JPS63171815A - Oxygen blast furnace - Google Patents
Oxygen blast furnaceInfo
- Publication number
- JPS63171815A JPS63171815A JP62001853A JP185387A JPS63171815A JP S63171815 A JPS63171815 A JP S63171815A JP 62001853 A JP62001853 A JP 62001853A JP 185387 A JP185387 A JP 185387A JP S63171815 A JPS63171815 A JP S63171815A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- oxygen
- burner
- pipe
- blast 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.)
- Granted
Links
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 23
- 239000001301 oxygen Substances 0.000 title claims abstract description 23
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 23
- 239000007789 gas Substances 0.000 claims abstract description 41
- 239000002737 fuel gas Substances 0.000 claims abstract description 7
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 238000007664 blowing Methods 0.000 abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 239000000498 cooling water Substances 0.000 abstract description 2
- 238000010276 construction Methods 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 229910000805 Pig iron Inorganic materials 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- WQGWDDDVZFFDIG-UHFFFAOYSA-N pyrogallol Chemical compound OC1=CC=CC(O)=C1O WQGWDDDVZFFDIG-UHFFFAOYSA-N 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
Abstract
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。(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.
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、特に羽目以外
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
蒸気等の羽目もしくは羽目近傍からの添加の他に、Nz
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02濃度40%
以上のガス吹き込みの場合は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。In this case, N2, which accounts for about 79% of the air, does not directly participate in the reduction of iron ore, but it provides a huge amount of sensible heat to the charge from the tuyere tip to the stock line, which is necessary for active gas reduction. Since it played a role of heat reinforcement, there was no need to supply heat from other sources than the siding.
In addition to adding top gas, steam, etc. from the siding or near the tuyere to control the temperature rise at the tuyere tip, Nz
02 concentration is 40% due to the narrowing of the gas reduction area above 700℃ due to the decrease in gas volume due to the absence of gas, and the decrease in the temperature at the top of the furnace.
In the case of the above gas blowing, heat supply from the shaft part is required. For example, Japanese Unexamined Patent Publication No. 159104/1988 discloses that a part of the furnace top gas is separated, combusted, and 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、熱風導管をシャフトまで上げしかもかなりな
重量の環状管を設は羽目への支管のような多くの分蛸管
を各吹込みロノズルへ連設する必要があり、重量的な不
安定さと、イニシャルコストの増大、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, it is necessary to raise the hot air conduit up to the shaft and install a fairly heavy annular pipe. It is necessary to connect the nozzle to the rotary nozzle, and there are many unresolved problems such as unstable 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、シャ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, and is an oxygen blast furnace equipped with a burner of a relatively simple structure without lifting heavy objects to the shaft. 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、シャフトか
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ャフト部に設けたことを特徴
とする酸素高炉、を芸に提供する。"Structure of the Invention" (Means for Solving the Problems) In order to achieve the object of the previous section, the present inventors have developed a fuel gas supply conduit,
An oxygen blast furnace characterized in that a plurality of gas burners each having an oxygen supply conduit and a gas temperature control gas conduit are provided in a shaft portion.
このようなバーナーをシャ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、羽目から酸素濃度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。(Function) In the present invention, an oxygen blast furnace refers to an oxygen concentration of 40% from the surface.
This is a blast furnace that operates by blowing the above gases at room temperature and by blowing preheated gas through a shaft.
シャ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 the need for a large-scale hot air annular pipe, so it was decided to install a burner in each nozzle. For burners,
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ってバーナ一本
体8へ連設されているパイロ、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。バーナ一本体の外
側は鉄皮7で被っである。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っている。冷
却水の導管は給水管3、排水管4で示されている。スト
ッ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. The flow rate of both the fuel gas supply conduit 1 and the oxygen supply conduit 2 can be freely controlled, and the pyro and burner 9 connected to the burner main body 8 are connected to the gas supply conduit 1 and the oxygen supply conduit 2.
It is installed at the oxygen outlet. 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. A 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ャ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。シャフト部に12本
のバーナーを固定し操業を行った。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 portion at an angle greater than the angle of repose of the blast furnace charge. From the oxygen tuyere 10, in addition to oxygen, there is a tuyere tip temperature adjusting gas,
Pulverized coal, steam, etc. are blown into it. Twelve burners were fixed to the shaft and the operation was carried out. 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
ャ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.
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:バーナ一本体
9:パイロットバーナー
10:酸素羽目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 lining
Claims (1)
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ャフト部に設けた
ことを特徴とする酸素高炉。An oxygen blast furnace characterized in that a plurality of gas burners each having a fuel gas supply conduit, an oxygen supply conduit, and a gas temperature control gas conduit are provided in the shaft portion as a preheating gas injection device from the shaft.
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 |
KR1019870014984A KR930004473B1 (en) | 1986-12-27 | 1987-12-26 | Process for making iron in the blast furnace |
CN87105991A CN1007161B (en) | 1986-12-27 | 1987-12-26 | Blast furnace |
DE87119248T DE3787518T2 (en) | 1986-12-27 | 1987-12-28 | Blast furnace process. |
EP87119248A EP0273420B1 (en) | 1986-12-27 | 1987-12-28 | A blast furnace method |
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 true JPS63171815A (en) | 1988-07-15 |
JPH0564203B2 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) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5706701A (en) * | 1995-04-28 | 1998-01-13 | Fuji Kiko Co., Ltd. | Wiring-harness connection structure of transmission shift-lever device |
JP2011106803A (en) * | 2009-10-22 | 2011-06-02 | Jfe Steel Corp | Method of burning blast furnace gas by combustion burner, and method of operating blast furnace |
JP2011106802A (en) * | 2009-10-22 | 2011-06-02 | Jfe Steel Corp | Method of burning gas of low calorific value by combustion burner and method of operating blast furnace |
JP2011153371A (en) * | 2009-04-30 | 2011-08-11 | Jfe Steel Corp | Blast furnace operation method |
JP2011214022A (en) * | 2010-03-31 | 2011-10-27 | Jfe Steel Corp | Method for operating blast furnace |
KR101314443B1 (en) * | 2009-04-30 | 2013-10-07 | 제이에프이 스틸 가부시키가이샤 | Blast furnace operation method, low-calorific-value gas combustion method for same, and blast furnace equipment |
-
1987
- 1987-01-09 JP JP62001853A patent/JPS63171815A/en active Granted
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5706701A (en) * | 1995-04-28 | 1998-01-13 | Fuji Kiko Co., Ltd. | Wiring-harness connection structure of transmission shift-lever device |
JP2011153371A (en) * | 2009-04-30 | 2011-08-11 | Jfe Steel Corp | Blast furnace operation method |
KR101314443B1 (en) * | 2009-04-30 | 2013-10-07 | 제이에프이 스틸 가부시키가이샤 | Blast furnace operation method, low-calorific-value gas combustion method for same, and blast furnace equipment |
JP2011106803A (en) * | 2009-10-22 | 2011-06-02 | Jfe Steel Corp | Method of burning blast furnace gas by combustion burner, and method of operating blast furnace |
JP2011106802A (en) * | 2009-10-22 | 2011-06-02 | Jfe Steel Corp | Method of burning gas of low calorific value by combustion burner and method of operating blast furnace |
JP2011214022A (en) * | 2010-03-31 | 2011-10-27 | Jfe Steel Corp | Method for operating blast furnace |
Also Published As
Publication number | Publication date |
---|---|
JPH0564203B2 (en) | 1993-09-14 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |