JPH03191013A - Method for cooling blast furnace - Google Patents
Method for cooling blast furnaceInfo
- Publication number
- JPH03191013A JPH03191013A JP32893289A JP32893289A JPH03191013A JP H03191013 A JPH03191013 A JP H03191013A JP 32893289 A JP32893289 A JP 32893289A JP 32893289 A JP32893289 A JP 32893289A JP H03191013 A JPH03191013 A JP H03191013A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- water
- cooling
- blast furnace
- cooling water
- 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
- 238000001816 cooling Methods 0.000 title claims description 38
- 238000000034 method Methods 0.000 title abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 229910001868 water Inorganic materials 0.000 claims abstract description 34
- 239000000498 cooling water Substances 0.000 claims abstract description 20
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 5
- 238000002347 injection Methods 0.000 claims description 6
- 239000007924 injection Substances 0.000 claims description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 12
- 229910052742 iron Inorganic materials 0.000 abstract description 6
- 238000004880 explosion Methods 0.000 abstract description 4
- 238000010079 rubber tapping Methods 0.000 abstract description 4
- 238000007664 blowing Methods 0.000 abstract description 3
- 239000002801 charged material Substances 0.000 abstract 3
- 239000007789 gas Substances 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 4
- 229910000805 Pig iron Inorganic materials 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 230000001186 cumulative effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000000571 coke Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 230000008439 repair process Effects 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 241000269333 Caudata Species 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Landscapes
- Blast Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野コ
本発明は吹き止め後の高炉装入物および炉底部の冷却方
法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for cooling a blast furnace charge and a furnace bottom after blow-stopping.
[従来技術]
鉄鉱石から溶銑を製造する高炉は、−旦火入れをすると
5〜10年間は連続操業することになる。そして、この
間に高炉の炉体各部は損傷が進み、ついには所定の生産
能力を維持することが困難となる。したがって、そのよ
うな状態になると、炉と構成する耐火煉瓦の巻替えを中
心とした改修を行なう必要が生じる。[Prior Art] A blast furnace for producing hot metal from iron ore will operate continuously for 5 to 10 years once fired. During this time, damage progresses to each part of the blast furnace body, and eventually it becomes difficult to maintain a predetermined production capacity. Therefore, in such a situation, it becomes necessary to carry out repairs mainly by replacing the refractory bricks that make up the furnace.
高炉の改修を短期間で効率よく行なうには、燃焼用とし
て供給されている空気を吹き止めると同時に、高炉の中
に残留している高温の装入物、溶融スラグ、溶銑および
炉底部をできるだけ速く冷却してやることが必要である
。In order to repair a blast furnace efficiently in a short period of time, it is necessary to stop the air supplied for combustion, and at the same time remove as much of the high-temperature charges, molten slag, hot metal, and bottom of the furnace as possible that remain in the blast furnace. It is necessary to cool it quickly.
従来の高炉の装入物および炉底部を冷却する方法におい
ては、燃焼用空気を吹き止めると、直ちに炉頂部より冷
却水を注水し、炉頂ガスの温度が上がりすぎない程度に
徐々に注水量を増していく方法がとられていた。In the conventional method of cooling the charge and the bottom of the blast furnace, cooling water is injected from the top of the furnace immediately after the combustion air is stopped, and the amount of water injected is gradually reduced to the extent that the temperature of the top gas does not rise too much. The method was to increase the number of
[発明が解決しようとする課題]
しかしながら、従来の高炉の冷却法においては、次のよ
うな問題点があった。[Problems to be Solved by the Invention] However, the conventional blast furnace cooling method has the following problems.
(1)炉頂部から数本のノズルを使って注水するため、
炉の水平断面でみると冷却水が十分にかかる所とそうで
ない所ができ、全体として十分な冷却ができない。(1) Water is injected from the top of the furnace using several nozzles,
When looking at the horizontal cross section of the furnace, there are areas where the cooling water is sufficiently applied and areas where it is not, resulting in insufficient cooling as a whole.
(2)注水初期には、注がれた冷却水が炉の上部で蒸発
して、上昇ガス流を形成するので、炉の中下部の冷却が
遅れる。また、最も冷却を必要とする炉底部には、熱水
のみしか供給されず、冷却効率が悪い。(2) In the early stage of water injection, the poured cooling water evaporates in the upper part of the furnace and forms an upward gas flow, which delays the cooling of the middle and lower parts of the furnace. In addition, only hot water is supplied to the bottom of the furnace, which requires the most cooling, resulting in poor cooling efficiency.
本発明は、従来技術の上記のような問題点を解消し、吹
き止め後の高炉の装入物および炉底部の冷却が効率よく
行なえる高炉冷却法を提供することを目的としている。SUMMARY OF THE INVENTION An object of the present invention is to provide a blast furnace cooling method that solves the above-mentioned problems of the prior art and allows efficient cooling of the blast furnace charge and the bottom of the blast furnace after blowdown.
[課題を解決するための手段]
この発明に係る高炉冷却法は、吹き止め後の高炉装入物
および炉底部を冷却するに際し、冷却水を出銑口から炉
内に注水するとともに、羽口レベル以上の高さから排水
する高炉冷却方法であり、この冷却法において炉頂部に
おける水素ガス濃度が10%を超えないように、冷却水
の注水速度を制御する高炉冷却方法である。[Means for Solving the Problems] In the blast furnace cooling method according to the present invention, when cooling the blast furnace charge and the bottom of the furnace after blow-stopping, cooling water is injected into the furnace from the taphole and the tuyere This is a blast furnace cooling method in which water is drained from a height higher than that of the blast furnace, and in this cooling method, the cooling water injection rate is controlled so that the hydrogen gas concentration at the top of the furnace does not exceed 10%.
[作用]
この発明に係る高炉冷却方法は、吹き止め後の高炉装入
物および炉底部を冷却するに際し、冷却水を出銑口から
炉内に注水するとともに、羽目レベル以上の高さから排
水するようにしている。[Function] In the blast furnace cooling method according to the present invention, when cooling the blast furnace charge and the bottom of the furnace after blowdown, cooling water is injected into the furnace from the taphole, and water is drained from a height above the siding level. I try to do that.
その理由は次のとおりである。本冷却方法においては、
冷却水が炉床近くの高温部に直接供給されるため、水の
気化だけにとどまらず、水と赤熱コークスとの水性ガス
反応を起こす割合が大幅に増加する。一般に、冷却水に
よる吸熱反応は次の2種類に大別される。The reason is as follows. In this cooling method,
Since the cooling water is supplied directly to the high temperature area near the hearth, the rate of water gas reaction between water and red-hot coke is significantly increased, in addition to the vaporization of water. Generally, endothermic reactions caused by cooling water are roughly classified into the following two types.
(1)気化による吸熱
H2O(液体) + 720.000 Kcal/ T
onH20→H20(ガス)
・・・(1)
(2)水性ガス反応による吸熱
C+820+1,600,000 Kcal/ Ton
H20→CO+H2
・・・(2)
まず、注水された冷却水は(1)式のように1トン当た
り720,000 Kcalの熱量を奪って水蒸気とな
る。そして、この水蒸気とコークスとが(2)式のよう
に反応して、COとH2とが生成されるが、その際もと
の水1トン当たりに換算して1.600000にcal
の熱を奪う、したがって、総計では水1トン当たりに換
算して2,320.000 Kcalの熱を奪うことに
なり、(1)式の吸熱反応しか利用しなかった従来の冷
却方法に比較して、3倍以上の冷却効果があり、冷却水
の所要量が少なくてすむとともに、冷却所要時間も短縮
できる。(1) Endothermic H2O (liquid) due to vaporization + 720.000 Kcal/T
onH20→H20 (gas)...(1) (2) Endothermic C+820+1,600,000 Kcal/Ton due to water gas reaction
H20→CO+H2 (2) First, the injected cooling water absorbs 720,000 Kcal of heat per ton and becomes water vapor, as shown in equation (1). Then, this water vapor and coke react as shown in equation (2) to generate CO and H2, but at this time, the amount of cal is reduced to 1.600000 per ton of water.
Therefore, in total, 2,320.000 Kcal of heat is removed per ton of water, compared to the conventional cooling method that only uses the endothermic reaction of equation (1). As a result, the cooling effect is three times or more greater, the amount of cooling water required is small, and the time required for cooling can be shortened.
また、この冷却方法において炉頂部における水素ガス濃
度が10%を超えないように、冷却水の注水速度を制御
するようにしたのは、次の理由による。すなわち、炉内
のガス爆発を防ぐため、注水に際しては、炉内を水蒸気
または窒素ガスでパージし、正圧状態を保ちながら注水
するが、(2)式のような水性ガス反応により、大量の
H2ガスが発生する。そして、その濃度が過度になると
、炉頂ガス出口等で爆発着火を起こす可能性がある0発
明者等は、炉頂ガス中のH2ガス濃度が10%以下であ
れば、爆発着火を防止できることを経験的に確認してお
り、したがって、この条件下で注水するようにしたので
ある。Further, in this cooling method, the cooling water injection rate is controlled so that the hydrogen gas concentration at the top of the furnace does not exceed 10% for the following reason. In other words, in order to prevent a gas explosion inside the furnace, when injecting water, the inside of the furnace is purged with water vapor or nitrogen gas, and water is injected while maintaining a positive pressure state. H2 gas is generated. If the concentration becomes excessive, there is a possibility of explosion and ignition occurring at the furnace top gas outlet, etc. The inventors believe that explosion and ignition can be prevented if the H2 gas concentration in the furnace top gas is 10% or less. We have empirically confirmed that this is the case, and therefore we decided to inject water under these conditions.
なお、出銑口から注水するようにしたのは、出銑口がす
でに設けられた開口であり、注水用として特別に開口工
事をする必要がないからであり、吹き止め直後に残銑を
除去するために炉底に臨時出銑口を設けた場合には、こ
れを注水口としてもよい。The reason why water is injected from the taphole is that the taphole is already installed and there is no need to make any special opening work for water injection, and the remaining pig iron can be removed immediately after blow-off. If a temporary tap hole is provided at the bottom of the furnace for this purpose, this may be used as a water inlet.
[実施例]
本発明の1実施例の高炉の冷却方法を第1図および第2
図により説明する。[Example] A cooling method for a blast furnace according to an embodiment of the present invention is shown in Figs. 1 and 2.
This will be explained using figures.
第1図は、1実施例の高炉の冷却方法を示す説明図であ
る。吹止め後、高炉1の出銑口2に給水用バルブ3を備
えた給水管4を接続する。そして、炉装入物5がすべて
水没できる高さの炉壁6の位置に排水ロアを開口し、排
水用バルブ8を備えた排水管9を接続する。このように
してから、給水用バルブ3を開き、冷却水を炉内に注水
する。FIG. 1 is an explanatory diagram showing a method for cooling a blast furnace according to one embodiment. After blowing off, a water supply pipe 4 equipped with a water supply valve 3 is connected to the tap hole 2 of the blast furnace 1. Then, a drain lower is opened at a position on the furnace wall 6 at a height where all the furnace charges 5 can be submerged in water, and a drain pipe 9 equipped with a drain valve 8 is connected. After doing this, the water supply valve 3 is opened and cooling water is injected into the furnace.
第2図は、冷却開始時から冷却完了までの累計冷却水注
水量の推移を示すグラフである0本発明の方法では、炉
頂部でH2ガス濃度を随時測定し、H2ガス濃度が10
%以下になるように注水量を制御しながら冷却した。こ
のグラフに見られるように、従来法では冷却完了まで1
9時間かかり、累計注水量も1.400 )ンを要した
のに比較して、本発明による方法では冷却完了までの時
間が13時間と従来の70%程度に短縮できるとともに
、所要冷却水星も950トンと従来の70%に低減でき
た。Figure 2 is a graph showing the transition of the cumulative amount of cooling water injected from the start of cooling to the completion of cooling.
Cooling was performed while controlling the amount of water injected so that the amount of water was below %. As seen in this graph, the conventional method takes 1 minute to complete cooling.
Compared to the previous method, which required 9 hours and a cumulative water injection amount of 1,400 tons, the method of the present invention can shorten the time to complete cooling to 13 hours, approximately 70% of the conventional method, and also reduce the amount of water required for cooling. The amount was reduced to 950 tons, 70% of the conventional amount.
特に、本冷却方法においては、第1図に示す出銑口2レ
ベル以下に残留している残銑(通称サラマンダーという
)10が、温度の低い冷却水で効率よく冷却されるため
、発破による残銑の解体作業もきわめて円滑に行なうこ
とができた。In particular, in this cooling method, the residual pig iron (commonly known as salamander) 10 remaining below the second level of the taphole shown in Fig. 1 is efficiently cooled with low-temperature cooling water, so the residual iron remaining from blasting is The dismantling of the pig iron was also carried out extremely smoothly.
なお、第1図中符号11は、羽口である。Note that the reference numeral 11 in FIG. 1 is a tuyere.
し発明の効果]
本発明により、高炉および高炉装入物の冷却において、
冷却時間が短縮できるとともに、冷却水量を低減できる
。[Effects of the Invention] According to the present invention, in cooling a blast furnace and blast furnace charge,
The cooling time can be shortened and the amount of cooling water can be reduced.
第1図は本発明の1実施例の高炉の冷却方法を示す説明
図、第2図は冷却開始から冷却完了までの累計冷却水の
推移を示すグラフ図である。
1・・高炉、2・出銑口、4 ・給水管、5・・炉装入
物、7・排水口、9・・・排水管。FIG. 1 is an explanatory diagram showing a method of cooling a blast furnace according to an embodiment of the present invention, and FIG. 2 is a graph diagram showing changes in cumulative cooling water from the start of cooling to the completion of cooling. 1.Blast furnace, 2.Tapping port, 4.Water supply pipe, 5.Furnace charge, 7.Drainage port, 9.Drainage pipe.
Claims (2)
に際し、冷却水を出銑口から炉内に注水するとともに、
羽口レベル以上の高さから排水することを特徴とする高
炉冷却方法。(1) When cooling the blast furnace charge and the bottom of the furnace after blow-stopping, cooling water is injected into the furnace from the taphole, and
A blast furnace cooling method characterized by draining water from a height above the tuyere level.
ように、冷却水の注水速度を制御することを特徴とする
請求項1の高炉冷却方法。(2) The blast furnace cooling method according to claim 1, characterized in that the cooling water injection rate is controlled so that the hydrogen gas concentration at the top of the furnace does not exceed 10%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32893289A JPH03191013A (en) | 1989-12-19 | 1989-12-19 | Method for cooling blast furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32893289A JPH03191013A (en) | 1989-12-19 | 1989-12-19 | Method for cooling blast furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03191013A true JPH03191013A (en) | 1991-08-21 |
Family
ID=18215708
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32893289A Pending JPH03191013A (en) | 1989-12-19 | 1989-12-19 | Method for cooling blast furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03191013A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011137212A (en) * | 2009-12-28 | 2011-07-14 | Nippon Steel Corp | Method for cooling inner part in blast furnace |
-
1989
- 1989-12-19 JP JP32893289A patent/JPH03191013A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011137212A (en) * | 2009-12-28 | 2011-07-14 | Nippon Steel Corp | Method for cooling inner part in blast furnace |
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