JPS62142707A - Method for blowing granular particle into blast furnace - Google Patents

Method for blowing granular particle into blast furnace

Info

Publication number
JPS62142707A
JPS62142707A JP28393885A JP28393885A JPS62142707A JP S62142707 A JPS62142707 A JP S62142707A JP 28393885 A JP28393885 A JP 28393885A JP 28393885 A JP28393885 A JP 28393885A JP S62142707 A JPS62142707 A JP S62142707A
Authority
JP
Japan
Prior art keywords
furnace
blowing
slurry
powder
pipe
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
Application number
JP28393885A
Other languages
Japanese (ja)
Inventor
Junichi Furuya
淳一 古谷
Yasuhiko Sakaguchi
泰彦 阪口
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 Steel Corp
Original Assignee
Kawasaki Steel Corp
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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP28393885A priority Critical patent/JPS62142707A/en
Publication of JPS62142707A publication Critical patent/JPS62142707A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/001Injecting additional fuel or reducing agents
    • C21B5/003Injection of pulverulent coal
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/001Injecting additional fuel or reducing agents
    • C21B5/003Injection of pulverulent coal
    • C21B5/004Injection of slurries

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Blast Furnaces (AREA)
  • Manufacture Of Iron (AREA)

Abstract

PURPOSE:To easily adjust the distribution of heat and gas in a furnace by respectively discharging granular particles and liquid independently through respectively separate pipes of a lance for blowing consisting of multiple pipes, mixing the granular particles and liquid at the top end of the lance and blowing the mixture in the form of a slurry into the furnace. CONSTITUTION:The lance 5 for blowing is constituted of double pipes consisting of the inside pipe 5a and the outside pipe 5b coaxially disposed to the outside thereof. The inside pipe 5a is connected to a granular particle supply pipe 7 via a shut off valve 8 and discharges the granular particles 11. The outside pipe 5b discharges water or oil 12 via a shut off valve 10. The top end of the inside pipe 5a is made shorter than the top end of the outside pipe 5b and therefore, the granular particles 11 and the liquid 12 are efficiently mixed to form the uniform slurry 13. The slurry 13 is blown together with hot air from a blow pipe 4 into the furnace through the tuyere 3 thereof.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、粉粒体と液体を吹込み用ランスの先端部で
スラリー状に混合することによりスラリーの流量や混合
比の変更が迅速に行えるような高炉への粉粒体吹込み方
法に関する。
[Detailed Description of the Invention] [Industrial Application Field] This invention enables rapid changes in slurry flow rate and mixing ratio by mixing powder and liquid at the tip of a blowing lance to form a slurry. This invention relates to a method for blowing powder into a blast furnace.

〔従来の技+Fj ) 一般に、高炉の炉内操業の言m整を行うために、補助燃
料としての微粉炭や溶銑の脱珪材としての鉄鉱石粉など
を羽口から炉内へ吹込んだり、ブローパイプ内の熱風温
度や湿分を調整したり、さらに炉頂からのコークス投入
量の調整や炉内挿入物の分布調整などが実施されている
[Conventional technique + Fj] Generally, in order to adjust the internal operation of a blast furnace, pulverized coal as an auxiliary fuel and iron ore powder as a desiliconizing agent for hot metal are injected into the furnace through the tuyeres, The temperature and humidity of the hot air inside the blow pipe are adjusted, the amount of coke introduced from the top of the furnace is adjusted, and the distribution of materials inserted into the furnace is adjusted.

そして、前記微粉炭や鉄鉱石粉等の粉粒体は、水やオイ
ルなどと予め混合機等によりスラリー状に均一に混合し
たものを配管輸送で高炉羽口から炉内へ吹込む方法が採
られている。また、この際に炉内反応に速やかに寄与さ
せるため、または炉内状況に対応した吹込みをするため
にスラリーの濃度や流量、あるいは粉粒体の粒度の調整
などが行われている。
Powdered materials such as pulverized coal and iron ore powder are uniformly mixed with water, oil, etc. in a slurry using a mixer, and then transported via piping and blown into the furnace through the blast furnace tuyeres. ing. At this time, the concentration and flow rate of the slurry or the particle size of the powder or granules are adjusted in order to quickly contribute to the reaction in the furnace or to inject in accordance with the conditions in the furnace.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、このような従来の粉粒体の吹込み方法に
あっては、粉粒体が水やオイル等と予め混合されてスラ
リー状となっているために、(11配管中を輸送される
過程で比重差による粉粒体と液体との分離が生じて均一
な吹込みができなかったり、輸送配管内で閉塞を生じた
りする、(2)予めスラリ−状となっているので、状況
に対応しては流量調整ができるのみで、各吹込み羽口毎
にスラリー濃度を調整することができないため、炉体の
内周方向に沿ったレースウェイにおける微調整がでキナ
い、(3)スラリー濃度を適時に変更できないため、炉
況変化に迅速に対応できない、といった問題点があった
However, in such conventional methods of blowing powder and granules, since the powder and granules are mixed with water, oil, etc. in advance to form a slurry, (11) (2) Since it is already in a slurry form, it can be used in situations where the powder or granules and liquid separate due to the difference in specific gravity, making it impossible to blow uniformly or causing blockages in the transportation piping. (3) Slurry There was a problem in that the concentration could not be changed in a timely manner, making it impossible to respond quickly to changes in furnace conditions.

この発明は、このような問題点にかんがみてなされたも
のであって、粉粒体と液体とを多重管の吹込用ランスに
よってそれぞれ単独に吐出させた後、混合させてスラリ
ー状として炉内へ吹込む方法とすることにより上記問題
点を解決することを目的としている。
This invention was made in view of these problems, and involves discharging powder and liquid separately using a multi-tube blowing lance, and then mixing them together to form a slurry into a furnace. The aim is to solve the above problems by using a blowing method.

〔問題点を解決するための手段〕[Means for solving problems]

この発明は、高炉羽口から炉内へ粉粒体と液体とを吹込
み用ランスを介して吹込む方法において、粉粒体と液を
それぞれ単独に多重管で構成された吹込み用ランスのそ
れぞれ別個の管を通って吐出させるとともに、この吹込
み用ランスの先端部において粉粒体と液体を混合せしめ
スラリー状として炉内へ吹込む粉粒体の吹込み方法を提
供するものである。
This invention relates to a method for blowing powder and liquid into a blast furnace from a blast furnace tuyere through a blowing lance. The present invention provides a method for blowing powder and granules by discharging them through separate tubes, mixing the powder and liquid at the tip of the blowing lance, and blowing the mixture into a slurry into a furnace.

〔作用〕[Effect]

多重管である吹込み用ランスの一方の管から粉粒体を、
他方の管から液体をそれぞれ単独に吐出させるため粉粒
体と液体の吐出量をそれぞれ単独に適時変更することで
即座にスラリー濃度を調整することができ、さらに高炉
の各羽口ごとについても空気輸送される粉粒体の流量を
調整することによりスラリー濃度を調整することができ
るため、炉況に迅速に対応し、炉内反応に寄与できる。
Powder is transferred from one tube of the multi-tube blowing lance.
Since the liquid is discharged separately from the other tube, the slurry concentration can be adjusted instantly by changing the discharge amount of the powder and granules and the liquid separately at the appropriate time, and the air Since the slurry concentration can be adjusted by adjusting the flow rate of the transported granular material, it is possible to quickly respond to furnace conditions and contribute to the reaction in the furnace.

〔実施例〕〔Example〕

以下この発明を図面に基づいて説明する。第1〜3図は
この発明の一実施例を示すものである。
The present invention will be explained below based on the drawings. 1 to 3 show one embodiment of this invention.

図において1は高炉、2は耐火れんがで構成された炉体
、3は羽口、4は炉内へ熱風を供給するためのブローパ
イプ、4aはブローパイプ4の鉄皮、4bはブローパイ
プ4の内張り耐火物、5は吹込み用ランス、6は吹込用
ランスの案内管、7は炭材または脱珪材の粉粒体の供給
管、8はこの供給管に設けられた遮断弁、9は反応調整
用液体である水あるいはオイル等の液体供給管、lOは
この液体供給管に設けられた遮断弁である。
In the figure, 1 is a blast furnace, 2 is a furnace body made of refractory bricks, 3 is a tuyere, 4 is a blow pipe for supplying hot air into the furnace, 4a is an iron shell of the blow pipe 4, and 4b is a blow pipe 4 5 is a lance for blowing, 6 is a guide pipe for the lance for blowing, 7 is a supply pipe for powdery material of carbonaceous material or desiliconized material, 8 is a shutoff valve provided in this supply pipe, 9 is a liquid supply pipe for a reaction regulating liquid such as water or oil, and lO is a cutoff valve provided in this liquid supply pipe.

吹込み用ランス5は第2図にその詳細を拡大して示すよ
うに、内管5aと、これの外側に同軸に配置される外管
5bとからなる二重管である。内管5aは遮断弁8を介
して粉粒体供給管7に連結されて粉粒体11を吐出し、
外管5bは遮断弁10を介して水あるいはオイル12を
吐出する。ここで内管5aの先端を外管5bの先端より
も短かくすることにより噴射吐出された粉粒体11と液
体12とは効率よく混合し、均一のスラリー13となる
。スラリー13はブローパイプ4の熱風とともに羽口3
から炉内へ吹込まれる。またスラリー13は、水+微粉
炭、水+鉄鉱石粉2重油+漱粉炭2重油+鉄鉱石粉から
成るが、水+微粉炭の場合は水の混合割合によって微粉
炭の炉内における燃焼位置を調整し適正な炉熱や炉内ガ
ス分布が得られ、水上鉄鉱石粉の場合は水の冷却効果に
よりブローパイプ4内や羽口3内での反応を抑制し、レ
ースウェイ内で適正な溶銑脱珪反応に寄与させることが
できる。
As shown in enlarged detail in FIG. 2, the blowing lance 5 is a double tube consisting of an inner tube 5a and an outer tube 5b disposed coaxially outside the inner tube 5a. The inner pipe 5a is connected to the powder supply pipe 7 via the shutoff valve 8, and discharges the powder and granule 11.
The outer pipe 5b discharges water or oil 12 through a shutoff valve 10. By making the tip of the inner tube 5a shorter than the tip of the outer tube 5b, the ejected granular material 11 and liquid 12 are efficiently mixed to form a uniform slurry 13. The slurry 13 is transferred to the tuyere 3 along with the hot air from the blow pipe 4.
is blown into the furnace. In addition, the slurry 13 consists of water + pulverized coal, water + iron ore powder dual fuel oil + starch coal dual fuel oil + iron ore powder, but in the case of water + pulverized coal, the combustion position of the pulverized coal in the furnace is adjusted by the mixing ratio of water. In the case of floating iron ore powder, the reaction in the blow pipe 4 and tuyere 3 is suppressed by the cooling effect of water, and proper hot metal desiliconization is achieved in the raceway. It can contribute to the reaction.

また増産操業時において、重油+微粉炭の場合は適正な
炉熱や炉内ガス分布が得られ、重油+鉄鉱石粉の場合は
重油による冷却効果でブローパイプ4内や羽口3内での
鉄鉱石粉の反応を抑制してレースウェイ内での溶銑脱珪
反応に寄与するとともに重油によって適正な炉熱や炉内
ガス分布を得ることができる。
In addition, during increased production operations, if heavy oil + pulverized coal is used, appropriate furnace heat and gas distribution in the furnace can be obtained, and if heavy oil + iron ore powder is used, the cooling effect of heavy oil will reduce the iron ore inside the blow pipe 4 and tuyere 3. It suppresses the reaction of stone powder and contributes to the desiliconization reaction of hot metal in the raceway, and the heavy oil makes it possible to obtain appropriate furnace heat and gas distribution in the furnace.

そして本出願人らは、本発明による上記方法を実施した
ところ、以下のような結果を得た、すなわち、高炉1に
配設した30本の羽口3から、吹込用ランス5の1本当
り10〜500μ程度の粒度構成からなる微粉炭を内管
5aから50〜1000kg/Hの量を吐出させ、外管
5bから水を10〜100 kg/ Hの量吐出させて
両者を吹込用ランス5の先端部で混合してスラリーとし
たものを炉内へ吹込んだ際の結果を従来例と比較して第
3図(81に示し、同様に内管5aから10〜1000
μ程度の粒度構成の鉄鉱石粉を50〜2000 kg/
H量吐出させ、外管5bから重油を10〜30kg /
 H量吐出させて両者を吹込用ランス5の先端部で混合
してスラリーとしたものを炉内へ吹き込んだ際の結果を
第3図(b)に示したものである。また、炉容積300
0 rn’、送風温度1100°C2出銑量5400t
/Dの高炉において、水と微粉炭を前記条件で吹込んだ
ところ、第3図(alに示すごとく、送風温度をほぼ一
定とした場合、水と微粉炭の混合吹込比(kg/ t 
−p )の増大に従い出銑量は増加し、燃料比(微粉炭
とコークス、kg/1−p)は低減した。
When the applicants carried out the above method according to the present invention, they obtained the following results. Pulverized coal having a particle size of about 10 to 500μ is discharged from the inner tube 5a in an amount of 50 to 1000 kg/H, water is discharged from the outer tube 5b in an amount of 10 to 100 kg/H, and both are connected to the blowing lance 5. The results of mixing the slurry at the tip of the tube and blowing it into the furnace are compared with the conventional example, as shown in Figure 3 (81).
50 to 2000 kg of iron ore powder with particle size composition of μ
H amount is discharged, and 10 to 30 kg of heavy oil is discharged from the outer pipe 5b.
FIG. 3(b) shows the result when a slurry was produced by discharging H amount and mixing both at the tip of the blowing lance 5 into the furnace. In addition, the furnace volume is 300
0 rn', blowing temperature 1100°C2 tapping amount 5400t
When water and pulverized coal were injected under the above conditions in a blast furnace of /D, the mixing ratio of water and pulverized coal (kg/t
-p), the pig iron output increased and the fuel ratio (pulverized coal and coke, kg/1-p) decreased.

一方、脱珪材として鉄鉱石粉を重油と一緒に前記条件で
吹込んだ場合1.第3図(blに見るごとく、重油+鉄
鉱石粉の吹込量の増大に従い、溶銑中のSi値を低減さ
せることができた。
On the other hand, when iron ore powder is injected as a desiliconization material together with heavy oil under the above conditions, 1. As seen in Figure 3 (bl), as the amount of heavy oil + iron ore powder injected increased, the Si value in the hot metal could be reduced.

以上により、粉粒体(微粉炭または鉄鉱石粉)と液体(
水または重油)のそれぞれの流量や混合比を変えて炉内
へ吹込む際に、水と共に吹込めば冷却用として、重油と
共に吹込めば助燃用として作用し、羽口内及びレースウ
ェイ内における燃焼性や温度の調整ができることにより
粉粒体の反応調整が可能となって、炉内反応の促進かつ
安定化に寄与することができ、さらに羽口毎にスラリー
の流量や混合比を調整することで炉の内周方向のバラン
ス調整ができ、また炉況に応じた迅速な吹込み調整がで
きるようになった。
As a result of the above, powder (pulverized coal or iron ore powder) and liquid (
When blowing water (water or heavy oil) into the furnace at different flow rates and mixing ratios, it acts as a cooling agent when injected with water, and as an auxiliary combustion agent when injected with heavy oil, resulting in combustion within the tuyere and raceway. By being able to adjust the temperature and temperature, it is possible to adjust the reaction of the powder and granules, contributing to the promotion and stabilization of the reaction in the furnace.In addition, it is possible to adjust the slurry flow rate and mixing ratio for each tuyere. This makes it possible to adjust the balance in the direction of the inner circumference of the furnace, and to quickly adjust the blowing according to the furnace conditions.

また、吹込用ランス5内は水や重油が通過することによ
る冷却効果から、ブローパイプ4内の1100℃にも及
ぶ熱風や炉内からの輻射熱による吹込用ランス5の熱変
形ないし溶損を防止することができる。
In addition, the cooling effect caused by water and heavy oil passing through the inside of the blowing lance 5 prevents thermal deformation or melting of the blowing lance 5 due to hot air reaching up to 1100 degrees Celsius in the blow pipe 4 or radiant heat from inside the furnace. can do.

なお、本実施例においては、内管5aから粉粒体を、外
管5bから液体を吐出させたが、内管5aから液体を、
外管5bから粉粒体を吐出させてもよい。
In this example, powder and granules were discharged from the inner tube 5a and liquid was discharged from the outer tube 5b, but the liquid was discharged from the inner tube 5a.
The powder may be discharged from the outer tube 5b.

〔発明の効果〕〔Effect of the invention〕

以上説明したように、この発明によればその構成を、高
炉への粉粒体吹込み方法において、粉粒体と液体をそれ
ぞれ単独に多重管によって構成された吹込み用ランスの
それぞれ別個の管を通って吐出させ、その吹込み用ラン
スの先端部において粉粒体と液体を混合してスラリー状
とし、炉内へ吹込む方法としたため、スラリーの流量や
混合比の変更が迅速にできることがら炉況に対応した炉
熱や炉内ガス分布の調整を速やかにかつ容易に行うこと
ができる。さらに、吹込み用ランスの外管に液体を通す
場合は吹込み用ランスの熱変形ないし溶(員を防止でき
る、という効果が得られる。
As explained above, according to the present invention, in a method for blowing powder into a blast furnace, the powder and the liquid are individually transported through separate tubes of a blowing lance constituted by multiple tubes. The powder and liquid are mixed at the tip of the injection lance to form a slurry, which is then blown into the furnace, making it possible to quickly change the slurry flow rate and mixing ratio. Furnace heat and gas distribution in the furnace can be adjusted quickly and easily in response to furnace conditions. Furthermore, when the liquid is passed through the outer tube of the blowing lance, it is possible to prevent thermal deformation or melting of the blowing lance.

【図面の簡単な説明】 第1図は本発明に係る実施例の断面図、第2図は第1図
における部分拡大断面図、第3図は本実施例によって操
業した結果を従来例・との比較において示した線図で、
同図(a)は水と微粉炭を混合したスラリーを吹込んだ
場合、同図(blは重油と鉄鉱石粉を混合したスラリー
を吹込んだ場合である。 l・・・・・・高炉、3・・・・・・羽口、5・・・・
・・吹込み用ランス、5a・・・・・・内管、5b・・
・・・・外管、13・・・・・・スラリー 第2図
[Brief Description of the Drawings] Fig. 1 is a sectional view of an embodiment according to the present invention, Fig. 2 is a partially enlarged sectional view of Fig. 1, and Fig. 3 shows the results of operation according to the present embodiment compared to the conventional example. In the diagram shown in the comparison of
Figure (a) shows the case where a slurry of water and pulverized coal is injected, and figure (bl) shows the case of injecting the slurry of heavy oil and iron ore powder. 3...tuyere, 5...
...Blowing lance, 5a...Inner pipe, 5b...
...Outer tube, 13...Slurry Fig. 2

Claims (1)

【特許請求の範囲】[Claims] 高炉羽口から炉内へ粉粒体と液体とを吹込み用ランスを
介して吹込む粉粒体吹込み方法において、前記粉粒体と
液体を、それぞれ単独に多重管によって構成された吹込
み用ランスのそれぞれ別個の管を通って吐出させるとと
もに、該吹込み用ランスの先端部において前記粉粒体と
液体を混合せしめスラリー状として炉内へ吹込むことを
特徴とする高炉の粉粒体吹込み方法。
In a powder blowing method in which powder and liquid are blown into the furnace from a blast furnace tuyere through a blowing lance, the powder and liquid are individually blown into the furnace by multiple pipes. A blast furnace powder and granular material is discharged through separate pipes of a blast furnace, and the powder and granular material are mixed with a liquid at the tip of the blowing lance and blown into the furnace as a slurry. Blowing method.
JP28393885A 1985-12-17 1985-12-17 Method for blowing granular particle into blast furnace Pending JPS62142707A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28393885A JPS62142707A (en) 1985-12-17 1985-12-17 Method for blowing granular particle into blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28393885A JPS62142707A (en) 1985-12-17 1985-12-17 Method for blowing granular particle into blast furnace

Publications (1)

Publication Number Publication Date
JPS62142707A true JPS62142707A (en) 1987-06-26

Family

ID=17672159

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28393885A Pending JPS62142707A (en) 1985-12-17 1985-12-17 Method for blowing granular particle into blast furnace

Country Status (1)

Country Link
JP (1) JPS62142707A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0447908A1 (en) * 1990-03-20 1991-09-25 Hoesch Stahl Aktiengesellschaft Method and apparatus for the introduction of pulverized fuel into a blast furnace
JP2018016854A (en) * 2016-07-28 2018-02-01 Jfeスチール株式会社 Blast furnace operation method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0447908A1 (en) * 1990-03-20 1991-09-25 Hoesch Stahl Aktiengesellschaft Method and apparatus for the introduction of pulverized fuel into a blast furnace
WO1991014791A1 (en) * 1990-03-20 1991-10-03 Küttner Gmbh & Co. Kg Process and device for injecting coal dust and oxygen into a blast furnace
JP2018016854A (en) * 2016-07-28 2018-02-01 Jfeスチール株式会社 Blast furnace operation method

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