JPH11241110A - Device for injecting reducing material into blast furnace - Google Patents
Device for injecting reducing material into blast furnaceInfo
- Publication number
- JPH11241110A JPH11241110A JP27248998A JP27248998A JPH11241110A JP H11241110 A JPH11241110 A JP H11241110A JP 27248998 A JP27248998 A JP 27248998A JP 27248998 A JP27248998 A JP 27248998A JP H11241110 A JPH11241110 A JP H11241110A
- Authority
- JP
- Japan
- Prior art keywords
- reducing material
- blast furnace
- material supply
- blow pipe
- reducing
- 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.)
- Withdrawn
Links
Landscapes
- Manufacture Of Iron (AREA)
- Blast Furnaces (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、高炉羽口のブロー
パイプから還元材を吹き込むための装置に関するもので
ある。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for blowing a reducing agent from a blow pipe of a tuyere of a blast furnace.
【0002】[0002]
【従来の技術】高炉操業にあっては、コークス代替とし
て、安価で燃焼性がよい燃料(微粉炭、石油、ナフサ
等)を羽口部より吹き込み、溶銑製造コスト低減、生産
性向上を図ってきており、特公昭40−23763号公
報にその技術が開示されている。特に直近では価格の点
から微粉炭吹き込みが主流となっている。2. Description of the Related Art In the blast furnace operation, as an alternative to coke, inexpensive and highly flammable fuels (pulverized coal, petroleum, naphtha, etc.) are blown from the tuyere to reduce hot metal production cost and improve productivity. The technology is disclosed in Japanese Patent Publication No. 40-23763. Especially recently, pulverized coal injection is the mainstream in terms of price.
【0003】また、微粉炭吹き込みに加えて種々のガス
を吹き込むことが、特開平4−268003号公報に提
示されている。この技術は該公報の記載によれば、羽口
部から微粉炭を高炉の内部に吹き込む場合において、微
粉炭吹き込み位置の手前100〜500mmより天然ガ
ス(LNG)、コークス炉ガス(COG)、プロパンガ
ス(LPG)などを吹き込み、微粉炭吹き込み位置の雰
囲気温度を1500〜2000℃に調整することに主眼
点を置いている。In addition, Japanese Patent Application Laid-Open No. 4-268003 discloses that various gases are blown in addition to pulverized coal. According to the description of this publication, according to the description of this publication, when pulverized coal is blown into the inside of a blast furnace from a tuyere, natural gas (LNG), coke oven gas (COG), propane gas is injected from 100 to 500 mm before the pulverized coal injection position. The main focus is on blowing gas (LPG) or the like and adjusting the ambient temperature at the pulverized coal blowing position to 1500 to 2000 ° C.
【0004】さらには、特開平4−358014号公報
には、高炉の羽口部から微粉炭を吹き込む際に、その分
解熱によるフレーム温度低下を防止し、高炉の炉熱を確
保し、かつ高炉の炉芯内温度を維持することにより、生
産性を向上させ燃料比を低下させることを目的とし、予
め微粉炭を高炉外にて熱分解し、生成したガス、ター
ル、チャーを全量羽口部から吹き込むか、或いは生成し
たガス、タールを除去し、残ったチャーのみを羽口部か
ら吹き込む技術が開示されている。また、その他にも生
産性を増すために送風中に酸素を富化した操業も通常実
施されている。Further, Japanese Patent Application Laid-Open No. 4-358014 discloses that when pulverized coal is blown from the tuyere of a blast furnace, a reduction in the frame temperature due to the decomposition heat thereof is prevented, the furnace heat of the blast furnace is secured, and The purpose is to improve productivity and lower the fuel ratio by maintaining the temperature inside the core of the furnace, and pulverized coal is thermally decomposed outside the blast furnace in advance, and all generated gas, tar, and char are A technique is disclosed in which gas or tar is blown from the air, or the generated gas and tar are removed, and only the remaining char is blown from the tuyere. In addition, an operation enriched with oxygen during blowing is usually performed to increase productivity.
【0005】上記燃料の吹き込みは殆ど高炉羽口のブロ
ーパイプ部分から行われており、固体燃料や液体燃料の
場合はランスを用いている。吹き込まれた燃料が送風中
の酸素と反応して部分燃焼し、CO、H2 等の還元材
を生成する位置は高炉羽口先端部の高炉内である。[0005] The above-mentioned fuel is mostly blown from the blowpipe portion of the tuyere of the blast furnace, and a lance is used in the case of solid fuel or liquid fuel. The injected fuel reacts with the oxygen in the blast to partially burn and reduce CO, H 2, etc.
Is generated in the blast furnace at the tip of the blast furnace tuyere.
【0006】通常の微粉炭吹き込み時のランス配設状態
を図6に模式的に示した。図において、高炉炉壁11に
は羽口12が設けられ、羽口12の後端にブローパイプ
13が連接されている。ブローパイプ13には加熱空気
等が供給されており、ブローパイプ13を介して羽口1
2から炉内14に送風される。このような送風羽口にお
いて、ランス17がブローパイプ13を貫通して加熱空
気の通路内で開口し、該ランス17を介して微粉炭がブ
ローパイプ13内に吹き込まれるように構成されてお
り、羽口12の前方にはガスにより噴流15が形成さ
れ、さらに、炉内14に充填されたコークスが旋回しな
がら燃焼する領域、すなわちレースウエイ16が形成さ
れている。FIG. 6 schematically shows a lance arrangement state during normal pulverized coal injection. In the figure, a tuyere 12 is provided on a blast furnace wall 11, and a blow pipe 13 is connected to a rear end of the tuyere 12. Heated air or the like is supplied to the blow pipe 13, and the tuyere 1 is
2 is blown into the furnace 14. In such a blowing tuyere, the lance 17 penetrates the blow pipe 13 and opens in the passage of the heated air, and the pulverized coal is blown into the blow pipe 13 through the lance 17, A jet 15 is formed by gas in front of the tuyere 12, and a region in which coke filled in the furnace 14 burns while rotating, that is, a raceway 16 is formed.
【0007】このような固体燃料または液体燃料では、
大量吹き込みによる高炉操業上発生する種々の障害を無
視すれば、その吹き込み量を増加することは、さほどの
困難を伴うこともないが気体燃料(還元材)において
は、固体および液体燃料に比較して単位重量当たりの容
量が多くなり、ランスからの吹き込みではランス(円筒
形を想定した場合)の径は極めて大きい径を持たざるを
得ず、特にこの気体燃料が高温度の場合には、気体容量
が温度に比例して増大するため、局部的な位置から大量
の気体燃料を供給するには設備的に不可能な状態であっ
た。In such a solid or liquid fuel,
Neglecting the various obstacles that occur during the operation of the blast furnace due to large-volume injection, increasing the amount of injection is not so difficult, but in gaseous fuels (reducing materials), compared to solid and liquid fuels. The volume per unit weight increases, and the diameter of the lance (assuming a cylindrical shape) must be extremely large when blowing from the lance. Since the capacity increases in proportion to the temperature, it has been impossible to supply a large amount of gaseous fuel from a local location.
【0008】[0008]
【発明が解決しようとする課題】本発明は従来のランス
によるブローパイプ内への還元材(燃料)吹き込み、特
に気体還元材の吹き込みには、その吹き込み量において
限界を有することから、その解決を図ったもので還元材
の大量吹き込みに適した装置を提供することを目的とす
るものである。SUMMARY OF THE INVENTION The present invention solves the problem of the conventional blowing of a reducing agent (fuel) into a blow pipe by a lance, particularly, the blowing of a gas reducing agent because the amount of the blowing is limited. It is an object of the present invention to provide an apparatus suitable for blowing a large amount of reducing material.
【0009】[0009]
【課題を解決するための手段】本発明の要旨とするとこ
ろは、下記手段を実施することにある。 (1) 還元材を高炉へ吹き込む高炉羽口のブローパイ
プにおいて、軸線に対して直角断面がほぼ長方形の扁平
形状を有する還元材供給管を、ブローパイプ軸線に対し
て長辺方向を平行とし、かつ該軸線に対して鋭角の傾斜
を持って前記ブローパイプ内面に臨ませた高炉への還元
材吹き込み装置。 (2) 前記高炉羽口のブローパイプ内面に臨ませた還
元材供給管において、該還元材供給管の短辺×長辺を5
〜30mm×50〜500mmとした(1)記載の高炉
への還元材吹き込み装置。The gist of the present invention is to implement the following means. (1) In a blowpipe of a blast furnace tuyere for injecting a reducing material into a blast furnace, a reducing material supply pipe having a flat shape whose cross section perpendicular to the axis is substantially rectangular is set so that the long side direction is parallel to the blowpipe axis, And an apparatus for injecting the reducing material into the blast furnace facing the inner surface of the blow pipe at an acute angle with respect to the axis. (2) In the reducing material supply pipe facing the inner surface of the blowpipe of the blast furnace tuyere, the short side x long side of the reducing material supply pipe is 5
The apparatus for blowing a reducing agent into a blast furnace according to (1), wherein the apparatus has a size of 3030 mm × 50-500 mm.
【0010】(3) 前記高炉羽口のブローパイプ内面
に臨ませた還元材供給管において、該還元材供給管の長
辺と短辺の扁平比(長辺/短辺)を5〜30とした
(1)または(2)記載の高炉への還元材吹き込み装
置。 (4) 前記高炉羽口のブローパイプ内面に臨ませた還
元材供給管において、該還元材供給管の傾斜角を20〜
60度とした(1)ないし(3)のいずれかに記載の高
炉への還元材吹き込み装置。(3) In the reducing material supply pipe facing the inner surface of the blowpipe of the blast furnace tuyere, an aspect ratio (long side / short side) of the long side and the short side of the reducing material supply pipe is 5 to 30. The apparatus for injecting a reducing agent into a blast furnace according to (1) or (2). (4) In the reducing material supply pipe facing the inner surface of the blow pipe of the blast furnace tuyere, the inclination angle of the reducing material supply pipe is 20 to
The apparatus for injecting a reducing material into a blast furnace according to any one of (1) to (3), wherein the apparatus is at 60 degrees.
【0011】(5) 前記高炉羽口のブローパイプ内面
に臨ませた還元材供給管において、該還元材供給管のブ
ローパイプ面接合部の短辺側先端部の形状を円弧形また
は尖頭形となした(1)ないし(4)のいずれかに記載
の高炉への還元材吹き込み装置。 (6) 前記高炉羽口のブローパイプ内面に臨ませて還
元材供給管を設置するに際し、該還元材供給管を前記ブ
ローパイプ円周面に対し、接線方向に配設した(1)な
いし(5)のいずれかに記載の高炉への還元材吹き込み
装置。(5) In the reducing material supply pipe facing the inner surface of the blow pipe of the blast furnace tuyere, the shape of the tip of the shorter side of the joint of the reducing material supply pipe and the blow pipe surface is arc-shaped or pointed. The apparatus for blowing a reducing agent into a blast furnace according to any one of (1) to (4). (6) When the reducing material supply pipe is installed facing the inner surface of the blow pipe of the blast furnace tuyere, the reducing material supply pipe is disposed tangentially to the circumferential surface of the blow pipe. 5) The apparatus for injecting a reducing material into a blast furnace according to any one of 5).
【0012】(7) 前記還元材供給管をブローパイプ
円周方向に、複数個配設した(1)ないし(6)のいず
れかに記載の高炉への還元材吹き込み装置。 (8) 前記複数個の還元材供給管をブローパイプ円周
方向に設置するに当たり、その個数を2〜8個とした
(1)ないし(7)のいずれかに記載の高炉への還元材
吹き込み装置。(7) The apparatus for blowing reducing material into a blast furnace according to any one of (1) to (6), wherein a plurality of the reducing material supply pipes are arranged in a circumferential direction of the blowpipe. (8) When setting the plurality of reducing material supply pipes in the circumferential direction of the blowpipe, reducing the number of the reducing material supply pipes to 2 to 8 and blowing the reducing material into the blast furnace according to any one of (1) to (7). apparatus.
【0013】(9) 前記複数個の還元材供給管をブロ
ーパイプ円周方向に設置するに当たり、その配設をブロ
ーパイプ円周面で千鳥状になした(1)ないし(8)の
いずれかに記載の高炉への還元材吹き込み装置。 (10) (9)において、前方還元材供給管と後方還
元材供給管のブローパイプ内開口部先端間の距離を50
〜500mmとした高炉への還元材吹き込み装置。(9) When the plurality of reducing material supply pipes are installed in the circumferential direction of the blowpipe, the arrangement is formed in a staggered manner on the circumferential surface of the blowpipe. The apparatus for injecting a reducing agent into a blast furnace according to item 1. (10) In (9), the distance between the front end of the opening in the blow pipe of the front reducing material supply pipe and the rear reducing material supply pipe is set to 50.
A blowing device for reducing material into a blast furnace of up to 500 mm.
【0014】(11) 前記複数個の還元材供給管をブ
ローパイプ円周方向に設置した際に、1個以上の還元材
供給管において該還元材供給管の断面積を異ならしめた
(1)ないし(10)のいずれかに記載の高炉への還元
材吹き込み装置。 (12) 前記還元材供給管をブローパイプに複数個配
設した場合に、そのうち何れか1以上の還元材供給管を
固体還元材とした(1)ないし(11)のいずれかに記
載の高炉への還元材吹き込み装置。(11) When the plurality of reducing material supply pipes are installed in the circumferential direction of the blowpipe, the cross-sectional areas of the reducing material supply pipes in one or more reducing material supply pipes are made different (1). The apparatus for injecting a reducing material into a blast furnace according to any one of (10) to (10). (12) The blast furnace according to any one of (1) to (11), wherein when a plurality of the reducing material supply pipes are provided in the blow pipe, at least one of the reducing material supply pipes is a solid reducing material. Reducing material injection device
【0015】(13) 前記還元材供給管をブローパイ
プに複数個千鳥状に配設し、そのうち何れかの還元材供
給管より固体還元材を供給する場合には、高炉側からの
距離が大きい方の還元材供給管を用いる(1)ないし
(12)のいずれかに記載の高炉への還元材吹き込み装
置。 (14) 前記ブローパイプに設置した複数個の還元材
供給管において、還元材供給管の断面積を異ならしめた
場合は、断面積の小さい方の還元材供給管から固体還元
材を供給する(12)または(13)に記載の高炉への
還元材吹き込み装置。(13) When a plurality of the reducing material supply pipes are arranged in a staggered manner on the blow pipe and a solid reducing material is supplied from any of the reducing material supply pipes, the distance from the blast furnace side is large. The apparatus for blowing a reducing agent into a blast furnace according to any one of (1) to (12), wherein the reducing agent supply pipe is used. (14) In the plurality of reducing material supply pipes installed in the blow pipe, when the sectional area of the reducing material supply pipe is changed, the solid reducing material is supplied from the reducing material supply pipe having the smaller sectional area ( 12) The apparatus for injecting a reducing material into a blast furnace according to (13) or (13).
【0016】(15) 前記還元材供給管を配設したブ
ローパイプに、還元材としての固体還元材を吹き込むた
めの専用ランスを別途設置した(1)ないし(11)の
いずれかに記載の高炉への還元材吹き込み装置。 (16) (15)において、微粉炭吹き込み専用ラン
スを別途設置するに当たり、該ランス先端を還元材供給
管のブローパイプ内開口部先端より50mm以上後方と
した高炉への還元材吹き込み装置。(15) The blast furnace according to any one of (1) to (11), wherein a dedicated lance for blowing a solid reducing material as a reducing material is separately provided in the blow pipe provided with the reducing material supply pipe. Reducing material injection device (16) An apparatus for injecting a reducing material into a blast furnace in which the dedicated lance for blowing pulverized coal according to (15) is arranged such that the end of the lance is at least 50 mm behind the end of the opening in the blow pipe of the reducing material supply pipe.
【0017】[0017]
【発明の実施の形態】本発明者らは、前述のようにブロ
ーパイプ内へ吹き込む還元材(固体,液体,気体を問わ
ず)量を如何にして増量することができるかについて、
鋭意研究検討を重ねた結果、本発明装置を開発すること
に成功した。BEST MODE FOR CARRYING OUT THE INVENTION The inventors of the present invention described how to increase the amount of a reducing agent (regardless of solid, liquid or gas) blown into a blow pipe as described above.
As a result of intensive research and studies, the inventors have succeeded in developing the device of the present invention.
【0018】以下、本発明を図面に基づいて説明する。
図1はブローパイプの概略を側断面図で示したものであ
る。図において、ブローパイプ13内に還元材供給管1
8を臨ませ、該還元材供給管18は該供給管軸線21に
対しその直角方向の断面がほぼ長方形の扁平形状を有
し、かつブローパイプ軸線20に対し長方形の長径方向
を平行にしてブローパイプ13に取り付けられ、ブロー
パイプ内面において開口している。また、該還元材供給
管18の軸線21はブローパイプ軸線20に対し傾斜角
θを付与せしめてある。Hereinafter, the present invention will be described with reference to the drawings.
FIG. 1 is a schematic side sectional view of a blow pipe. In the figure, a reducing material supply pipe 1 is provided in a blow pipe 13.
8, the reducing material supply pipe 18 has a flat shape whose cross section in a direction perpendicular to the supply pipe axis 21 is substantially rectangular, and the rectangular major axis direction is parallel to the blow pipe axis 20 and blows. It is attached to the pipe 13 and is open on the inner surface of the blowpipe. The axis 21 of the reducing material supply pipe 18 is given an inclination angle θ with respect to the blow pipe axis 20.
【0019】還元材供給管18をほぼ長方形とすること
により、ブローパイプ13の長手方向に還元材を広い領
域に亙って吹き込むことが可能となり、また、傾斜角θ
を持たすことによってブローパイプ13内を流れる熱風
に逆らわずに混入させることができる。還元材供給管1
8のブローパイプ13に対する開口寸法は、水平方向で
短辺(S)×長辺(L)は5〜30mm×50〜500
mm程度が適しており、その扁平比(長辺(L)/短辺
(S))は5〜30の範囲とすることが、還元材供給管
18の強度または、ブローパイプ13の開切による強度
低下を抑制するうえでも適当な値である。なお、還元材
供給管18の軸線とブローパイプ13の軸線に対する傾
斜角θについては、20〜60度程度が還元材を熱風中
へ均一に拡散させる意味合いから適切な値である。Since the reducing material supply pipe 18 has a substantially rectangular shape, the reducing material can be blown over a wide area in the longitudinal direction of the blow pipe 13, and the inclination angle θ
, It is possible to mix hot air flowing in the blow pipe 13 without opposing it. Reducing material supply pipe 1
The opening dimension for the blow pipe 13 of No. 8 is such that the short side (S) × the long side (L) is 5 to 30 mm × 50 to 500 in the horizontal direction.
mm is suitable, and its aspect ratio (long side (L) / short side (S)) is in the range of 5 to 30 depending on the strength of the reducing material supply pipe 18 or the cutoff of the blow pipe 13. This is an appropriate value for suppressing the reduction in strength. As for the inclination angle θ with respect to the axis of the reducing material supply pipe 18 and the axis of the blow pipe 13, about 20 to 60 degrees is an appropriate value from the viewpoint of uniformly diffusing the reducing material into the hot air.
【0020】また、還元材供給管18はブローパイプ1
3との接続面において扁平断面を有するが、還元材供給
元では通常のパイプ形状(円筒形)でブローパイプ13
に近傍において扁平形にすればよい。また、ブローパイ
プ13との接合面においてその断面が必ずしも正確な直
方形に限らず、製作上の容易性から図5に示すように長
方形の短辺側に丸味(例えば、円弧形)を持たせたもの
(a)、または尖頭角を持たせたもの(b)であっても
差し支えない。さらには楕円形のもの(c)であっても
よく、本発明において断面形状がほぼ長方形とは、これ
らの形状を全て包含して総称したものである。The reducing material supply pipe 18 is connected to the blow pipe 1
3 has a flat cross-section at the connecting surface, and the reducing material supply source has a normal pipe shape (cylindrical shape).
May be made flat in the vicinity. In addition, the cross section of the joint surface with the blow pipe 13 is not necessarily an accurate rectangular shape, but has a round shape (for example, an arc shape) on the short side of the rectangle as shown in FIG. (A) or (b) having a pointed angle. Further, the shape may be an elliptical shape (c), and the term “substantially rectangular” in the present invention is a generic name including all these shapes.
【0021】図2はブローパイプ13の周辺から還元材
供給管18を複数本(本例では4本)設置した状態を示
した正面図で、図に示すようにブローパイプ13へ円周
方向に複数個設置した方が還元材量を大量に吹き込むの
に適しており、2〜8個程度が望ましい。また、該還元
材供給管18を図3に示すように、ブローパイプ円周面
に対してその長径面を接線方向に設置するならば、吹き
込まれた還元材はブローパイプ13の内面を旋回しなが
ら熱風と共に高炉内へ搬送されるので好ましい態様と言
える。FIG. 2 is a front view showing a state in which a plurality of reducing material supply pipes 18 (four in this example) are installed from the periphery of the blow pipe 13, and as shown in FIG. It is more suitable to install a plurality of the reducing materials in a large amount, and it is desirable to use a plurality of the reducing materials. If the reducing material supply pipe 18 is installed with its long diameter surface tangential to the circumferential surface of the blow pipe as shown in FIG. 3, the blown reducing material swirls on the inner surface of the blow pipe 13. It can be said that this is a preferable mode because the blast furnace is transported together with the hot air into the blast furnace.
【0022】図4は還元材供給管18をブローパイプ1
3の外面へ千鳥状に配設したときの状態を側面図で示し
たもので、還元材供給管18の配置はブローパイプ13
の同一円周面に限らず、千鳥状になすことも可能であ
り、後述するように気体還元材と固体還元材を同時に供
給するときに有利に働く。また、千鳥状に配設する場合
は、前方還元材供給管と後方還元材供給管のブローパイ
プ内開口部先端間の距離(D)を50〜500mmの間
隔を保持せしめることが望ましい。FIG. 4 shows the reducing material supply pipe 18 connected to the blow pipe 1
3 is a side view showing a state where the reducing material supply pipe 18 is arranged in a staggered manner on the outer surface of the blow pipe 13.
Not only the same circumferential surface but also a zigzag shape can be used, which is advantageous when the gas reducing material and the solid reducing material are simultaneously supplied as described later. In the case of the staggered arrangement, it is desirable that the distance (D) between the front reducing material supply pipe and the tip of the opening in the blow pipe of the rear reducing material supply pipe be maintained at an interval of 50 to 500 mm.
【0023】以上ブローパイプ13内への還元材の吹き
込み装置について説明したが、該還元材が気体の場合
は、これらの装置に固体還元材(微粉炭)の吹き込みを
併用することを妨げるものではない。ブローパイプ13
に複数の還元材供給管18を有する場合は、いずれかの
還元材供給管18を固体還元材吹き込み専用とすること
が望ましく、この場合固体還元材の搬送速度は前記単管
ランスから供給する場合に比べ遅くなり、また、固体還
元材が拡散された状態で高炉内に吹き込まれるため、高
炉内における反応領域を拡大せしめることができる。The apparatus for blowing the reducing agent into the blow pipe 13 has been described above. However, in the case where the reducing agent is a gas, it does not prevent the simultaneous use of the blowing of the solid reducing agent (pulverized coal) into these devices. Absent. Blow pipe 13
When a plurality of the reducing agent supply pipes 18 are provided, it is desirable that any one of the reducing agent supply pipes 18 is dedicated to the blowing of the solid reducing agent. In addition, since the solid reducing agent is blown into the blast furnace in a diffused state, the reaction region in the blast furnace can be expanded.
【0024】さらに、還元材の供給量によっては固体還
元材供給管と、気体還元材供給管での断面積を異ならし
め、通常は固体還元材供給管の断面積を小さく採ること
も当然考慮すべきである。前述した還元材供給管をブロ
ーパイプに千鳥状に配設した場合(図3)に、固体還元
材は高炉側からの距離が大きい方の還元材供給管を用い
る方と、固体還元材が前方へ既に供給されている気体還
元材によって包囲されるような状態で、高炉内に搬送さ
れるので後述する単管ランスから固体還元材を供給した
時と同様の効果が期待できる。Further, the sectional area of the solid reducing material supply pipe and the sectional area of the gas reducing material supplying pipe are made different depending on the supply amount of the reducing material, and it is naturally taken into consideration that the sectional area of the solid reducing material supply pipe is usually made small. Should. When the reducing material supply pipes described above are arranged in a staggered manner on the blow pipe (FIG. 3), the solid reducing material is used in a direction in which the distance from the blast furnace is larger and the solid reducing material is disposed in front. Since it is conveyed into the blast furnace in a state surrounded by the gas reducing material already supplied to the blast furnace, the same effect as when a solid reducing material is supplied from a single tube lance described later can be expected.
【0025】また、固体還元材(微粉炭)の吹き込みは
前記に限られることなく、例えば、図1に点線で示した
ように、微粉炭吹き込みランス17を併設し、吹き込ま
れた微粉炭の周囲を気体還元材で包み込むような状態に
なるよう、該微粉炭吹き込みランス17を配設するなら
ば、微粉炭燃焼が高炉レースウエイ16内で行われ、羽
口先端部温度を高めることがなく、羽口の寿命の延長ま
たは高炉炉壁の損耗を防ぐことができ好ましい。この場
合、微粉炭吹き込みランス17の設定位置としては、そ
のランス先端を還元材供給管がブローパイプ内面で開口
している先端部より50mm以上後方とした方が前記理
由から望ましい。Further, the injection of the solid reducing agent (pulverized coal) is not limited to the above. For example, as shown by a dotted line in FIG. If the pulverized coal blowing lance 17 is arranged so as to wrap the pulverized coal with a gas reducing material, the pulverized coal combustion is performed in the blast furnace raceway 16 without increasing the tuyere tip temperature, This is preferable because it can prevent the tuyere's life from being prolonged or the blast furnace wall from being worn. In this case, as the setting position of the pulverized coal blowing lance 17, it is preferable that the leading end of the lance is located at least 50 mm behind the leading end of the reducing material supply pipe opened on the inner surface of the blow pipe for the above reason.
【0026】[0026]
【発明の効果】本発明装置によれば、高炉羽口のブロー
パイプ内への還元材吹き込みに当たって、従来装置によ
る吹き込み量の制約をうけることなく、吹き込み量を増
大させることが容易にでき、特に気体還元材吹き込みに
適しており、また、例えば気体還元材と固体還元材の同
時吹き込みも簡易に実施でき、高炉操業上有益な発明で
ある。According to the apparatus of the present invention, when blowing the reducing agent into the blowpipe of the blast furnace tuyere, the blowing amount can be easily increased without being restricted by the blowing amount of the conventional apparatus. The present invention is suitable for blowing a gas reducing material, and can simultaneously perform, for example, simultaneous blowing of a gas reducing material and a solid reducing material, which is useful in blast furnace operation.
【図1】ブローパイプに還元材供給管を設置した状態を
示す側断面図。FIG. 1 is a side sectional view showing a state in which a reducing material supply pipe is installed on a blow pipe.
【図2】ブローパイプに還元材供給管を複数配設した状
態を示す正面図。FIG. 2 is a front view showing a state in which a plurality of reducing material supply pipes are arranged on a blow pipe.
【図3】ブローパイプに還元材供給管を接線方向に設置
した状態を示す正面図。FIG. 3 is a front view showing a state in which a reducing material supply pipe is installed in a tangential direction on a blow pipe.
【図4】ブローパイプに還元材供給管を千鳥状に設置し
た状態を示す側面図。FIG. 4 is a side view showing a state in which reducing material supply pipes are installed in a staggered manner on a blow pipe.
【図5】ブローパイプへの還元材供給管の取付部形状の
1例を示した図。FIG. 5 is a diagram showing an example of a shape of a mounting portion of a reducing material supply pipe to a blow pipe.
【図6】従来のブローパイプへ微粉炭吹き込みランスを
設置した状態を示す概略図。FIG. 6 is a schematic diagram showing a state where a pulverized coal blowing lance is installed in a conventional blow pipe.
11 高炉炉壁 12 羽口 13 ブローパイプ 14 炉内 15 噴流 16 レースウェイ 17 微粉炭供給ランス 18 還元材供給管 20 ブローパイプ軸線 21 還元材供給管軸線 θ 還元材供給管の傾斜角 L 還元材供給管の長辺 S 還元材供給管の短辺 D 還元材供給管の先端部間の距離 REFERENCE SIGNS LIST 11 Blast furnace wall 12 Tuyere 13 Blow pipe 14 Furnace 15 Jet 16 Raceway 17 Pulverized coal supply lance 18 Reducing material supply pipe 20 Blow pipe axis 21 Reducing material supply pipe axis θ Reducing material supply pipe inclination angle L Reducing material supply Long side of pipe S Short side of reducing material supply pipe D Distance between tip of reducing material supply pipe
Claims (16)
ーパイプにおいて、軸線に対して直角断面がほぼ長方形
の扁平形状を有する還元材供給管を、ブローパイプ軸線
に対して長辺方向を平行とし、かつ該軸線に対して鋭角
の傾斜を持って前記ブローパイプ内面に臨ませたことを
特徴とする高炉への還元材吹き込み装置。In a blowpipe of a blast furnace tuyere for blowing a reducing agent into a blast furnace, a reducing agent supply pipe having a flat shape whose cross section perpendicular to the axis is substantially rectangular is parallel to a long side direction of the blowpipe axis. And a blower for reducing material injected into the blast furnace, wherein the blower faces the inner surface of the blow pipe at an acute angle with respect to the axis.
せた還元材供給管において、該還元材供給管の短辺×長
辺を5〜30mm×50〜500mmとしたことを特徴
とする請求項1記載の高炉への還元材吹き込み装置。2. A reducing material supply pipe facing the inner surface of a blow pipe of the blast furnace tuyere, wherein a short side × a long side of the reducing material supply pipe is 5-30 mm × 50-500 mm. Item 2. An apparatus for blowing a reducing agent into a blast furnace according to Item 1.
せた還元材供給管において、該還元材供給管の長辺と短
辺の扁平比(長辺/短辺)を5〜30としたことを特徴
とする請求項1または請求項2記載の高炉への還元材吹
き込み装置。3. An aspect ratio (long side / short side) of a long side and a short side of the reducing material supply pipe facing the inner surface of the blow pipe of the blast furnace tuyere is 5 to 30. The apparatus for injecting a reducing material into a blast furnace according to claim 1 or 2, wherein:
せた還元材供給管において、該還元材供給管の傾斜角を
20〜60度としたことを特徴とする請求項1ないし請
求項3のいずれかに記載の高炉への還元材吹き込み装
置。4. The reducing material supply pipe facing the inner surface of the blowpipe of the blast furnace tuyere, wherein the inclination angle of the reducing material supply pipe is set to 20 to 60 degrees. The apparatus for injecting a reducing agent into a blast furnace according to any one of the above.
せた還元材供給管において、該還元材供給管のブローパ
イプ面接合部の短辺側先端部の形状を円弧形または尖頭
形となしたことを特徴とする請求項1ないし請求項4の
いずれかに記載の高炉への還元材吹き込み装置。5. A reducing material supply pipe facing an inner surface of a blowpipe of the blast furnace tuyere, wherein a shape of an end portion on a short side of a joint portion of a blowpipe surface of the reducing material supply pipe is arc-shaped or pointed. The apparatus for injecting a reducing agent into a blast furnace according to any one of claims 1 to 4, characterized in that:
せて還元材供給管を設置するに際し、該還元材供給管を
前記ブローパイプ円周面に対し、接線方向に配設したこ
とを特徴とする請求項1ないし請求項5のいずれかに記
載の高炉への還元材吹き込み装置。6. When the reducing material supply pipe is installed facing the inner surface of the blow pipe of the blast furnace tuyere, the reducing material supply pipe is disposed tangentially to the circumferential surface of the blow pipe. The apparatus for injecting a reducing material into a blast furnace according to any one of claims 1 to 5.
向に、複数個配設したことを特徴とする請求項1ないし
請求項6のいずれかに記載の高炉への還元材吹き込み装
置。7. The apparatus for blowing reducing agent into a blast furnace according to claim 1, wherein a plurality of said reducing agent supply pipes are arranged in a circumferential direction of the blowpipe.
プ円周方向に設置するに当たり、その個数を2〜8個と
したことを特徴とする請求項1ないし請求項7のいずれ
かに記載の高炉への還元材吹き込み装置。8. The apparatus according to claim 1, wherein the number of the plurality of reducing material supply pipes is set to 2 to 8 in the circumferential direction of the blowpipe. For blowing reducing material into the blast furnace.
プ円周方向に設置するに当たり、その配設をブローパイ
プ円周面で千鳥状になしたことを特徴とする請求項1な
いし請求項8のいずれかに記載の高炉への還元材吹き込
み装置。9. The method according to claim 1, wherein the plurality of reducing material supply pipes are arranged in a staggered manner on the circumferential surface of the blow pipe when the plurality of reducing material supply pipes are installed in the circumferential direction of the blow pipe. 8. The apparatus for injecting a reducing agent into a blast furnace according to any one of 8.
と後方還元材供給管のブローパイプ内開口部先端間の距
離を50〜500mmとしたことを特徴とする高炉への
還元材吹き込み装置。10. The apparatus for blowing reducing agent into a blast furnace according to claim 9, wherein the distance between the front reducing agent supply pipe and the front end of the opening in the blow pipe of the rear reducing material supply pipe is 50 to 500 mm.
イプ円周方向に設置した際に、1個以上の還元材供給管
において該還元材供給管の断面積を異ならしめたことを
特徴とする請求項1ないし請求項10のいずれかに記載
の高炉への還元材吹き込み装置。11. When one of the plurality of reducing material supply pipes is installed in the circumferential direction of the blowpipe, the cross-sectional area of the reducing material supply pipe is changed in one or more reducing material supply pipes. The apparatus for injecting a reducing material into a blast furnace according to any one of claims 1 to 10.
数個配設した場合に、そのうち何れか1以上の還元材供
給管を固体還元材としたことを特徴とする請求項1ない
し請求項11のいずれかに記載の高炉への還元材吹き込
み装置。12. The method according to claim 1, wherein when a plurality of said reducing agent supply pipes are provided on the blow pipe, at least one of the reducing agent supply pipes is a solid reducing agent. The apparatus for injecting a reducing agent into a blast furnace according to any one of the above.
数個千鳥状に配設し、そのうち何れかの還元材供給管よ
り固体還元材を供給する場合には、高炉側からの距離が
大きい方の還元材供給管を用いることを特徴とする請求
項1ないし請求項12のいずれかに記載の高炉への還元
材吹き込み装置。13. A plurality of reducing material supply pipes are arranged in a staggered manner on a blow pipe, and when a solid reducing material is supplied from any of the reducing material supply pipes, the distance from the blast furnace side is larger. The apparatus for injecting a reducing agent into a blast furnace according to any one of claims 1 to 12, wherein the reducing agent supply pipe is used.
還元材供給管において、還元材供給管の断面積を異なら
しめた場合は、断面積の小さい方の還元材供給管から固
体還元材を供給することを特徴とする請求項12または
請求項13に記載の高炉への還元材吹き込み装置。14. When a plurality of reducing material supply pipes installed in the blow pipe have different cross-sectional areas, the solid reducing material is supplied from the reducing material supply pipe having a smaller cross-sectional area. The apparatus for injecting a reducing material into a blast furnace according to claim 12 or 13, wherein the apparatus is used.
イプに、還元材としての固体還元材を吹き込むための専
用ランスを別途設置したことを特徴とする請求項1ない
し請求項11のいずれかに記載の高炉への還元材吹き込
み装置。15. A lance for blowing a solid reducing material as a reducing material is separately provided in a blow pipe provided with the reducing material supply pipe. The apparatus for injecting a reducing agent into a blast furnace according to item 1.
専用ランスを別途設置するに当たり、該ランス先端を還
元材供給管のブローパイプ内開口部先端より50mm以
上後方としたことを特徴とする高炉への還元材吹き込み
装置。16. The blast furnace according to claim 15, wherein, when separately installing a lance for injecting pulverized coal, the end of the lance is at least 50 mm behind the end of the opening in the blow pipe of the reducing material supply pipe. Reducing material injection device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27248998A JPH11241110A (en) | 1997-12-24 | 1998-09-10 | Device for injecting reducing material into blast furnace |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP36604897 | 1997-12-24 | ||
JP9-366048 | 1997-12-24 | ||
JP27248998A JPH11241110A (en) | 1997-12-24 | 1998-09-10 | Device for injecting reducing material into blast furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11241110A true JPH11241110A (en) | 1999-09-07 |
Family
ID=26550229
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27248998A Withdrawn JPH11241110A (en) | 1997-12-24 | 1998-09-10 | Device for injecting reducing material into blast furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11241110A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006291251A (en) * | 2005-04-06 | 2006-10-26 | Jfe Steel Kk | Method for blowing reducing material into blast furnace and device therefor |
JP2007162038A (en) * | 2005-12-09 | 2007-06-28 | Jfe Steel Kk | Method and apparatus for injecting reduction material into blast furnace |
KR101009031B1 (en) | 2008-06-16 | 2011-01-18 | 주식회사 포스코 | Apparatus for injecting a fuel and apparatus for manufacturing molten iron comprising the same |
-
1998
- 1998-09-10 JP JP27248998A patent/JPH11241110A/en not_active Withdrawn
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006291251A (en) * | 2005-04-06 | 2006-10-26 | Jfe Steel Kk | Method for blowing reducing material into blast furnace and device therefor |
JP4720260B2 (en) * | 2005-04-06 | 2011-07-13 | Jfeスチール株式会社 | Method and apparatus for injecting reducing material into blast furnace |
JP2007162038A (en) * | 2005-12-09 | 2007-06-28 | Jfe Steel Kk | Method and apparatus for injecting reduction material into blast furnace |
KR101009031B1 (en) | 2008-06-16 | 2011-01-18 | 주식회사 포스코 | Apparatus for injecting a fuel and apparatus for manufacturing molten iron comprising the same |
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