JPH0613251Y2 - Iron ore fluidized bed reduction device - Google Patents
Iron ore fluidized bed reduction deviceInfo
- Publication number
- JPH0613251Y2 JPH0613251Y2 JP997588U JP997588U JPH0613251Y2 JP H0613251 Y2 JPH0613251 Y2 JP H0613251Y2 JP 997588 U JP997588 U JP 997588U JP 997588 U JP997588 U JP 997588U JP H0613251 Y2 JPH0613251 Y2 JP H0613251Y2
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- bed reduction
- separator
- iron ore
- ore
- 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 - Lifetime
Links
Landscapes
- Manufacture Of Iron (AREA)
Description
【考案の詳細な説明】 [産業上の利用分野] 本考案は鉱石の流動層還元装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial application] The present invention relates to a fluidized bed reduction apparatus for ore.
[従来の技術] 鉄鉱石を還元して溶銑を製造するために、高炉を使用す
る方法、シャフト炉で還元した鉄鉱石を電気炉で溶解す
る方法等が従来から採用されている。[Prior Art] In order to reduce iron ore to produce hot metal, a method of using a blast furnace, a method of melting iron ore reduced in a shaft furnace in an electric furnace, and the like have been conventionally used.
このような従来の溶銑製造技術に代わるものとして、溶
融還元法が注目を浴びている。この方法で使用する溶融
還元炉は、使用する原料に制約を受けることなく、より
小規模な設備により鉄系合金の溶湯を製造することを目
的として開発されたものである。The smelting reduction method has been attracting attention as an alternative to such conventional hot metal production technology. The smelting reduction furnace used in this method was developed for the purpose of producing a molten iron-based alloy by a smaller-scale facility without being restricted by the raw material used.
本発明者等は、先に特開昭61-64807号公報にこのような
溶融還元法の一つを提案した。The present inventors previously proposed one of such smelting reduction methods in Japanese Patent Laid-Open No. 61-64807.
このような溶融還元法においては、特にその開発過程か
ら明らかなように、使用可能な原料の範囲の拡大、還元
効率の向上溶融還元炉における積錬反応の促進を如何に
して達成するかの課題がある。In such a smelting reduction method, as is clear from the development process, the range of usable raw materials is expanded, and the reduction efficiency is improved. There is.
[考案が解決しようとする課題] ところで、溶融還元炉に供給する還元鉱は1mmφ以下は
キャリアガスとともにインジェクション供給され、1mm
φ超は上部から投入供給される。[Problems to be solved by the invention] By the way, the reduction ore supplied to the smelting reduction furnace is injection-supplied with carrier gas up to 1 mmφ
Exceeding φ is supplied from above.
しかしながら循環流動層では、細粒、粗粒が混合状態で
循環流するので、粒度別に分離することは困難であっ
た。However, in the circulating fluidized bed, since fine particles and coarse particles circulate in a mixed state, it was difficult to separate them according to particle size.
本考案は、還元鉱石を粒度別に回収する鉄鉱石流動層還
元装置を提供するものである。The present invention provides an iron ore fluidized bed reduction apparatus for recovering reduced ores by particle size.
[課題を解決するための手段] 本考案は、還元鉱石を製造する装置において、流動層還
元炉に原料ホッパー及び排出口を設け、外部粒子循環装
置を付設し、外部粒子循環装置に、前段粗細分離器及び
後段固気分離器を設け、各分離器にニューマチックフィ
ーダを介して排出口を設けると共に、各分離器は、排出
管を介して流動層還元炉に連接されている鉄鉱石流動還
元装置である。[Means for Solving the Problems] The present invention relates to a device for producing reduced ore, in which a raw material hopper and a discharge port are provided in a fluidized bed reduction furnace, an external particle circulation device is attached, and an external particle circulation device is provided with a pre-stage coarse particle A separator and a post-stage solid-gas separator are provided, each separator is provided with a discharge port via a pneumatic feeder, and each separator is connected to a fluidized bed reduction furnace via a discharge pipe. It is a device.
以下に図面について本考案を説明する。The present invention will be described below with reference to the drawings.
第1図は本考案の説明図である。図において流動層還元
炉15は原料ホッパー16及び排出口30を有し、還元ガス吹
込ノズル18が設けられる。17は切出し弁である。FIG. 1 is an explanatory view of the present invention. In the figure, a fluidized bed reduction furnace 15 has a raw material hopper 16 and a discharge port 30, and is provided with a reducing gas injection nozzle 18. Reference numeral 17 is a cutoff valve.
本考案の外部粒子循環装置11は前段粗細分離器(以下前
段サイクロンという)20及び後段固気分離器(以下後段
サイクロンという)21が併設されている。The external particle circulation device 11 of the present invention is provided with a pre-stage coarse / fine separator (hereinafter referred to as a pre-stage cyclone) 20 and a post-stage solid gas separator (hereinafter referred to as a post-stage cyclone) 21.
各サイクロンはニューマチックフィーダ25,26を介して
排出口31,32をそれぞれ設けている。Each cyclone is provided with outlets 31 and 32 through pneumatic feeders 25 and 26, respectively.
本考案の還元鉱石の製造装置10は以上により構成される
が、原料ホッパー16から供給される原料鉱石は流動層還
元炉15において、還元ガス圧入下のもとに流動層を形成
して還元反応をうける。還元鉱石は還元炉から排ガスと
ともに前段サイクロン20に導入され、一方粗大粒鉱石は
排出口30からバルブ17を介して適量回収される。The apparatus 10 for producing reduced ore of the present invention is constituted by the above, but the raw ore supplied from the raw material hopper 16 forms a fluidized bed in the fluidized bed reduction furnace 15 under the injection of reducing gas to carry out the reduction reaction. Receive The reduced ore is introduced from the reduction furnace together with the exhaust gas into the preceding cyclone 20, while the coarse-grained ore is recovered from the discharge port 30 through the valve 17 in an appropriate amount.
前段サイクロン20で粗細分離された粗粒分は、ニューマ
チックフィーダ25を介して排出口31から回収され、細粒
分はガスとともに後段サイクロン21に導入され、更に分
級され、完全に固気分級され、ニューマチックフィーダ
26を介して排出口32から回収される。The coarse particles that have been coarsely separated by the pre-stage cyclone 20 are recovered from the outlet 31 via the pneumatic feeder 25, and the fine particles are introduced into the post-stage cyclone 21 together with the gas, further classified, and completely solidified. , Pneumatic feeder
It is recovered from the outlet 32 via 26.
第2図はニューマチックフィーダ25の一例を示す。FIG. 2 shows an example of the pneumatic feeder 25.
前段サイクロン20の導管41は滞留域44、導管42を介して
排出管40に導入される。43は分割ベンダーを示し、ガス
系18から還元ガスが圧入される。粗粒分は導管41の上流
から図示しない導管を介して、ニューマチックフィーダ
25を操作して回収される。The conduit 41 of the preceding cyclone 20 is introduced into the discharge pipe 40 via the retention area 44 and the conduit 42. Reference numeral 43 indicates a split bender, and reducing gas is injected from the gas system 18. Coarse particles are collected from the upstream side of the conduit 41 through a conduit (not shown) to the pneumatic feeder.
25 is recovered and collected.
後段サイクロン21に設けられるニューマチックフィーダ
26は特に図示しないが、上記ニューマチックフィーダ25
と同一でよい。Pneumatic feeder installed in the rear cyclone 21
26 is not particularly shown, but the pneumatic feeder 25
Can be the same as.
[考案の効果] 本考案は流動層還元炉に外部粒子循環装置を付設し、外
部粒子循環装置として、前段マイクロン及び後段サイク
ロンを併設したので、流動層還元炉の排出口から粗大粒
の鉱石、前段サイクロンから粗粒鉱石、後段サイクロン
から細粒鉱石を還元鉱石として、それぞれ各別に回収す
ることが可能である。[Advantage of the Invention] In the present invention, an external particle circulation device is attached to the fluidized bed reduction furnace, and a front stage micron and a latter stage cyclone are provided as external particle circulation devices. It is possible to separately collect coarse ores from the former cyclone and fine ores from the latter cyclone as reduced ores, respectively.
従って溶融還元炉に適正粒度の還元鉱石を供給できるの
で、その実用的価値は大である。Therefore, it is possible to supply the reduction ore of an appropriate grain size to the smelting reduction furnace, and its practical value is great.
第1図は本考案の説明図、第2図は本考案の一部説明図
である。 10…還元鉱石製造装置 11…外部粒子循環装置、15…流動層還元炉 20…前段サイクロン、21…後段サイクロンFIG. 1 is an explanatory view of the present invention, and FIG. 2 is a partial explanatory view of the present invention. 10 ... Reduced ore manufacturing equipment 11 ... External particle circulation equipment, 15 ... Fluidized bed reduction furnace 20 ... Pre-stage cyclone, 21 ... Post-stage cyclone
Claims (1)
還元炉に原料ホッパー及び排出口を設け、外部粒子循環
装置を付設し、外部粒子循環装置に、前段粗細分離器及
び後段固気分離器を設け、各分離器にニューマチックフ
ィーダを介して排出口を設けると共に、各分離器は、排
出管を介して流動層還元炉に連接されていることを特徴
とする鉄鉱石流動層還元装置。In an apparatus for producing reduced ore, a fluidized bed reduction furnace is provided with a raw material hopper and a discharge port, an external particle circulation device is attached, and the external particle circulation device is provided with a pre-stage coarse / fine separator and a post-stage solid gas separator. An iron ore fluidized bed reduction apparatus, wherein each separator is provided with a discharge port via a pneumatic feeder, and each separator is connected to a fluidized bed reduction furnace via a discharge pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP997588U JPH0613251Y2 (en) | 1988-01-28 | 1988-01-28 | Iron ore fluidized bed reduction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP997588U JPH0613251Y2 (en) | 1988-01-28 | 1988-01-28 | Iron ore fluidized bed reduction device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01114653U JPH01114653U (en) | 1989-08-02 |
| JPH0613251Y2 true JPH0613251Y2 (en) | 1994-04-06 |
Family
ID=31217196
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP997588U Expired - Lifetime JPH0613251Y2 (en) | 1988-01-28 | 1988-01-28 | Iron ore fluidized bed reduction device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0613251Y2 (en) |
-
1988
- 1988-01-28 JP JP997588U patent/JPH0613251Y2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01114653U (en) | 1989-08-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR960023101A (en) | Reduction furnace for reducing iron ore in manufacturing molten pig iron and molten steel and method for reducing iron ore using the same | |
| CN108380360B (en) | Production process of steel slag and iron fine powder | |
| ZA200007676B (en) | A fluidized bed reactor for preventing the fine ore from sticking therein and method therefor. | |
| US4447261A (en) | Method for separating non-ferrous metals from iron-containing materials | |
| JP2608736B2 (en) | Method of charging exhaust gas dust in smelting reduction furnace | |
| CN111020225A (en) | Novel furnace for simultaneous mixed smelting of antimony ore in same hearth through volatilization smelting and flash smelting and smelting method thereof | |
| JPH01184211A (en) | Fluidized bed reduction device for ore | |
| AU717927B2 (en) | Two step twin-single fluidized bed type pre-reduction apparatus for pre-reducing fine iron ore, and method therefor | |
| JP2562172B2 (en) | Iron ore fluidized bed reduction device | |
| JPH02175809A (en) | Smelting reduction iron making method | |
| JP2579785B2 (en) | Pre-reduction device for smelting reduction | |
| JPH0699734B2 (en) | Circulating fluidized bed type pre-reduction furnace for fine iron ore | |
| JPH077313Y2 (en) | Pre-reduction equipment for smelting reduction of iron ore | |
| JPH06145749A (en) | Ore reduction method by circulating fluidized bed | |
| CN222821606U (en) | A circulating belt type continuous roasting system with adjustable and controllable atmosphere and temperature | |
| Prokhorov et al. | The Use of Waste Materials Arising From Metallurgical Production in Sinter Plants and Blast Furnaces | |
| JPH0723491B2 (en) | Circulating fluidized bed preliminary reduction device | |
| JP2003505240A (en) | Beneficiation process of granular ore | |
| JPH10238957A (en) | Circulating fluidized bed reduction device | |
| JPH0328305A (en) | Fluidized bed type pre-reduction furnace for iron or nonferrous ore | |
| JPS6311610A (en) | Prereduction device for iron ore | |
| JPH0792343B2 (en) | Iron ore preliminary reduction device | |
| JPH01114691A (en) | Iron ore fluidized-bed reducing device | |
| Kepplinger | Process for the production of molten pig iron and plant for carrying out the process | |
| JPH0331412A (en) | Fluidized bed type prereduction furnace for iron or non-ferrous ore |