JPH04301020A - Structure for furnace lower part in fluidized bed reduction furnace - Google Patents
Structure for furnace lower part in fluidized bed reduction furnaceInfo
- Publication number
- JPH04301020A JPH04301020A JP6667291A JP6667291A JPH04301020A JP H04301020 A JPH04301020 A JP H04301020A JP 6667291 A JP6667291 A JP 6667291A JP 6667291 A JP6667291 A JP 6667291A JP H04301020 A JPH04301020 A JP H04301020A
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- ore
- furnace
- gas
- nozzle
- 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
Links
Landscapes
- Manufacture Of Iron (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【0001】0001
【産業上の利用分野】本発明は、流動層還元炉を用いて
鉄鉱石を還元する設備に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to equipment for reducing iron ore using a fluidized bed reduction furnace.
【0002】0002
【従来の技術】従来の高炉による溶銑製造技術に替わる
ものとして、溶融還元法が注目を浴びている。この方法
は、粉鉱石の使用、一般炭の使用、コークス工程の省略
等により溶銑を安価に製造することを目的に開発されて
いる。また、溶融還元炉で発生した排ガスの還元力およ
び熱を有効に利用するために、流動ガスとして流動層還
元炉に供給して原料鉱石を予熱、予備還元する方法等も
開発されている。BACKGROUND OF THE INVENTION The smelting reduction method is attracting attention as an alternative to the conventional method of producing hot metal using a blast furnace. This method has been developed with the aim of producing hot metal at low cost by using fine ore, steam coal, and omitting the coking process. In addition, in order to effectively utilize the reducing power and heat of the exhaust gas generated in the smelting reduction furnace, a method has been developed in which the raw material ore is preheated and pre-reduced by supplying it to the fluidized bed reduction furnace as a fluidized gas.
【0003】かかる流動層還元装置として、特開昭62
−269283号公報、特開平1−111807号公報
に開示されているように、側部に粉鉱石投入部と底部付
近に流動層形成用のキャリアガス導入部とさらに流動層
の底板の全面にノズルを設けた流動用ガス導入部とを設
けた流動層(ライザー)と、その外側にサイクロンを介
して粉体を循環するための粉体循環流動部(ダウンカマ
ー)とからなる循環型の流動層を有するものと、サイク
ロンで捕集した粉状の還元鉱石をライザーへ戻さない非
循環型の流動層とがある。[0003] As such a fluidized bed reduction device, Japanese Patent Application Laid-Open No. 1982
As disclosed in JP-A-269283 and JP-A-1-111807, there is a fine ore input part on the side, a carrier gas introduction part for forming a fluidized bed near the bottom, and a nozzle on the entire surface of the bottom plate of the fluidized bed. A circulating fluidized bed consisting of a fluidized bed (riser) equipped with a fluidizing gas introduction section and a powder circulation fluidization section (downcomer) for circulating powder via a cyclone outside of the fluidized bed (riser). There are two types: one with a cyclone and the other with a non-circulating fluidized bed in which the powdered reduced ore collected by the cyclone is not returned to the riser.
【0004】この流動層還元装置における問題点の一つ
として、流動層を形成する粉鉱が還元ガス吹き込みノズ
ルから落下して、装置の安定操業を阻害したり、生産性
を低下させることがある。One of the problems with this fluidized bed reduction equipment is that the fine ore forming the fluidized bed may fall from the reducing gas injection nozzle, interfering with the stable operation of the equipment and reducing productivity. .
【0005】このノズルからの落鉱防止対策として、還
元ガスの吹き込み孔を小さくして吹き込み孔を一面に分
布した多孔床の使用や、吹き込みノズルを用いる型式の
ものにあっては、ノズルの頂部にキャップを設けて吹き
込み口を水平方向に指向したものがある。[0005] As a measure to prevent ore from falling from the nozzle, the blowing holes for the reducing gas are made small and a porous bed is used, in which the blowing holes are distributed over the entire surface, and in the case of a type that uses a blowing nozzle, the top of the nozzle is Some types have a cap attached to the top and have the air inlet oriented horizontally.
【0006】[0006]
【発明が解決しようとする課題】ところが、このような
対策は、使用する還元ガスがクリーンなガスの場合には
相当の効果が期待できるが、上記溶融還元法の場合のよ
うに、溶融還元炉の排ガスを還元ガスとして吹き込む場
合には、この排ガス中に溶融還元工程で発生したダスト
や金属酸化物からなるフューム等の不純物が多量に含有
しており、この不純物が吹き込み口に付着して閉塞し、
ガス吹き込みが不均一になったり、通気不可能になって
操業を一時停止しなければならない事態を生じる。ガス
吹き込みが不均一になると、粒子の流動が悪い個所のノ
ズルから下方へ還元鉱が落鉱し、操業が不安定になる。[Problem to be solved by the invention] However, although such measures can be expected to have a considerable effect when the reducing gas used is a clean gas, as in the case of the above-mentioned smelting reduction method, the smelting reduction furnace When exhaust gas is injected as a reducing gas, this exhaust gas contains a large amount of impurities such as dust and metal oxide fumes generated during the melting reduction process, and these impurities adhere to the injection port and cause blockages. death,
Gas blowing becomes uneven, or ventilation becomes impossible, resulting in a situation where operations have to be temporarily stopped. If gas injection becomes uneven, reduced ore will fall downward from the nozzle in areas where particle flow is poor, making operations unstable.
【0007】本発明において解決すべき課題は、このよ
うなフュームを多量に含有する還元ガスであっても、流
動層からの落鉱を防止できると共に、付着物の形成を最
小に抑えて流動層の操業を安定して行うことができる流
動層の炉下部構造を完成することにある。The problem to be solved by the present invention is to prevent ore from falling from the fluidized bed even with a reducing gas containing a large amount of fumes, and to minimize the formation of deposits in the fluidized bed. The aim is to complete a fluidized bed furnace lower structure that allows stable operation.
【0008】[0008]
【課題を解決するための手段】本発明は、流動層内に還
元ガスを吹き込む炉下部構造として、ノズルの下方位置
に落鉱排出機構を設け、この落鉱排出機構の上方位置に
還元ガス導入管を接続したことを特徴とする。[Means for Solving the Problems] The present invention provides a furnace lower structure for blowing reducing gas into a fluidized bed, and provides a falling ore discharge mechanism at a position below a nozzle, and introduces reducing gas into a position above this falling ore discharge mechanism. It is characterized by connecting pipes.
【0009】具体的な落鉱排出機構の取付け位置として
は、流動層還元装置の還元ガスヘッダーの下方位置に総
括的な装置として設けることもできるし、また、各吹き
込みノズルの下方に個別の排出機構を設けることもでき
る。[0009] As for the specific installation position of the falling ore discharge mechanism, it can be installed as a comprehensive device below the reducing gas header of the fluidized bed reducing device, or it can be installed as an individual device below each blow nozzle. A mechanism may also be provided.
【0010】また、落鉱排出機構としては、一旦落鉱を
収納するホッパーにロック機構を設けたロックホッパー
を設けることができる。[0010] Further, as the fallen ore discharge mechanism, a lock hopper can be provided in which a locking mechanism is provided on the hopper that temporarily stores the fallen ore.
【0011】[0011]
【作用】本発明は、ノズル内への落鉱防止よりは、積極
的にノズル内への落鉱を回収することで、この循環・再
利用を図るもので、これによって、還元ガス吹き込みノ
ズルの構造として、最も吹き込み効率の良いシンプルな
円筒状のもの、しかも、径が比較的大きいものの使用が
可能である。これによって、ノズルへの付着物の形成を
最小に抑えることができ、流動層の安定操業が達成でき
る。[Operation] Rather than preventing ore from falling into the nozzle, the present invention aims to circulate and reuse the ore by actively collecting the ore into the nozzle. As for the structure, it is possible to use a simple cylindrical structure with the highest blowing efficiency and a relatively large diameter. Thereby, the formation of deposits on the nozzle can be minimized and stable operation of the fluidized bed can be achieved.
【0012】また、炉が緊急停止した時にノズルより上
方にある還元鉱石がノズルから落鉱しても、落鉱排出機
構を用いることにより、容易に且つ迅速に系外へ排出で
きるため、再立ち上げが可能となる。[0012] Furthermore, even if the reduced ore above the nozzle falls out of the nozzle during an emergency shutdown of the furnace, by using the falling ore discharge mechanism, it can be easily and quickly discharged from the system, so that it can be restarted. It is possible to raise it.
【0013】落鉱排出機構として、ロックホッパーを使
用することによって、落鉱量が一定量以上になったとき
、上方の仕切弁を閉にしてホッパー内へ落鉱を収納する
。ホッパー内にはN2 パージガスが導入されており、
ホッパー内をN2 パージして炉内の有害な還元ガスの
侵入を防止する。その後、上方の弁を閉にして下方の弁
を開いて系外へ落鉱を排出する。これにより落鉱処理が
スムーズに行える。ホッパー内をN2 パージすること
によって、落鉱の排出時に装置内のガスが装置外にリー
クすることがない。By using a rock hopper as the falling ore discharge mechanism, when the amount of falling ore exceeds a certain amount, the upper gate valve is closed and the falling ore is stored in the hopper. N2 purge gas is introduced into the hopper,
Purge the inside of the hopper with N2 to prevent harmful reducing gas from entering the furnace. After that, the upper valve is closed and the lower valve is opened to discharge the fallen ore out of the system. This allows for smooth treatment of fallen ore. By purging the inside of the hopper with N2, the gas inside the device will not leak out of the device when discharging fallen ore.
【0014】[0014]
【実施例】以下本発明の実施例として、本発明を循環型
の流動層還元装置に適用した例を示す。[Example] As an example of the present invention, an example in which the present invention is applied to a circulating type fluidized bed reduction apparatus will be shown below.
【0015】図1は、本発明の第1の実施例として、落
鉱排出機構を還元ガスヘッダーの下方位置に設けた例を
示す。FIG. 1 shows a first embodiment of the present invention in which a fallen ore discharge mechanism is provided at a position below a reducing gas header.
【0016】同図において、循環流動還元装置20は鉱
石供給管21と還元鉱石排出管22を有するライザー2
3と、サイクロン24とダウンカマー25とから構成さ
れる外部粒子循環装置26とからなり、それぞれライザ
ー23と外部粒子循環装置26とは上部においては循環
導入管27によって、下部においては連結管28で連結
されている。29はライザー23への不活性のキャリア
ガス導入管であって、同導入管29からのキャリアガス
は、一旦キャリアガスヘッダー30に導入され、そこか
ら通気性のノズル支持板31を経てライザー23内に噴
出される。図示されない溶融還元炉から、還元ガス導入
管32によってライザー23内に導入された還元ガスは
、床底板33から下方に位置する還元ガスのヘッダー3
4を経て、床底板33面に多数均一に配置したノズル3
5からライザー23内に導入される。In the figure, a circulating fluid reduction device 20 includes a riser 2 having an ore supply pipe 21 and a reduced ore discharge pipe 22.
3, and an external particle circulation device 26 consisting of a cyclone 24 and a downcomer 25, and the riser 23 and external particle circulation device 26 are connected to each other by a circulation introduction pipe 27 in the upper part and a connecting pipe 28 in the lower part. connected. Reference numeral 29 denotes an inert carrier gas introduction pipe to the riser 23. The carrier gas from the introduction pipe 29 is once introduced into the carrier gas header 30, and from there passes through the breathable nozzle support plate 31 into the riser 23. It is squirted. Reducing gas is introduced into the riser 23 from a melting reduction furnace (not shown) through a reducing gas introduction pipe 32, and is supplied to a reducing gas header 3 located below the floor bottom plate 33.
4, a large number of nozzles 3 are uniformly arranged on the 33 sides of the floor bottom plate.
5 into the riser 23.
【0017】10は本発明に係る落鉱排出装置を示す。
この落鉱排出装置10は底面を逆円錐状に形成した還元
ガスのヘッダー34の最低位置に設けた排出管1に入口
弁2を介して設けたホッパー3を有する。そして、この
ホッパー3にはパージ用N2 ガスを導入するためのパ
ージガス導入管4と排出のための出口弁5とが設けられ
ている。Reference numeral 10 shows a fallen ore discharge device according to the present invention. This ore discharge device 10 has a hopper 3 which is connected via an inlet valve 2 to a discharge pipe 1 which is provided at the lowest position of a reducing gas header 34 whose bottom surface is shaped like an inverted cone. The hopper 3 is provided with a purge gas introduction pipe 4 for introducing purge N2 gas and an outlet valve 5 for discharging it.
【0018】この装置において、還元ガスはヘッダー3
4を経て、ノズル35から流動層ライザー23内に吐出
される。鉱石供給管21から流動層内に供給された粉鉱
石は還元ガスによって還元される。この還元ガスの吐出
過程で粉鉱石の中の比較的粗粒のものが、ノズル35か
らヘッダー34内に落下して蓄積する。落鉱がヘッダー
34内に一定量以上蓄積したとき、ホッパーの入口弁2
が開き、落鉱はホッパー3内に投入される。このホッパ
ー3内へはパージガス導入管4からN2 ガスが供給さ
れており、これにより、ホッパー3内のガスをパージし
ている。落鉱が投入された後、入口弁2を閉にし、その
後、出口弁5を開にして系外に排出して再利用する。[0018] In this device, the reducing gas is supplied to the header 3.
4, and is discharged from the nozzle 35 into the fluidized bed riser 23. The fine ore supplied into the fluidized bed from the ore supply pipe 21 is reduced by the reducing gas. During the discharge process of this reducing gas, relatively coarse particles in the fine ore fall from the nozzle 35 into the header 34 and accumulate there. When a certain amount or more of fallen ore accumulates in the header 34, the hopper inlet valve 2
is opened and the fallen ore is thrown into the hopper 3. N2 gas is supplied into the hopper 3 from a purge gas introduction pipe 4, thereby purging the gas inside the hopper 3. After the fallen ore is thrown in, the inlet valve 2 is closed, and then the outlet valve 5 is opened to discharge it out of the system and reuse it.
【0019】図2は、本発明の他の実施例として、落鉱
排出機構を還元ガス吹き込みノズル自体に設けた例を示
す。FIG. 2 shows another embodiment of the present invention in which the ore discharge mechanism is provided in the reducing gas injection nozzle itself.
【0020】この例においては、落鉱排出装置10は、
比較的長く形成されたノズル35への還元ガス導入管3
2の下方に位置する排出管1に落鉱溜め6が設けられて
おりさらにその下方に入口弁2を介して設けたホッパー
3を有する。そして、このホッパー3にはパージ用N2
ガスを導入するためのパージガス導入管4と排出のた
めの出口弁5とが設けられており、上記図1と同様に操
作される。[0020] In this example, the ore discharge device 10 includes:
Reducing gas introduction pipe 3 to the nozzle 35 formed relatively long
A sump 6 is provided in a discharge pipe 1 located below the sump 2, and a hopper 3 is provided below the sump 6 via an inlet valve 2. And this hopper 3 has N2 for purging.
A purge gas introduction pipe 4 for introducing gas and an outlet valve 5 for discharging gas are provided, and are operated in the same manner as in FIG. 1 above.
【0021】[0021]
【発明の効果】本発明によって、以下の効果を奏する。[Effects of the Invention] The present invention provides the following effects.
【0022】(1)落鉱処理を円滑に行うことができる
ので、流動層装置の操業性が向上する。(1) Since the treatment of fallen ore can be carried out smoothly, the operability of the fluidized bed apparatus is improved.
【0023】(2)系外への流動層内のガスの流出量が
少なく、装置全体の安全性が高い。(2) The amount of gas in the fluidized bed flowing out of the system is small, and the safety of the entire apparatus is high.
【0024】(3)ノズル孔への詰まりによる流動層還
元装置の機能が停止することがなく、操業性が向上する
。(3) The function of the fluidized bed reducing apparatus does not stop due to clogging of the nozzle hole, and operability is improved.
【図1】本発明の第1の実施例を示すもので、本発明に
係る落鉱排出機構をヘッダー底部に設けた例を示す。FIG. 1 shows a first embodiment of the present invention, and shows an example in which a falling ore discharge mechanism according to the present invention is provided at the bottom of a header.
【図2】本発明の他の実施例を示すもので、本発明に係
る落鉱排出機構を各吹き込みノズルに直結して設けた例
を示す。FIG. 2 shows another embodiment of the present invention, in which an ore discharge mechanism according to the present invention is directly connected to each blowing nozzle.
10 排出装置 20
循環型の流動層還元装置
21 鉱石供給管 22
還元鉱石排出口23 ライザー
24 サイクロン25 ダウンカマー
26 外部粒子循環装置27 循
環導入管 28 連結管29
キャリアガス導入管 30 キャリアガス
ヘッダー10 Discharge device 20
Circulating fluidized bed reduction device 21 Ore supply pipe 22
Reduced ore discharge port 23 riser
24 Cyclone 25 Downcomer
26 External particle circulation device 27 Circulation introduction pipe 28 Connecting pipe 29
Carrier gas introduction pipe 30 Carrier gas header
Claims (1)
を複数本配設した炉下部構造において、該還元ガスノズ
ルの下方へガスヘッダーを設け、前記ガスヘッダーの下
端部に、両端に仕切弁を設けたホッパーで構成される落
鉱排出機構を備えたことを特徴とする流動層還元炉の炉
下部構造。1. In a furnace lower structure in which a plurality of reducing gas nozzles are arranged at the bottom of a fluidized bed reduction furnace, a gas header is provided below the reducing gas nozzles, and gate valves are provided at both ends at the lower end of the gas header. The lower structure of a fluidized bed reduction furnace is characterized by being equipped with a falling ore discharge mechanism consisting of a hopper.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6667291A JPH04301020A (en) | 1991-03-29 | 1991-03-29 | Structure for furnace lower part in fluidized bed reduction furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6667291A JPH04301020A (en) | 1991-03-29 | 1991-03-29 | Structure for furnace lower part in fluidized bed reduction furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04301020A true JPH04301020A (en) | 1992-10-23 |
Family
ID=13322640
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6667291A Pending JPH04301020A (en) | 1991-03-29 | 1991-03-29 | Structure for furnace lower part in fluidized bed reduction furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04301020A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001053544A1 (en) * | 2000-01-20 | 2001-07-26 | Voest-Alpine Industrieanlagenbau Gmbh & Co | Fluidized bed aggregate for reducing oxide-containing material |
US8964249B2 (en) | 2011-07-14 | 2015-02-24 | Ricoh Company, Limited | Image test apparatus, image test system, and image test method for testing a print image based on master image data |
-
1991
- 1991-03-29 JP JP6667291A patent/JPH04301020A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001053544A1 (en) * | 2000-01-20 | 2001-07-26 | Voest-Alpine Industrieanlagenbau Gmbh & Co | Fluidized bed aggregate for reducing oxide-containing material |
US8964249B2 (en) | 2011-07-14 | 2015-02-24 | Ricoh Company, Limited | Image test apparatus, image test system, and image test method for testing a print image based on master image data |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2635544C (en) | Method for manufacturing molten irons and apparatus for manufacturing molten irons | |
RU2070936C1 (en) | Method and device for treatment of gases and solid particles in fluidized bed | |
JPH0631345B2 (en) | Method and apparatus for gasifying or burning solid carbonaceous material | |
JPH02290406A (en) | Apparatus for gasification or combustion of solid carbonaceous materials in circulating fluidized bed reactors | |
JPH09506935A (en) | Fluidized bed type reducing apparatus for iron ore particles and method for reducing iron ore particles using the apparatus | |
US5634516A (en) | Method and apparatus for treating or utilizing a hot gas flow | |
RU2077595C1 (en) | Method and apparatus (alternatives) for producing iron and/or alloys thereof from iron oxide materials | |
US5759495A (en) | Method and apparatus for treating hot gases | |
AU655699B2 (en) | Process and apparatus for cooling hot solids coming from a fluidized bed reactor | |
US7803268B2 (en) | Method and plant for producing low-temperature coke | |
RU2195501C1 (en) | Fluidized-bed reactor preventing ground iron ore from sticking and method proposed for this reactor | |
JPH04301020A (en) | Structure for furnace lower part in fluidized bed reduction furnace | |
KR100431863B1 (en) | Apparatus for cleaning dispersion plate in fluid-bed reducing furnace | |
RU2218418C2 (en) | Device for prevention of disruption of fluidized bed designed for reduction reactor with fluidized bed | |
JP4234204B2 (en) | Equipment for selective injection of fine particles into the reactor | |
KR100711776B1 (en) | Molten iron | |
US7144447B2 (en) | Method and device for treating particulate material | |
UA46849C2 (en) | MELTING AND GASIFICATION APPARATUS FOR OBTAINING METAL MELT AND INSTALLATION FOR METAL MELTING | |
RU2195500C2 (en) | Device for two-stage reduction of iron ore fines in fluidized layer and method of reduction of iron ore fines | |
KR100321051B1 (en) | Apparatus for manufacturing pig iron and method therefor | |
RU2165984C2 (en) | Method of charging metal carriers into melting-gasifying zone and plant for method embodiment | |
JP2916516B2 (en) | Method for producing liquid metal from metal oxide fine particles and reduction smelting furnace for carrying out this method | |
KR100321052B1 (en) | Apparatus for classifying dust supplied to melter gasifier and method therefor | |
CA2222958A1 (en) | Method of and apparatus for treating process gases in a circulating fluidized bed | |
KR100376499B1 (en) | Apparatus for discharging through standpipe in fluidized bed reactor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 19990402 |