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JP2877026B2 - How to protect the refining tuyere - Google Patents

How to protect the refining tuyere

Info

Publication number
JP2877026B2
JP2877026B2 JP10800195A JP10800195A JP2877026B2 JP 2877026 B2 JP2877026 B2 JP 2877026B2 JP 10800195 A JP10800195 A JP 10800195A JP 10800195 A JP10800195 A JP 10800195A JP 2877026 B2 JP2877026 B2 JP 2877026B2
Authority
JP
Japan
Prior art keywords
tuyere
heat
rate
gas
mushroom
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.)
Expired - Fee Related
Application number
JP10800195A
Other languages
Japanese (ja)
Other versions
JPH08283822A (en
Inventor
敬太 中川
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries Ltd
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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP10800195A priority Critical patent/JP2877026B2/en
Publication of JPH08283822A publication Critical patent/JPH08283822A/en
Application granted granted Critical
Publication of JP2877026B2 publication Critical patent/JP2877026B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treatment Of Steel In Its Molten State (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Furnace Charging Or Discharging (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、溶銑および溶鋼の撹
拌を目的とする精錬炉等の金属溶湯容器のN2、CO2
Arガス等を吹込む底吹き羽口の保護方法に関する。
BACKGROUND OF THE INVENTION This invention, N 2 of the molten metal container refining furnace for the purpose of agitation of the molten iron and molten steel, CO 2,
The present invention relates to a method for protecting a tuyere that blows Ar gas or the like.

【0002】[0002]

【従来の技術】金属溶湯を精錬、保温、貯蔵、運搬等の
目的で収納する容器としては、種々のタイプのものがあ
る。例えば、精錬炉としては、LD転炉のほか、LF
炉、VAD炉、AOD炉、STB炉、RH真空装置、K
R真空装置等が知られている。精錬炉以外の容器として
は、取鍋、混銑炉、混銑車、タンディッシュ等が知られ
ている。これらの容器は、常に、あるいは時として撹拌
を行う必要の生じることがあり、機械撹拌方式やガス撹
拌方式が採用されている。このうち、ガス撹拌方式を採
用する場合は、一般に単管、二重管およびSA(Sin
gle Annular)羽口等の金属パイプを用いる
方法と、MHP(Multi Hole Dlug)、
PE(Permeable Element)、多孔ノ
ズル等の耐火物を用いる方法とに区分される(日本鉄鋼
協会、第100、101回西山記念技術講座:「撹拌を
利用した最近の製鋼技術の動向」より)。
2. Description of the Related Art There are various types of containers for storing molten metal for the purpose of refining, keeping heat, storing, transporting, and the like. For example, as refining furnaces, in addition to LD converters, LF
Furnace, VAD furnace, AOD furnace, STB furnace, RH vacuum equipment, K
R vacuum devices and the like are known. Ladles, mixed iron furnaces, mixed iron wheels, tundishes and the like are known as containers other than smelting furnaces. These containers sometimes or occasionally need to be stirred, and a mechanical stirring method or a gas stirring method is employed. Among them, when the gas stirring method is adopted, generally, a single tube, a double tube and an SA (Sin
A method using a metal pipe such as a tuyere (gle Annular) tuyere, MHP (Multi Hole Drug),
It is classified into a method using a refractory such as PE (Permable Element) and a perforated nozzle (from the Iron and Steel Institute of Japan, 100th and 101st Nishiyama Memorial Technical Lecture: "Recent trends in steelmaking technology using agitation").

【0003】上記金属溶湯容器の底部羽口から不活性ガ
ス吹込みによるガス撹拌においては、図5に示すとお
り、炉底耐火物1近傍の溶湯2は底部羽口3吹込まれた
ガス4による一次的冷却作用を受けて羽口3上部で固化
し、マッシュルーム5と呼称される地金の塊を形成す
る。そしてマッシュルーム5内には、細いガス抜き道6
が形成され、吹込みガス4はこのガス抜き道6を通って
溶湯2中に噴出し、気泡となって上昇してゆく。しか
し、このマッシュルーム5の状態如何によっては、ガス
抜き道6が十分に形成されず、かなりの頻度で閉塞を生
じることがあって、ガスの安定吹込みが達成できない場
合がある。また、金属溶湯容器のガス撹拌においては、
上記の問題以外に溶湯内に噴射されたガスジェットの挙
動、特に噴射直後の下向流による底叩き(バックアタッ
ク)が大きく、図6に示すとおり、羽口3ばかりでなく
羽口3近傍の炉底耐火物1の溶損や亀裂が激しいという
問題点を有している。
[0003] In the gas stirring by blowing inert gas from the bottom tuyere of the above molten metal vessel, as shown in FIG. The metal is solidified at the upper part of the tuyere 3 by the cooling action, and forms a metal lump called mushroom 5. And inside the mushroom 5, there is a thin venting path 6
Is formed, and the blown gas 4 is ejected into the molten metal 2 through the gas vent path 6, and rises as bubbles. However, depending on the state of the mushroom 5, the gas vent path 6 may not be formed sufficiently, and may be blocked at a considerable frequency, so that stable gas blowing may not be achieved. Also, in the gas stirring of the molten metal container,
In addition to the problems described above, the behavior of the gas jet injected into the molten metal, particularly the bottom strike (back attack) due to the downward flow immediately after the injection, is large, and as shown in FIG. There is a problem that the furnace bottom refractory 1 is severely melted or cracked.

【0004】上記金属溶湯容器のガス撹拌用の羽口の溶
損を防止する方法としては、溶融金属中に精錬または撹
拌のための流体を吹込むべく設けられる羽口において、
その断面の内周長と、その内周断面積に等しい面積を有
する円の周長との比が1.07以上とした羽口(特公昭
56−52100号公報)、金属溶湯容器の底部ないし
側壁に設けられるガス吹込みノズルであって、中心部に
位置する芯体の外側に、外管を該芯体との間に適当な間
隔を開けて嵌挿固定し、リング状のガス吐出流路を形成
させたノズル(特開昭57−114623号公報)等が
提案されている。
[0004] As a method of preventing the gas stirring tuyere of the molten metal vessel from being melted, a tuyere provided to blow a fluid for refining or stirring into the molten metal is provided as follows.
A tuyere (JP-B-56-52100) in which the ratio of the inner peripheral length of the cross section to the circumference of a circle having an area equal to the inner peripheral cross-sectional area is 1.07 or more. A gas injection nozzle provided on a side wall, wherein an outer tube is fitted and fixed at an appropriate interval between the core body and the outside of a core body located at a central portion, thereby forming a ring-shaped gas discharge flow. A nozzle having a passage formed therein (Japanese Patent Laid-Open No. 57-114623) has been proposed.

【0005】[0005]

【発明が解決しようとする課題】上記特公昭56−52
100号公報に開示の羽口は、バックアタックの発生抑
制による衝撃低下によって羽口の溶損を防止するもの
で、マッシュルームの形成により羽口ならびに羽口近傍
の耐火物の寿命延長を図るものではない。また、特開昭
57−114623号公報に開示のノズルは、中心部に
位置する芯体の外側に、外管を該芯体との間に適当な間
隔を開けて嵌挿固定し、リング状のガス吐出流路を形成
させることによって、マッシュルームをポーラス化し、
マッシュルームでの圧損を低下ならびにバックアタック
の発生抑制を図るものであるが、外管と芯体との間の間
隔については特定されておらず、僅かに実施例にノズル
の背圧と外管と芯体との間の間隔と吹込み時のノズル閉
塞との関係が示されているのみである。
SUMMARY OF THE INVENTION The above-mentioned Japanese Patent Publication No. Sho 56-52.
The tuyere disclosed in Japanese Patent Publication No. 100 is intended to prevent the erosion of the tuyere by reducing the impact by suppressing the occurrence of the back attack, and to extend the life of the tuyere and the refractory in the vicinity of the tuyere by forming a mushroom. Absent. Further, the nozzle disclosed in Japanese Patent Application Laid-Open No. 57-114623 has an outer tube fitted and fixed to the outside of a core located at a central portion thereof with an appropriate gap between the core and the core. The mushroom is made porous by forming a gas discharge flow path of
Although it is intended to reduce the pressure loss in the mushroom and suppress the occurrence of back attack, the interval between the outer tube and the core is not specified, and slightly in the embodiment, the back pressure of the nozzle and the outer tube Only the relationship between the spacing between the core and the nozzle blockage during blowing is shown.

【0006】この発明の目的は、上記従来技術の欠点を
解消し、操業可能なガス吹込み圧力範囲で、羽口部に適
正なマッシュルームを形成させることによって、羽口な
らびに羽口近傍の耐火物の寿命延長を図ることができる
精錬用底吹き羽口の保護方法を提供することにある。
SUMMARY OF THE INVENTION It is an object of the present invention to solve the above-mentioned drawbacks of the prior art and to form an appropriate mushroom in a tuyere portion in an operable gas injection pressure range, so that the tuyere and a refractory in the vicinity of the tuyere can be formed. It is an object of the present invention to provide a method for protecting a bottom blowing tuyere for refining, which can extend the life of the bottom.

【0007】[0007]

【課題を解決するための手段】本発明者らは、上記目的
を達成すべく精錬用底吹き羽口形状とマッシュルーム形
成状況の定量化について、種々試験研究を行った。その
結果、底吹きガスによる冷却は、羽口の溶損防止には必
要であるが、底吹きガスの冷却により発生する底部耐火
物内の熱応力はスポーリング抑制には有害である。ま
た、本来底吹きガス量は、精錬特性により決定されるた
め、羽口ならびに羽口近傍の耐火物の寿命延長とは相反
する因子の整合が要求される。また、底吹き羽口部への
マッシュルームの形成は、マッシュルームの形成量が大
きくなると、マッシュルームでの圧損量が大きくなり、
吹込み可能ガス流量域が狭くなるが、羽口溶損抑制効果
が大きくなる。一方、マッシュルームの形成量が小さい
と、マッシュルームでの圧損量が小さくなり、吹込み可
能ガス流量域が広くなるが、羽口溶損抑制効果が小さく
なる。
Means for Solving the Problems The present inventors have conducted various tests and studies on the quantification of the shape of the bottom blowing tuyere for refining and the state of mushroom formation in order to achieve the above object. As a result, cooling with the bottom blown gas is necessary to prevent melting of the tuyere, but thermal stress in the bottom refractory generated by cooling the bottom blown gas is harmful to spalling suppression. In addition, since the bottom blown gas amount is originally determined by the refining characteristics, it is necessary to match factors that are inconsistent with the life extension of the tuyere and the refractory near the tuyere. Also, the formation of mushrooms in the tuyere part of the bottom blow, the larger the amount of mushrooms formed, the greater the pressure loss in the mushrooms,
Although the blowable gas flow rate area is narrowed, the effect of suppressing tuyere erosion is increased. On the other hand, if the formation amount of the mushroom is small, the pressure loss amount in the mushroom is small, and the blowable gas flow rate region is wide, but the tuyere erosion suppression effect is small.

【0008】すなわち、マッシュルームの形成量は、大
きいほど羽口保護効果があると考えられるが、マッシュ
ルームによる圧損増加によって、吹込みガス流量が制限
されるため、操業可能な範囲でマッシュルームを形成す
る必要がある。さらに、試験研究を進めた結果、マッシ
ュルームの生成量は、羽口形状による熱バランスにより
制御可能であることを究明し、この発明に到達した。
[0008] That is, it is considered that the larger the amount of mushrooms formed, the more effective the tuyere protection effect is. However, the increase in pressure loss due to the mushrooms restricts the flow rate of the blown gas, so that the mushrooms must be formed within an operable range. There is. Furthermore, as a result of further study, it was found that the amount of mushrooms produced can be controlled by the heat balance of the tuyere shape, and the present invention has been achieved.

【0009】すなわちこの発明は、中心部に位置する芯
体の外側内管に、外管を前記内管との間に適当な隙間を
開けて嵌挿固定し、リング状のガス吐出流路を形成して
なるガス吹込みノズルを有する精錬用底吹き羽口の保護
方法において、底吹きガス流量に基づいて、下記(1)
式による受熱指数、すなわち、下記(2)式により求め
た受熱速度を下記(3)式により求めた抜熱速度で除し
て求めた値が20〜40となる内管および外管の内外径
を選択することを特徴とする精錬用底吹き羽口の保護方
法である。 受熱指数=受熱速度/抜熱速度 (1)式 受熱速度=D0 2−(D1 2−d0 2) (2)式 抜熱速度=(0.13×D1×V0.8)/(D1 2−d0 22 (3)式 ただし、D0:外管の外径(mm)、D1:外管の内径
(mm)、d0:内管の外径(mm)、d1:内管の内径
(mm)、V:ガス流量(Nm3/hr)
That is, according to the present invention, an outer tube is fitted and fixed to an outer inner tube of a core located at a central portion with an appropriate gap provided between the inner tube and the outer tube, thereby forming a ring-shaped gas discharge passage. In the method for protecting a bottom blowing tuyere for refining having a formed gas blowing nozzle, the following (1)
The inner and outer diameters of the inner tube and the outer tube having a value obtained by dividing the heat receiving rate determined by the following equation (2) by the heat removal rate determined by the following equation (3) is 20 to 40. And a method for protecting a bottom blowing tuyere for refining. Heat index = heat rate / heat extraction rate (1) heat rate = D 0 2 - (D 1 2 -d 0 2) (2) Equation heat extraction rate = (0.13 × D 1 × V 0.8) / ( D 1 2 -d 0 2) 2 (3) equation However, D 0: the outside diameter of the outer tube (mm), D 1: inside diameter of the outer tube (mm), d 0: the outside diameter of the inner tube (mm), d 1 : inner diameter of inner tube (mm), V: gas flow rate (Nm 3 / hr)

【0010】[0010]

【作用】マッシュルームの生成は、羽口の熱バランス、
すなわち、溶鋼からの受熱と吹込みガスによる冷却の影
響を受けるため、羽口形状による熱バランスの変化を定
量化するため、前記(1)式による受熱指数、すなわ
ち、前記(2)式により求めた受熱速度を前記(3)式
により求めた抜熱速度で除して求めた値をマッシュルー
ム形成の指標とした。なお、受熱速度は、スリット部を
除く羽口断面積とし、抜熱速度はガスによる対流抜熱速
度とした。そして、受熱指数でマッシュルーム圧損量を
整理した結果、図1に示すとおり、マッシュルームの形
成量は、羽口形状による熱バランスにより制御可能であ
ることが判明した。また、受熱指数を20未満では、マ
ッシュルームの圧損量(kg/cm2)が大きくなり過
ぎ、十分な溶鋼撹拌が不可能である。したがって、操業
可能なマッシュルーム圧損範囲内で受熱指数を低下さ
せ、適正なマッシュルームを形成させれば、羽口金物は
直接溶鋼と接触することなく、ガス吹込みが可能とな
り、羽口の溶損を抑制することができる。
[Function] The mushrooms are generated by the tuyere heat balance,
That is, the heat receiving index by the above equation (1), that is, the heat receiving index by the above equation (2), is used to quantify the change in the heat balance due to the tuyere shape because it is affected by the heat received from the molten steel and the cooling by the blown gas. The value obtained by dividing the obtained heat receiving rate by the heat removal rate obtained by the equation (3) was used as an index of mushroom formation. The heat receiving speed was the tuyere cross-sectional area excluding the slit portion, and the heat removal speed was the convection heat removal speed by gas. Then, as a result of arranging the mushroom pressure loss amount by the heat receiving index, as shown in FIG. 1, it was found that the mushroom formation amount could be controlled by the heat balance by the tuyere shape. When the heat receiving index is less than 20, the pressure loss (kg / cm 2 ) of the mushroom becomes too large, and sufficient molten steel stirring is impossible. Therefore, if the heat receiving index is lowered within the operable mushroom pressure loss range and an appropriate mushroom is formed, the tuyere metal can be blown without direct contact with the molten steel, and the tuyere can be melted. Can be suppressed.

【0011】この発明においては、底吹きガス流量に基
づいて、前記(1)式による受熱指数、すなわち、前記
(2)式により求めた受熱速度を前記(3)式により求
めた抜熱速度で除して求めた値が20〜40となる内管
および外管の内外径を選択することによって、適正なマ
ッシュルームが形成され、羽口金物は直接溶鋼と接触す
ることなく、ガス吹込みが可能となり、羽口金物の溶損
を抑制することができる。
In the present invention, based on the flow rate of the bottom blown gas, the heat receiving index obtained by the above equation (1), that is, the heat receiving rate obtained by the above equation (2) is calculated by the heat removal rate obtained by the above equation (3). By selecting the inner and outer diameters of the inner and outer pipes, the value of which is obtained by dividing by 20 to 40, an appropriate mushroom is formed, and the tuyere fitting can blow gas without directly contacting the molten steel Thus, it is possible to suppress erosion of the tuyere hardware.

【0012】[0012]

【実施例】【Example】

実施例1 150Ton/チャージ、19チャージ/日、吹錬時間
25分、出鋼温度1675℃、底吹き羽口数箱型4個の
上底吹き転炉を用い、受熱指数が21、33、46の中
心部に位置する芯体の外側内管に、外管を前記内管との
間に適当な隙間を開けて嵌挿固定し、リング状のガス吐
出流路を底部に形成してなる試験羽口を用い、4個の底
吹き試験羽口からのN2、CO2の吹込み量は、吹錬中M
ax350Nm3/hr、非吹錬中50Nm3/hr、上
吹き酸素量は、吹錬初期が5〜10Nm3/Ton、吹
錬中期が20〜25Nm3/Ton、吹錬末期が40〜
45Nm3/Tonで吹込んで精錬した場合において、
吹錬初期、吹錬中期、吹錬末期および排滓期におけるマ
ッシュルームの抵抗を測定した。その結果を図2に示
す。なお、4個の試験羽口からのN2、CO2の吹込み量
は、吹錬中Max350Nm3/hr、非吹錬中は50
Nm3/hr一定とした。
Example 1 150 Ton / charge, 19 charges / day, blowing time 25 minutes, tapping temperature 1675 ° C., four bottom-blowing tuyere type box-type four top-bottom-blowing converters, and a heat receiving index of 21, 33, 46 A test wing formed by inserting and fixing an outer tube to an outer inner tube of a core body located at a central portion with an appropriate gap between the inner tube and the inner tube, and forming a ring-shaped gas discharge channel at a bottom portion. The amount of N 2 and CO 2 blown from the four bottom-blown test tuyeres was
ax350Nm 3 / hr, the non-blowing in 50 Nm 3 / hr, top-blown oxygen amount is blow early 5 to 10 nm 3 / Ton, blowing metaphase 20-25 nm 3 / Ton, the blow end 40
When refined by blowing at 45 Nm 3 / Ton,
The mushroom resistance was measured at the beginning of blowing, during the middle of blowing, at the end of blowing, and during the tailing phase. The result is shown in FIG. The amount of N 2 and CO 2 blown from the four test tuyeres was Max 350 Nm 3 / hr during blowing and 50 during non-blowing.
Nm 3 / hr was constant.

【0013】図2に示すとおり、受熱指数が小さいほど
マッシュルームによるガス抵抗は大きく、大きなマッシ
ュルームが形成されていると推定された。また、各羽口
に形成されたマッシュルームは、吹錬初期から吹錬末期
にかけて成長し、最末期に溶解して排滓期に最低とな
る。各羽口の受熱指数による排滓期でのマッシュルーム
圧損量と各羽口のガス流量との関係を調査した。その結
果を図3に示す。図3に示すとおり、受熱指数46の羽
口と比較して、受熱指数33の羽口ではマッシュルーム
圧損量が約1.5倍、受熱指数21の羽口では約4倍に
増加している。また、転炉補修時に採取した羽口マッシ
ュルームは、受熱指数が小さいほどマッシュルームの形
成量が大きいことを目視により確認した。
As shown in FIG. 2, it was estimated that the smaller the heat receiving index was, the higher the gas resistance due to the mushroom was, and that a large mushroom was formed. The mushrooms formed in each tuyere grow from the early stage of blowing to the last stage of blowing, dissolve at the last stage and become the lowest at the tailing stage. The relationship between the mushroom pressure loss during the slag period based on the heat receiving index of each tuyere and the gas flow rate at each tuyere was investigated. The result is shown in FIG. As shown in FIG. 3, as compared with the tuyere with the heat receiving index 46, the mushroom pressure loss amount increases about 1.5 times in the tuyere with the heat receiving index 33 and about 4 times in the tuyere with the heat receiving index 21. Further, with respect to the tuyere mushrooms collected during the converter repair, it was visually confirmed that the smaller the heat receiving index, the larger the amount of mushrooms formed.

【0014】実施例2 前記実施例1の転炉を用い、受熱指数21、33、46
および105の中心部に位置する芯体の外側内管に、外
管を前記内管との間に適当な隙間を開けて嵌挿固定し、
リング状のガス吐出流路を底部に形成してなる試験羽口
を用い、実施例1と同条件で精錬を行い、転炉内のレー
ザー方式による羽口の溶損状況を測定した。その結果を
図4に示す。また、羽口の影響のない炉底部の溶損速度
指数をAとして図4に示す。図4に示すとおり、受熱指
数20〜40の羽口を用いることによって、羽口影響の
ない炉底部の溶損速度指数Aとほぼ同じ溶損速度指数に
抑制することができることを示している。
Example 2 The converter of Example 1 was used, and heat receiving indices 21, 33, and 46 were used.
The outer tube is inserted and fixed in the outer inner tube of the core located at the center of the and 105 with an appropriate gap between the inner tube and the outer tube.
Using a test tuyere formed with a ring-shaped gas discharge channel at the bottom, refining was performed under the same conditions as in Example 1, and the state of erosion of the tuyere by a laser method in the converter was measured. FIG. 4 shows the results. In addition, FIG. 4 shows the erosion rate index at the bottom of the furnace without the influence of the tuyere as A. As shown in FIG. 4, it is shown that the use of tuyeres having heat receiving indices of 20 to 40 can suppress the melting loss rate index to be substantially the same as the melting rate index A at the furnace bottom without tuyere influence.

【0015】[0015]

【発明の効果】以上述べたとおり、この発明方法によれ
ば、羽口に形成するマッシュルーム形成量を、羽口形状
による熱バランス、すなわち受熱速度を抜熱速度で除し
た値、すなわち受熱指数で制御することによって、適正
なマッシュルームを形成でき、羽口からのガス流量範囲
に制限を加えることなく、羽口の溶損を抑制して長寿命
化を図ることができる。
As described above, according to the method of the present invention, the amount of mushrooms formed in the tuyere is determined by the heat balance by the tuyere shape, that is, the value obtained by dividing the heat receiving speed by the heat removal speed, ie, the heat receiving index. By controlling, a proper mushroom can be formed, and without limiting the gas flow rate range from the tuyere, it is possible to suppress the melting loss of the tuyere and extend the life.

【図面の簡単な説明】[Brief description of the drawings]

【図1】受熱指数とマッシュルームの圧損量との関係を
示すグラフである。
FIG. 1 is a graph showing a relationship between a heat receiving index and a pressure loss amount of a mushroom.

【図2】羽口の受熱指数と吹錬初期、吹錬中期、吹錬末
期、排滓期におけるマッシュルームの抵抗の変化を示す
グラフである。
FIG. 2 is a graph showing changes in the heat receiving index of the tuyere and the resistance of the mushroom at the beginning of blowing, during the middle of blowing, at the end of blowing, and at the tailing stage.

【図3】羽口の受熱指数とガス流量とマッシュルームの
圧損量との関係を示すグラフである。
FIG. 3 is a graph showing a relationship among a tuyere heat receiving index, a gas flow rate, and a mushroom pressure loss amount.

【図4】羽口の受熱指数と溶損速度との関係を示すグラ
フである。
FIG. 4 is a graph showing a relationship between a heat receiving index of a tuyere and a erosion rate.

【図5】羽口に形成されたマッシュルームを示す概略断
面図である。
FIG. 5 is a schematic sectional view showing a mushroom formed in a tuyere.

【図6】羽口ならびに羽口近傍の耐火物の溶損状況を示
す概略断面図である。
FIG. 6 is a schematic sectional view showing the state of erosion of the tuyere and the refractory near the tuyere.

【符号の説明】[Explanation of symbols]

1 炉底耐火物 2 溶湯 3 羽口 4 ガス 5 マッシュルーム 6 ガス抜き道 1 Furnace refractory 2 Molten metal 3 Tuyere 4 Gas 5 Mushroom 6 Degassing path

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) C21C 5/48 C21C 5/34 C21C 7/072 F27B 1/16 F27D 3/16 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 6 , DB name) C21C 5/48 C21C 5/34 C21C 7/072 F27B 1/16 F27D 3/16

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 中心部に位置する芯体の外側内管に、外
管を前記内管との間に適当な隙間を開けて嵌挿固定し、
リング状のガス吐出流路を形成してなるガス吹込みノズ
ルを有する精錬用底吹き羽口の保護方法において、底吹
きガス流量に基づいて、下記(1)式による受熱指数、
すなわち、下記(2)式により求めた受熱速度を下記
(3)式により求めた抜熱速度で除して求めた値が20
〜40となる内管および外管の内外径を選択することを
特徴とする精錬用底吹き羽口の保護方法。 受熱指数=受熱速度/抜熱速度 (1)式 受熱速度=D0 2−(D1 2−d0 2) (2)式 抜熱速度=(0.13×D1×V0.8)/(D1 2−d0 22 (3)式 ただし、D0:外管の外径(mm)、D1:外管の内径
(mm)、d0:内管の外径(mm)、d1:内管の内径
(mm)、V:ガス流量(Nm3/hr)
1. An outer tube is fitted and fixed to an outer inner tube of a core body located at a central portion with an appropriate gap between the inner tube and the outer tube.
In the method for protecting a bottom blowing tuyere for refining having a gas injection nozzle formed with a ring-shaped gas discharge flow path, a heat receiving index according to the following equation (1) based on the bottom blowing gas flow rate;
That is, the value obtained by dividing the heat receiving rate determined by the following equation (2) by the heat removal rate determined by the following equation (3) is 20.
A method for protecting a bottom blowing tuyere for refining, comprising selecting inner and outer diameters of an inner pipe and an outer pipe of up to 40. Heat index = heat rate / heat extraction rate (1) heat rate = D 0 2 - (D 1 2 -d 0 2) (2) Equation heat extraction rate = (0.13 × D 1 × V 0.8) / ( D 1 2 -d 0 2) 2 (3) equation However, D 0: the outside diameter of the outer tube (mm), D 1: inside diameter of the outer tube (mm), d 0: the outside diameter of the inner tube (mm), d 1 : inner diameter of inner tube (mm), V: gas flow rate (Nm 3 / hr)
JP10800195A 1995-04-07 1995-04-07 How to protect the refining tuyere Expired - Fee Related JP2877026B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10800195A JP2877026B2 (en) 1995-04-07 1995-04-07 How to protect the refining tuyere

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10800195A JP2877026B2 (en) 1995-04-07 1995-04-07 How to protect the refining tuyere

Publications (2)

Publication Number Publication Date
JPH08283822A JPH08283822A (en) 1996-10-29
JP2877026B2 true JP2877026B2 (en) 1999-03-31

Family

ID=14473477

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10800195A Expired - Fee Related JP2877026B2 (en) 1995-04-07 1995-04-07 How to protect the refining tuyere

Country Status (1)

Country Link
JP (1) JP2877026B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101424642B1 (en) * 2012-09-17 2014-07-31 주식회사 포스코 Refining method of the molten steel

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4880826B2 (en) * 2001-06-11 2012-02-22 日本曹達株式会社 Oxygen blowing nozzle

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101424642B1 (en) * 2012-09-17 2014-07-31 주식회사 포스코 Refining method of the molten steel

Also Published As

Publication number Publication date
JPH08283822A (en) 1996-10-29

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