JPS5938310A - Cooling method of furnace inside after blowing out of blast furnace - Google Patents
Cooling method of furnace inside after blowing out of blast furnaceInfo
- Publication number
- JPS5938310A JPS5938310A JP14955382A JP14955382A JPS5938310A JP S5938310 A JPS5938310 A JP S5938310A JP 14955382 A JP14955382 A JP 14955382A JP 14955382 A JP14955382 A JP 14955382A JP S5938310 A JPS5938310 A JP S5938310A
- Authority
- JP
- Japan
- Prior art keywords
- water
- furnace
- blast furnace
- tuyere
- gas
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Iron (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、高炉吹卸し後に炉内、特に炉内装入物を短期
間でしかも安全に冷却する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for safely cooling the inside of a blast furnace, particularly the contents inside the furnace, in a short period of time after blowing down the blast furnace.
従来、高炉の吹止め冷却する際には、装入物の供給を停
止し減風操業に入り、装入線の降下とともに送風量を漸
減し、次いで出銑口を開放して、出銑ロレペル以上の溶
銑及びIg融ススラグ出銑口から流出させた後、炉底の
れんがをポーリングして炉外から炉内底部に貫通する横
穴を開設し、この横穴から炉床に残留している溶銑を例
外に排出した後送風を停止する。つぎに・m内下部に残
った赤熱コークス、スラグなどの高温物質は通常人の方
法により例外へ掻き出される。Conventionally, when cooling a blast furnace, the supply of the charge was stopped and a reduced-air operation was started, the amount of air blown was gradually reduced as the charging line descended, and then the taphole was opened and the After the above hot metal and Ig molten slag have flowed out from the taphole, the bricks at the bottom of the furnace are polled to create a horizontal hole that penetrates from outside the furnace to the bottom of the furnace, and the hot metal remaining in the hearth is drained from this horizontal hole. Exceptionally, stop the air blower after discharging. Next, high-temperature substances such as red-hot coke and slag remaining in the lower part of the m are scraped out by ordinary human methods.
■ コークスを自然燃焼させ・m内残留物を100°C
以下に放冷した後炉外へ掻き出す。■ Naturally burn coke and reduce residue within m to 100°C
After allowing it to cool, scrape it out of the furnace.
(リ 無線ブルドーザなどの遠隔操作機械により熱間(
700〜800°C以上)で直接掻き出す。(Remotely controlled machines such as wireless bulldozers
700-800°C or higher).
■ 炉頂からの散水により強制冷却した後炉外へ掻き出
す。■ After being forcibly cooled by water spraying from the top of the furnace, it is scraped out of the furnace.
■ 羽目からの散水により・国内残留物下部より強fr
ill冷却後・扉外へ掻き出す。■ By watering from the siding, stronger fr than the lower part of the domestic residue
After the ill cools down, scrape it out of the door.
しかしながら■の方法は半年から1年に及ぶ放置期間を
必要とし、高炉の改修期間を著しく延長する問題かめる
。■の遠隔操作機械による方法は機械が特殊で技術的な
問題があり、作業期間も約1週間を要する。■の方法は
散水により炉内残留物を強制的に冷却するため1〜3日
で作業を終えることができる。しかし炉内残留物のなか
の赤熱コークスが水と反応しくC+H20→H2+ G
o )誘爆の危険の高い水性ガスを多最に生じ、炉内の
水性ガス濃度が安全限界以上に増大するため、安全面で
大きな問題がある。■の方法は炉内装入物の周辺部から
炉心部へ順次水冷冷却して、装入物を強制的に消火冷却
するとともに、当該消火冷却により生じる水性ガスを装
入物の上部に残る火種により逐次燃焼させて前記水性ガ
スが炉内に進数するのを防止するようにしているが、羽
口からの自然ドラフト空気源によりコークスが燃焼し′
扉内温度が過剰に上昇するという問題がある。この方法
も冷却期間に1〜3日を要す。However, the method (2) requires a period of 6 months to 1 year, which poses the problem of significantly extending the period for blast furnace repair. The method (2) using a remote-controlled machine involves technical problems because the machine is special, and the work takes about a week. Method (2) forcibly cools the residue in the furnace by sprinkling water, so the work can be completed in 1 to 3 days. However, the red-hot coke in the reactor residue reacts with water, resulting in C+H20→H2+ G
o) Water gas with a high risk of explosion is generated frequently, and the concentration of water gas in the reactor increases beyond the safe limit, which poses a major safety problem. Method (2) involves water-cooling the contents of the reactor from the periphery to the core, forcing the charge to be extinguished and cooled, and the water gas produced by the extinguishing cooling to be used as the spark remaining at the top of the charge. The coke is burned sequentially to prevent the water gas from entering the furnace, but the natural draft air source from the tuyeres causes the coke to burn.
There is a problem that the temperature inside the door increases excessively. This method also requires a cooling period of 1 to 3 days.
本発明は、羽口レベルまで降下させた前記・炉内装入物
を短期間でしかも安全に冷却しようとするもので、高炉
炉内装入物を羽口レベルまで降ドさせた後、羽口及び送
風支管は取付けた状態で羽目部のノズルより注水すると
共に、酸素5〜22%を含X7だ常温気体を羽口より送
風し・罪内装人物を冷却することを特徴とする。The present invention aims to safely cool the above-mentioned blast furnace contents that have been lowered to the tuyere level in a short period of time. The air blowing branch pipe is characterized in that when it is installed, water is injected from the nozzle in the paneling part, and normal temperature gas containing 5 to 22% oxygen at X7 is blown from the tuyere to cool the person inside the crime.
以下、本発明の詳細を第1図にて説明すると、まず、炉
内装入物(1)を高炉(2)の羽目(3)のレベルまで
降Fさせ溶銑を排出した後羽口部の液態吹込ノズル(4
)等より注水を行うと共に送風系統、環状管(6)、送
風支管(5)より酸素を含んだ常温気体(酸素濃度5〜
22チ)を吹込む。ここで、羽口より吹込む疵体中の酸
素濃度5チ以Fでは炉内で発生したCOガスを確実に燃
焼することが困難であり、22チ以Eでは炉内で発生し
たCOガスの急速な燃焼により矩内ガス濡度の異常上昇
をまねく。この注水による消火冷却時に赤熱コークスと
水とが反応して(C+H,,0→H2+CO)水性ガス
が生成する。Hereinafter, the details of the present invention will be explained with reference to FIG. 1. First, the contents in the furnace (1) are F lowered to the level of the slats (3) of the blast furnace (2), and after the hot metal is discharged, the liquid state at the tuyere section is Blow nozzle (4
), etc. while injecting water at room temperature containing oxygen (oxygen concentration 5~
22ch) is injected. Here, it is difficult to reliably burn the CO gas generated in the furnace if the oxygen concentration in the cracked body injected from the tuyere is 5 degrees F or higher, and if the CO gas generated in the furnace exceeds 22 degrees F. Rapid combustion leads to an abnormal increase in the wetness of the gas inside the tank. During extinguishing and cooling by this water injection, red-hot coke and water react to generate water gas (C+H,,0→H2+CO).
しかし部分的に燃焼が継続しているのと送風系統より吹
込まれる酸素とにより、水性ガスは安全に燃焼する。又
酸素と同時に吹込まれる常温気体の窒素により燃焼温度
は低下する。ここで、炉頂ガス温度および炉頂カス成分
は、前記の■注水蝋、■酸素濃度、■気体流喰を調整す
ることによりでき、安全に作業を行うことができる。し
かも羽口を取付けたままでfP業ができるため、吹止め
から冷却まで短期間ですむ。However, due to continued partial combustion and oxygen blown in from the ventilation system, the water gas is safely combusted. Furthermore, the combustion temperature is lowered by the room-temperature nitrogen gas that is blown in at the same time as the oxygen. Here, the furnace top gas temperature and furnace top scum components can be adjusted by adjusting the above-mentioned (1) water injection wax, (2) oxygen concentration, and (2) gas flow rate, so that work can be carried out safely. Moreover, fP operation can be performed with the tuyere attached, so the process from blowing off to cooling can be completed in a short period of time.
実施例として、炉内容@2,600扉の高・脳(羽口個
数28)において、炉内装入物を羽口まで降ドさせ、溶
銑を排出した後、羽目及び送風支管は取付けた状態で、
全ての羽口部の液態吹込みノズルより毎時85tの冷却
水を注入するとともに、羽口からも常温気体の窒素(酸
素濃度18%残り窒素)を流r! 250 Nm’/m
inで吹込み、12時間目で二酸化炭素の発生が停止し
た。これを炉内装入物の事実、ヒの消火完了と断定して
、さらに約8時間注水を続行し、15時間で炉内冷却作
業を終えることができた。この方法によると、従来1〜
3日要した冷却期間を15時間で完了することができる
。As an example, in a high-temperature furnace with a furnace content of 2,600 doors (28 tuyeres), after the contents in the furnace were lowered to the tuyere and the hot metal was discharged, the siding and the blower branch pipe were left attached. ,
In addition to injecting 85 tons of cooling water per hour from the liquid injection nozzles at all tuyeres, room temperature gaseous nitrogen (oxygen concentration 18% remaining nitrogen) is also flowed from the tuyeres! 250 Nm'/m
The generation of carbon dioxide stopped after 12 hours. Assuming that this was a fact of the contents in the reactor and that the fire had been extinguished, water injection continued for about 8 hours, and the cooling work in the reactor was completed in 15 hours. According to this method, conventionally 1 to
The cooling period that used to take three days can be completed in 15 hours.
第2図にこのときの羽口部からの注水ノスターン、平均
垣頂ガス温度変化、ならびに炉頂ガス各成分(co、c
o□e H210! )の量的経時変化をタイムチャー
トにより示す。注水開始時には一時的に炉頂ガス温度は
上昇するが、時間の経過とともに低下する。又、水性ガ
ス(H2,CO)は注水開始から冷却終了までの全期間
にわたって極めて低く抑制されている。Figure 2 shows the water injection nostern from the tuyere, the average fence top gas temperature change, and the top gas components (co, c
o□e H210! ) is shown in a time chart. At the start of water injection, the furnace top gas temperature temporarily increases, but decreases over time. Furthermore, water gas (H2, CO) is kept extremely low over the entire period from the start of water injection to the end of cooling.
以北の説明から明らかなように、本発明の方法は高炉吹
卸し後の炉内装入物を液体(水)及び気体(窒素、酸素
)により強制的に消火冷却するから、冷却期間が短く、
高炉改修の工期短縮などに大きな効果を発揮するのは勿
論のこと、その消火冷却により発生する水性ガスは羽口
より吹込まれる酸素により完全に燃焼させることができ
るため、作業の安全にも大きな効果を発揮するものであ
る。As is clear from the above explanation, the method of the present invention forcibly extinguishes and cools the contents in the blast furnace after blowing down the blast furnace with liquid (water) and gas (nitrogen, oxygen), so the cooling period is short;
Not only does it have a great effect on shortening the construction period for blast furnace renovation, but it also greatly improves work safety because the water gas generated by the extinguishing and cooling process can be completely combusted by the oxygen injected from the tuyeres. It is effective.
第1図は高炉下部の縦断面図、第2図はタイムチャート
である。
図中、1・・・装入物、2・・・高炉、3・・・羽口、
4・・・液態吹込ノズル、5・・・送風支管、6・・・
環状管。
出願人 住友金属工業、株式会社
第1図
第2図
注水開始力゛5の時間(H1FIG. 1 is a longitudinal sectional view of the lower part of the blast furnace, and FIG. 2 is a time chart. In the figure, 1...burden, 2...blast furnace, 3...tuyere,
4...Liquid state blowing nozzle, 5...Blower branch pipe, 6...
Annular tube. Applicant: Sumitomo Metal Industries, Ltd. Figure 1 Figure 2 Time of water injection start force 5 (H1
Claims (1)
口及び送風支管は取付けた状態で羽口部のノズルより注
水すると共に、酸素5〜22チを含んだ常温気体を羽口
より送風し、炉内装入物を冷却することを特徴とする高
炉吹卸し後の・炉内冷却法。1 After the contents in the blast furnace are lowered to the blade lorepel, water is injected from the nozzle in the tuyere section with the tuyere and air branch pipe attached, and room temperature gas containing 5 to 22 inches of oxygen is blown from the tuyere. A method for cooling the inside of a blast furnace after blowdown, which is characterized by cooling the contents inside the furnace.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14955382A JPS5938310A (en) | 1982-08-27 | 1982-08-27 | Cooling method of furnace inside after blowing out of blast furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14955382A JPS5938310A (en) | 1982-08-27 | 1982-08-27 | Cooling method of furnace inside after blowing out of blast furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5938310A true JPS5938310A (en) | 1984-03-02 |
Family
ID=15477673
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14955382A Pending JPS5938310A (en) | 1982-08-27 | 1982-08-27 | Cooling method of furnace inside after blowing out of blast furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5938310A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1628784A2 (en) | 2003-04-07 | 2006-03-01 | The Material Works Ltd. | Method of removing scale and inhibiting oxidation in processed sheet metal |
-
1982
- 1982-08-27 JP JP14955382A patent/JPS5938310A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1628784A2 (en) | 2003-04-07 | 2006-03-01 | The Material Works Ltd. | Method of removing scale and inhibiting oxidation in processed sheet metal |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2006312757A (en) | Injection lance for gaseous reducing material, blast furnace and blast furnace operation method | |
JPS62263906A (en) | Method for blowing pulverized coal from blast furnace tuyere | |
AU2012350144B2 (en) | Starting a smelting process | |
RU2621513C2 (en) | Way of starting melting process | |
JPS5938310A (en) | Cooling method of furnace inside after blowing out of blast furnace | |
JPS591606A (en) | Method of raising hot blast temperature | |
CA1258179A (en) | Method of producing a mixed gas and a plant therefor | |
JPH0463215A (en) | Method and apparatus for refining metal | |
JPS601362B2 (en) | Method for recovering thermal energy from converter exhaust gas | |
JPS5910964B2 (en) | Cooling method inside the blast furnace after blowing down | |
JPH0368710A (en) | Water cooling method for blast furnace contents | |
JPS63171810A (en) | Firing method for oxygen blast furnace | |
JPS6034602B2 (en) | Blast furnace reduced-scale blowdown method | |
JPS63176407A (en) | Production of molten iron | |
JP2002275554A (en) | Method for heat-insulating converter | |
SU1013481A1 (en) | Method for blast furnace smelting | |
JPH0586445B2 (en) | ||
JPS61228088A (en) | Coke dry quenching equipment | |
CN116516087A (en) | Method for increasing temperature of top gas of hydrogen-rich carbon circulating oxygen blast furnace | |
BR112020019543A2 (en) | DIRECT CASTING PROCESS WITH COMPLETE COMBUSTION | |
GB1601009A (en) | Process and plant for treating flue dust | |
JPS6115921B2 (en) | ||
JPH03191013A (en) | Method for cooling blast furnace | |
JPS59143012A (en) | Manufacture of steel in bottom or top and bottom blowing converter | |
JPS58100604A (en) | Operating method for blowing-down of blast furnace |