of the hole 6 is scraped off by the moving ball and finally discharged into a prereducing chamber 13 above the diffuser plate 5. The waste gas is stably blown into the fluidized bed in this way.

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おける予備還元炉
の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] This invention relates to an improvement of a preliminary reduction furnace in an iron ore smelting reduction facility.

〔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、溶融還元炉で発生する排ガス
を予備還元炉流動層の流動化、還元ガスとして利用する
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。
For smelting reduction of iron ore, an economical method is to configure the equipment with a smelting reduction furnace and a fluidized bed pre-reduction furnace, and use the exhaust gas generated in the smelting reduction furnace to fluidize the fluidized bed of the pre-reduction furnace and as reducing gas. It is preferable. And 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 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
、分散板下方のガス吹込室(風箱)に溶融還元炉からの
排ガス(還元ガス)が導入される。この還元ガスは、分
散板のノズル孔を通じて上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 (reducing gas) from the melting reduction furnace is introduced into the gas blowing chamber (wind box) below the distribution plate. This reducing gas is blown out through the nozzle holes of the dispersion plate into the preliminary reduction chamber above, 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
ストが含まれており、このうち10μ園以下の微粒ダス
トは、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ト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, and of this, fine dust of less than 10 microns cannot be removed by dust removal equipment such as cyclones in many cases. The exhaust gas is directly introduced into the preliminary reduction furnace.

上記ダストはSやNa、 K等のアルカリ化合物を多く
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に導入された
ダスト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(流速二数十m /see以上)なるため、ノズル
孔内面ではダスト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、適正な流動層を形成できなくなる。
Since the above dust contains a large amount of alkaline compounds such as S, Na, and K, it becomes sticky in the exhaust gas at a temperature exceeding 900°C. Therefore, the dust introduced into the pre-reduction furnace will stick to the bottom surface of the dispersion plate and the like. It will adhere to 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 rate inside the nozzle hole is extremely high (flow rate of more than 200 m/see), so dust is generated on the inner surface of the nozzle hole. Particularly easy to adhere firmly. Such dust deposits gradually grow and eventually impede the smooth flow of the reducing gas, making it impossible to form a proper fluidized bed.

第2図はこのような状況を示すもので、1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。
Figure 2 shows this situation, where 1 is a fluidized bed and 2 is a fluidized bed.
3 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、特にノズル孔内面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。
The present invention has been 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, particularly on the inner surface of a nozzle hole.

〔課題を解決するための手段〕[Means to solve the problem]

このため本発明は、多数のノズル孔が貫設された分散板
を炉内部に有する流動層式の予備還元炉において、分散
板の各ノズル孔の内面に、ノズル孔入口から出口にかけ
て螺旋溝を設け、分散板の内部には、端部が前記ノズル
孔入口近傍の螺旋溝に開口した球体供給路を設けたこと
をその特徴とする。
For this reason, the present invention provides a fluidized bed pre-reduction furnace that has a dispersion plate with a large number of nozzle holes inserted therein, in which a spiral groove is formed on the inner surface of each nozzle hole of the dispersion plate from the inlet to the outlet of the nozzle hole. The present invention is characterized in that a spherical supply channel is provided inside the dispersion plate, the end of which opens into a spiral groove near the nozzle hole entrance.

〔作用〕[Effect]

供給路を通じて固形の球体をノズル孔の入口側内部に供
給する。ノズル孔内でのガス流速は数十m7880以上
あり、ノズル孔内部に押し出された球体はガス流の力に
より螺旋溝に沿って旋回しつつノズル孔出口方向に移動
し、この移動中、ノズル孔内面に付着したダストを削り
取る。最終的に球体は、ノズル孔出口から分散板上方の
流動層に排出される。
A solid sphere is supplied to the inside of the nozzle hole on the inlet side through the supply path. The gas flow velocity inside the nozzle hole is several tens of meters or more, and the sphere pushed into the nozzle hole moves toward the exit of the nozzle hole while rotating along the spiral groove due to the force of the gas flow. Scrape off the dust attached to the inner surface. Finally, the spheres are discharged from the nozzle hole exit into the fluidized bed above the distribution plate.

〔実施例〕〔Example〕

第1図は本発明の一実施例を示すもので、予備還元炉内
の分散板5に設けられる1つのノズル孔6を示している
。分散板5は予備還元炉の内部を上下に仕切るもので、
その上部が予備還元室13を、また、下部がガス吹込室
14をそれぞれ構成している。このガス吹込室14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。
FIG. 1 shows an embodiment of the present invention, and shows one nozzle hole 6 provided in a dispersion plate 5 in a preliminary reduction furnace. The distribution plate 5 partitions the inside of the preliminary reduction furnace into upper and lower parts.
The upper part constitutes a preliminary reduction chamber 13, and the lower part constitutes a gas blowing chamber 14, respectively. This gas blowing chamber 14 is provided with a gas blowing port (not shown), to which a gas conduit from the melting reduction furnace is connected.

前記ノズル孔6は耐火物製の分散板本体7に埋め込まれ
る金属筒8により構成されている。
The nozzle hole 6 is constituted by a metal tube 8 embedded in a dispersion plate main body 7 made of refractory material.

金属筒Bにより構成されるノズル孔の内面には、ノズル
孔出口(下端)から出口(上端)にかけて螺旋溝9が設
けられている。この螺旋溝9は、断面が半円形状であり
、これに沿って移動する球体がノズル孔内面の広い範囲
に接触できるよう、溝どうしの間隔が密に構成されてい
る。
A spiral groove 9 is provided on the inner surface of the nozzle hole constituted by the metal cylinder B from the nozzle hole outlet (lower end) to the outlet (upper end). This spiral groove 9 has a semicircular cross section, and the grooves are closely spaced so that the sphere moving along the spiral groove can come into contact with a wide range of the inner surface of the nozzle hole.

一方、ガス吹込室14寄りの分散板5の内部には、球体
供給路10が設けられ、その端部が前記ノズル孔入口近
傍の螺旋溝9に開白11している。
On the other hand, a spherical supply channel 10 is provided inside the dispersion plate 5 near the gas blowing chamber 14, and the end thereof opens 11 into the spiral groove 9 near the nozzle hole entrance.

この球体供給路10の他端側は予備還元炉の炉体を通し
て炉外に通じている。
The other end of this sphere supply path 10 communicates with the outside of the furnace through the furnace body of the preliminary reduction furnace.

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5を通過すると、ノズル孔6の内面に
ダストによる付着物が生成する。本発明の予備還元炉で
は、このように付着物が生成した状態で、固形の球体1
2を球体供′給路1oを通じてノズル孔6の入口側内部
に供給する。この球体の供給はN2ガスによる圧送等に
より行われる。ノズル孔内でのガス流速は数+m/se
e以上あり、ノズル孔内部に押し出された球体12は、
ガス流の力により螺旋溝9に沿って旋回しつつノズル孔
出口方向に移動し、この移動中、ノズル孔内面に付着し
た付着物を削り取る。そして、最終的に球体12は、ノ
ズル孔出口から分散板上方の予備還元室13(流動層)
に排出される。したがって、上記球体12としては、鉄
鉱石と同様の成分(Fe、O,、Fed)のもの、或い
は鋼球を用いることが好ましい。
In the preliminary reduction furnace, when high temperature exhaust gas containing a large amount of dust passes through the dispersion plate 5 for a long time, deposits of dust are generated on the inner surface of the nozzle hole 6. In the pre-reduction furnace of the present invention, the solid spheres 1 are
2 is supplied to the inside of the nozzle hole 6 on the entrance side through the sphere supply path 1o. The supply of the spheres is performed by pressure feeding using N2 gas or the like. The gas flow velocity inside the nozzle hole is several + m/sec.
e or more, the sphere 12 pushed out inside the nozzle hole is
It moves toward the exit of the nozzle hole while turning along the spiral groove 9 due to the force of the gas flow, and during this movement, the deposits adhering to the inner surface of the nozzle hole are scraped off. Finally, the sphere 12 is moved from the nozzle hole exit to the preliminary reduction chamber 13 (fluidized bed) above the dispersion plate.
is discharged. Therefore, as the sphere 12, it is preferable to use one having the same composition as iron ore (Fe, O, Fed) or a steel ball.

以上のような球体12の供給を定期的に行うことにより
、ノズル孔内面での付着物の生成、成長を防止すること
ができる。
By periodically supplying the spheres 12 as described above, it is possible to prevent the formation and growth of deposits on the inner surface of the nozzle hole.

〔発明の効果〕〔Effect of the invention〕

以上述へた本発明によれば、分散板のノズル孔内面での
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 as described above, since adhesion and growth of dust on the inner surface of the nozzle hole of 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図は本発明の一実施例における分散板の縦断面図で
ある。第2図は従来の予i還元炉におけるダストの付着
状況を示す説明図である。 図において、5は分散板、6はノズル孔、9は螺旋溝、
10は球体供給路、11は開口、12は球体である。 第
FIG. 1 is a longitudinal sectional view of a dispersion plate in one embodiment of the present invention. FIG. 2 is an explanatory diagram showing the state of dust adhesion in a conventional pre-reduction furnace. In the figure, 5 is a dispersion plate, 6 is a nozzle hole, 9 is a spiral groove,
10 is a sphere supply path, 11 is an opening, and 12 is a sphere. No.

Claims (1)

【特許請求の範囲】[Claims] 多数のノズル孔が貫設された分散板を炉内部に有する流
動層式の予備還元炉において、分散板の各ノズル孔の内
面に、ノズル孔入口から出口にかけて螺旋溝を設け、分
散板の内部には、端部が前記ノズル孔入口近傍の螺旋溝
に開口した球体供給路を設け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。
In a fluidized bed pre-reduction furnace that has a dispersion plate with a large number of nozzle holes penetrated inside the furnace, a spiral groove is provided on the inner surface of each nozzle hole of the dispersion plate from the nozzle hole inlet to the outlet. A preliminary reduction furnace for iron ore smelting and reduction equipment, characterized in that a spherical supply path is provided whose end opens into a spiral groove near the nozzle hole entrance.
JP23625890A 1990-09-06 1990-09-06 Prereducing furnace for iron ore smelting reduction equipment Pending JPH04116113A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23625890A JPH04116113A (en) 1990-09-06 1990-09-06 Prereducing furnace for iron ore smelting reduction equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23625890A JPH04116113A (en) 1990-09-06 1990-09-06 Prereducing furnace for iron ore smelting reduction equipment

Publications (1)

Publication Number Publication Date
JPH04116113A true JPH04116113A (en) 1992-04-16

Family

ID=16998117

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23625890A Pending JPH04116113A (en) 1990-09-06 1990-09-06 Prereducing furnace for iron ore smelting reduction equipment

Country Status (1)

Country Link
JP (1) JPH04116113A (en)

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