JP6201971B2 - How to cut the bullion of the converter - Google Patents

How to cut the bullion of the converter Download PDF

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JP6201971B2
JP6201971B2 JP2014245561A JP2014245561A JP6201971B2 JP 6201971 B2 JP6201971 B2 JP 6201971B2 JP 2014245561 A JP2014245561 A JP 2014245561A JP 2014245561 A JP2014245561 A JP 2014245561A JP 6201971 B2 JP6201971 B2 JP 6201971B2
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furnace
metal
converter
nozzle
ingot
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JP2016108591A (en
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洋輔 住元
洋輔 住元
孝毅 伊豆永
孝毅 伊豆永
吏彦 杉原
吏彦 杉原
大地 井上
大地 井上
周大 井上
周大 井上
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JFE Steel Corp
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JFE Steel Corp
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本発明は、転炉の炉口金物および地金切り方法に関する。   The present invention relates to a furnace mouthpiece for a converter and a method for cutting a metal.

製鉄所の製鋼工程では、溶銑を酸化精錬するための精錬設備として転炉が用いられる。酸化精錬である吹錬処理を転炉で行う際、転炉内部の鋼浴から飛散する地金が転炉の炉口や排ガスダクトのスカート部に付着する。さらに、吹錬処理が繰り返し行われることで、炉口やスカート部への地金の堆積が進む。炉口に堆積した地金は、炉内へ送酸処理をする際や副原料を投入する際に、各処理動作に支障をきたす。また、スカート部に堆積した地金は、炉口に堆積した地金とつながってしまうと、転炉炉体の傾動動作に支障をきたす。このため、炉口やスカート部に付着した地金を吹錬処理の合間にスクラップシュート等を用いて剥ぎ取る作業が行われる。   In the steelmaking process of steelworks, a converter is used as a refining facility for oxidizing and refining hot metal. When performing blow smelting treatment, which is oxidative refining, in the converter, bullion scattered from the steel bath inside the converter adheres to the furnace port of the converter and the skirt of the exhaust gas duct. Furthermore, by repeating the blowing process, the accumulation of metal at the furnace port and the skirt portion proceeds. The bullion deposited at the furnace opening hinders each processing operation when the acid is fed into the furnace or when the auxiliary material is added. Moreover, if the metal deposited on the skirt portion is connected to the metal deposited on the furnace port, the tilting operation of the converter furnace body is hindered. For this reason, the operation | work which strips off the metal | bulb adhering to a furnace port or a skirt part using a scrap chute | shoot etc. between blowing processes is performed.

また、炉口近傍への地金の付着防止および炉口近傍に付着した地金を溶解・除去する方法として、転炉炉口と上方のスカートとの間隙内に円周上にガス噴射用ノズルを配設し、吹錬中にはノズルから不活性ガスを噴出し、吹錬後にはノズルから酸素ガスを噴出する方法が知られている(特許文献1)。
さらに、転炉の炉口および内部に付着する地金を溶解・除去する方法として、炉口から炉内へ挿入するランスの先端部から酸素ガスを噴射して除去する方法が知られている(特許文献2)。
さらに、炉口耐火物の損傷を抑制しつつ、効率的に炉口地金の付着を抑制する方法として、吹錬期間の前期には吹錬用ランスに設けられた地金溶解用ノズルから酸素を供給し、吹錬期間の後期には地金溶解用ノズルからパージガスを供給する方法が知られている(特許文献3)。
In addition, as a method for preventing the adhesion of metal to the vicinity of the furnace opening and melting and removing the metal that has adhered to the vicinity of the furnace opening, a gas injection nozzle is provided on the circumference in the gap between the converter furnace opening and the upper skirt. A method is known in which an inert gas is ejected from a nozzle during blowing and oxygen gas is ejected from the nozzle after blowing (Patent Document 1).
Furthermore, as a method for melting and removing the metal bar attached to the furnace port and the inside of the converter, a method is known in which oxygen gas is injected and removed from the tip of the lance inserted into the furnace from the furnace port ( Patent Document 2).
Furthermore, as a method of efficiently suppressing the adhesion of the furnace mouth bullion while suppressing damage to the furnace refractory, oxygen from the metal melting nozzle provided in the lance for blowing during the first half of the blowing period. A method is known in which purge gas is supplied from a nozzle for melting a metal in the later stage of the blowing period (Patent Document 3).

特開平11−264009号公報JP-A-11-264909 特開平11−350015号公報JP-A-11-350015 特開2000−96119号公報JP 2000-96119 A

ここで、通常の転炉の構造では、炉口に設けられた炉口金物に付着・堆積した地金と、炉内に付着・堆積した地金とがつながる場合があった。このような場合、スクラップシュートを用いて炉口の地金を剥ぎ取る方法では、炉口に付着した地金を十分に除去することが困難となるため、地金除去に要する時間が長くなることが問題であった。
また、特許文献1に記載の方法では、炉口金物の側面部のノズルの個数や不活性ガスの噴射条件などは明らかにされておらず、ノズル出口やノズル間での地金の堆積による閉塞が生じる可能性がある。このため、ノズル出口やノズル間での地金の堆積が生じた場合、炉口金物に付着・堆積した地金と、炉内に付着・堆積した地金とがつながってしまい、地金除去に要する時間が長くなることが問題であった。
Here, in a normal converter structure, there is a case in which the bullion attached to and deposited on the furnace mouth metal provided in the furnace throat is connected to the bullion attached to and deposited in the furnace. In such a case, the method of stripping the metal from the furnace port using a scrap chute makes it difficult to sufficiently remove the metal from the furnace port, which increases the time required for removing the metal. Was a problem.
Further, in the method described in Patent Document 1, the number of nozzles on the side portion of the furnace mouth metal and the injection condition of the inert gas are not clarified, and blockage due to the accumulation of metal at the nozzle outlet or between the nozzles. May occur. For this reason, when metal deposits occur at the nozzle outlet or between the nozzles, the metal that adheres or accumulates on the furnace mouth metal and the metal that adheres or accumulates in the furnace are connected, which can be used to remove the metal. The problem was that the time required increased.

さらに、特許文献2および3に記載の方法では、地金を溶解させるために噴射する酸素ガスによる炉口金物の溶解が懸念されることから、炉口近傍に付着した地金を溶解させることが困難であった。このため、炉口金物に付着・堆積した地金と、炉内に付着・堆積した地金とがつながってしまい、地金除去に要する時間が長くなることが問題であった。
そこで、本発明は、上記従来例の未解決の課題に着目してなされたものであり、転炉の炉口に付着した地金の除去に要する時間を短縮することができる転炉の炉口金物および地金切り方法を提供することを目的としている。
Furthermore, in the methods described in Patent Documents 2 and 3, since there is a concern about melting of the furnace mouth metal by the oxygen gas injected to dissolve the metal, it is possible to dissolve the metal attached near the furnace mouth. It was difficult. For this reason, the bullion attached / deposited to the furnace mouth metal and the bullion attached / deposited in the furnace are connected to each other, and it takes a long time to remove the bullion.
Therefore, the present invention has been made paying attention to the unsolved problems of the above-described conventional example, and it is possible to shorten the time required for removing the metal that has adhered to the furnace port of the converter. The purpose is to provide hardware and bullion cutting methods.

上記目的を達成するために、本発明の一態様に係る転炉の炉口金物は、転炉の中心軸に対向する面に複数のノズルを有し、ノズルから中心軸に向かう方向に、転炉の排ガス流量と炉口直径とから算出される転炉の炉口における空塔速度以上の噴射速度でノズルから不活性ガスを噴出することを特徴とする。
また、本発明の一態様に係る転炉の地金切り方法は、少なくとも転炉の吹錬処理時において、転炉の中心軸に対向する面に設けられた複数のノズルから、ノズルから中心軸に向かう方向に、転炉の排ガス流量と炉口直径とから算出される転炉の炉口での空塔速度以上の噴射速度で不活性ガスを噴出することを特徴とする。
In order to achieve the above object, a furnace mouthpiece of a converter according to an aspect of the present invention has a plurality of nozzles on a surface facing the central axis of the converter, and the converter is moved in a direction from the nozzle toward the central axis. An inert gas is ejected from the nozzle at an injection speed equal to or higher than the superficial velocity at the furnace port of the converter calculated from the exhaust gas flow rate of the furnace and the diameter of the furnace port.
Further, a method for cutting a metal bar of a converter according to an aspect of the present invention includes a plurality of nozzles provided on a surface facing the central axis of the converter, at least during the blowing process of the converter, from the nozzle to the central axis. The inert gas is jetted at a jetting speed equal to or higher than the superficial velocity at the furnace port of the converter, which is calculated from the exhaust gas flow rate of the converter and the diameter of the furnace port.

本発明に係る転炉の炉口金物および地金切り方法によれば、転炉の炉口に付着した地金の除去に要する時間を短縮することができる。   According to the furnace metal fitting and the metal cutting method according to the present invention, it is possible to shorten the time required to remove the metal attached to the furnace furnace opening.

本発明の一実施形態に係る転炉の構成を示す説明図である。It is explanatory drawing which shows the structure of the converter which concerns on one Embodiment of this invention. 炉口金物を示す平面図である。It is a top view which shows a furnace mouth metal fitting. 炉口金物の一部を示す平面図である。It is a top view which shows a part of furnace mouth metal fitting. 図3のI−I線矢視図である。It is the II arrow directional view of FIG. 図3のII−II線矢視図である。It is the II-II arrow directional view of FIG. 図3のIII−III線矢視図である。It is the III-III arrow directional view of FIG. 炉口金物の地金の付着状態を示す断面図である。It is sectional drawing which shows the adhesion state of the base metal of a furnace mouth metal fitting.

以下、本発明を実施するための形態(以下、実施形態という。)を、図面を参照しながら詳細に説明する。
<炉口金物の構成>
はじめに、図1〜図6を参照して、本発明の一実施形態に係る転炉1の炉口金物4の構成について説明する。図1に示すように、転炉1は、金属製の炉体2と、耐火物3と、炉口金物4と、底吹きノズル5と、ランス6と、スカート部7と、フード8とを備える。
DESCRIPTION OF EMBODIMENTS Hereinafter, modes for carrying out the present invention (hereinafter referred to as embodiments) will be described in detail with reference to the drawings.
<Composition of furnace fitting>
First, with reference to FIGS. 1-6, the structure of the furnace mouthpiece 4 of the converter 1 which concerns on one Embodiment of this invention is demonstrated. As shown in FIG. 1, the converter 1 includes a metal furnace body 2, a refractory 3, a furnace mouthpiece 4, a bottom blowing nozzle 5, a lance 6, a skirt portion 7, and a hood 8. Prepare.

炉体2は、上部が開口した洋梨型の形状を有し、内側壁の全面に耐火物3が設けられる。
炉口金物4は、炉体2および耐火物3の上部の開口端である円形の炉口の外周を覆って設けられ、炉体2および耐火物3を保護する。炉口金物4は、図2に示すように、8個の扇型の炉口金物部材4a〜4hからなり、炉口金物部材4a〜4hがそれぞれ隣接して配された状態で炉口の外周に設けられる。炉口金物4の中心には、炉口の開口端に対応して円形の開口部が形成される。以下では炉口金物4の開口部側の面であり、図1の一点鎖線で示す炉体2の中心軸に対向する面を炉口内面40a(40)と称する。
The furnace body 2 has a pear-shaped shape with an open top, and a refractory 3 is provided on the entire inner wall.
The furnace mouth metal 4 is provided so as to cover the outer periphery of a circular furnace mouth which is an open end of the upper part of the furnace body 2 and the refractory 3 and protects the furnace body 2 and the refractory 3. As shown in FIG. 2, the furnace mouthpiece 4 includes eight fan-shaped furnace mouthpiece members 4 a to 4 h, and the outer periphery of the furnace mouth is in a state where the furnace mouthpiece members 4 a to 4 h are arranged adjacent to each other. Is provided. In the center of the furnace mouthpiece 4, a circular opening is formed corresponding to the opening end of the furnace mouth. Hereinafter, the surface on the opening side of the furnace mouthpiece 4 and facing the central axis of the furnace body 2 shown by the one-dot chain line in FIG. 1 is referred to as a furnace mouth inner surface 40a (40).

炉口金物部材4aは、図3〜図6に示すように、ガス供給配管41a(41)と、ヘッダー管42a(42)と、複数のガス供給路43a(43)と、複数のノズル44a(44)とを有する。
ガス供給配管41aは、炉口の外周方向から炉口金物部材4aの内部へ設けられる。ガス供給配管41aの炉口金物部材4a内部の一端は、ヘッダー管42aへと接続される。また、ガス供給配管41aの他端は、不図示のガス供給装置へと接続される。
ヘッダー管42aは、炉口金物部材4aの内部に、炉口の周方向に延在して設けられる。ヘッダー管42aは、ガス供給配管41aの一端、および複数のガス供給路43aへと接続され、ガス供給装置からガス供給配管41aを通じて送られる不活性ガスを複数のガス供給路43aへと供給する。不活性ガスには、窒素ガスやアルゴンガス等が用いられる。
As shown in FIGS. 3 to 6, the furnace mouthpiece member 4 a includes a gas supply pipe 41 a (41), a header pipe 42 a (42), a plurality of gas supply paths 43 a (43), and a plurality of nozzles 44 a ( 44).
The gas supply piping 41a is provided from the outer peripheral direction of the furnace port to the inside of the furnace port metal member 4a. One end of the gas supply pipe 41a inside the furnace mouthpiece member 4a is connected to the header pipe 42a. The other end of the gas supply pipe 41a is connected to a gas supply device (not shown).
The header pipe 42a is provided in the furnace port metal member 4a so as to extend in the circumferential direction of the furnace port. The header pipe 42a is connected to one end of the gas supply pipe 41a and the plurality of gas supply paths 43a, and supplies an inert gas sent from the gas supply apparatus through the gas supply pipe 41a to the plurality of gas supply paths 43a. Nitrogen gas, argon gas, or the like is used as the inert gas.

ガス供給路43aは、ヘッダー管42aとノズル44aとを繋げる孔であり、ノズル44aと同じ数だけ設けられる。
ノズル44aは、ガス供給路43aから炉口内面40a(40)まで延在して設けられる。ノズル44aは、ガス供給路43aから供給される不活性ガスを、炉口内面40aから噴射する。また、ノズル44aは、ヘッダー管42aの延在する方向に略等間隔に並んで20個設けられる。各ノズル44aの炉口内面40a側の先端が、炉口内面40aに対して、上下方向に2列に略千鳥配置するように設けられる。つまり、図5に示すように、隣接するノズル44a同士は、最中央部の2個のノズル44を除いた各ノズル44aの炉口内面40a側の先端が、炉口内面40aに対して上下にそれぞれずれて配置される。このうち、先端が炉口内面40aの下側に配されるノズル44aは、図4に示すように、ヘッダー管42aから水平方向に延在して設けられる。また、先端が炉口内面40aの上側に配されるノズル44aは、図6に示すように、ヘッダー管42aから水平方向に対して傾きをもって延在して設けられる。
The gas supply paths 43a are holes that connect the header pipe 42a and the nozzles 44a, and are provided in the same number as the nozzles 44a.
The nozzle 44a extends from the gas supply path 43a to the furnace port inner surface 40a (40). The nozzle 44a injects the inert gas supplied from the gas supply path 43a from the furnace port inner surface 40a. Further, 20 nozzles 44a are provided side by side at substantially equal intervals in the direction in which the header pipe 42a extends. The tip of each nozzle 44a on the furnace port inner surface 40a side is provided so as to be substantially staggered in two rows in the vertical direction with respect to the furnace port inner surface 40a. That is, as shown in FIG. 5, the adjacent nozzles 44a are arranged such that the tips on the furnace inner surface 40a side of the nozzles 44a excluding the two nozzles 44 at the center are vertically above the furnace inner surface 40a. They are offset from each other. Among these, as shown in FIG. 4, the nozzle 44a whose tip is disposed below the furnace port inner surface 40a is provided to extend in the horizontal direction from the header pipe 42a. Further, as shown in FIG. 6, the nozzle 44a whose tip is disposed above the furnace port inner surface 40a is provided to extend from the header pipe 42a with an inclination with respect to the horizontal direction.

上記構成の炉口金物部材4aは、ガス供給配管41aおよびヘッダー管42aが、炉口金物部材4aに鋳包まれた後、炉口内面40aからヘッダー管42aまで複数の孔が設けられることでガス供給路43aが形成され、形成された孔にノズル44aがそれぞれ埋め込まれることで製造される。
炉口金物部材4b〜4hは、炉口金物部材4aと同じ形状および構成を有する。つまり、炉口金物部材4b〜4hは、炉口金物部材4aと同様に、ガス供給配管41と、ヘッダー管42と、複数のガス供給路43と、複数のノズル44とをそれぞれ有する。
The furnace mouthpiece member 4a having the above-described configuration is formed by providing a plurality of holes from the furnace mouth inner surface 40a to the header pipe 42a after the gas supply pipe 41a and the header pipe 42a are cast into the furnace mouthpiece member 4a. The supply path 43a is formed, and the nozzles 44a are embedded in the formed holes, respectively.
The furnace mouth metal members 4b to 4h have the same shape and configuration as the furnace mouth metal member 4a. That is, each of the furnace mouthpiece members 4b to 4h includes a gas supply pipe 41, a header pipe 42, a plurality of gas supply paths 43, and a plurality of nozzles 44, similarly to the furnace mouthpiece member 4a.

また、ノズル44から噴射される不活性ガスのガス噴射速度は、転炉1の炉口における空塔速度以上になるように設定される。空塔速度は、転炉1の吹錬処理に伴い発生する排ガスの流量と、炉口の直径とから決定される。本実施形態では、ガス噴射速度を空塔速度以上とすることにより、ノズル44の出側圧力を、炉口での炉内雰囲気と外気との差圧である空塔圧力以上にすることができる。   The gas injection speed of the inert gas injected from the nozzle 44 is set to be equal to or higher than the superficial speed at the furnace port of the converter 1. The superficial velocity is determined from the flow rate of exhaust gas generated by the blowing process of the converter 1 and the diameter of the furnace port. In the present embodiment, by setting the gas injection speed to be equal to or higher than the superficial velocity, the outlet pressure of the nozzle 44 can be set to be equal to or higher than the superficial pressure, which is the differential pressure between the atmosphere in the furnace and the outside air at the furnace port. .

さらに、炉口金物部材4a〜4hにより形成される炉口金物4は、下記(1)式で示される、炉口内面40の円周方向の長さに対するノズル44の円周占有率Aが、0.20以上0.90以下となることが好ましい。なお、(1)式において、Nは炉口内面40の円周あたりに設けられるノズル44の数(個)、dはノズル44の直径(mm)、πは円周率、Eは炉口金物4により外周が覆われる炉口の直径(mm)をそれぞれ示す。
A=(N・d)/(π・E) ・・・(1)
Furthermore, the furnace mouthpiece 4 formed by the furnace mouthpiece members 4a to 4h has a circumferential occupancy ratio A of the nozzle 44 with respect to the length in the circumferential direction of the furnace mouth inner surface 40 represented by the following equation (1): It is preferably 0.20 or more and 0.90 or less. In equation (1), N is the number (number) of nozzles 44 provided around the circumference of the inner surface 40 of the furnace port, d is the diameter (mm) of the nozzle 44, π is the circumference ratio, and E is the furnace mouth metal. 4 indicates the diameter (mm) of the furnace port whose outer periphery is covered.
A = (N · d) / (π · E) (1)

底吹きノズル5は、炉体2の底部に、炉体2の外側面から耐火物3を含む内側面へと挿通して複数設けられる。底吹きノズル5は、不活性ガスを供給する複数のパイプが埋め込まれた耐火物からなり、パイプを通じて転炉1の炉内へと不活性ガスを吹き込むことで、炉内に収容された溶銑Mを撹拌させる。
ランス6は、炉体2の上方に上下方向に移動自在に設けられ、先端から酸素ガスを噴射させることで、炉内に収容された溶銑Mを酸化精錬処理する。
スカート部7およびフード8は、炉内から排出される排ガスを回収するOG設備の一部である。スカート部7は、炉体2の炉口の上部を覆うように形成され、フード8に接続される。フード8は、集塵機等の他のOG設備へと接続される。
A plurality of bottom blowing nozzles 5 are provided at the bottom of the furnace body 2 from the outer surface of the furnace body 2 to the inner surface including the refractory 3. The bottom blowing nozzle 5 is made of a refractory in which a plurality of pipes for supplying an inert gas are embedded, and the hot metal M accommodated in the furnace is blown into the furnace of the converter 1 through the pipes. Is allowed to stir.
The lance 6 is provided above the furnace body 2 so as to be movable in the vertical direction, and oxidizes and refines the hot metal M accommodated in the furnace by injecting oxygen gas from the tip.
The skirt portion 7 and the hood 8 are part of an OG facility that collects exhaust gas discharged from the furnace. The skirt portion 7 is formed so as to cover the upper part of the furnace port of the furnace body 2 and is connected to the hood 8. The hood 8 is connected to other OG equipment such as a dust collector.

<地金切り方法>
次に、図7を参照して、本発明の一実施形態に係る転炉1の地金切り方法について説明する。転炉1では、炉内に収容された溶銑Mを酸化精錬するための吹錬処理が行われる。吹錬処理では、主にランス6の先端から噴射される酸素ガスによって溶銑Mが酸化する。このとき、炉内では、溶銑Mや酸化された溶鋼等の地金が飛散するスピッティング現象や、処理に伴い発生するスラグが一部に地金が混入した状態で噴出するスロッピング現象が生じる。スピッティング現象やスロッピング現象によって飛散する地金(スラグに混入した地金を含む)は、炉口近傍に付着・堆積する。
<How to cut bullion>
Next, with reference to FIG. 7, the metal cutting method of the converter 1 which concerns on one Embodiment of this invention is demonstrated. In the converter 1, the blowing process for carrying out the oxidation refining of the hot metal M accommodated in the furnace is performed. In the blowing process, the hot metal M is oxidized mainly by oxygen gas injected from the tip of the lance 6. At this time, in the furnace, a spitting phenomenon in which the metal such as molten iron M or oxidized molten steel scatters, or a slopping phenomenon in which the slag generated by the process is ejected in a state where the metal is mixed in part. . Ingots scattered by spitting and slopping phenomena (including ingots mixed in slag) adhere and accumulate near the furnace entrance.

本実施形態では、転炉1の吹錬処理時において、炉口金物4のノズル44から不活性ガスGを噴射させる。この際、図7に示すように、ノズル44から転炉1の中心軸に向かう方向に不活性ガスGを噴射させることで、ノズル44周辺への地金の付着を防止する。このため、炉口近傍に付着する地金を、炉口上部に付着した炉口地金S1と、炉内に付着した炉内地金S2とに縁切りさせた状態にすることができる。   In the present embodiment, the inert gas G is injected from the nozzle 44 of the furnace mouthpiece 4 during the blowing process of the converter 1. At this time, as shown in FIG. 7, the inert gas G is injected from the nozzle 44 toward the central axis of the converter 1, thereby preventing adhesion of the metal around the nozzle 44. For this reason, the metal in the vicinity of the furnace port can be in a state of being cut into the furnace metal ingot S1 attached to the upper part of the furnace port and the furnace metal S2 attached in the furnace.

上記のような吹錬処理が複数回行われ、炉口地金S1がある程度堆積したところで、炉口地金S1の除去処理が行われる。除去処理では、炉体2を傾動させた状態で、スクラップシュートの先端を炉口地金S1に当てて、炉口地金S1を掻き取ることで炉口地金S1が除去される。この際、炉口地金S1が炉内地金S2と縁切りされているため、炉口地金S1を容易に削り取ることができる。   The blowing process as described above is performed a plurality of times, and when the furnace opening ingot S1 is deposited to some extent, the removal process of the furnace opening ingot S1 is performed. In the removal process, with the furnace body 2 tilted, the tip of the scrap chute is applied to the furnace mouth metal S1, and the furnace mouth metal S1 is scraped off to remove the furnace mouth metal S1. At this time, since the furnace opening ingot S1 is cut off from the furnace ingot S2, the furnace opening ingot S1 can be easily scraped off.

<変形例>
以上、添付図面を参照しながら本発明の好適な実施形態について詳細に説明したが、本発明はかかる例に限定されない。本発明の属する技術の分野における通常の知識を有する者であれば、特許請求の範囲に記載された技術的思想の範疇内において、各種の変更例または修正例に想到し得ることは明らかであり、これらについても、当然に本発明の技術的範囲に属するものと了解される。
<Modification>
The preferred embodiments of the present invention have been described in detail above with reference to the accompanying drawings, but the present invention is not limited to such examples. It is obvious that a person having ordinary knowledge in the technical field to which the present invention pertains can come up with various changes or modifications within the scope of the technical idea described in the claims. Of course, it is understood that these also belong to the technical scope of the present invention.

例えば、上記実施形態では、転炉1の吹錬処理時にノズル44から不活性ガスGを噴射させるとしたが、本発明はかかる例に限定されない。例えば、非吹錬処理時においても、吹錬処理時と同様にノズル44から不活性ガスGを噴射させてもよい。この際、不活性ガスの噴射速度は、吹錬処理時よりも低くてもよい。非吹錬処理時に不活性ガスGを噴射させることにより、ノズル44が冷却され、ノズル44の溶損を防止することができる。   For example, in the said embodiment, although the inert gas G was injected from the nozzle 44 at the time of the blowing process of the converter 1, this invention is not limited to this example. For example, in the non-blowing process, the inert gas G may be injected from the nozzle 44 as in the blowing process. At this time, the injection speed of the inert gas may be lower than that during the blowing process. By injecting the inert gas G during the non-blowing process, the nozzle 44 is cooled, and the nozzle 44 can be prevented from being melted.

また、上記実施形態では、炉口内面40に対して、ノズル44を上下2列に設けるとしたが、本発明はかかる例に限定されない。炉口内面40において炉口地金S1と炉内地金S2とが縁切りできれば、炉口内面40の上下方向に対して、ノズル44を1列または3列以上設けてもよい。この際、ノズル44の列を多く設けることで、炉口地金S1と炉内地金S2とが縁切りされる領域が増えるため、確実に縁切りすることができる。
さらに、ノズル44の長手方向に垂直な断面の形状は、矩形等の円形以外の形状を有していてもよい。
Moreover, in the said embodiment, although the nozzle 44 was provided in the upper and lower two rows with respect to the furnace port inner surface 40, this invention is not limited to this example. As long as the furnace opening ingot S1 and the in-furnace ingot S2 can be cut off at the furnace inner surface 40, one or more nozzles 44 may be provided in the vertical direction of the furnace inner surface 40. At this time, by providing a large number of rows of nozzles 44, an area where the furnace opening metal S1 and the furnace metal S2 are edged increases, so that the edge can be surely cut.
Furthermore, the shape of the cross section perpendicular to the longitudinal direction of the nozzle 44 may have a shape other than a circle such as a rectangle.

<実施形態の効果>
(1)本発明の実施形態に係る転炉の炉口金物は、転炉1の中心軸に対向する面40に複数のノズル44を有し、ノズル44から中心軸に向かう方向に、転炉1の排ガス流量と炉口直径とから算出される転炉1の炉口における空塔速度以上の噴射速度でノズル44から不活性ガスGを噴出する。
<Effect of embodiment>
(1) A furnace mouthpiece for a converter according to an embodiment of the present invention has a plurality of nozzles 44 on a surface 40 facing the central axis of the converter 1, and the converter in a direction from the nozzle 44 toward the central axis. The inert gas G is ejected from the nozzle 44 at an injection speed equal to or higher than the superficial velocity at the furnace port of the converter 1 calculated from the exhaust gas flow rate of 1 and the furnace port diameter.

ここで、上記構成の炉口金物を用いない場合、吹錬処理を行うことで付着・堆積した炉口地金S1と炉内地金S2とがつながってしまい、スクラップシュートを用いて炉口地金S1を剥ぎ取ろうとしても、十分に炉口地金S1を除去することが難しかった。この際、つながった炉口地金S1と炉内地金S2とを溶断することで縁切りする方法が考えられるが、溶断処理に時間がかかってしまうために、炉口地金S1の除去に要する時間が長くなる。また、これらの地金除去の作業は、非吹錬処理時に行われるため、地金除去にかかる時間が長くなることで、転炉1での生産性が大きく低下することとなる。これに対して、上記構成によれば、噴射される不活性ガスGによって、ノズル44周囲への地金付着を防止することができる。これにより、炉口地金S1と炉内地金S2とを縁切りすることができ、堆積した炉口地金S1を容易に除去することができるため、炉口に付着した地金の除去に要する時間を短くすることができる。さらに、炉口地金S1と炉内地金S2とを縁切りするための溶断処理を行う必要がないため、転炉1の耐火物3や炉口金物4といった設備の溶断処理に伴う溶損等を防止することができ、安定的に転炉1を使用することができる。   Here, in the case of not using the furnace mouthpiece having the above configuration, the furnace mouth ingot S1 and the furnace ingot S2 which are attached and deposited by performing the blowing process are connected to each other, and the furnace mouth ingot using a scrap chute is used. Even if it was going to strip off S1, it was difficult to remove the furnace mouth metal S1 sufficiently. At this time, a method of cutting the edges by fusing the connected furnace ingot S1 and in-furnace ingot S2 can be considered, but since the fusing process takes time, the time required for removing the furnace inlet ingot S1. Becomes longer. Moreover, since these bullion removal operations are performed during the non-blowing process, the time required for the bullion removal becomes longer, and the productivity in the converter 1 is greatly reduced. On the other hand, according to the said structure, the inactive gas G injected can prevent metal adhesion to the nozzle 44 periphery. Thereby, the furnace ingot S1 and the in-furnace ingot S2 can be trimmed, and the deposited furnace mouth ingot S1 can be easily removed, so the time required for removing the ingot attached to the furnace mouth Can be shortened. In addition, since it is not necessary to perform a fusing process for cutting the furnace ingot S1 and the in-furnace ingot S2, it is possible to cause melting damage associated with the fusing process of equipment such as the refractory 3 and the furnace mouth metal 4 of the converter 1. The converter 1 can be used stably.

また、特許文献1の図3および図4に開示された発明では、炉口金物の上面側にもノズルを設ける必要があり、上部フード等の内側面に付着した地金が落下する際に、ノズルや配管が破損する可能性があった。さらに、特許文献1の図3および図4に開示された発明では、炉口金物上に落下または堆積する地金によって、閉塞等によってノズルの稼働状況が悪化するといった問題があった。しかし、上記構成によれば、ノズル44は、炉口内面40に設ければよいだけなので、炉口金物4の上部から地金が落下してきても、ノズル44や配管が破損することがない。このため、炉口金物4による地金付着の防止効果を安定的に得ることができる。また、炉口金物4の上面に地金が落下または堆積しても、ノズル44のガス噴射動作には影響しないため、地金付着の防止効果を安定的に得ることができる。
なお、上記構成において、不活性ガスの噴射速度が空塔速度未満となる場合、飛散する地金を十分に吹き飛ばすことができなくなるため、ノズル44の周辺に地金が付着してしまう可能性がある。このような場合、炉口地金S1と炉内地金S2とがつながってしまうと、上記の炉口地金S1の除去に要する時間が長くなる。
Moreover, in the invention disclosed in FIG. 3 and FIG. 4 of Patent Document 1, it is necessary to provide a nozzle also on the upper surface side of the furnace mouthpiece, and when the metal attached to the inner surface of the upper hood falls, There was a possibility that the nozzle and piping were damaged. Furthermore, in the invention disclosed in FIGS. 3 and 4 of Patent Document 1, there is a problem that the operating state of the nozzle is deteriorated due to blockage or the like due to the metal falling or depositing on the furnace metal fitting. However, according to the said structure, since the nozzle 44 should just be provided in the furnace opening inner surface 40, even if a base metal falls from the upper part of the furnace opening metal fitting 4, the nozzle 44 and piping will not be damaged. For this reason, the prevention effect of the adhesion of the bullion by the furnace mouthpiece 4 can be stably obtained. Further, even if the metal falls or accumulates on the upper surface of the furnace base metal 4, it does not affect the gas injection operation of the nozzle 44, so that the effect of preventing the adhesion of the metal can be stably obtained.
In the above configuration, when the injection speed of the inert gas is less than the superficial velocity, the scattered metal cannot be blown out sufficiently, so that the metal may adhere to the periphery of the nozzle 44. is there. In such a case, if the furnace opening ingot S1 and the in-furnace ingot S2 are connected, the time required for removing the furnace opening ingot S1 becomes longer.

(2)複数のノズル44は、下記(1)式で定義され、面40の周方向の長さに対するノズル44の占有率を示す円周占有率Aが0.20以上0.90以下である。
A=(N・d)/(π・E) ・・・(1)
N:転炉の中心軸に対向する面の円周あたりに設けられるノズルの数(個)
d:ノズルの直径(mm)
π:円周率
E:炉口の直径(mm)
(2) The plurality of nozzles 44 is defined by the following equation (1), and the circumferential occupation ratio A indicating the occupation ratio of the nozzles 44 with respect to the circumferential length of the surface 40 is 0.20 or more and 0.90 or less. .
A = (N · d) / (π · E) (1)
N: Number of nozzles provided per circumference of the surface facing the central axis of the converter (pieces)
d: Nozzle diameter (mm)
π: Circumference ratio E: Furnace port diameter (mm)

上記構成によれば、炉口金物4の強度を十分に保ちながらも、炉口地金S1と炉内地金S2との縁切りを確実に行うことができる。円周占有率Aが0.20未満の場合、ノズル44の周辺において、不活性ガスGにより地金が吹き飛ばされないために、地金が付着してしまう領域が生じる場合がある。このため、十分な縁切りの効果を得ることができない可能性がある。一方、円周占有率Aが0.90超の場合、炉口金物4に占めるノズル44およびガス供給路43による空腔の割合が過大となる。このため、炉口金物4の満足な機械的強度を得ることができない。   According to the above-described configuration, it is possible to reliably perform the edge cutting between the furnace port metal S1 and the furnace metal S2 while maintaining the strength of the furnace metal 4 sufficiently. When the circumferential occupancy A is less than 0.20, the metal is not blown off by the inert gas G in the vicinity of the nozzle 44, and thus a region where the metal is attached may occur. For this reason, there is a possibility that a sufficient edge cutting effect cannot be obtained. On the other hand, when the circumferential occupation ratio A is more than 0.90, the ratio of the cavities due to the nozzle 44 and the gas supply path 43 in the furnace mouthpiece 4 becomes excessive. For this reason, the satisfactory mechanical strength of the furnace mouthpiece 4 cannot be obtained.

(3)ノズル44は、面40に対して上下方向に複数段設けられる。上記構成によれば、炉口地金S1と炉内地金S2との縁切りする領域を大きくすることができるため、より確実に縁切りをすることができる。
(4)本発明の実施形態に係る転炉の地金切り方法は、少なくとも転炉1の吹錬処理時において、転炉1の中心軸に対向する面に設けられた複数のノズル44から、ノズル44から中心軸に向かう方向に、転炉1の排ガス流量と炉口直径とから算出される転炉1の炉口での空塔速度以上の噴射速度で不活性ガスを噴出する。上記構成によれば、吹錬処理時において、上記(1)と同様な効果を得ることができる。
(5)転炉1の非吹錬時において、ノズル44から不活性ガスを噴出する。上記構成によれば、非吹錬処理時において、ノズル44の溶損等の損耗を防止することができる。
(3) The nozzles 44 are provided in a plurality of stages in the vertical direction with respect to the surface 40. According to the said structure, since the area | region to cut off the edge of the furnace inlet metal S1 and the furnace inner metal S2 can be enlarged, the edge cutting can be more reliably performed.
(4) The method of cutting the metal in the converter according to the embodiment of the present invention includes a plurality of nozzles 44 provided on the surface facing the central axis of the converter 1 at least during the blowing process of the converter 1. Inert gas is ejected in a direction from the nozzle 44 toward the central axis at an injection speed equal to or higher than the superficial velocity at the furnace port of the converter 1 calculated from the exhaust gas flow rate of the converter 1 and the furnace port diameter. According to the said structure, the effect similar to said (1) can be acquired at the time of a blowing process.
(5) When the converter 1 is not blown, an inert gas is ejected from the nozzle 44. According to the above configuration, wear such as melting of the nozzle 44 can be prevented during the non-blowing process.

次に、本発明者らが行った実施例について説明する。実施例では、図1〜図6に示す上記実施形態に係る炉口金物4を用いた。炉口金物4の円周占有率Aは、0.26とした。ノズル44およびヘッダー管42には、以下の仕様のものを使用した。なお、以下のノズル44の仕様に示す最低ピッチは、隣接するノズル44同士の周方向における距離のうち、最も短い距離を示す。   Next, examples performed by the present inventors will be described. In the Example, the furnace mouthpiece 4 which concerns on the said embodiment shown in FIGS. 1-6 was used. The circumferential occupation ratio A of the furnace mouthpiece 4 was set to 0.26. The nozzle 44 and the header pipe 42 having the following specifications were used. In addition, the minimum pitch shown in the specification of the following nozzle 44 shows the shortest distance among the distances in the circumferential direction between adjacent nozzles 44.

[ノズルの仕様]
材質:FCD400
内径:φ5mm
スプレー角度:90°
最低ピッチ:48.2mm
[ヘッダー管の仕様]
材質:STS370
サイズ:100A×Sch160
長さ:2238mm(40°曲げ)
[Nozzle specifications]
Material: FCD400
Inner diameter: φ5mm
Spray angle: 90 °
Minimum pitch: 48.2mm
[Header tube specifications]
Material: STS370
Size: 100A x Sch160
Length: 2238mm (40 ° bending)

また、実施例では、ノズル44から噴射する不活性ガスとして窒素ガスを用い、噴射速度を転炉1の炉口における計算空塔速度と同じ17m/sとした。なお、窒素ガスの噴射速度17m/sは、一つの炉口金物部材4aから噴射される窒素ガスの標準状態におけるガス流量に換算すると24Nm/minとなる。この条件下において、ノズル44の出側における圧力は、炉内の設定空塔圧力と同じ10Paとなる。実施例では、上記の噴射条件において、転炉1での吹錬処理中は、不活性ガスGを常時噴射させた。 Moreover, in the Example, nitrogen gas was used as the inert gas injected from the nozzle 44, and the injection speed was set to 17 m / s, which is the same as the calculated superficial velocity at the furnace port of the converter 1. The nitrogen gas injection speed of 17 m / s is 24 Nm 3 / min when converted to the gas flow rate in the standard state of nitrogen gas injected from one furnace end member 4a. Under this condition, the pressure on the outlet side of the nozzle 44 is 10 Pa, which is the same as the set superficial pressure in the furnace. In an Example, the inert gas G was always injected during the blowing process in the converter 1 on said injection conditions.

さらに、実施例における空塔速度から、吹錬処理時に生じる微粒地金の揚力を算出した。微粒地金の揚力Lは下記(2)式を用いて算出した。(2)式において、Lは揚力(N)、ρは排ガス密度(kg/m)、uはダスト速度(m/s)、Aは球投影面積となるダスト代表面積(m)、Cは球径ダストの抵抗係数をそれぞれ示す。なお、ダスト速度は、空塔速度と同じとして算出した。

Figure 0006201971
Furthermore, the lift of the fine bullion generated during the blowing process was calculated from the superficial velocity in the example. The lift L of the fine bullion was calculated using the following equation (2). In the formula (2), L is lift (N), ρ is exhaust gas density (kg / m 3 ), u is dust velocity (m / s), A is a dust representative area (m 2 ) that is a spherical projection area, C D represents the resistance coefficient of spherical dust. The dust velocity was calculated as the same as the superficial velocity.
Figure 0006201971

(2)式を用いて揚力Lを算出した結果、微粒地金の粒径を2mmとした場合、揚力L=4.0×10−3kgfとなった。これは、2mmの粒径の微粒地金の自重(0.3×10−3kgf)に対して過大な値であるため、ノズル44から空塔速度以上の噴射速度で不活性ガスGを噴射させることで、炉口へと飛散する地金を吹き飛ばすことができることが確認できた。 As a result of calculating the lift L using the equation (2), the lift L was 4.0 × 10 −3 kgf when the particle diameter of the fine metal bar was 2 mm. Since this is an excessive value with respect to the dead weight (0.3 × 10 −3 kgf) of the fine ingot having a particle diameter of 2 mm, the inert gas G is injected from the nozzle 44 at an injection speed higher than the superficial velocity. By doing so, it was confirmed that the bullion scattered to the furnace port could be blown away.

また、実施例に対する比較例として、通常の炉口金物を用いて吹錬処理を行い、実施例との一日当たりに掛かる地金除去の作業時間を比較した。比較例では、通常の炉口金物として、ガス供給配管41、ヘッダー管42、ガス供給路43およびノズル44の構成がない炉口金物を用いた。また、比較例において炉口地金を除去する際には、炉口地金と炉内地金とを溶断することで縁切りした後、スクラップシュートを用いて炉口地金を掻き取った。それ以外の条件については、実施例と同様とした。
実施例および比較例の結果、比較例では転炉一基の一日当たりの地金除去の作業時間が157分であったのに対して、実施例では123分となり、実施例の炉口金物および地金切り方法を用いることで、地金除去の作業時間を大幅に短縮できることを確認した。
Moreover, as a comparative example with respect to the examples, a blowing operation was performed using a normal furnace mouthpiece, and the working time for removing the bullion per day with the examples was compared. In the comparative example, as a normal furnace mouthpiece, a furnace mouthpiece having no gas supply pipe 41, header pipe 42, gas supply path 43, and nozzle 44 configuration was used. Moreover, when removing the furnace opening ingot in the comparative example, the furnace opening ingot was cut off by melting the furnace opening ingot and the furnace ingot, and then scraped off using the scrap chute. The other conditions were the same as in the example.
As a result of the examples and comparative examples, in the comparative example, the work time for removing the bullion per day for one converter was 157 minutes, whereas in the example, it was 123 minutes, and the furnace mouthpiece of the example and By using the bullion cutting method, it was confirmed that the work time for removing the bullion can be greatly shortened.

1 :転炉
2 :炉体
3 :耐火物
4 :炉口金物
4a〜4h :炉口金物部材
40,40a :炉口内面
41,41a :ガス供給配管
42,42a :ヘッダー管
43,43a :ガス供給路
44,44a :ノズル
5 :底吹きノズル
6 :ランス
7 :スカート部
8 :フード
1: Converter 2: Furnace 3: Refractory 4: Furnace metal fittings 4a to 4h: Furnace metal fittings 40 and 40a: Furnace inner surface 41 and 41a: Gas supply piping 42 and 42a: Header pipe 43 and 43a: Gas Supply path 44, 44a: Nozzle 5: Bottom blowing nozzle 6: Lance 7: Skirt portion 8: Hood

Claims (1)

炉の吹錬処理時において、転炉の中心軸に対向する面に設けられた複数のノズルから、前記ノズルから前記中心軸に向かう方向に、前記転炉の排ガス流量と炉口直径とから算出される前記転炉の炉口での空塔速度以上の噴射速度で不活性ガスを噴出させ、
前記転炉の非吹錬処理時において、前記ノズルから前記不活性ガスを噴出させることを特徴とする転炉の地金切り方法
During the blowing process of the converter, from the plurality of nozzles provided on the surface facing the central axis of the converter, in the direction from the nozzle toward the central axis, from the exhaust gas flow rate and the furnace port diameter of the converter Injecting an inert gas at an injection speed equal to or higher than the superficial velocity at the furnace outlet of the converter ,
During the non blowing process of the converter, bullion cutting method of the converter, characterized in Rukoto is ejected the inert gas from the nozzle.
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JPH0129232Y2 (en) * 1986-10-08 1989-09-06
JPH02133507A (en) * 1988-11-15 1990-05-22 Nkk Corp Converter blowing method
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JPH11264009A (en) * 1998-03-17 1999-09-28 Kawasaki Steel Corp Device for preventing and removing metal deposition on nose of converter

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