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JPH0564203B2 - - Google Patents
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JPH0564203B2 - - Google Patents

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Publication number
JPH0564203B2
JPH0564203B2 JP185387A JP185387A JPH0564203B2 JP H0564203 B2 JPH0564203 B2 JP H0564203B2 JP 185387 A JP185387 A JP 185387A JP 185387 A JP185387 A JP 185387A JP H0564203 B2 JPH0564203 B2 JP H0564203B2
Authority
JP
Japan
Prior art keywords
gas
oxygen
furnace
temperature
burner
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 - Fee Related
Application number
JP185387A
Other languages
Japanese (ja)
Other versions
JPS63171815A (en
Inventor
Kazuhiko Tsujimoto
Yotaro Oono
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.)
JFE Engineering Corp
Original Assignee
Nippon Kokan Ltd
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 Kokan Ltd filed Critical Nippon Kokan Ltd
Priority to JP62001853A priority Critical patent/JPS63171815A/en
Priority to AU82946/87A priority patent/AU596253B2/en
Priority to CN87105991A priority patent/CN1007161B/en
Priority to KR1019870014984A priority patent/KR930004473B1/en
Priority to EP87119248A priority patent/EP0273420B1/en
Priority to DE87119248T priority patent/DE3787518T2/en
Publication of JPS63171815A publication Critical patent/JPS63171815A/en
Publication of JPH0564203B2 publication Critical patent/JPH0564203B2/ja
Granted legal-status Critical Current

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  • Manufacture Of Iron (AREA)
  • 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、特に酸素高炉の構造に
関する発明である。
DETAILED DESCRIPTION OF THE INVENTION Object of the Invention (Industrial Field of Application) This invention relates to the structure of a blast furnace for iron-making, particularly an oxygen blast furnace.

(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
トツ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
要はなかつたが、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、炉頂部の温度低下のため
にO2濃度40%以上のガス吹き込みの場合はシヤ
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
燃焼しシヤフトから吹き込むことが示されてい
る。
(Prior art) Conventionally, in the so-called blast furnace operation method for producing pig iron from ore, although some oxygen enrichment is carried out, when it comes to practical blast furnaces with high productivity, almost all of the high-temperature oxygen is Mainly uses air blowing. In this case, N2 , which accounts for about 79% of the air, does not directly participate in the reduction of iron ore, but it gives a huge amount of sensible heat to the charge from the tuyere tip to the stock line.
Since it played the role of thermal reinforcement necessary for active gas reduction, there was no need to supply heat from any other source other than the tuyeres. In addition to the addition of top gas and water vapor from the tuyere or near the tuyere to control the temperature rise at the tuyere tip, the gas reduction region above 700℃ due to the decrease in gas amount due to the absence of N2 . Heat supply from the shaft is required when blowing gas with an O 2 concentration of 40% or more due to the narrowing of the furnace and the drop in temperature at the top of the furnace. For example, Japanese Patent Application Laid-Open No. 159104/1983 discloses that a part of the furnace top gas is separated, combusted, and then blown into the furnace through a shaft.

この公開公報の第1図には高炉の周辺に炉頂ガ
スと酸素を用いて高温の予熱ガスを発生せしめる
ための燃焼炉を必要とする旨記載されている。
FIG. 1 of this publication states that a combustion furnace is required around the blast furnace to generate high-temperature preheated gas using furnace top gas and oxygen.

しかし高温の予熱ガスを炉周から均一に炉内に
吹き込むためには、熱風導管をシヤフトまで上げ
しかもかなりな重量の環状管を設け羽口への支菅
のような多くの分岐管を各吹込み口ノズルへ連設
する必要があり、重量的な不安定さと、イニシヤ
ルコストの増大、保温対策など未解決の問題点が
多い。
However, in order to uniformly blow high-temperature preheated gas into the furnace from the furnace periphery, the hot air conduit must be raised up to the shaft, an annular pipe of considerable weight must be installed, and many branch pipes such as branch pipes to the tuyeres must be installed at each blower. It needs to be connected to the inlet nozzle, and there are many unresolved problems such as instability in weight, increased initial cost, and heat retention measures.

(発明が解決しようとする問題点) 本発明は上記したような酸素高炉の現状に鑑み
創案されたものであり、シヤフト部へ重量物をあ
げないで比較的簡単な構造のバーナーを具備した
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 was devised in view of the current state of oxygen blast furnaces as described above. The purpose is to provide blast furnaces.

「発明の構成」 (問題点を解決するための手段) 前項の目的を達成するために本発明者等は、シ
ヤフトからの予熱ガス吹き込み装置として、燃料
ガスの供給導管、酸素の供給導管およびガス温度
制御用ガス導管を有するガスバーナーの複数本を
シヤフト部に設けたことを特徴とする酸素高炉、 を茲に提供する。
"Structure of the Invention" (Means for Solving the Problems) In order to achieve the object of the preceding paragraph, the present inventors have developed a fuel gas supply conduit, an oxygen supply conduit, and a gas supply conduit as a preheating gas blowing device from the shaft. An oxygen blast furnace characterized in that a shaft portion is provided with a plurality of gas burners each having a temperature control gas conduit.

このようなバーナーをシヤフトに設けることに
より熱風環状管の設置は不要となるだけに止まら
ず、各バーナー毎のガス温度、ガス量の調整が自
由になる利点を併せ持つことになる。
Providing such a burner on the shaft not only eliminates the need to install a hot air annular tube, but also has the advantage of allowing free adjustment of gas temperature and gas amount for each burner.

(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、且つシヤフ
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。
(Function) In the present invention, an oxygen blast furnace is a blast furnace operated by blowing gas having an oxygen concentration of 40% or more through the tuyere at room temperature and blowing preheated gas through the shaft.

シヤフトから吹き込む予熱ガスの温度、送風量
を各ノズル毎に調整可能とすること、大規模な熱
風環状管を設けないことが開発のポイントであ
り、そのため各ノズル毎にバーナーを取りつける
ことにした。バーナーの場合、燃焼させるまでの
移送配管は常温で行なう利点がある。
The key points in the development were to be able to adjust the temperature of the preheated gas blown in from the shaft and the amount of air blown for each nozzle, and to avoid installing a large-scale hot air annular pipe, so it was decided to install a burner in each nozzle. In the case of a burner, there is an advantage that the transfer piping until combustion is carried out at room temperature.

(実施例) 第1図は本発明で使用するバーナの長さ方向の
概略断面図である。燃料ガス供給導管1、酸素供
給導管2はいずれも流量の制御が自在にできるよ
うになつてバーナー本体8へ連設されているパイ
ロツトバーナー9が、ガス−酸素の噴出口の所に
設けられている。バーナー本体の外側は鉄皮7で
被つてある。又、ガスバーナーで発生したガスの
ガス温度の調整用のガス導管5も連設されており
温度コントロールが自在にできるようになつてい
る。冷却水の導管は給水管3、排水管4で示され
ている。ストツクラインから羽口までを100とし
て上から40の位置にガスバーナーを設置した。
(Example) FIG. 1 is a schematic longitudinal sectional view of a burner used in the present invention. Both the fuel gas supply conduit 1 and the oxygen supply conduit 2 have a pilot burner 9 connected to the burner body 8 so that the flow rate can be freely controlled, and a pilot burner 9 is provided at the gas-oxygen jet port. There is. The outside of the burner body is covered with an iron skin 7. Further, a gas conduit 5 for adjusting the gas temperature of the gas generated by the gas burner is also connected, so that the temperature can be freely controlled. Cooling water conduits are shown as a water supply pipe 3 and a drain pipe 4. The gas burner was installed at a position of 40 from the top, with the distance from the stock line to the tuyere being 100.

第2図は本発明の高炉の垂直断面略図であり高
炉装入物の安息角より大きな角度でシヤフト部に
固定されている。酸素羽口10からは酸素の外に
羽口先温度調整ガス、微粉炭、水蒸気等が吹き込
まれる。シヤフト部に12本のバーナーを固定し操
業を行つた。燃料ガスに炉頂ガスを使用した。
FIG. 2 is a schematic vertical cross-sectional view of the blast furnace of the present invention, which is fixed to the shaft at an angle greater than the angle of repose of the blast furnace charge. In addition to oxygen, tuyere tip temperature adjusting gas, pulverized coal, steam, etc. are blown into the oxygen tuyere 10. Twelve burners were fixed to the shaft and operated. Furnace top gas was used as fuel gas.

「発明の効果」 各ノズルに共通する大型ガス燃焼装置からの熱
風の送給と異なり各ノズル毎の温度、吹込み量の
調整が自在でしかも簡単であるから本発明を利用
する高炉においてはシヤフト部の炉周に重量物の
熱風環状管等を必要とせずしかも炉況の変動に敏
速に対応することが可能である。
"Effects of the Invention" Unlike hot air supplied from a large gas combustion device common to each nozzle, the temperature and blowing amount for each nozzle can be freely and easily adjusted. There is no need for a heavy hot air annular tube around the furnace periphery, and it is possible to quickly respond to changes in furnace conditions.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明において使用するバーナーの縦
断面略図、第2図は本発明の高炉の垂直断面略図
である。 1……燃料ガス供給導管、2……酸素供給導
管、3……給水管、4……排水管、5……ガス温
度調整用ガス導管、6……耐火物、7……鉄皮、
8……バーナー本体、9……パイロツトバーナ
ー、10……酸素羽口。
FIG. 1 is a schematic longitudinal cross-sectional view of a burner used in the present invention, and FIG. 2 is a schematic vertical cross-sectional view of the blast furnace of the present invention. 1... Fuel gas supply pipe, 2... Oxygen supply pipe, 3... Water supply pipe, 4... Drain pipe, 5... Gas temperature adjustment gas pipe, 6... Refractory, 7... Iron shell,
8... Burner body, 9... Pilot burner, 10... Oxygen tuyere.

Claims (1)

【特許請求の範囲】[Claims] 1 シヤフトからの予熱ガス吹込み装置として、
燃料ガスの供給導管、酸素の供給導管およびガス
温度制御用ガス導管を有するガスバーナーの複数
本をシヤフト部に設けたことを特徴とする酸素高
炉。
1. As a preheating gas blowing device from the shaft,
An oxygen blast furnace characterized in that a shaft portion is provided with a plurality of gas burners each having a fuel gas supply conduit, an oxygen supply conduit, and a gas temperature control gas conduit.
JP62001853A 1986-12-27 1987-01-09 oxygen blast furnace Granted JPS63171815A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP62001853A JPS63171815A (en) 1987-01-09 1987-01-09 oxygen blast furnace
AU82946/87A AU596253B2 (en) 1986-12-27 1987-12-22 A blast furnace
CN87105991A CN1007161B (en) 1986-12-27 1987-12-26 blast furnace
KR1019870014984A KR930004473B1 (en) 1986-12-27 1987-12-26 Process for making iron in the blast furnace
EP87119248A EP0273420B1 (en) 1986-12-27 1987-12-28 A blast furnace method
DE87119248T DE3787518T2 (en) 1986-12-27 1987-12-28 Blast furnace process.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62001853A JPS63171815A (en) 1987-01-09 1987-01-09 oxygen blast furnace

Publications (2)

Publication Number Publication Date
JPS63171815A JPS63171815A (en) 1988-07-15
JPH0564203B2 true JPH0564203B2 (en) 1993-09-14

Family

ID=11513102

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62001853A Granted JPS63171815A (en) 1986-12-27 1987-01-09 oxygen blast furnace

Country Status (1)

Country Link
JP (1) JPS63171815A (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3410248B2 (en) * 1995-04-28 2003-05-26 富士機工株式会社 Harness connection structure of shift lever device
JP4760985B2 (en) * 2009-04-30 2011-08-31 Jfeスチール株式会社 Blast furnace operation method
JP4760977B2 (en) * 2009-10-22 2011-08-31 Jfeスチール株式会社 Blast furnace operation method
EP2426223B1 (en) * 2009-04-30 2016-11-23 JFE Steel Corporation Blast furnace operation method and blast furnace equipment
JP4760976B2 (en) * 2009-10-22 2011-08-31 Jfeスチール株式会社 Blast furnace operation method
JP5779839B2 (en) * 2010-03-31 2015-09-16 Jfeスチール株式会社 Blast furnace operation method

Also Published As

Publication number Publication date
JPS63171815A (en) 1988-07-15

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