JPH09194921A - Connecting tube for fluidized bed reduction furnace - Google Patents

Connecting tube for fluidized bed reduction furnace

Info

Publication number
JPH09194921A
JPH09194921A JP776596A JP776596A JPH09194921A JP H09194921 A JPH09194921 A JP H09194921A JP 776596 A JP776596 A JP 776596A JP 776596 A JP776596 A JP 776596A JP H09194921 A JPH09194921 A JP H09194921A
Authority
JP
Japan
Prior art keywords
fluidized bed
furnace
connecting tube
bed reduction
pressure guiding
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.)
Withdrawn
Application number
JP776596A
Other languages
Japanese (ja)
Inventor
Tatsuhiko Egashira
達彦 江頭
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP776596A priority Critical patent/JPH09194921A/en
Publication of JPH09194921A publication Critical patent/JPH09194921A/en
Withdrawn legal-status Critical Current

Links

Landscapes

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

Abstract

PROBLEM TO BE SOLVED: To provide a connecting tube, in which particles are not intruded, as the connecting tube for a fluidized bed reduction furnace. SOLUTION: The tip end part of the connecting tube 12 inside the fluidized bed reduction furnace is formed as a cylindrical shape sealing porous state tip part, and a flange 17 is arranged outside the furnace of the connecting tube 12, and this connecting tube is connected with a connecting tube 18 at the outside of the furnace. In the connecting tube 18 at the outside of the furnace, a purge pipe 20 for purging the tip end is arranged and a stop valve 21b for shutting off a pressure sensor at the time of purging to constitute the connecting tube in the fluidized bed reduction furnace.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、鉱石の還元、製鉄
ダストの還元あるいは脱亜鉛等を行う流動層還元装置に
関し、特に、炉の圧力センサーの導圧管に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fluidized bed reduction apparatus for reducing ore, reduction of iron making dust, dezincification, etc., and more particularly to a pressure guiding tube of a pressure sensor of a furnace.

【0002】[0002]

【従来の技術】従来の高炉等を使用した製銑技術に代わ
るものとして、溶融還元法が開発された。この方法は、
溶融還元炉で発生した排ガスを有効に利用するために、
排ガスを流動化ガスとして流動層還元炉に圧入して鉱石
を予熱、予備還元するものである(特開昭56ー105
409号参照)。
BACKGROUND ART A smelting reduction method has been developed as an alternative to the conventional iron making technique using a blast furnace or the like. This method
In order to effectively use the exhaust gas generated in the smelting reduction furnace,
The exhaust gas is injected as a fluidizing gas into a fluidized bed reduction furnace to preheat or pre-reduce the ore (JP-A-56-105).
No. 409).

【0003】また、製銑・製鋼等において、製錬炉の耐
火物に悪影響を及ぼす製鉄ダスト中の亜鉛、鉛等を除去
するため、製鉄ダストを流動層還元炉で処理することも
提案されている(特開平7ー18346号参照)。
Further, it has been proposed to treat iron-making dust in a fluidized bed reduction furnace in order to remove zinc, lead and the like in the iron-making dust that adversely affects refractory materials in the smelting furnace in iron and steel making and the like. (See JP-A-7-18346).

【0004】図3は従来の循環流動層還元装置の説明図
で、流動層還元装置には、流動層還元炉1、原料ホッパ
ー2からの鉱石、製鉄ダスト等の原料供給部3、成品の
排出部4及び還元ガス吹込部5が設けられている。流動
層還元炉1のガス出口6に設けられた外部粒子循環装置
7は、前段に1次サイクロン8、後段に2次サイクロン
9が設けられ、各サイクロンは下降管10a,10bで
ニューマッチクフィーダ11a,11bと連結されてい
る。
FIG. 3 is an explanatory view of a conventional circulating fluidized bed reduction apparatus. The fluidized bed reduction apparatus includes a fluidized bed reduction furnace 1, a raw material supply section 3 for ores and iron-making dust from a raw material hopper 2, and discharge of products. A section 4 and a reducing gas blowing section 5 are provided. The external particle circulation device 7 provided at the gas outlet 6 of the fluidized bed reduction furnace 1 is provided with a primary cyclone 8 at the front stage and a secondary cyclone 9 at the rear stage, and each cyclone is provided with a down-match pipe 10a, 10b in a new match feeder. It is connected to 11a and 11b.

【0005】原料ホッパー2から流動層還元炉1に供給
された鉱石、製鉄ダスト等の原料は、流動層還元炉1内
で炉底から供給される還元ガスの圧入により流動層が形
成され、還元されながらガスとともに上昇し、1次サイ
クロン8へ移動する。1次サイクロン8で、還元粒子
は、ガスと分離され、下降管10aを下降し、ニューマ
チックフィーダ11aを経て流動層還元炉1へ戻され
る。1次サイクロン8を出たガスは、2次サイクロン9
で還元粒子とガスに分離され、還元粒子は、下降管10
b、ニューマチックフィーダ11bを経て1次サイクロ
ン8の下降管10aに送られ、ガスは排ガス処理設備へ
導かれる。
The raw materials such as ore and iron-making dust supplied from the raw material hopper 2 to the fluidized bed reduction furnace 1 are reduced by the injection of the reducing gas supplied from the bottom of the fluidized bed reduction furnace 1 to form a fluidized bed. While rising, it rises with the gas and moves to the primary cyclone 8. In the primary cyclone 8, the reduced particles are separated from the gas, descended through the downcomer 10a, and returned to the fluidized bed reduction furnace 1 through the pneumatic feeder 11a. The gas leaving the primary cyclone 8 is the secondary cyclone 9
Is separated into reduced particles and gas, and the reduced particles are collected in the downcomer 10.
b, sent to the downcomer 10a of the primary cyclone 8 via the pneumatic feeder 11b, and the gas is guided to the exhaust gas treatment facility.

【0006】流動床還元炉では、操炉の主な操作因子と
して、差圧コントロールがある。そのため、炉壁の貫通
孔に導圧管を設けているが、炉内粒子濃度が大きく、高
速で粒子が炉内全体を振動しているので、図3に示すよ
うに、導圧管12は炉壁13内を60度程度の角度を付
けて貫通させている。
In the fluidized bed reduction furnace, the differential pressure control is a main operating factor of the operation. Therefore, a pressure guiding tube is provided in the through hole of the furnace wall, but since the particle concentration in the furnace is large and the particles vibrate in the entire furnace at high speed, as shown in FIG. The inside of 13 is penetrated at an angle of about 60 degrees.

【0007】[0007]

【発明が解決しようとする課題】しかしながら、炉内圧
が高く、圧力変動が激しいため、炉内の粒子濃度が大き
いことと相まって、導圧管内に粒子の侵入・排出が繰り
返され、還元された粉状粒子は付着性が大きいため、導
圧管壁に付着してしまい、ついには導圧管を閉塞してし
まい、逆洗パージしても鉄系粒子の密度が大きいことと
付着性が大きいことから、詰まりを解消することが困難
であった。その結果、圧力の測定が不可能となり、炉の
差圧コントロールができなくなる。
However, since the pressure inside the furnace is high and the fluctuations in pressure are severe, the concentration of particles in the furnace is high, and the particles are repeatedly invaded and discharged into the pressure guiding tube to reduce the powder. Since the particulate particles have a high adhesiveness, they adhere to the wall of the pressure guiding tube, and eventually block the pressure guiding tube, and the density of the iron-based particles is large and the adhesiveness is large even when backwashing and purging. , It was difficult to clear the blockage. As a result, the pressure cannot be measured and the differential pressure of the furnace cannot be controlled.

【0008】また、導圧管を傾斜して設置するために設
備的に複雑となるだけでなく、圧力測定精度も悪かっ
た。
Further, since the pressure guiding tube is installed at an inclination, not only the equipment becomes complicated, but also the pressure measurement accuracy is poor.

【0009】そこで、本発明は、流動層還元炉の導圧管
において、管内に粒子が侵入しないようにした導圧管を
提供するものである。
Therefore, the present invention provides a pressure guiding tube for a fluidized bed reduction furnace in which particles are prevented from entering the tube.

【0010】[0010]

【課題を解決するための手段】本発明は、流動層還元炉
内側の導圧管の先端部を多孔質状の先端封じの円筒形状
とし、前記導圧管の炉外側にフランジを設け、炉外の導
圧管と接続し、炉外の導圧管には先端をパージするパー
ジ管を設け、パージの時に圧力センサーとを遮断するス
トップ弁を設けたことを特徴とする。
According to the present invention, the tip of the pressure guiding tube inside the fluidized bed reduction furnace is made into a cylindrical shape with a porous tip closed, and a flange is provided outside the pressure guiding tube outside the furnace. It is characterized in that it is connected to a pressure guiding pipe, a purge pipe for purging the tip of the pressure guiding pipe outside the furnace is provided, and a stop valve for shutting off the pressure sensor at the time of purging is provided.

【0011】導圧管先端部を多孔質にすることによっ
て、μmオーダーの粒子でも侵入が防止でき、導圧管の
詰まり、閉塞が防止できる。
By making the tip of the pressure guiding tube porous, even particles of the order of μm can be prevented from entering, and clogging and clogging of the pressure guiding tube can be prevented.

【0012】導圧管に先端をパージするパージ管を設
け、定期的に圧力センサー側のストップ弁を閉めて、パ
ージガスを導入して先端部をパージして、多孔質部への
微粉の付着を防止する。
A purge pipe for purging the tip of the pressure guiding pipe is provided, and a stop valve on the pressure sensor side is periodically closed to introduce a purge gas to purge the tip portion to prevent adhesion of fine powder to the porous portion. To do.

【0013】[0013]

【発明の実施の形態】図1は、本発明による導圧管の縦
断面図で、流動層還元炉の炉壁13は外周は鉄皮14で
覆われた耐火物壁からなり、炉壁13には貫通孔にフラ
ンジ付の導圧管12が挿入されており、導圧管内に内挿
管15が挿入され、内挿管15は、そのフランジ16が
導圧管12のフランジ17と圧力センサーに通じる導圧
管18のフランジ19との間に固定され、保持される。
1 is a vertical cross-sectional view of a pressure guiding tube according to the present invention. A furnace wall 13 of a fluidized bed reduction furnace is made of a refractory wall whose outer periphery is covered with a steel shell 14. Has a pressure guiding tube 12 with a flange inserted in the through hole, and an insertion tube 15 is inserted into the pressure guiding tube. The insertion tube 15 has a flange 16 of the pressure guiding tube 12 and a pressure guiding tube 18 communicating with a pressure sensor. It is fixed and held between the flange 19 and the flange 19.

【0014】内装管15の先端は多孔質製で先端は封じ
られた形状になっている。多孔質材としては、例えばス
テンレス製金網を多数枚重ねて焼結したもの等を用いる
(例えば、セントラルフィルター工業製 商品名「ポア
メット」、「ニューポアメット」等)。
The tip of the inner tube 15 is made of a porous material and has a closed shape. As the porous material, for example, a material obtained by stacking and sintering a plurality of stainless steel wire nets is used (for example, product names "Poremet" and "New Poremet" manufactured by Central Filter Industry Co., Ltd.).

【0015】炉外の導圧管18には先端をパージするパ
ージ管20を設け、ストップ弁21a,21bを導圧管
及びパージ管に設け、パージの時には、パージ管20の
ストップ弁21aを開き、導圧管18のストップ弁21
bは閉め、パージ管と圧力センサーとは遮断して、導圧
管12の先端をパージして還元粒子を除去する。
The pressure guiding pipe 18 outside the furnace is provided with a purge pipe 20 for purging the tip, and stop valves 21a and 21b are provided in the pressure guiding pipe and the purge pipe, and at the time of purging, the stop valve 21a of the purge pipe 20 is opened to conduct. Stop valve 21 of pressure pipe 18
b is closed, the purge pipe and the pressure sensor are shut off, and the tip of the pressure guiding pipe 12 is purged to remove the reducing particles.

【0016】[0016]

【発明の効果】【The invention's effect】

(1) 導圧管の詰まり、閉塞がないので安定した操業
ができる。
(1) Since the pressure guiding tube is not clogged or blocked, stable operation is possible.

【0017】(2) 導圧管を炉壁に対して傾斜させて
取り付ける必要がないので、設備的な繁雑さがなくな
る。
(2) Since it is not necessary to mount the pressure guiding pipe in an inclined manner with respect to the furnace wall, the complexity of equipment is eliminated.

【0018】(3) 金属材質の多孔質のものを採用す
れば、導圧管の先端部のみ多孔質として、他の導圧管は
パイプとすることができ、圧力測定精度の向上とコスト
削減になる。
(3) If a porous metal material is used, only the tip of the pressure guiding tube can be made porous and the other pressure guiding tubes can be pipes, which improves the pressure measurement accuracy and reduces the cost. .

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

【図1】本発明による導圧管の縦断面図。FIG. 1 is a vertical sectional view of a pressure guiding tube according to the present invention.

【図2】流動層還元炉の説明図。FIG. 2 is an explanatory view of a fluidized bed reduction furnace.

【図3】従来の導圧管の取付けを示す縦断面図。FIG. 3 is a vertical cross-sectional view showing attachment of a conventional pressure guiding tube.

【符号の説明】[Explanation of symbols]

1 流動層還元炉、 2 原料ホッパー、 3 原料供
給部、 4 成品の排出部、 5 還元ガス吹込部、
6 ガス出口、 7 外部粒子循環装置、 81次サイ
クロン、 9 2次サイクロン、 10a,10b下降
管、 11a,11b ニューマッチクフィーダ、 1
2 導圧管、13 炉壁、 14 鉄皮、 15 内挿
管、 16 フランジ、 17フランジ、 18 導圧
管、 19 フランジ、 20 パージ管、 21a,
21b ストップ弁
1 fluidized bed reduction furnace, 2 raw material hopper, 3 raw material supply section, 4 product discharge section, 5 reducing gas injection section,
6 gas outlet, 7 external particle circulation device, 8 1st cyclone, 9 2nd cyclone, 10a, 10b downcomer, 11a, 11b new match feeder, 1
2 pressure guiding pipes, 13 furnace walls, 14 iron skins, 15 insertion pipes, 16 flanges, 17 flanges, 18 pressure guiding pipes, 19 flanges, 20 purge pipes, 21a,
21b stop valve

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 流動層還元炉内側の導圧管の先端部を多
孔質状の先端封じの円筒形状とし、前記導圧管の炉外側
にフランジを設け、炉外の導圧管と接続し、炉外の導圧
管には先端をパージするパージ管を設け、パージの時に
圧力センサーとを遮断するストップ弁を設けたことを特
徴とする流動層還元炉における導圧管。
1. A tip of a pressure guiding tube inside a fluidized bed reduction furnace is formed into a cylindrical shape with a porous tip closed, a flange is provided on the outside of the pressure guiding tube, and the flange is connected to the pressure guiding tube outside the furnace. A pressure guiding tube in a fluidized bed reduction furnace characterized in that a pressure guiding tube is provided with a purge tube for purging the tip, and a stop valve for blocking the pressure sensor at the time of purging is provided.
JP776596A 1996-01-19 1996-01-19 Connecting tube for fluidized bed reduction furnace Withdrawn JPH09194921A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP776596A JPH09194921A (en) 1996-01-19 1996-01-19 Connecting tube for fluidized bed reduction furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP776596A JPH09194921A (en) 1996-01-19 1996-01-19 Connecting tube for fluidized bed reduction furnace

Publications (1)

Publication Number Publication Date
JPH09194921A true JPH09194921A (en) 1997-07-29

Family

ID=11674788

Family Applications (1)

Application Number Title Priority Date Filing Date
JP776596A Withdrawn JPH09194921A (en) 1996-01-19 1996-01-19 Connecting tube for fluidized bed reduction furnace

Country Status (1)

Country Link
JP (1) JPH09194921A (en)

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Legal Events

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Effective date: 20030401