JPH06180186A - Gas injection device for circulating fluidization reduction device - Google Patents
Gas injection device for circulating fluidization reduction deviceInfo
- Publication number
- JPH06180186A JPH06180186A JP32963892A JP32963892A JPH06180186A JP H06180186 A JPH06180186 A JP H06180186A JP 32963892 A JP32963892 A JP 32963892A JP 32963892 A JP32963892 A JP 32963892A JP H06180186 A JPH06180186 A JP H06180186A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- fluidized bed
- gas injection
- injection device
- reduction furnace
- 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
- Crucibles And Fluidized-Bed Furnaces (AREA)
Abstract
(57)【要約】
【目的】 流動層還元炉に還元ガスを均一分散するガス
吹込み装置を提供する。
【構成】 ウインドボックスを有する流動層還元炉に固
気分離器とダウンカマーとを並設し、複数の導入管によ
り流動層還元炉とウインドボックスとを連結するととも
に、それぞれの導入管内にオリフィスを設けたことを特
徴とする循環流動還元装置のガス吹込み装置。
(57) [Summary] [Objective] To provide a gas injection device for uniformly dispersing a reducing gas in a fluidized bed reduction furnace. [Structure] A solid-gas separator and a downcomer are installed in parallel in a fluidized bed reduction furnace having a windbox, and the fluidized bed reduction furnace and the windbox are connected by a plurality of introduction pipes, and an orifice is provided in each introduction pipe. A gas injection device of a circulating fluidization reduction device characterized by being provided.
Description
【0001】[0001]
【産業上の利用分野】本発明は循環流動還元装置のガス
吹込み装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas injection device for a circulating fluidization reduction device.
【0002】[0002]
【従来の技術】鉄鉱石を装入した流動層還元炉内に還元
ガスを主要な流動ガスとして導入して流動還元せしめ、
排出された還元鉱石とガスとを固気分離器で分離し、還
元鉱石を炉の下方に循環供給する循環流動還元法が知ら
れている。本発明者は、さきに特開平1−244277
号において、高循環量高速流動装置として主流動化ガス
を、循環粒子供給合流部の上方に開口させ、合流部付近
の傾斜管および合流部下部より補助ガスを吹込み高循環
量を得る流動装置を提案した。2. Description of the Related Art A reducing gas is introduced as a main fluidizing gas into a fluidized-bed reduction furnace charged with iron ore for fluidized reduction.
A circulating fluidized reduction method is known in which the reduced ore and the gas that have been discharged are separated by a solid-gas separator, and the reduced ore is circulated and supplied below the furnace. The inventor of the present invention has previously mentioned that the Japanese Patent Application Laid-Open No. 1-244277.
No. 6, the main fluidizing gas as a high-circulation-amount high-speed flow device is opened above the circulating particle supply confluence part, and the auxiliary gas is blown from the inclined pipe near the confluence part and the lower part of the confluence part to obtain a high circulation amount Proposed.
【0003】更に特開平3−294410号の循環流動
層還元装置のガス吹き込み装置において、主流動化ガス
の導入管先端にガス旋回用フィンを設けた循環流動層還
元装置を提案した。Further, in the gas blowing apparatus of the circulating fluidized bed reducing apparatus of Japanese Patent Laid-Open No. 3-294410, a circulating fluidized bed reducing apparatus was proposed in which a gas swirling fin was provided at the tip of the main fluidizing gas introduction pipe.
【0004】一方生産性の向上、設備費の低減を狙い、
流動層還元炉の大型化が図られているが、1本の主流動
ガス導入管では流動層還元炉内に還元ガスを均一分散さ
せることは困難となり、複数の主流動ガス導入管を設け
ることが志向されてきた。しかし、炉内の流動状態によ
っては複数設けた主流動ガス導入管のある管のみガスが
通過し、それ以外の管はガスの通過量が少なく炉内の鉱
石がその管を伝ってウインドボックスに落下し、効率の
低下はもとより安定的な操業が継続し得ない状況が生じ
る。On the other hand, with the aim of improving productivity and reducing equipment costs,
The size of the fluidized bed reduction furnace has been increased, but it is difficult to uniformly disperse the reducing gas in the fluidized bed reduction furnace with one main fluidized gas introduction pipe, and multiple main fluidized gas introduction pipes must be provided. Has been aimed at. However, depending on the flow condition in the furnace, the gas passes through only the pipe with the multiple main flow gas introduction pipes, and the other pipes have a small amount of gas passage, and the ore in the furnace travels along the pipe to the windbox. There is a situation in which a stable operation cannot be continued as well as a drop in efficiency.
【0005】[0005]
【発明が解決しようとする課題】本発明は流動層還元炉
に還元ガスを均一分散するガス吹込み装置を提供するも
のである。SUMMARY OF THE INVENTION The present invention provides a gas injection device for uniformly dispersing a reducing gas in a fluidized bed reduction furnace.
【0006】[0006]
【課題を解決するための手段】本発明の要旨はウインド
ボックスを有する流動層還元炉に固気分離器とダウンカ
マーとを並設し、複数のガス導入管により流動層還元炉
とウインドボックスとを連結するとともに、それぞれの
導入管内にオリフィスを設けたことを特徴とする循環流
動還元装置のガス吹込み装置である。更に本発明は導入
管域の圧力損失/流動層域の圧力損失≧20%のオリフ
ィスを導入管に設けた循環流動還元装置のガス吹込み装
置である。SUMMARY OF THE INVENTION The gist of the present invention is to provide a fluidized bed reduction furnace having a windbox with a solid-gas separator and a downcomer in parallel, and to provide a fluidized bed reduction furnace and a windbox with a plurality of gas introduction pipes. And an orifice provided in each of the introduction pipes. Further, the present invention is a gas injection device of a circulating fluidization reduction device in which an orifice having a pressure loss in the introduction pipe region / a pressure loss in the fluidized bed region ≧ 20% is provided in the introduction pipe.
【0007】[0007]
【作用】以下本発明を図面に基づいて詳述する。図1に
おいて鉄鉱石を装入した流動層還元炉1内に還元ガス2
を主要な流動ガスとして複数のガス導入管3を通して、
ウインドボックス4から炉内に導入する。流動還元した
還元鉱石を炉の上方で固気分離器5でガスと分離して、
還元鉱石はダウンカマー6を介して炉の下方に循環供給
し、一部は製品還元鉱石排出口7より取り出す。図2は
本発明の要部でガス導入管3において、ガス導入ノズル
3−1,3−2,3−3を有し、ウインドボックス4と
流動層還元炉1とを結合する主要ガスの導入管3内にオ
リフィス11を設け、管途中の断面積d2 をガス吹出し
口の断面積d1 より小さくする。12は支持板である。The present invention will be described in detail below with reference to the drawings. In FIG. 1, a reducing gas 2 is placed in a fluidized bed reduction furnace 1 charged with iron ore.
Through a plurality of gas introduction pipes 3 as a main flowing gas,
It is introduced into the furnace from the wind box 4. The reduced ore that has been fluidized and reduced is separated from the gas in the solid gas separator 5 above the furnace,
The reduced ore is circulated and supplied to the lower side of the furnace through the downcomer 6, and a part thereof is taken out from the product reduced ore discharge port 7. FIG. 2 is a main part of the present invention, in which the gas introduction pipe 3 has gas introduction nozzles 3-1, 3-2, 3-3, and the introduction of the main gas that connects the wind box 4 and the fluidized bed reduction furnace An orifice 11 is provided in the pipe 3 so that the cross-sectional area d 2 in the middle of the pipe is smaller than the cross-sectional area d 1 of the gas outlet. Reference numeral 12 is a support plate.
【0008】本発明は複数の主流動ガス導入管内のそれ
ぞれに、オリフィスを設け管内をガスが通過する時の通
気抵抗を増加させるので複数のガス導入管に均一に還元
ガスを分散することが可能となる。またその部分での圧
力降下を流動層部分の総圧力損失の20%以上とするこ
とにより、ウインドボックスに落下する落鉱はほとんど
なくなる。即ち図3に示すように流動層部分の圧力損失
Δp1 の20%以上の圧力降下をガス導入管部分で確保
することにより落鉱量はほとんどなくなり、ガス利用率
も向上する。In the present invention, an orifice is provided in each of the plurality of main flow gas introduction pipes to increase the ventilation resistance when the gas passes through the pipes, so that the reducing gas can be uniformly dispersed in the plurality of gas introduction pipes. Becomes Further, by setting the pressure drop in that portion to 20% or more of the total pressure loss in the fluidized bed portion, almost no falling ore is dropped into the windbox. That is, as shown in FIG. 3, by securing a pressure drop of 20% or more of the pressure loss Δp 1 in the fluidized bed portion in the gas introduction pipe portion, the amount of falling ore is almost eliminated and the gas utilization rate is improved.
【0009】従って本発明においてはガス導入管にオリ
フィスを形成するが、好ましくは、ガス導入管圧損Δp
2 /流動層圧損Δp1 ≧20%とする。本発明は主流動
ガス導入管内にオリフィスを設けることにより、特定の
管にガス流が集中することがなくなるとともに、流動状
態が変動しても各管より安定して均一なガスの供給が可
能となる。このため、流動層の各部分の鉱石が安定的に
還元ガスと接触し流動するため、炉全体が還元に有効に
活用でき、ガス利用率も向上する。Therefore, in the present invention, an orifice is formed in the gas introducing pipe, but preferably the gas introducing pipe pressure loss Δp.
2 / Fluidized bed pressure loss Δp 1 ≧ 20%. The present invention eliminates the concentration of gas flow in a specific pipe by providing an orifice in the main flow gas introduction pipe, and enables stable and uniform gas supply from each pipe even if the flow state changes. Become. For this reason, the ore in each part of the fluidized bed stably contacts and flows with the reducing gas, so that the entire furnace can be effectively utilized for the reduction and the gas utilization rate is improved.
【0010】[0010]
【発明の効果】本発明は複数の主流動ガス導入管を必要
とする大型の流動層還元炉においても、炉内全体に均一
にガスが分配でき、落鉱がなくなるとともに流動および
還元反応が安定的に進行し実用上極めて大きな効果を有
する。INDUSTRIAL APPLICABILITY The present invention can evenly distribute gas throughout the furnace even in a large fluidized bed reduction furnace that requires a plurality of main fluidized gas introduction pipes, eliminates falling mine, and stabilizes the flow and reduction reactions. Progresses rapidly and has an extremely great effect in practical use.
【図1】本発明の全体説明図である。FIG. 1 is an overall explanatory view of the present invention.
【図2】本発明の要部の説明図である。FIG. 2 is an explanatory diagram of a main part of the present invention.
【図3】ガス導入管圧損/流動層圧損と落鉱量、ガス利
用率との関係を示す図表である。FIG. 3 is a chart showing the relationship between gas inlet pipe pressure loss / fluidized bed pressure loss and the amount of orefall and gas utilization rate.
Claims (2)
に固気分離器とダウンカマーとを並設し、複数のガス導
入管により流動層還元炉とウインドボックスとを連結す
るとともに、それぞれの導入管内にオリフィスを設けた
ことを特徴とする循環流動還元装置のガス吹込み装置。1. A solid-gas separator and a downcomer are installed side by side in a fluidized bed reduction furnace having a windbox, and the fluidized bed reduction furnace and the windbox are connected by a plurality of gas introduction pipes, and in each of the introduction pipes. A gas injection device for a circulating fluidization reduction device, which is characterized in that an orifice is provided in the.
失≧20%のオリフィスを導入管に設けたことを特徴と
する請求項1記載の循環流動還元装置のガス吹込み装
置。2. The gas blowing device of the circulating fluidization reduction apparatus according to claim 1, wherein the introduction pipe is provided with an orifice having a pressure loss in the introduction pipe region / a pressure loss in the fluidized bed region ≧ 20%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32963892A JPH06180186A (en) | 1992-12-09 | 1992-12-09 | Gas injection device for circulating fluidization reduction device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32963892A JPH06180186A (en) | 1992-12-09 | 1992-12-09 | Gas injection device for circulating fluidization reduction device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06180186A true JPH06180186A (en) | 1994-06-28 |
Family
ID=18223582
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32963892A Pending JPH06180186A (en) | 1992-12-09 | 1992-12-09 | Gas injection device for circulating fluidization reduction device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06180186A (en) |
-
1992
- 1992-12-09 JP JP32963892A patent/JPH06180186A/en active Pending
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