JPH10273714A - Bottom blowing tuyere - Google Patents
Bottom blowing tuyereInfo
- Publication number
- JPH10273714A JPH10273714A JP9497597A JP9497597A JPH10273714A JP H10273714 A JPH10273714 A JP H10273714A JP 9497597 A JP9497597 A JP 9497597A JP 9497597 A JP9497597 A JP 9497597A JP H10273714 A JPH10273714 A JP H10273714A
- Authority
- JP
- Japan
- Prior art keywords
- tuyere
- gas
- tube
- blowing
- heat insulating
- 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
Landscapes
- Carbon Steel Or Casting Steel Manufacturing (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は底吹き羽口に係り、
特に純酸素底吹き転炉、もしくは純酸素上底吹き転炉に
用いられる多重構造の底吹き羽口に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a tuyere
In particular, the present invention relates to a multi-layer bottom blowing tuyere used in a pure oxygen bottom-blowing converter or a pure oxygen top-bottom blowing converter.
【0002】[0002]
【従来の技術】従来、純酸素底吹き転炉もしくは純酸素
上底吹き転炉の底吹き羽口においては、図3に示す如き
2重管構造の底吹き羽口が使用されている。鉄皮2にラ
イニングされた永久れんが3および炉底れんが4には内
管6と外管8の2重管構造の羽口が羽口取付けフランジ
12上に固定して設けられ、内管6からは精錬用ガスと
して純酸素、窒素、アルゴン、炭酸ガスを吹込み、外管
8と内管6の間隙10からは羽口の保護冷却用ガスとし
てプロパン、窒素、アルゴン、炭酸ガス等を吹込み、炉
底羽口の損傷の防止を図っている。上記の如き2重管構
造の羽口においては保護冷却用ガスにより羽口先端に生
成する凝固鉄いわゆるマッシュルームを安定して生成
し、存在させることが重要である。しかし、操業中に
は、加熱、冷却による温度の変動が大きいうえ、炉底耐
火物とマッシュルームの含熱量(比熱)、熱伝導率、線
膨張率の差異から、マッシュルームが羽口保護の効果を
従来十分に挙げ得ないことがある。2. Description of the Related Art Conventionally, in a bottom blowing tuyere of a pure oxygen bottom blowing converter or a pure oxygen top bottom blowing converter, a bottom blowing tuyere having a double pipe structure as shown in FIG. 3 is used. In the permanent brick 3 and the hearth brick 4 lined with the steel shell 2, a tuyere having a double pipe structure of an inner pipe 6 and an outer pipe 8 is fixedly provided on a tuyere mounting flange 12, and is provided from the inner pipe 6. Blows pure oxygen, nitrogen, argon and carbon dioxide gas as refining gases, and blows propane, nitrogen, argon, carbon dioxide gas, etc. from the gap 10 between the outer tube 8 and the inner tube 6 as a tuyere protective cooling gas. To prevent damage to the furnace tuyere. In the tuyere having the double tube structure as described above, it is important that solidified iron, so-called mushroom, generated at the tip of the tuyere by the protective cooling gas is stably generated and present. However, during operation, the temperature fluctuates greatly due to heating and cooling, and the difference in the heat content (specific heat), thermal conductivity, and linear expansion coefficient of the refractory and the mushroom in the hearth indicates that the mushroom has the effect of protecting the tuyere. Conventionally, there are cases where it cannot be mentioned sufficiently.
【0003】底吹き機能を有する上記の如き転炉の冶金
的な優位性、長所は周知であるが、底吹き羽口が、安定
操業、炉寿命を左右し、その長寿命化、安定化が底吹き
転炉の最大の課題の一つである。この課題に対し、従来
以下の如き数々の対策、技術開発が行なわれてきてい
る。 耐スポーリング性に優れた羽口れんがの開発 スラグコーティング技術の開発 操業方法の改善(Q、D、T法;Quick Dir
ect Tapping) 羽口冷却の適正化 (イ)プロパン等の冷却ガス流量の適正制御 (ロ)酸素ガスへのAr、N2、CO2等の希釈冷却ガス
の混入[0003] Although the metallurgical advantages and advantages of the above-described converter having a bottom blowing function are well known, the bottom blowing tuyere affects the stable operation and furnace life. This is one of the biggest issues for bottom blown converters. To solve this problem, various countermeasures and technical developments as described below have been conventionally performed. Development of tuyere brick with excellent spalling resistance Development of slag coating technology Improvement of operation method (Q, D, T method; Quick Dir)
(Elect Tapping) Optimization of tuyere cooling (A) Proper control of cooling gas flow rate such as propane (B) Mixing diluted cooling gas such as Ar, N 2 , CO 2 into oxygen gas
【0004】以上の従来技術は、いずれも羽口寿命の向
上、損耗抑制に大きな効果を発揮しており、一応の成功
を収めている。しかし、羽口損耗現象面からみると、以
下の点で未だ問題が残されている。すなわち、羽口れん
がの吹錬中と非吹錬中との大きな温度変化を抑制し、羽
口冷却を適正化する手段としての下記技術において満足
すべき技術が開発されていない。 プロパン等の羽口冷却ガスの流量を低下させ、吹錬中
の羽口外管温度、羽口れんがの過冷却を防止する。 羽口冷却ガス(プロパン)に希釈ガス(Ar、N2、
CO2など)を混合し、吹錬中の羽口外管温度、羽口れ
んがの過冷却を防止する。 、と併せ、羽口内管から吹込まれる純酸素ガスに
希釈ガス(Ar、N2、CO2)を混合し、冷却ガスによ
る必要冷却量を減少させる。[0004] All of the above-mentioned prior arts have shown great effects on the improvement of the tuyere life and the suppression of the abrasion, and they have achieved some success. However, from the viewpoint of tuyere wear phenomenon, problems still remain in the following points. That is, a satisfactory technology has not been developed in the following technology as a means for suppressing a large temperature change between during and after blowing of tuyere brick and optimizing tuyere cooling. The flow rate of tuyere cooling gas such as propane is reduced to prevent the tuyere outer tube temperature during blowing and the supercooling of tuyere bricks. The dilution gas (Ar, N 2 ,
CO 2, etc.) are mixed, to prevent blade extraoral tube temperature during blowing, the supercooling of the tuyere brick. In addition, the diluent gas (Ar, N 2 , CO 2 ) is mixed with the pure oxygen gas blown from the tuyere inner tube to reduce the required cooling amount by the cooling gas.
【0005】以上の方法、手段は、羽口外管の過冷却を
防止し、羽口れんがの温度変化を抑制可能であるが、羽
口先端に形成されるマッシュルームまでもが縮小してし
まい、羽口れんがのクラック発生、れんが欠落は抑制で
きても、溶鋼と接する面の保護層が小さくなることによ
り、羽口先端からの損耗を抑制できない。また、の方
法はマッシュルームに与える熱量が小さくなり、マッシ
ュルーム維持保護には有効であるが、底吹きガスのほと
んどを占める内管ガスに希釈ガスを混合することは、精
錬ガスコストの上昇を招く結果となる。The above method and means can prevent the tuyere outer tube from overcooling and suppress the temperature change of the tuyere brick. However, even the mushroom formed at the tip of the tuyere is reduced. Even though crack generation and brick loss of the brick can be suppressed, wear from the tuyere tip cannot be suppressed because the protective layer on the surface in contact with the molten steel becomes small. In addition, the method of (1) reduces the amount of heat applied to the mushroom and is effective for maintaining and protecting the mushroom.However, mixing the diluting gas with the inner pipe gas, which accounts for most of the bottom blown gas, results in an increase in the cost of the smelting gas. Becomes
【0006】[0006]
【発明が解決しようとする課題】本発明の目的は、上記
底吹き羽口の従来技術の問題点、特に羽口れんがの吹錬
中と非吹錬中との大なる温度変化を抑制し、羽口冷却を
適正化し、もってマッシュルームの適正保護を有効とす
る底吹き羽口構造を提供しようとするものである。SUMMARY OF THE INVENTION It is an object of the present invention to suppress the problems of the prior art of the above-mentioned tuyere-blow tuyeres, in particular, to suppress a large temperature change during the tuyere brick blowing and non-blowing. It is an object of the present invention to provide a bottom-blow tuyere structure that optimizes tuyere cooling and thereby effectively protects mushrooms.
【0007】[0007]
【課題を解決するための手段】本発明者は底吹き羽口構
造の内、特に、羽口外管は吹錬時の過冷却ならびに非吹
錬時の温度上昇により甚しい温度変化によって羽口れん
が内にクラックの発生、れんがの欠落が生じ、一方羽口
冷却ガス流量を低下させた場合には溶鋼と接する面のマ
ッシュルームの保護層が小さくなり、羽口先端からの損
耗も甚しい現状に鑑み、外管の外側に更に最外管を設け
て不活性ガスを流す断熱管を設けることに着目し、試験
を重ねた結果、本発明を完成したもので、その要旨とす
るところは次のとおりである。 (1)精錬用ガスを吹込む内管と羽口の保護冷却用ガス
を吹込む外管との2重管構造を有して成る純酸素底吹き
もしくは純酸素上底吹き転炉の底吹き羽口において、前
記外管の更に外側に不活性ガスを流す断熱管を設けたこ
とを特徴とする底吹き羽口。 (2)前記内管、外管および断熱管より成る羽口周囲の
耐火物中に埋没して、もしくは前記断熱管の外面に接し
て設けられた温度センサーを有して成り、該温度センサ
ーによる温度情報に基づき前記不活性ガスの流量を制御
することを特徴とする上記(1)に記載の底吹き羽口。 (3)前記断熱管は高温強度の大なるステンレス鋼もし
くは耐熱鋼より成ることを特徴とする上記(1)もしく
は(2)に記載の底吹き羽口。 (4)前記外管の外面と断熱管の内面との間隙はほぼ1
mmであることを特徴とする上記(1)、(2)、
(3)のいずれかの項に記載の底吹き羽口。SUMMARY OF THE INVENTION The inventor of the present invention has found that the tuyere bricks, especially the tuyere outer tube, are subjected to excessive temperature change due to supercooling during blowing and temperature rise during non-blowing. In the event that cracks occur in the inside and bricks are lost, but when the tuyere cooling gas flow rate is reduced, the protective layer of the mushroom in contact with the molten steel becomes smaller, and the wear from the tuyere tip is extremely large. Focusing on providing an outermost tube outside the outer tube and providing an insulated tube through which the inert gas flows, as a result of repeated tests, the present invention was completed, and the gist thereof is as follows. It is. (1) Pure oxygen bottom blow or pure oxygen top bottom blow converter having a double pipe structure of an inner pipe for blowing refining gas and an outer pipe for blowing tuyere protection cooling gas A bottom-blow tuyere, wherein a heat-insulating tube through which an inert gas flows is provided further outside the outer tube at the tuyere. (2) It has a temperature sensor buried in the refractory around the tuyere consisting of the inner pipe, the outer pipe and the heat insulating pipe, or provided in contact with the outer surface of the heat insulating pipe. The tuyere according to (1), wherein the flow rate of the inert gas is controlled based on temperature information. (3) The bottom-blowing tuyere according to the above (1) or (2), wherein the heat-insulating pipe is made of stainless steel or heat-resistant steel having high high-temperature strength. (4) The gap between the outer surface of the outer tube and the inner surface of the heat insulating tube is substantially 1
(1), (2),
The bottom-blow tuyere according to any one of (3).
【0008】[0008]
【発明の実施の形態】本発明の実施の形態を添付図面を
参照して説明する。図1は本発明の底吹き羽口の構成を
示す断面図である。図1で示す本発明の底吹き羽口の構
成は、先に図3で説明した従来技術の2重管の底吹き羽
口の外管の更に外側に、外管の過冷却を防止する断熱管
を設けたものである。すなわち、転炉鉄皮13にライニ
ングされた永久れんが14および炉底れんが15には、
羽口内管16と羽口外管18の2重構造の羽口が設けら
れ、羽口の外側には羽口れんが20が設けられており、
羽口内管16からは精錬用ガスとして主として純酸素を
吹込み、羽口外管18と羽口内管16との間隙19から
は羽口の保護冷却用ガスとして主としてプロパンが吹込
まれることは従来と同一である。Embodiments of the present invention will be described with reference to the accompanying drawings. FIG. 1 is a cross-sectional view showing the configuration of the bottom blowing tuyere of the present invention. The configuration of the bottom blow tuyere of the present invention shown in FIG. 1 is provided on the outer side of the outer tube of the bottom blow tuyere of the prior art double tube described above with reference to FIG. A tube is provided. That is, the permanent brick 14 and the hearth brick 15 lined to the converter steel shell 13 include:
A tuyere having a double structure of a tuyere inner tube 16 and a tuyere outer tube 18 is provided, and a tuyere brick 20 is provided outside the tuyere.
Conventionally, pure oxygen is blown from the tuyere inner tube 16 as a refining gas, and propane is mainly blown from the gap 19 between the tuyere outer tube 18 and the tuyere inner tube 16 as a tuyere protection cooling gas. Are identical.
【0009】本発明は羽口外管18および羽口れんが2
0が冷却ガス、プロパン、により過冷却されるのを防止
するため、羽口外管の更に外側に断熱管22を設けたの
が大きな特徴である。羽口外管18と断熱管22との間
の間隙24は一定に保ち、設置することにより、2重管
羽口の外管18と、周囲の羽口れんが20との断熱化を
図ることができ、羽口れんが20の温度変化を抑制し、
羽口外管18の損耗速度を低減する作用を有している。
断熱管22の内面と羽口外管18の外面との間に形成さ
れる間隙24には、溶銑もしくは溶鋼26が侵入し閉塞
するのを防止するため最低流量のガスを吹込む。このガ
スは羽口冷却ガスのように熱分解して吸熱冷却効果を有
せず、また溶銑、溶鋼26と反応して発熱しない不活性
ガス、例えば、アルゴンガス(Ar)、もしくは窒素ガ
ス(N2ガス)を用いるのが望ましい。本発明では、こ
のガスを断熱管保護ガスと呼ぶこととする。The present invention relates to a tuyere outer tube 18 and a tuyere brick 2.
A major feature is that a heat insulating tube 22 is provided further outside the tuyere outer tube in order to prevent 0 from being supercooled by a cooling gas or propane. By keeping the gap 24 between the tuyere outer tube 18 and the heat insulating tube 22 constant and installing it, the outer tube 18 of the double tube tuyere and the surrounding tuyere brick 20 can be insulated. , Suppress the temperature change of tuyere brick 20,
It has the function of reducing the rate of wear of the tuyere outer tube 18.
A gas of a minimum flow rate is blown into a gap 24 formed between the inner surface of the heat insulating tube 22 and the outer surface of the tuyere outer tube 18 to prevent the hot metal or the molten steel 26 from entering and closing. This gas is thermally decomposed like a tuyere cooling gas, has no endothermic cooling effect, and reacts with hot metal or molten steel 26 to generate no inert gas, such as argon gas (Ar) or nitrogen gas (N). 2 ) is desirable. In the present invention, this gas is referred to as a heat insulating pipe protection gas.
【0010】断熱管22には、その長手方向の適当な箇
所に温度センサー28を設け、この温度センサー28よ
り得られる温度情報に基づいて、断熱管保護ガス30の
流量を制御する。具体的には該羽口れんが20の温度変
化が小さくなるように断熱管保護ガス30の流量の増減
を行う。温度センサー28の設置位置は、必ずしも断熱
管22の長手方向の位置でなくてもよい。すなわち、羽
口れんが20の中の適当な位置に埋没して設けてもよ
い。また、断熱管22の材料としては、溶融温度が高
く、かつ高温強度の大なる材料の使用が望ましく、具体
的にはステンレス鋼もしくは耐熱鋼が望ましい。The heat insulating pipe 22 is provided with a temperature sensor 28 at an appropriate position in the longitudinal direction, and controls the flow rate of the heat insulating pipe protection gas 30 based on temperature information obtained from the temperature sensor 28. Specifically, the flow rate of the heat insulating pipe protection gas 30 is increased or decreased so that the temperature change of the tuyere brick 20 is reduced. The installation position of the temperature sensor 28 does not necessarily have to be a position in the longitudinal direction of the heat insulating tube 22. That is, the tuyere brick may be provided so as to be buried in an appropriate position in the inside of the tuyere. Further, as a material of the heat insulating tube 22, it is desirable to use a material having a high melting temperature and high strength at high temperature, specifically, stainless steel or heat-resistant steel.
【0011】[0011]
【実施例】250tのK−BOPと称される上底吹き転
炉に本発明を適用し底吹き羽口の損耗速度を調査した。
すなわち、図1において、底吹き羽口は2重管羽口で羽
口内管16からは酸素ガスに希釈ガスとしてAr、N2
を混入し、羽口外管18と内管16との間隙19から冷
却ガスとしてプロパンに少量の希釈ガスAr、N2を吹
込み、更に外管18の外側に本発明の断熱管22を組込
み実吹錬した。断熱管22と外管18との間の間隙24
はほぼ1mmとし、その間隙を均一に維持するために外
管18の外面に管長手方向に連続した突起のスプライン
を数本設けた。この間隙24に流すガス、すなわち、断
熱管保護ガス30は、ArもしくはN2とし、鋼種によ
り適宜選択した。断熱管保護ガスの流量は吹錬中は最低
流量を1Nm3/min(羽口1本当り)とし、断熱管
22に設けた温度センサー28の値が適切な温度になる
ように、間隙24に流す不活性ガス流量を制御した。EXAMPLE The present invention was applied to a 250-ton top-bottom blow converter called K-BOP, and the wear rate of the bottom-blowing tuyere was investigated.
That, Ar 1, bottom blowing tuyeres as a diluent gas to the oxygen gas from the tuyere pipe 16 by a double tube tuyere, N 2
And a small amount of diluent gas Ar, N 2 is blown into propane as cooling gas from the gap 19 between the tuyere outer tube 18 and the inner tube 16, and the heat insulating tube 22 of the present invention is incorporated outside the outer tube 18. Blew up. Gap 24 between heat insulating tube 22 and outer tube 18
Is approximately 1 mm, and several splines of projections continuous in the longitudinal direction of the tube are provided on the outer surface of the outer tube 18 in order to keep the gap uniform. Gas flowing into the gap 24, i.e., the heat insulating tube protective gas 30, and Ar or N 2, and appropriately selected by grades. The flow rate of the protective gas for the adiabatic pipe is set to a minimum flow rate of 1 Nm 3 / min (per one tuyere) during the blowing, and is set in the gap 24 so that the value of the temperature sensor 28 provided in the adiabatic pipe 22 becomes an appropriate temperature. The flowing inert gas flow was controlled.
【0012】非吹錬中に間隙24が溶鋼16の侵入によ
り閉塞するおそれがない場合には、保護ガス30の流量
をゼロとし、それ以外の場合には羽口1本当り0.1N
m3/minまで減少して操業を行った。この試験操業
の結果を従来法と比較して、羽口れんがの吹錬中および
非吹錬中の温度変化量(最大値)および従来法における
羽口損耗速度を1とした場合の本発明実施例の値を表1
に示した。なお、吹錬操業条件は従来法および本実施例
ともほとんど同一とした。また羽口先端のマッシュルー
ムも目視観察では両者ともにほとんど差異は認められな
かった。If there is no possibility that the gap 24 will be closed by the intrusion of the molten steel 16 during non-blowing, the flow rate of the protective gas 30 is set to zero, otherwise 0.1 N per tuyere is used.
The operation was performed at a reduced m 3 / min. The results of the test operation were compared with those of the conventional method, and the present invention was carried out in the case where the amount of temperature change (maximum value) during blowing and non-blowing of tuyere brick and the tuyere wear rate in the conventional method were set to 1. Table 1 shows example values
It was shown to. The blowing operation conditions were almost the same in both the conventional method and this embodiment. The mushrooms at the tuyere tip also showed little difference between the two by visual observation.
【0013】[0013]
【表1】 [Table 1]
【0014】[0014]
【発明の効果】本発明は従来の2重管羽口の外側に1m
m程度の間隙をもって断熱管を設け、その間隙24に不
活性ガスを流し、この断熱管22の長手方向に温度セン
サー28を設けて該温度センサーが適正な温度値になる
ように不活性ガス流量を制御したので次の効果を挙げる
ことができた。 (イ)羽口先端に生成するマッシュルーム31を縮少さ
せることなく、羽口れんが20の吹錬時および非吹錬時
の最大温度変化量を従来の500℃から約50℃に1/
10に激減させ、かつ羽口損耗指数を従来法の1から
0.32まで低減させることができ、羽口寿命の延長を
低コストで実現させることができた。 (ロ)(イ)の結果、底吹き、上底吹き転炉の炉寿命を
向上でき、生産性の向上、コスト低減に大きく寄与でき
た。According to the present invention, 1 m is provided outside the conventional double tube tuyere.
An insulated pipe is provided with a gap of about m, an inert gas flows through the gap 24, and a temperature sensor 28 is provided in the longitudinal direction of the insulated pipe 22 so that the flow rate of the inert gas is adjusted so that the temperature sensor has an appropriate temperature value. , The following effects could be obtained. (A) The maximum temperature change during the blowing and non-blowing of the tuyere brick 20 is reduced from 500 ° C. in the related art to about 50 ° C. without reducing the mushroom 31 generated at the tuyere tip.
10, and the tuyere attrition index can be reduced from 1 of the conventional method to 0.32, and the extension of the tuyere life can be realized at low cost. (B) As a result of (a), the furnace life of the bottom-blowing and top-bottom-blowing converters can be improved, and it has greatly contributed to improvement in productivity and cost reduction.
【図1】本発明による底吹き羽口の実施例の構成を示す
断面図である。FIG. 1 is a sectional view showing a configuration of an embodiment of a bottom blowing tuyere according to the present invention.
【図2】従来の底吹き羽口の構成を示す断面図である。FIG. 2 is a cross-sectional view showing a configuration of a conventional tuyere.
2、13 転炉鉄皮 4、15 炉底れんが 6 内管 8 外管 10 間隙 14 永久れんが 16 羽口内管 18 羽口外管 19 間隙 20 羽口れんが 22 断熱管 24 間隙 26 溶鋼 28 温度センサー 30 断熱管保護ガス 31 マッシュルーム 2,13 converter iron shell 4,15 hearth brick 6 inner tube 8 outer tube 10 gap 14 permanent brick 16 tuyere inner tube 18 tuyere outer tube 19 gap 20 tuyere brick 22 heat insulating tube 24 gap 26 molten steel 28 temperature sensor 30 heat insulation Pipe protection gas 31 mushroom
Claims (4)
却用ガスを吹込む外管との2重管構造を有して成る純酸
素底吹きもしくは純酸素上底吹き転炉の底吹き羽口にお
いて、前記外管の更に外側に不活性ガスを流す断熱管を
設けたことを特徴とする底吹き羽口。1. A pure oxygen bottom-blowing or pure oxygen top-blowing converter having a double-pipe structure of an inner pipe for blowing refining gas and an outer pipe for blowing tuyere protective cooling gas. A bottom-blow tuyere, wherein a heat-insulating tube through which an inert gas flows is provided further outside the outer tube.
口周囲の耐火物中に埋没して、もしくは前記断熱管の外
面に接して設けられた温度センサーを有して成り、該温
度センサーによる温度情報に基づき前記不活性ガスの流
量を制御することを特徴とする請求項1に記載の底吹き
羽口。2. A temperature sensor buried in a refractory around a tuyere comprising the inner pipe, the outer pipe, and the heat insulating pipe, or provided in contact with an outer surface of the heat insulating pipe, The tuyere according to claim 1, wherein a flow rate of the inert gas is controlled based on temperature information obtained by a sensor.
ス鋼もしくは耐熱鋼より成ることを特徴とする請求項1
もしくは2に記載の底吹き羽口。3. The heat insulating tube according to claim 1, wherein the heat insulating tube is made of stainless steel or heat resistant steel having high strength at high temperature.
Or the bottom tuyere described in 2.
はほぼ1mmであることを特徴とする請求項1、2、3
のいずれかの項に記載の底吹き羽口。4. A gap between an outer surface of the outer tube and an inner surface of the heat insulating tube is approximately 1 mm.
The tuyere according to any one of the above items.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09497597A JP3882260B2 (en) | 1997-03-28 | 1997-03-28 | Bottom-blown tuyere and converter operation method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09497597A JP3882260B2 (en) | 1997-03-28 | 1997-03-28 | Bottom-blown tuyere and converter operation method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10273714A true JPH10273714A (en) | 1998-10-13 |
JP3882260B2 JP3882260B2 (en) | 2007-02-14 |
Family
ID=14124920
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP09497597A Expired - Fee Related JP3882260B2 (en) | 1997-03-28 | 1997-03-28 | Bottom-blown tuyere and converter operation method |
Country Status (1)
Country | Link |
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JP (1) | JP3882260B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002168375A (en) * | 2000-11-28 | 2002-06-14 | Toho Titanium Co Ltd | High temperature molten matter transfer pipe |
JP2017071852A (en) * | 2015-10-05 | 2017-04-13 | Jfeスチール株式会社 | Method for gas blowing by bottom-blown tuyere and refining method of steel |
-
1997
- 1997-03-28 JP JP09497597A patent/JP3882260B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002168375A (en) * | 2000-11-28 | 2002-06-14 | Toho Titanium Co Ltd | High temperature molten matter transfer pipe |
JP2017071852A (en) * | 2015-10-05 | 2017-04-13 | Jfeスチール株式会社 | Method for gas blowing by bottom-blown tuyere and refining method of steel |
Also Published As
Publication number | Publication date |
---|---|
JP3882260B2 (en) | 2007-02-14 |
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