JPH0619088B2 - Oxygen blast furnace - Google Patents
Oxygen blast furnaceInfo
- Publication number
- JPH0619088B2 JPH0619088B2 JP30913586A JP30913586A JPH0619088B2 JP H0619088 B2 JPH0619088 B2 JP H0619088B2 JP 30913586 A JP30913586 A JP 30913586A JP 30913586 A JP30913586 A JP 30913586A JP H0619088 B2 JPH0619088 B2 JP H0619088B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- blast furnace
- furnace
- nozzle
- oxygen
- 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
- Blast Furnaces (AREA)
Description
【発明の詳細な説明】 「発明の目的」 (産業上の利用分野) この発明は製鉄用高炉、特にシャフトから予熱ガスを吹
き込む酸素高炉に関するものである。DETAILED DESCRIPTION OF THE INVENTION “Object of the Invention” (Field of Industrial Application) The present invention relates to an iron blast furnace, and more particularly to an oxygen blast furnace in which preheated gas is blown from a shaft.
(従来の技術) 従来、鉱石から銑鉄を製するための所謂、高炉操業方法
においては、若干の酸素富化は行うものの、生産性の高
い実用高炉について云えば、略全部が羽口からの高温の
空気送風を主体としている。この場合空気中の約79%
を占めるN2は、鉄鉱石の還元には直接関与しないが、
羽口先からストックラインまでの装入物に膨大な顕熱を
与え、ガス還元を活発に行うに必要な熱補強の役目を果
していたので、特に羽口以外から熱を補給する必要はな
かったが、高炉の生産性向上の見地から近年開発されつ
つある酸素高炉においては、羽口先きの温度上昇に対す
る温度制御用の炉頂ガス、水蒸気等の羽口もしくは羽口
近傍からの添加の他に、N2不在のためのガス量低下に
伴う700℃以上のガス還元域の狭少化、炉上部の温度
低下のためにシャフト部からの熱補給が必要とされる。
例えば特開昭60−159104には炉頂ガスの一部を
分取しこれを燃焼しシャフトから吹き込むことが示され
ている。又、酸素高炉ではないが高酸素富化送風と炉頂
ガスの再生還元ガスを羽口より送風する特公昭50−2
2966でもガス量不足をおぎなうためにシャフト部か
ら非酸化性ガスが吹き込まれている。(Prior Art) Conventionally, in a so-called blast furnace operating method for producing pig iron from ore, although oxygen is slightly enriched, when it comes to a highly productive practical blast furnace, almost all of the high temperature from the tuyere is high. The main purpose is air blowing. In this case, about 79% of the air
N 2, which accounts for are not involved directly in the reduction of iron ore,
It gave a huge amount of sensible heat to the charge from the tuyere to the stock line, and played the role of heat reinforcement necessary to actively carry out gas reduction, so it was not necessary to supply heat from other than the tuyere. In the oxygen blast furnace which is being developed in recent years from the viewpoint of improving the productivity of the blast furnace, in addition to addition of top gas for temperature control against temperature rise at the tuyere, addition of steam, etc. from or near the tuyere, Due to the decrease in the gas amount due to the absence of N 2, the gas reduction region is narrowed to 700 ° C. or more, and the temperature in the upper part of the furnace is lowered, so that heat supply from the shaft portion is required.
For example, Japanese Unexamined Patent Publication No. 60-159104 discloses that a part of the furnace top gas is taken, burned, and blown from a shaft. Also, although it is not an oxygen blast furnace, high oxygen enriched blast and regenerated reducing gas of the furnace top gas are blown from the tuyere.
Also in 2966, the non-oxidizing gas is blown from the shaft portion in order to fill the gas shortage.
しかし乍ら、これらは全て炉壁に設うけた複数の固定ノ
ズルから吹き込まれたものであり、予熱ガスが炉心まで
到達し難い欠陥があった。However, all of them were blown from a plurality of fixed nozzles provided on the furnace wall, and there was a defect that preheated gas did not easily reach the core.
(発明が解決しようとする問題点) 本発明は、このような現状に鑑み創案されたものであ
り、従来の複数の固定ノズルの内の一部もしくは全部を
可動式ノズルとして炉心までのガスの到達を容易にする
ことにより、炉内装入物の温度調整を自在に行ない還元
領域を拡大し燃料比の低減を図ると共に長期安定操業を
可能とする酸素高炉を提供することを目的とする。(Problems to be Solved by the Invention) The present invention has been devised in view of such a current situation, and a part or all of a plurality of conventional fixed nozzles is used as a movable nozzle to supply gas to the core. It is an object of the present invention to provide an oxygen blast furnace in which the temperature of the contents inside the furnace can be freely adjusted, the reduction region is expanded to reduce the fuel ratio, and long-term stable operation is possible by facilitating the arrival.
「発明の構成」 (問題点を解決するための手段) 上記の目的を達成するために本発明者等は、シャフト部
に設うけた複数の予熱ガス吹き込みノズルの一部もしく
は全部を炉心方向への前後進自在としたことを特徴とす
る酸素高炉、 を茲に提案する。“Structure of the Invention” (Means for Solving Problems) In order to achieve the above-mentioned object, the present inventors have made a part or all of a plurality of preheating gas blowing nozzles provided in a shaft portion in a core direction. We propose an oxygen blast furnace, which is characterized by its ability to move forward and backward.
本発明の採用により、炉上部に対する単なる熱補給に止
まらず、炉内装入物温度分布の制御も併せて行うことが
可能となり、しかも炉心までの吹き込みが可能となるの
で、最終的には燃料比の低減、安定操業の長期継続が可
能となる。By adopting the present invention, it is possible to control not only the heat supply to the upper part of the furnace but also the temperature distribution of the temperature inside the furnace, and it is also possible to blow into the core. And stable operation can be continued for a long period of time.
(作用) 本発明において酸素高炉とは、羽口から酸素濃度40%
以上のガスを常温で吹き込み、且つシャフトから予熱ガ
スを吹き込んで操業する高炉のことである。(Operation) In the present invention, the oxygen blast furnace means an oxygen concentration of 40% from the tuyere
This is a blast furnace in which the above gases are blown at room temperature and preheated gas is blown from the shaft to operate.
第1図は高炉シャフト部の平面図に本発明において使用
する固定式ノズルおよび可動式ノズルを具備せしめた場
合を模式的に示したものである。FIG. 1 schematically shows a plan view of a shaft portion of a blast furnace in which a fixed nozzle and a movable nozzle used in the present invention are provided.
この図面においては炉壁1に固定式ノズル2と可動式ノ
ズル3を交互に設けた例を示しているが、固定ノズル2
〜3本につき可動ノズルを1本としてもよく、これらは
炉容もしくは1本当りのノズルからのガス吹き込み量の
大小により任意選択できる。尚、可動ノズルの移動しう
る距離は、その先端位置が炉壁から略炉心近くまでに到
達する位置まで炉内に挿入できるように設計する必要が
ある。In this drawing, an example in which a fixed nozzle 2 and a movable nozzle 3 are alternately provided on the furnace wall 1 is shown.
There may be one movable nozzle for every three nozzles, which can be arbitrarily selected depending on the furnace volume or the amount of gas blown from each nozzle. It should be noted that the movable distance of the movable nozzle needs to be designed so that it can be inserted into the furnace up to the position where the tip position reaches from the furnace wall to near the core.
尚、本発明の実施に際しては、中間ゾンデ等による事前
の炉内ガス温度分布の測定、炉内装入物の温度分布の測
定を条件とし適確な効果を確認しつつ予熱ガスを吹き込
むものとする。本発明の効果を発揮するためには等間隔
に少なくとも3本の可動式ノズルを設ける必要がある。
又、何れのタイプのノズルも吹き込みガス量を可変とし
ておく必要があることは勿論である。Incidentally, in carrying out the present invention, preheating gas shall be blown while confirming an appropriate effect under the conditions of pre-measurement of gas temperature distribution in the furnace by an intermediate sonde, etc., and measurement of temperature distribution of the contents of the furnace interior. . In order to exert the effect of the present invention, it is necessary to provide at least three movable nozzles at equal intervals.
Also, it is needless to say that the amount of gas blown into each type of nozzle must be variable.
(実施例) 第3図は炉壁1に可動式ノズル3を設置した概略図であ
り、架台5の上に載置された油圧シリンダー6により可
動式ノズル3は前後進する。フレキシブルな予熱ガス供
給管7からガスは炉内に送られる。仕切弁8によりノズ
ルの補修などの際の炉内雰囲気のガス遮断ができる。(Example) FIG. 3 is a schematic view in which the movable nozzle 3 is installed on the furnace wall 1, and the movable nozzle 3 is moved forward and backward by the hydraulic cylinder 6 mounted on the pedestal 5. The gas is sent from the flexible preheating gas supply pipe 7 into the furnace. The sluice valve 8 can shut off the gas in the furnace atmosphere when the nozzle is repaired.
第2図は本発明酸素高炉の垂直断面略図を示し可動ノズ
ルの高さ方向の位置のみを示した(固定ノズルの図示は
省略)ものである。FIG. 2 is a schematic vertical sectional view of the oxygen blast furnace of the present invention, showing only the position of the movable nozzle in the height direction (the fixed nozzle is not shown).
尚第1図、第2図においては可動式ノズルの駆動機構は
省略してある。The drive mechanism for the movable nozzle is omitted in FIGS. 1 and 2.
全部を可動式ノズルとした例は第5図で図示した。An example in which all of them are movable nozzles is shown in FIG.
第4図は本発明を実施する酸素高炉の操業フローを示す
概要図であって、高炉11よりの炉頂はガス清浄係12
を経てガスホルダー13へ導かれるがガスの1部はブー
スター14を経て予熱ガス燃焼装置15へ導びかれ酸素
源16からのガスにより燃焼せられ高温の予熱ガスとな
って予熱ガス吹き込みノズル19より炉内に吹き込まれ
る。FIG. 4 is a schematic diagram showing the operation flow of the oxygen blast furnace for carrying out the present invention. The top of the blast furnace 11 is the gas cleaning section 12.
Part of the gas is guided to the preheated gas combustor 15 via the booster 14 and burned by the gas from the oxygen source 16 to become high-temperature preheated gas from the preheated gas injection nozzle 19. It is blown into the furnace.
一方羽口17へは、酸素源16からの酸素、ブースター
14′を経た羽口先温度調整ガスとしての炉頂ガス、微
粉炭貯槽18からの微粉炭が送給される。On the other hand, to the tuyere 17, oxygen from the oxygen source 16, the furnace top gas as the tuyere tip temperature adjusting gas passing through the booster 14 ', and the pulverized coal from the pulverized coal storage tank 18 are fed.
「発明の効果」 以上詳述したように、本発明による場合にはシャフト部
からの単なる熱補給のみに止らず、従来の固定式予熱ガ
ス吹き込みノズルでは調整不充分な炉心部の温度制御が
自在にできるので、還元域の拡大、炉況の正常化に寄与
することが極めて大きく、燃料比の低減に大きな効果が
ある。[Advantages of the Invention] As described in detail above, in the case of the present invention, not only the heat supply from the shaft portion is simply stopped, but also the temperature control of the core portion is insufficiently adjusted by the conventional fixed type preheating gas blowing nozzle. Therefore, it greatly contributes to the expansion of the reduction zone and the normalization of the furnace condition, which has a great effect on the reduction of the fuel ratio.
第1図は本発明において使用する固定式ガス吹き込みノ
ズル並びに可動式吹き込みノズルの実施の態様を示す平
面図(模式図)である。第2図は本発明の高炉の垂直断
面図である。 第3図は油圧式駆動機構を備えた可動式ノズルをシャフ
トに設置した概略図。第4図は本発明の実施される高炉
操業のフローを示す概要図である。 第5図はノズル全部を可動式とした場合の水平断面略図
である。 1:炉壁 2:固定ノズル 3:可動式ノズル 4:羽口 5:架台 6:油圧シリンダー 7:予熱ガス供給管 8:仕切弁 11:高炉 12:ガス清浄機構 13:ガスホルダー 14:ブースター 14′:ブースター 15:予熱ガス燃焼装置 16:酸素源 17:羽口 18:微粉炭貯槽 19:予熱ガス吹込ノズルFIG. 1 is a plan view (schematic diagram) showing an embodiment of a fixed gas blowing nozzle and a movable gas blowing nozzle used in the present invention. FIG. 2 is a vertical sectional view of the blast furnace of the present invention. FIG. 3 is a schematic view in which a movable nozzle having a hydraulic drive mechanism is installed on a shaft. FIG. 4 is a schematic diagram showing the flow of blast furnace operation in which the present invention is carried out. FIG. 5 is a schematic horizontal cross-sectional view when all the nozzles are movable. 1: Furnace wall 2: Fixed nozzle 3: Movable nozzle 4: Tuyer 5: Stand 6: Hydraulic cylinder 7: Preheating gas supply pipe 8: Gate valve 11: Blast furnace 12: Gas cleaning mechanism 13: Gas holder 14: Booster 14 ′: Booster 15: Preheated gas combustion device 16: Oxygen source 17: Tuyere 18: Pulverized coal storage tank 19: Preheated gas injection nozzle
Claims (1)
みノズルの一部もしくは全部を、炉心方向への前後進自
在としたことを特徴とする酸素高炉。1. An oxygen blast furnace characterized in that a part or all of a plurality of preheating gas injection nozzles provided on a shaft portion can be moved forward and backward in the direction of the core.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30913586A JPH0619088B2 (en) | 1986-12-27 | 1986-12-27 | Oxygen blast furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30913586A JPH0619088B2 (en) | 1986-12-27 | 1986-12-27 | Oxygen blast furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63166913A JPS63166913A (en) | 1988-07-11 |
| JPH0619088B2 true JPH0619088B2 (en) | 1994-03-16 |
Family
ID=17989318
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP30913586A Expired - Lifetime JPH0619088B2 (en) | 1986-12-27 | 1986-12-27 | Oxygen blast furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0619088B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2024224927A1 (en) | 2023-04-27 | 2024-10-31 | Jfeスチール株式会社 | Method for treating filling layer housed in cylindrical container |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110747303B (en) * | 2018-07-24 | 2021-11-16 | 宝山钢铁股份有限公司 | Blast furnace |
-
1986
- 1986-12-27 JP JP30913586A patent/JPH0619088B2/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2024224927A1 (en) | 2023-04-27 | 2024-10-31 | Jfeスチール株式会社 | Method for treating filling layer housed in cylindrical container |
| TWI898528B (en) * | 2023-04-27 | 2025-09-21 | 日商杰富意鋼鐵股份有限公司 | Method for processing the filling layer contained in a cylindrical container |
| EP4674987A1 (en) | 2023-04-27 | 2026-01-07 | JFE Steel Corporation | Method for treating filling layer housed in cylindrical container |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63166913A (en) | 1988-07-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP2016222949A (en) | Oxygen blast furnace operation method | |
| KR20090099538A (en) | Method for manufacturing pig iron in the furnace | |
| AU2001267365B2 (en) | Method and device for producing pig iron or liquid steel pre-products from charge materials containing iron ore | |
| JPH0619088B2 (en) | Oxygen blast furnace | |
| JP6604344B2 (en) | Preheating gas blowing device to blast furnace shaft, preheating gas blowing method and blast furnace operating method | |
| US2515670A (en) | Manufacture of open-hearth steel | |
| DE3579672D1 (en) | METHOD FOR OPERATING A BLAST FURNACE. | |
| WO2026020621A1 (en) | Tuyere nose of hydrogen-rich carbon-recycling oxygen blast furnace and control method | |
| EP1373580B1 (en) | Modular shaft furnace for reduction smelting | |
| US1623797A (en) | Method of converting nickel-containing matte | |
| US1849658A (en) | Apparatus for treatment of iron ore | |
| GB1222236A (en) | Improvements in or relating to iron making | |
| JPH0619091B2 (en) | Oxygen blast furnace | |
| JPS63171815A (en) | oxygen blast furnace | |
| JPH0619090B2 (en) | Oxygen blast furnace | |
| US1645968A (en) | Process of making sponge iron from its oxide ores | |
| CN88100068A (en) | Blast-furnace tuyere | |
| US3764300A (en) | Method of operating a blast furnace by blowing variable gaseous auxiliary reduction medium | |
| US3722871A (en) | Blast furnace with staggered tuyere system | |
| US3844767A (en) | Method of operating a blast furnace | |
| JPS63166914A (en) | High oxygen-rich blasting blast furnace | |
| CN223103014U (en) | Blast furnace tuyere oxygen spray gun | |
| JP2881840B2 (en) | Blast furnace tuyere powder injection method | |
| US2549720A (en) | Method of and apparatus for regulating blast furnace top temperature | |
| CA1161637A (en) | Installation and process for the production of hot air |