JP2013082969A - Lower structure of vacuum degassing apparatus - Google Patents

Lower structure of vacuum degassing apparatus Download PDF

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JP2013082969A
JP2013082969A JP2011223671A JP2011223671A JP2013082969A JP 2013082969 A JP2013082969 A JP 2013082969A JP 2011223671 A JP2011223671 A JP 2011223671A JP 2011223671 A JP2011223671 A JP 2011223671A JP 2013082969 A JP2013082969 A JP 2013082969A
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arc
reflux
shaped sleeve
pipe
sleeve
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JP5712891B2 (en
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Masaaki Yamamoto
雅章 山本
Masaharu Sato
正治 佐藤
Nobumitsu Takai
宣光 鷹居
Kenichi Tokumaru
健一 得丸
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Nippon Steel Corp
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Nippon Steel and Sumitomo Metal Corp
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Abstract

PROBLEM TO BE SOLVED: To provide a lower structure of vacuum degassing apparatus having two circulating tubes improved in durability with a conduit through which a molten metal passes.SOLUTION: There is provided the lower structure of vacuum degassing apparatus. The circulating tube includes a circular sleeve having a cross section with center angle of ≥90° and ≤180° and a circulating tube body and has a complementary shape to form the conduit by being fitted. When a virtual line segment is defined by linking center points of two conduits on the cross section, both ends in the circumferential direction of the circular sleeve exist in a position having an angle of 45° or larger in the circumferential direction across the virtual line segment.

Description

この発明は、取鍋等に入れられた溶融金属を槽内に吸い上げて脱ガス等を行う真空脱ガス装置の下部構造に関し、詳しくは、それぞれ浸漬管が接続される2つの環流管の耐久性を向上させた真空脱ガス装置の下部構造に関する。   The present invention relates to a lower structure of a vacuum degassing apparatus for degassing by sucking molten metal put in a ladle or the like into a tank, and more specifically, durability of two reflux tubes each connected to a dip tube The present invention relates to a lower structure of a vacuum degassing apparatus with improved performance.

真空脱ガス装置は、溶鋼等の溶融金属から水素や窒素等を脱ガスしたり、COとして炭素を取り除く脱炭など、溶融金属を成分調整する処理に利用されている。例えば、RH(Ruhrstahl-Heraus)式真空脱ガス装置では、一般に、天蓋を有する上部構造には、成分調整として合金を投入するのに利用される合金投入口や槽内の雰囲気を排気する排気口を備え、また、炉底側には先端に浸漬管が繋がれる環流管を2つ備えて下部構造を形成しており、取鍋に入れられた溶融金属を槽内に環流させるようにしている。これら真空脱ガス装置の上部構造と下部構造は、図7に示したように、各々に接続フランジが取り付けられて上部槽と下部槽のように分離可能に形成される場合もあれば、特に継ぎ目を有さずに一体に形成されることもある。   A vacuum degassing apparatus is used for a process of adjusting the components of a molten metal, such as degassing hydrogen or nitrogen from a molten metal such as molten steel or decarburizing to remove carbon as CO. For example, in the RH (Ruhrstahl-Heraus) type vacuum degassing apparatus, generally, the upper structure having a canopy has an alloy inlet used for introducing an alloy as a component adjustment and an exhaust outlet for exhausting the atmosphere in the tank. In addition, the bottom of the furnace bottom is provided with two reflux pipes connected to the tip of the dip pipe, and the molten metal placed in the ladle is circulated into the tank. . As shown in FIG. 7, the upper structure and the lower structure of these vacuum degassing apparatuses may be formed to be separable like an upper tank and a lower tank by attaching a connection flange to each of them. It may be formed integrally without having.

このうち、溶融金属が入れられた取鍋側に配設される下部構造は、一方の浸漬管から溶融金属を吸い上げて環流管を介して槽内に流入させ、真空中で脱ガス等の処理を行った後、他方の環流管及び浸漬管を通じて処理後の溶融金属を取鍋に戻すことから、比較的損傷が激しい。なかでも、先端が溶鋼中に浸漬される浸漬管は、溶融金属の流れによる作用や、取鍋中の溶融金属表面に発生するスラグによる溶損等によって消耗が著しいことから、一般的にRH式真空脱ガス装置では、溶融金属を40〜250チャージ程度処理した後に、新しい浸漬管に交換される。   Among these, the lower structure arranged on the ladle side where the molten metal is put, sucks the molten metal from one dip tube, flows it into the tank through the reflux tube, and processes such as degassing in a vacuum Since the molten metal after treatment is returned to the ladle through the other reflux tube and dip tube, the damage is relatively severe. Among them, the dip tube whose tip is immersed in molten steel is generally RH type because it is conspicuous due to the action of the molten metal flow and the slag generated by the molten metal surface in the ladle. In the vacuum degassing apparatus, the molten metal is treated for about 40 to 250 charges and then replaced with a new dip tube.

これに対して環流管は、浸漬管ほどではないが、脱ガス処理等を続けていくにつれて、溶融金属の通過する管路にひび割れや亀裂が生じてしまう。一旦、亀裂等が形成されるとその部分に溶融金属が差し込み、溶損が促進されてしまうことから、下部構造の本体の寿命を全うする前に、環流管の管路を中心とした大規模な補修工事が必要になる。   On the other hand, the reflux tube is not as large as the dip tube, but as the degassing process or the like is continued, cracks and cracks occur in the pipeline through which the molten metal passes. Once cracks are formed, molten metal will be inserted into the part and melting damage will be promoted. Therefore, before the life of the main body of the substructure is completed, a large scale centering on the conduit of the reflux pipe will be used. Repair work is required.

そこで、円筒状をした一体構造のスリーブ煉瓦を環流管に配設して管路を形成する技術がこれまで採用されてきた(例えば特許文献1、2参照)。すなわち、溶融金属の通過する管路を一体構造のスリーブ煉瓦によって形成することで、管路に目地を無くして溶融金属の差し込みによる局所的な損傷を防ぐようにしている。   In view of this, a technique has been employed in which a sleeve-shaped sleeve brick having a cylindrical structure is disposed in a reflux pipe to form a pipe line (see, for example, Patent Documents 1 and 2). That is, the conduit through which the molten metal passes is formed by a monolithic sleeve brick so as to eliminate joints in the conduit and prevent local damage due to insertion of the molten metal.

また、これに関連して、アルミナ系の原料に流動性促進材とセメントを添加したキャスタブル材を鋳込み成形して円筒状スリーブを形成することで、耐摩耗性や耐熱スポーリングを向上させる技術(特許文献3参照)や、一体構造の円筒状スリーブの下端を環流管と浸漬管との接合位置からずらして配設することで、環流管と浸漬管との境界部での溶損を防ぐ方法(特許文献4参照)など、数多くの改良技術が提案されて現在に至っている。そして、この円筒状スリーブは、浸漬管の交換と合わせて環流管から抜き取られ、新品に置き換えられて操業を続けるのが実情である。   In this regard, a technology that improves wear resistance and heat spalling by forming a cylindrical sleeve by casting a castable material in which a fluidity promoter and cement are added to an alumina-based raw material ( Patent Document 3) and a method of preventing melting damage at the boundary between the reflux tube and the dip tube by disposing the lower end of the cylindrical sleeve having an integral structure from the joining position of the reflux tube and the dip tube. Many improved techniques have been proposed, such as (see Patent Document 4). The actual situation is that this cylindrical sleeve is extracted from the reflux tube together with the replacement of the dip tube, replaced with a new one, and continues to operate.

特開平2−25513号公報JP-A-2-25513 特開平2−34714号公報JP-A-2-34714 特開平11−279629号公報JP 11-279629 A 特開平9−241721号公報Japanese Patent Laid-Open No. 9-241721

ところで、従来技術において、上記のような円筒形状をしたスリーブを配設する要因となった環流管の管路に発生する亀裂等について、本発明者等は改めて詳細な検討を行った。すなわち、煉瓦の目地部分以外でも管路にひび割れや亀裂が発生することがあり、また、不定形耐火物によって目地の無い管路を形成した場合でも亀裂等が確認されることがあることから、これらの原因について、熱応力計算に基づき環流管の構造解析を実施した。その結果、環流管の管路に発生するひび割れや亀裂は、従来考えられていたような環流管の内側(溶融金属が流れる管路側)から発生するのではなく、むしろ、環流管の外側で発生して管路に到達すると理解した方が合理的であるという結論を得た。また、この環流管の外側から発生するひび割れや亀裂は、ある所定の領域に集中して起こることも分った。   By the way, in the prior art, the present inventors have made a detailed examination again on cracks and the like generated in the conduit of the reflux pipe, which has been a factor in disposing the cylindrical sleeve as described above. That is, cracks and cracks may occur in pipes other than the joint parts of bricks, and cracks etc. may be confirmed even when pipes without joints are formed by irregular refractories, For these causes, structural analysis of the reflux tube was conducted based on the thermal stress calculation. As a result, cracks and cracks that occur in the conduit of the reflux pipe do not occur from the inside of the reflux pipe (the side of the pipeline through which the molten metal flows) as previously thought, but rather occur outside the reflux pipe. The conclusion was that it would be more reasonable to understand that it would reach the pipeline. It has also been found that cracks and cracks generated from the outside of the reflux tube are concentrated in a predetermined region.

そこで、本発明者等は、上記のような新たな知見に基づいて、横断面が円弧状のスリーブを環流管本体の所定の位置に嵌め合わせて、このスリーブの内壁面と環流管本体の内壁面とによって管路を形成することで、環流管でのひび割れや亀裂の発生を効率的に抑制することができることを見出し、本発明を完成した。   Accordingly, the present inventors have fitted a sleeve having a circular cross section into a predetermined position of the reflux tube main body based on the above-described new knowledge, and the inner wall surface of the sleeve and the inner tube of the reflux tube main body are fitted. It was found that by forming a pipe line with a wall surface, the occurrence of cracks and cracks in the reflux pipe can be efficiently suppressed, and the present invention has been completed.

したがって、本発明の目的は、真空脱ガス装置における環流管の耐久性を向上させた下部構造を提供することにある。   Accordingly, an object of the present invention is to provide a lower structure in which the durability of the reflux tube in the vacuum degassing apparatus is improved.

すなわち、本発明は、溶融金属の通過する管路を有した環流管を2つ備えた真空脱ガス装置の下部構造であって、前記各環流管は、環流管本体と横断面が90°以上180°以下の中心角度を有した円弧状のスリーブとを備えると共に、これらが互いに相補的な形状を有して環流管本体の一部に円弧状スリーブが嵌め合わされ、環流管本体の内壁面と円弧状スリーブの内壁面とによって管路を形成しており、かつ、2つの環流管の横断面において、一方の環流管P1の管路の中心点O1と他方の環流管P2の管路の中心点O2とを結んで仮想線分Lとしたとき、環流管P1に配設された円弧状スリーブS1の周方向における両方の端部は、いずれも仮想線分Lを基準にして中心点O1における角度が45°以上となる位置に存在すると共に、環流管P2に配設された円弧状スリーブS2の周方向における両方の端部は、いずれも仮想線分Lを基準にして中心点O2における角度が45°以上となる位置に存在する、真空脱ガス装置の下部構造である。 That is, the present invention is a lower structure of a vacuum degassing apparatus having two reflux tubes each having a conduit through which molten metal passes, and each of the reflux tubes has a cross section of 90 ° or more with the reflux tube body. And an arc-shaped sleeve having a central angle of 180 ° or less, and these have complementary shapes, and the arc-shaped sleeve is fitted to a part of the reflux tube body, A pipe line is formed by the inner wall surface of the arc-shaped sleeve, and the center point O 1 of the pipe line of one of the circulating pipes P 1 and the pipe of the other circulating pipe P 2 in the cross section of the two circulating pipes When the virtual line segment L is connected to the center point O 2 of the road, both ends in the circumferential direction of the arc-shaped sleeve S 1 disposed in the reflux pipe P 1 are both based on the virtual line segment L. with present on angle is 45 ° or more positions at the central point O 1 in the, reflux condenser Both ends of 2 to disposed the circumferential direction of the arc-shaped sleeve S 2 are both present at a position angle at the center point O 2 with respect to the virtual line segment L is 45 ° or more, vacuum de It is the lower structure of a gas apparatus.

本発明では、下部構造における2つの環流管は、それぞれ環流管本体と円弧状スリーブとが互いに相補的な形状を有して一体に嵌め合わされ、環流管本体の内壁面と円弧状スリーブの内壁面とによって管路を形成する。このうち、円弧状スリーブは、横断面が90°以上180°以下の中心角度を有したものである。この中心角度が90°未満であると、以下で詳述するように環流管本体に発生する可能性のあるひび割れや亀裂の位置を確実に保護することができなくなる。一方で、実際の操業時に加熱されると、スリーブ自身の熱膨張や環流管本体の熱膨張によってスリーブの周方向の端部に力が掛かるため、中心角度が180°を超えるとスリーブが座屈するように割れてしまうおそれがある。特に、従来技術のようにスリーブを円筒形にした場合、スリーブに掛かる応力を解放することができないため、スリーブ自身が応力ひずみによって縦方向に割れてしまう。なお、環流管本体と円弧状スリーブとが互いに相補的な形状を有しているとは、双方が嵌め合わされた状態で互いの内壁面が揃って管路を形成できることを意味し、環流管本体と円弧状スリーブとの間に膨張吸収材を配したような場合や、ずれを防ぐために円弧状スリーブに突起部等を設けたような場合でも、これに含まれることは勿論である。   In the present invention, each of the two reflux tubes in the lower structure includes a reflux tube main body and an arc-shaped sleeve that are integrally fitted with each other having a complementary shape, and the inner wall surface of the reflux tube main body and the inner wall surface of the arc-shaped sleeve To form a conduit. Among these, the arc-shaped sleeve has a central angle of 90 ° to 180 ° in the cross section. If this central angle is less than 90 °, it will not be possible to reliably protect the positions of cracks and cracks that may occur in the reflux tube body as will be described in detail below. On the other hand, when heated during actual operation, a force is applied to the end of the sleeve in the circumferential direction due to the thermal expansion of the sleeve itself and the thermal expansion of the reflux tube body, so that the sleeve buckles when the center angle exceeds 180 °. There is a risk of cracking. In particular, when the sleeve is cylindrical as in the prior art, the stress applied to the sleeve cannot be released, and the sleeve itself is cracked in the longitudinal direction due to stress strain. Note that the fact that the reflux tube main body and the arcuate sleeve have complementary shapes means that the inner wall surfaces can be aligned to form a pipe line in a state where both are fitted together, and the reflux tube body Needless to say, this includes a case where an expansion absorbing material is disposed between the sleeve and the arcuate sleeve, or a case where a protrusion or the like is provided on the arcuate sleeve to prevent displacement.

また、上記のような円弧状スリーブを環流管本体に配設するにあたっては、槽底面に平行となるような2つの環流管の横断面において、一方の環流管P1の管路の中心点O1と他方の環流管P2の管路の中心点O2とを結んで仮想線分Lとしたとき、環流管P1に配設される円弧状スリーブS1の周方向における両方の端部が、いずれも仮想線分Lの位置を基準にして(0°として)、中心点O1における角度が45°以上、好ましくは60°以上となる場所に存在するようにする。環流管P2に配設される円弧状スリーブS2についても同様とする。 Further, when the arc-shaped sleeve as described above is arranged in the main body of the reflux pipe, the center point O of the pipe line of one of the reflux pipes P 1 in the cross section of the two reflux pipes parallel to the bottom of the tank. 1 and when the other reflux condenser P 2, line virtual line L connects the center point O 2 of both ends in the circumferential direction of the arc-shaped sleeve S 1 which is disposed reflux condenser P 1 However, in any case, the angle at the center point O 1 is 45 ° or more, preferably 60 ° or more with reference to the position of the virtual line segment L (assuming 0 °). The same applies to the arcuate sleeve S 2 disposed in the reflux pipe P 2 .

言い換えれば、円弧状スリーブS1の周方向における両端部を点A1及び点B1で表したとき(すなわち円弧状スリーブが中心角度90°以上180°以下の円弧A11を有する)、線分O11と仮想線分Lとのなす角が45°以上、好ましくは60°以上となると共に線分O11と仮想線分Lとのなす角が45°以上、好ましくは60°以上となるようにし、また、円弧状スリーブS2についても、同様に線分O22と仮想線分Lとのなす角が45°以上、好ましくは60°以上となると共に線分O22と仮想線分Lとのなす角が45°以上、好ましくは60°以上となるようにする。 In other words, when both ends in the circumferential direction of the arc-shaped sleeve S 1 are represented by the points A 1 and B 1 (that is, the arc-shaped sleeve has an arc A 1 B 1 having a central angle of 90 ° to 180 °). The angle between the line segment O 1 A 1 and the virtual line segment L is 45 ° or more, preferably 60 ° or more, and the angle between the line segment O 1 B 1 and the virtual line segment L is 45 ° or more, preferably Similarly, for the arc-shaped sleeve S 2 , the angle formed by the line segment O 2 A 2 and the imaginary line segment L is 45 ° or more, preferably 60 ° or more, and the line segment. The angle formed by O 2 B 2 and the imaginary line segment L is 45 ° or more, preferably 60 ° or more.

これは、本発明者等が熱応力計算による環流管の構造解析を実施したことに基づく。すなわち、2つの環流管P1、P2によって形成される炉底側の股部付近には、環流管本体の外壁面に高い引張応力が掛かる場所があり、2つの環流管の横断面において仮想線分Lを挟んで両方向に45°ずつの中心角度を有した円弧上の領域に集中して、ひび割れや亀裂が発生することを突き止めた。そのため、少なくともその領域をカバーするように管路側に上記のような円弧状スリーブを配設して、ひびや亀裂の進行を食い止めるようにする。 This is based on the fact that the present inventors conducted structural analysis of the reflux tube by thermal stress calculation. That is, in the vicinity of the crotch portion on the furnace bottom side formed by the two reflux tubes P 1 and P 2 , there is a place where high tensile stress is applied to the outer wall surface of the reflux tube body, and there is a virtual cross section of the two reflux tubes. It was found that cracks and cracks occurred by concentrating on a region on an arc having a central angle of 45 ° in both directions across the line segment L. For this reason, an arc-shaped sleeve as described above is provided on the pipe line side so as to cover at least the region so as to prevent the progress of cracks and cracks.

このような引張応力が発生する理由は完全には明らかになっていないが、溶融金属が流れる稼働面側(管路側)と外側との熱膨張の差による応力が要因となると考えられる。また、実際に真空脱ガス装置の操業を続けるにつれて、上記仮想線分Lの中点mを基点に左右両方向に位置する環流管P1、P2が、それぞれに接続された浸漬管の先端を広げるような挙動(ハの字に開く)を示すことから、このことも上記のような個所に集中して引張応力を発生させる要因のひとつと推測する。なお、円弧状スリーブは環流管の長さに合わせて配設するのが良いが、先端側の一部を浸漬管側に貫くように配することも可能である。 The reason why such tensile stress occurs is not completely clarified, but it is considered that the stress is caused by the difference in thermal expansion between the working surface side (pipeline side) through which the molten metal flows and the outside. Further, as the vacuum degassing apparatus is actually operated, the reflux pipes P 1 and P 2 positioned in both the left and right directions with the midpoint m of the imaginary line segment L as the base point are connected to the tips of the dip pipes respectively connected thereto. Since it shows a widening behavior (opens in a square shape), it is assumed that this is one of the factors that cause concentration of stress in the above-mentioned places. The arc-shaped sleeve is preferably arranged in accordance with the length of the reflux tube, but it is also possible to arrange the arc-shaped sleeve so that a part of the tip side penetrates the dip tube side.

また、本発明においては、環流管本体と円弧状スリーブとの間にモルタル等の膨張吸収材を介在させて、環流管本体の一部に円弧状スリーブが嵌め合わされるようにしてもよい。具体的には、円弧状スリーブの背面側(管路側の反対)や円弧状スリーブの周方向における端部に膨張吸収材を配して膨張代を設けることで、環流管本体や円弧状スリーブの熱膨張を吸収するのが良い。なかでも、円弧状スリーブの両端部に膨張吸収材を配すれば、スリーブ自身に掛かる応力ひずみを効果的に緩和して、環流管の耐久性を更に向上させることができる。   In the present invention, an arcuate sleeve may be fitted to a part of the reflux tube body by interposing an expansion absorbing material such as mortar between the reflux tube body and the arcuate sleeve. Specifically, an expansion absorber is provided at the back side of the arc-shaped sleeve (opposite to the pipe line side) or at the end in the circumferential direction of the arc-shaped sleeve to provide an expansion allowance. It is good to absorb thermal expansion. Especially, if an expansion | swelling absorber is distribute | arranged to the both ends of an arc-shaped sleeve, the stress distortion concerning a sleeve itself can be relieve | moderated effectively and the durability of a reflux tube can be improved further.

円弧状スリーブを形成する手段については特に制限されず、プレス成形や鋳込み成形するなどして所定の形状となるようにすればよいが、好ましくは、静水圧加圧成形(Cold Isostatic Press:C.I.P.)によって円弧状スリーブを得るようにするのが良い。一般に、静水圧加圧成形は無限多軸加圧となることから、金型プレスによる一軸成形に比べて均一な成形品を得ることができ、目地や耐火物の境界等を無くすることができることから、本発明のように管路の一部を形成する円弧状スリーブを得る上で、無用な溶融金属の差し込み等のおそれを排除できて好適である。   The means for forming the arc-shaped sleeve is not particularly limited, and may be formed into a predetermined shape by press molding or cast molding. Preferably, isostatic pressing (CIP) is performed. It is preferable to obtain an arc-shaped sleeve. In general, hydrostatic pressure molding is infinite multi-axial pressure, so it is possible to obtain a uniform molded product compared to uniaxial molding with a die press, and eliminate joints and refractory boundaries. Therefore, in obtaining the arc-shaped sleeve forming a part of the pipe line as in the present invention, it is preferable that the possibility of unnecessary insertion of molten metal can be eliminated.

円弧状スリーブの厚みは、一般的なRH式真空脱ガス装置での下部構造を想定すれば、少なくとも70mmを有するようにするのが望ましい。特に、操業による円弧状スリーブの消耗(化学溶損)を考慮して、真空脱ガス装置の寿命に合わせて環流管の耐久性を確保するとすれば、好ましくは150mm以上の厚みを有するようにするのが良い。なお、円弧状スリーブの厚みを増すにつれて耐久性は更に向上するが、実用的な効果が飽和するばかりか、経済的な理由等から200mm程度の厚みがあれば十分であると考えられる。   The thickness of the arc-shaped sleeve is desirably at least 70 mm, assuming a substructure in a general RH type vacuum degassing apparatus. In particular, if the durability of the reflux tube is ensured in accordance with the life of the vacuum degassing apparatus in consideration of the consumption of the arc-shaped sleeve (chemical erosion) due to operation, the thickness should preferably be 150 mm or more. Is good. Although the durability is further improved as the thickness of the arc-shaped sleeve is increased, it is considered that a thickness of about 200 mm is sufficient not only for practical effects but also for economic reasons.

また、円弧状スリーブには、その周方向の端部や背面の一部に突起部(だぼ)や溝を形成したり、円弧状スリーブの背面側を槽底側に向かって漸次縮径(薄肉化)させるなどして、環流管本体に対するずれを防ぐようにしてもよい。また、円弧状スリーブを槽底よりも下げて配設し、スリーブの頂部を環流管本体の一部で抑えるようにして浮上するのを防止するようにしてもよい。   Further, the arcuate sleeve is formed with a protrusion or a groove at a circumferential end or a part of the back surface, or the diameter of the arcuate sleeve is gradually reduced toward the bottom of the tank ( It is also possible to prevent deviation from the main body of the reflux tube by reducing the thickness). Further, the arc-shaped sleeve may be disposed lower than the bottom of the tank, and the top of the sleeve may be restrained by a part of the reflux tube main body to prevent floating.

また、円弧状スリーブを形成するための材料については、一般に、耐食性や耐スラグ性等を考慮すると塩基性材料を用いるのが望ましいが、使用条件によっては中性材料や酸性材料を用いることもできる。但し、静水圧加圧成形やプレス成形によって円弧状スリーブを得る際は、製造時の摺動性を考慮して炭素を含有した材料を用いるのが望ましい。このような炭素含有材料として、例えば、MgO−C質、Al23−C質、ZrO2−C質、ZrO2−CaO−C質(ZCG)等の材料を挙げることができる。 In addition, as a material for forming the arc-shaped sleeve, it is generally desirable to use a basic material in consideration of corrosion resistance, slag resistance, etc., but a neutral material or an acidic material can also be used depending on use conditions. . However, when an arc-shaped sleeve is obtained by hydrostatic pressure molding or press molding, it is desirable to use a material containing carbon in consideration of slidability during production. Examples of such a carbon-containing material include materials such as MgO—C, Al 2 O 3 —C, ZrO 2 —C, and ZrO 2 —CaO—C (ZCG).

また、環流管本体は、円弧状スリーブと共に形成された管路を備えるようにすれば特に制限はなく、その形状は定形煉瓦や不定形耐火物を用いて、或いはこれらを組み合わせて形成することができる。なお、本発明は、環流管本体に対して所定の位置に円弧状スリーブを嵌め合わせて環流管を形成するものであるが、これ以外に他のスリーブを環流管本体に配設することを妨げるものではない。   Further, the reflux pipe body is not particularly limited as long as it is provided with a pipe line formed with an arc-shaped sleeve, and the shape thereof may be formed using shaped bricks or amorphous refractories, or a combination thereof. it can. In the present invention, the circular tube is formed by fitting an arc-shaped sleeve at a predetermined position with respect to the reflux tube main body. However, other sleeves are prevented from being arranged on the reflux tube main body. It is not a thing.

本発明における真空脱ガス装置の下部構造は、上記で説明したような環流管を2つ備えたものであればよく、通常は、これら環流管の先端にそれぞれ浸漬管が接続される。また、環流管本体や浸漬管を含めて耐火物の周りは鉄皮で覆われて下部構造を形成する。この下部構造は、真空脱ガス装置を構成する上部構造と共に一体に形成されていてもよく、接続フランジを介して上部槽と下部槽とに分かれる2槽構造(更に中間槽を含めた3槽構造)を形成するものであってもよい。そして、ガス吹き出し孔を有した浸漬管からガスリフトポンプの原理を用いて、取鍋に入れられた溶鋼等の溶融金属を吸い上げて槽内を通過させ、他方の環流管側へと溶融金属を環流させて、所定の脱ガス処理等を行う。   The lower structure of the vacuum degassing apparatus according to the present invention may be any structure provided with two reflux tubes as described above, and usually, a dip tube is connected to the tip of each of the reflux tubes. In addition, the surroundings of the refractory including the reflux pipe body and the dip pipe are covered with an iron skin to form a lower structure. This lower structure may be formed integrally with the upper structure that constitutes the vacuum degassing apparatus, and is divided into an upper tank and a lower tank via a connection flange (a three-tank structure including an intermediate tank). ) May be formed. Then, using the principle of the gas lift pump from the dip tube having the gas blowing holes, the molten metal such as molten steel put in the ladle is sucked up and passed through the tank, and the molten metal is circulated to the other reflux tube side. Then, a predetermined degassing process or the like is performed.

本発明によれば、下部構造を形成する一対の環流管について、横断面が円弧状のスリーブを環流管本体の所定の位置に嵌め合わせて、このスリーブの内壁面と環流管本体の内壁面とによって管路を形成することから、環流管本体に生じる可能性のあるひび割れや亀裂の発生を効率的に抑制することができる。そのため、環流管の耐久性を向上させた下部構造とすることができる。   According to the present invention, with respect to the pair of reflux tubes forming the lower structure, a sleeve having a circular cross section is fitted into a predetermined position of the reflux tube body, and the inner wall surface of the sleeve and the inner wall surface of the reflux tube body are fitted. Since the pipe is formed by the above, it is possible to efficiently suppress the occurrence of cracks and cracks that may occur in the circulating pipe main body. Therefore, it can be set as the lower structure which improved the durability of the reflux tube.

図1は、本発明における真空脱ガス装置の下部構造の縦断面の様子を示す斜視説明図である。FIG. 1 is an explanatory perspective view showing a state of a longitudinal section of a lower structure of a vacuum degassing apparatus according to the present invention. 図2は、下部構造における環流管の横断面を炉底側から見た断面説明図である。FIG. 2 is a cross-sectional explanatory view of the cross section of the reflux tube in the lower structure as viewed from the furnace bottom side. 図3は、環流管における円弧状スリーブの変形配設例を示す断面説明図である。FIG. 3 is a cross-sectional explanatory view showing a modified arrangement example of the arc-shaped sleeve in the reflux tube. 図4は、環流管の周方向における熱応力分布を示すグラフである。FIG. 4 is a graph showing the thermal stress distribution in the circumferential direction of the reflux tube. 図5は、図4のグラフにおける環流管の測定位置を説明するための模式図である。FIG. 5 is a schematic diagram for explaining the measurement position of the reflux tube in the graph of FIG. 図6は、本発明における円弧状スリーブの周方向における熱応力分布を示すグラフである。FIG. 6 is a graph showing the thermal stress distribution in the circumferential direction of the arc-shaped sleeve in the present invention. 図7は、RH式真空脱ガス装置の断面模式図を示す。FIG. 7 shows a schematic cross-sectional view of an RH type vacuum degassing apparatus.

以下、添付図面に基づいて、本発明をより具体的に説明する。
図1には、本発明の真空脱ガス装置における下部構造1の一例について、縦断面の様子を示す斜視説明図である。この実施形態に係る下部構造1は、下部構造本体2と、溶融金属の行き帰り用の管路4を備えた2つの環流管3と、2つの浸漬管5とを有しており、環流管3と浸漬管5とは、それぞれに備え付けられたフランジ6、7によって接続され、図示外のボルトによって締め付け固定されている。また、この下部構造1は、下部構造本体2に備え付けられてフランジ8により、真空脱ガス装置の上部構造(図示外)に対して接続可能になっている。そして、下部構造本体2と環流管3は、それらの外周側面が鉄皮16で覆われて下部構造1を形成している。
Hereinafter, the present invention will be described in more detail with reference to the accompanying drawings.
FIG. 1 is a perspective explanatory view showing a longitudinal section of an example of the lower structure 1 in the vacuum degassing apparatus of the present invention. The lower structure 1 according to this embodiment includes a lower structure body 2, two reflux pipes 3 having a pipeline 4 for returning and returning molten metal, and two dip pipes 5. And the dip tube 5 are connected to each other by flanges 6 and 7 which are respectively provided, and are fastened and fixed by bolts (not shown). The lower structure 1 is provided on the lower structure main body 2 and can be connected to an upper structure (not shown) of the vacuum degassing apparatus by a flange 8. And the lower structure main body 2 and the reflux tube 3 form the lower structure 1 by covering the outer peripheral side surfaces thereof with the iron skin 16.

このうち、環流管3は、それぞれ不定形耐火物からなる環流管本体9と、横断面が円弧状をなす円弧状スリーブ10(図1では半分のみが図示されている)とを有して、各管路4はこの環流管本体9による内壁面と円弧状スリーブ10の内壁面とによって形成され、浸漬管5の管路11を形成する不定形耐火物からなる浸漬管本体12を含めて内壁面は全て揃えられている。また、環流管本体9を形成する不定形耐火物は、中ノ島となる敷き煉瓦13を囲うようにしながら槽底14を形成しており、下部構造本体2を形成する側壁煉瓦15と共に溶融金属を一時的に溜めて脱ガス処理等が行えるようにしている。一方、炉底側には、2つの環流管3に挟まれるようにして股部17が形成される。これらの環流管3に配設された円弧状スリーブ10について、環流管本体9に対する位置関係を以下で図2を用いながら説明する。   Among these, the reflux tube 3 has a reflux tube main body 9 made of an irregular refractory, and an arc-shaped sleeve 10 (only half of which is shown in FIG. 1) having a circular cross section. Each pipe line 4 is formed by the inner wall surface of the reflux pipe body 9 and the inner wall surface of the arc-shaped sleeve 10, and includes the dip pipe body 12 made of an irregular refractory material that forms the pipe path 11 of the dip pipe 5. The walls are all prepared. In addition, the irregular refractory forming the reflux pipe main body 9 forms a tank bottom 14 so as to surround the laying brick 13 serving as Nakanoshima, and temporarily melted metal together with the side wall brick 15 forming the lower structure main body 2. Therefore, it is possible to perform degassing treatment and the like. On the other hand, a crotch portion 17 is formed on the furnace bottom side so as to be sandwiched between the two reflux tubes 3. With respect to the arc-shaped sleeve 10 disposed in these reflux tubes 3, the positional relationship with respect to the reflux tube main body 9 will be described below with reference to FIG.

図2は、槽底14に対して平行な2つの環流管3の横断面を示しており、炉底側から見た図である。この図においては、便宜上、向かって右側の環流管3を環流管P1とし、左側を環流管P2とし、また、環流管P1に配設された円弧状スリーブ10を円弧状スリーブS1とし、環流管P2の方を円弧状スリーブS2とする。ここでは、2つの円弧状スリーブS1、S2が、それぞれ180°の中心角度を有する場合を示しており、互いに背面を対峙させるようにして環流管本体9に嵌め込まれている。そして、環流管P1の管路4の中心点O1と環流管P2の管路4の中心点O2とを結んで仮想線分Lとしたとき、円弧状スリーブS1の周方向における両方の端部が、いずれも仮想線分Lの位置を基準にして(0°として)、中心点O1における角度が45°以上、好ましくは60°以上となる場所に存在するようにする。円弧状スリーブS2の周方向における両方の端部についても同様にする。なお、この図2では、2つの円弧状スリーブS1、S2の両端部が、いずれも中心点O1、O2における角度が90°の位置に存在した状態(仮想線分Lに対して線分O11、O11、O22、及びO22が90°のなす角を有した状態)を示している。 FIG. 2 shows a cross section of the two reflux tubes 3 parallel to the tank bottom 14 and is a view seen from the furnace bottom side. In this figure, for the sake of convenience, the right reflux tube 3 is the reflux tube P 1 , the left is the reflux tube P 2, and the arc-shaped sleeve 10 disposed in the reflux tube P 1 is the arc-shaped sleeve S 1. The recirculation pipe P 2 is an arcuate sleeve S 2 . Here, the case where the two arc-shaped sleeves S 1 and S 2 each have a center angle of 180 ° is shown, and is fitted into the reflux tube main body 9 so that the back surfaces thereof face each other. Then, when a virtual line segment L by connecting the center point O 2 of the reflux condenser P line center point O 1 of 4 1 and the pipe 4 reflux condenser P 2, in the circumferential direction of the arc-shaped sleeve S 1 Both ends are located at a position where the angle at the center point O 1 is 45 ° or more, preferably 60 ° or more, both based on the position of the virtual line segment L (assuming 0 °). To same for both ends in the circumferential direction of the arc-shaped sleeve S 2. In FIG. 2, both end portions of the two arc-shaped sleeves S 1 and S 2 are in a state where the angles at the center points O 1 and O 2 are 90 ° (with respect to the imaginary line segment L). The line segments O 1 A 1 , O 1 B 1 , O 2 A 2 , and O 2 B 2 have a 90 ° angle).

また、円弧状スリーブは、上記で説明したような条件を満たせば、図3に示したように、その周方向の両端部が仮想線分Lを挟んで非対称の位置になるように配設されても構わない。更には、図3に示したように、内壁面側(又は背面側)の円弧が迫り出したり、端部に突起部を設けたりして端部が半径方向に完全に揃っていなくても、本発明における作用効果を奏する限り構わない。   Further, the arc-shaped sleeve is disposed so that both ends in the circumferential direction thereof are asymmetric with respect to the imaginary line segment L as shown in FIG. 3 if the conditions described above are satisfied. It doesn't matter. Furthermore, as shown in FIG. 3, even if the arc on the inner wall surface side (or the back side) protrudes or a protrusion is provided at the end, the end is not completely aligned in the radial direction, It does not matter as long as the effects of the present invention are exhibited.

この実施形態に係る下部構造1を得る手段については特に制限されないが、以下のような方法を例示することができる。例えば、下部構造本体2と環流管3の外周側面を覆うと共に、両端に下部構造本体側のフランジ8と環流管側のフランジ6とを備えた鉄皮16を外枠として用い、先に、環流管側のフランジ6に沿って養生面を形成しておく。次いで、プレス成形や鋳込み成形等によって形成した円弧状スリーブ10を所定の位置に配置し、環流管3の管路4を形作る中子や敷き煉瓦13の部分の中子を入れて、隙間にキャスタブル(不定形耐火物)を流し込んで充填し、養生、乾燥させて槽底14を形成する。その際、円弧状スリーブ10の背面や周方向の端面に予めシートモルタル等を塗布しておき、得られた環流管本体9との間に膨張吸収材を介在させるようにしてもよい。そして、側壁煉瓦15等を築造して下部構造本体を完成させて、別途形成された浸漬管5を接続すれば、下部構造1を得ることができる。   The means for obtaining the lower structure 1 according to this embodiment is not particularly limited, but the following method can be exemplified. For example, an iron skin 16 that covers the outer peripheral side surfaces of the lower structure main body 2 and the reflux pipe 3 and includes the flange 8 on the lower structure main body side and the flange 6 on the reflux pipe side at both ends is used as an outer frame. A curing surface is formed along the flange 6 on the tube side. Next, the arc-shaped sleeve 10 formed by press molding, casting molding, or the like is placed at a predetermined position, and the core that forms the conduit 4 of the reflux pipe 3 or the core of the laying brick 13 is inserted, and castable in the gap. (Unshaped refractory) is poured and filled, cured and dried to form the tank bottom 14. At that time, sheet mortar or the like may be applied in advance to the back surface of the arc-shaped sleeve 10 or the end face in the circumferential direction, and an expansion absorbing material may be interposed between the obtained reflux tube main body 9. Then, the lower structure 1 can be obtained by building the side wall bricks 15 and the like to complete the lower structure main body and connecting the separately formed dip tube 5.

或いは、環流管3の管路4を形作る中子に円弧状スリーブ10の形状に相当する部分を設けておき、キャスタブルを流し込んで養生・乾燥させた後に中子を脱枠し、背面及び周方向の端面にモルタルを塗布した円弧状スリーブ10を挿入してモルタルを乾燥させるようにしてもよい。更には、円弧状スリーブ10の厚み分だけ全周にわたって大きくした中子を入れてキャスタブルを流し込み、養生・乾燥させた後に中子を脱枠し、一方、円筒状に成形したスリーブを長手方向(縦方向)に2つに分割して得たそれぞれの円弧状スリーブの周方向の端面にモルタルを塗布して、再度円筒状になるように組み合わせ、各円弧状スリーブの背面にモルタルを塗布して所定の位置に挿入するようにしてもよい。勿論、環流管本体9は、キャスタブル以外にも煉瓦を用いて形成することも可能である。   Alternatively, a portion corresponding to the shape of the arc-shaped sleeve 10 is provided in the core that forms the pipe line 4 of the reflux pipe 3, the castable is poured into the core, and after curing and drying, the core is removed, and the back surface and the circumferential direction The mortar may be dried by inserting an arc-shaped sleeve 10 coated with mortar on the end face. Furthermore, a core that is enlarged over the entire circumference by the thickness of the arc-shaped sleeve 10 is inserted, castable is poured, and after curing and drying, the core is removed from the frame. Apply the mortar to the end face in the circumferential direction of each arcuate sleeve obtained by dividing it into two in the vertical direction) and combine it so that it becomes cylindrical again, and apply the mortar to the back of each arcuate sleeve You may make it insert in a predetermined position. Of course, the reflux tube main body 9 can also be formed using bricks in addition to the castable.

次に、円弧状スリーブの配設位置を決定するにあたって参考にした、熱応力計算による環流管の構造解析について説明する。
先ずは、従来技術の下部構造について、操業時に1つの環流管に掛かる熱応力をその周方向に沿って解析した。すなわち、図1に示した本発明の下部構造において円弧状スリーブ10を配設せずに、環流管本体9のみによって管路4を形成した場合の下部構造について、管路を形成する環流管本体9の内側(管路側)と外側を、周方向に沿って熱応力を測定した。結果を図4に示す。なお、図4のグラフの横軸は、図5に示したように、上述した仮想線分Lと環流管本体9とが交わる位置を角度0°として、股部側からその反対側まで180°回転させたものであり、この間で10°ずつ位置を変えて周方向における熱応力の分布を算出した。また、この算出に際しては有限要素法を用いて、実際の真空脱ガス槽の温度変化データを用いて計算した。
Next, the structural analysis of the circulating pipe by the thermal stress calculation, which was referred to when determining the arrangement position of the arc-shaped sleeve, will be described.
First, regarding the lower structure of the prior art, the thermal stress applied to one reflux tube during operation was analyzed along its circumferential direction. That is, in the lower structure of the present invention shown in FIG. 1, the circular flow tube main body forming the pipe is formed in the lower structure when the pipe 4 is formed only by the circular flow pipe main body 9 without providing the arc-shaped sleeve 10. Thermal stress was measured along the circumferential direction on the inner side (duct side) and the outer side of 9. The results are shown in FIG. The horizontal axis of the graph of FIG. 4 is 180 ° from the crotch side to the opposite side, with the position where the imaginary line segment L and the reflux tube body 9 intersect as shown in FIG. This was rotated, and the position was changed by 10 ° during this period, and the distribution of thermal stress in the circumferential direction was calculated. In this calculation, the finite element method was used to calculate the temperature change data of the actual vacuum degassing tank.

図4に示したグラフから分るように、仮想線分Lの中点mを挟んで左右両方向に位置する環流管は、互いに最短距離で隣接する位置において(角度=0°)、環流管本体9の外側には約120MPaの引張応力が発生し、そこから周方向に45°の角度を有した位置で150MPaを超えて引張応力が最大になる。更に周方向に角度60°を有する位置までは高い値で引張応力が発生し、そして、周方向に沿って回転させるにつれて徐々に引張応力は低減し、角度120°付近でほぼ値はゼロになる。これに対して、環流管本体9の内側(管路側)には、外側に掛かる引張応力の関係と正反対のように、角度60°の位置あたりまでは高い値で圧縮応力が発生し、それ以降は徐々に圧縮応力は少なくなり120°付近でほぼ一定になる。   As can be seen from the graph shown in FIG. 4, the reflux tubes located in the left and right directions across the midpoint m of the imaginary line segment L are adjacent to each other at the shortest distance (angle = 0 °). A tensile stress of about 120 MPa is generated on the outer side of 9, and the tensile stress reaches a maximum exceeding 150 MPa at a position having an angle of 45 ° in the circumferential direction therefrom. Further, a tensile stress is generated at a high value up to a position having an angle of 60 ° in the circumferential direction, and the tensile stress gradually decreases as it is rotated along the circumferential direction, and the value becomes almost zero near an angle of 120 °. . On the other hand, on the inner side (the pipe line side) of the reflux pipe body 9, a compressive stress is generated at a high value up to the position of an angle of 60 °, as opposed to the relation of the tensile stress applied to the outer side, and thereafter. Gradually decreases in compressive stress and becomes almost constant around 120 °.

このような熱応力計算による環流管の構造解析に基づき、本発明では、仮想線分Lを挟んで少なくとも±45°の中心角度を有した円弧領域に対応させて円弧状スリーブを配設し、好ましくは仮想線分Lを挟んで±60°の中心角度を有した円弧領域に対応させて円弧状スリーブを配設して環流管の耐久性を高めるようにする。   Based on the structural analysis of the reflux tube by such thermal stress calculation, in the present invention, an arc-shaped sleeve is disposed corresponding to an arc region having a central angle of at least ± 45 ° across the virtual line segment L, Preferably, an arc-shaped sleeve is provided in correspondence with an arc region having a central angle of ± 60 ° across the imaginary line segment L so as to enhance the durability of the reflux tube.

そこで、横断面における中心角度が180°の円弧状スリーブ10を図2に示した位置関係となるように、モルタルを介して環流管本体9に嵌め合わせて本発明の下部構造1とし、この円弧状スリーブ10の背面(外側面)における周方向の熱応力分布を測定した。結果を図6に示す。なお、測定環境や測定条件については先の場合と同様であるが、測定範囲は図5に示した0°〜90°である(中心角度が180°の円弧状スリーブのため)。また、この測定において使用した円弧状スリーブは、静水圧加圧成形によって厚み200mmの円筒状成形品を得て、これを縦方向に2つに分割したものである。   Therefore, the circular sleeve 10 having a center angle of 180 ° in the cross section is fitted to the reflux tube body 9 through a mortar so as to have the positional relationship shown in FIG. The thermal stress distribution in the circumferential direction on the back surface (outer surface) of the arc-shaped sleeve 10 was measured. The results are shown in FIG. The measurement environment and measurement conditions are the same as in the previous case, but the measurement range is 0 ° to 90 ° shown in FIG. 5 (because the arc-shaped sleeve has a central angle of 180 °). In addition, the arc-shaped sleeve used in this measurement is a cylindrical molded product having a thickness of 200 mm obtained by hydrostatic pressure molding, and is divided into two in the vertical direction.

図6のグラフから分るように、円弧状スリーブ10の背面は周方向の全ての範囲で引張応力が発生しないことが分る。すなわち、先に説明した環流管本体9の外側で発生した引張応力は、円弧状スリーブ10に対してほぼ伝達されないことから、仮に環流管本体9の外側でひび割れや亀裂が発生したとしても、円弧状スリーブ10ではこれを食い止めることができる。また、この円弧状スリーブ10の稼動面(内側面)での熱応力分布についても測定したところ、図6と略同様の結果が得られたことから、円弧状スリーブ10自体が割れてしまうような深刻な応力ひずみを受けるようなおそれもない。   As can be seen from the graph of FIG. 6, it can be seen that the back surface of the arcuate sleeve 10 does not generate tensile stress in the entire circumferential range. That is, since the tensile stress generated outside the circulating tube body 9 described above is hardly transmitted to the arc-shaped sleeve 10, even if cracks or cracks occur outside the circulating tube body 9, The arcuate sleeve 10 can stop this. Further, when the thermal stress distribution on the working surface (inner side surface) of the arcuate sleeve 10 was also measured, a result almost the same as that shown in FIG. 6 was obtained, so that the arcuate sleeve 10 itself was broken. There is no risk of severe stress strain.

次に、本発明の実施例及び比較例を説明する。なお、以下では、1チャージあたり390トンの溶鋼を環流できるRH式の真空脱ガス装置の下部構造を形成した。また、環流管3の製造にあたっては、先に述べたように、両端に下部構造本体側のフランジ8と環流管側のフランジ6とを備えた鉄皮16を外枠として用い、予め、環流管側のフランジ6に沿って養生面を形成しておいた。   Next, examples and comparative examples of the present invention will be described. In the following, the lower structure of an RH vacuum degassing apparatus capable of circulating 390 tons of molten steel per charge was formed. In manufacturing the reflux pipe 3, as described above, the iron skin 16 provided with the flange 8 on the lower structure main body side and the flange 6 on the reflux pipe side at both ends is used as an outer frame, and the reflux pipe is preliminarily provided. A curing surface was formed along the flange 6 on the side.

[実施例1]
先ず、9質量%黒鉛を含んだMgO−C粉体を用いて、1000kg/cm2の圧力による静水圧成形によって、内径φ700mm×外径φ1090mm×高さ1040mmの円筒形の成形品を準備した。脱枠後、この円筒形成形品をダイヤモンドカッターにて縦方向に切断して半円にし、横断面が180°の中心角度を有した円弧状スリーブを得た。
[Example 1]
First, a cylindrical molded product having an inner diameter φ700 mm × outer diameter φ1090 mm × height 1040 mm was prepared by hydrostatic pressing at a pressure of 1000 kg / cm 2 using MgO—C powder containing 9 mass% graphite. After removing the frame, this cylindrically formed product was cut longitudinally with a diamond cutter into a semicircle, and an arc-shaped sleeve having a central angle of 180 ° in the cross section was obtained.

得られた2つの円弧状スリーブは特に研磨等をせずに無加工のまま、それぞれの背面と周方向の端面とに厚さ2mmで塩基性のモルタルを塗布し(膨張代)、図1及び図2に示したような位置関係になるように円弧状スリーブを配置して、それぞれ外径700mmの中子を入れて隙間にAl23−MgO系キャスタブルを流し込んだ。養生・乾燥後、MgO−Cr23質の側壁煉瓦を内張りするなどして下部構造本体を形成し、また、別途用意した浸漬管を環流管側に取り付けて、実施例1に係る下部構造を完成させた。 The obtained two arc-shaped sleeves were applied with basic mortar with a thickness of 2 mm (expansion allowance) on the back surface and the end surface in the circumferential direction, without being particularly processed without polishing. Arc-shaped sleeves were arranged so as to have a positional relationship as shown in FIG. 2, cores having an outer diameter of 700 mm were inserted, and Al 2 O 3 —MgO-based castables were poured into the gaps. After curing and drying, the lower structure main body is formed by lining a side wall brick of MgO-Cr 2 O 3 or the like, and a separately prepared dip pipe is attached to the reflux pipe side to form the lower structure according to the first embodiment. Was completed.

上記で得られた下部構造を備えたRH式真空脱ガス装置を使って、溶鋼の二次精錬で実機操業した。その結果、550チャージのところで下部構造本体を形成する側壁煉瓦の残厚が少なくなり、操業を中止した。このとき、2つの環流管ともに、管路を形成する環流管本体と円弧状スリーブの内壁面にはいずれもひび割れや亀裂は確認されなかった。そのため、本発明の下部構造によれば、真空脱ガス装置自体の寿命まで特段の補修等を要さずに使用することも可能になる。   Using the RH vacuum degassing apparatus having the substructure obtained above, the actual operation was performed by secondary refining of molten steel. As a result, the remaining thickness of the side wall bricks forming the lower structure body at 550 charges decreased, and the operation was stopped. At this time, neither cracks nor cracks were observed on the inner surface of the reflux tube main body and the arc-shaped sleeve forming the pipeline in both of the reflux tubes. Therefore, according to the lower structure of the present invention, the vacuum degassing apparatus itself can be used without requiring special repairs until the lifetime of the vacuum degassing apparatus itself.

[実施例2]
内径φ650mm×外径φ1120mm×高さ1040mmの円筒形の成形品を縦方向に2つに分割して、横断面の中心角度が180°の円弧状スリーブを得た。次いで、円弧状スリーブに塩基性モルタルを塗布することなく、鉄皮からなる外枠に2つともそのまま配置した以外は実施例1と同様にして、下部構造を完成させた。
[Example 2]
A cylindrical molded product having an inner diameter of 650 mm, an outer diameter of 1120 mm, and a height of 1040 mm was divided into two in the longitudinal direction to obtain an arc-shaped sleeve having a central angle of 180 ° in cross section. Next, the lower structure was completed in the same manner as in Example 1 except that the basic mortar was not applied to the arc-shaped sleeve, and both were arranged as they were on the outer frame made of iron skin.

上記で得られた下部構造を備えたRH式真空脱ガス装置を使って、実施例1と同様に実機操業したところ、350チャージを過ぎても環流管の管路にひび割れや亀裂が入ることはなかったが、500チャージのところで円弧状スリーブのほぼ中央に長手方向に向かった亀裂が顕在化し、操業を中止した。   Using the RH-type vacuum degassing apparatus having the substructure obtained above, the actual machine was operated in the same manner as in Example 1. As a result, cracks and cracks could enter the pipe of the reflux tube even after 350 charges. Although there was no crack, the crack in the longitudinal direction became apparent at the approximate center of the arc-shaped sleeve at 500 charges, and the operation was stopped.

[実施例3]
円弧状スリーブに塩基性モルタルを塗布することなく、鉄皮からなる外枠に2つともそのまま配置した以外は実施例1と同様にして、下部構造を完成させた。
[Example 3]
The substructure was completed in the same manner as in Example 1 except that the basic mortar was not applied to the arc-shaped sleeve, and both were arranged as they were on the outer frame made of iron skin.

上記で得られた下部構造を備えたRH式真空脱ガス装置を使って、実施例1と同様に実機操業したところ、350チャージを過ぎても環流管の管路にひび割れや亀裂が入ることはなかったが、450チャージのところで円弧状スリーブのほぼ中央に長手方向に向かった亀裂が顕在化し、操業を中止した。   Using the RH-type vacuum degassing apparatus having the substructure obtained above, the actual machine was operated in the same manner as in Example 1. As a result, cracks and cracks could enter the pipe of the reflux tube even after 350 charges. Although there was no crack, a crack toward the longitudinal direction became apparent at the center of the arc-shaped sleeve at 450 charges, and the operation was stopped.

[実施例4]
実施例1で使用したものと同じサイズの円弧状スリーブを、それぞれ直接オイルプレス機を用いて成形圧2500トンで成形した。得られた円弧状スリーブの背面と周方向の端面とにそれぞれ厚さ2mmで塩基性のモルタルを塗布し(膨張代)、実施例1と同様にして環流管及び下部構造本体を形成し、浸漬管を取り付けて下部構造を完成させた。
[Example 4]
Each of the arc-shaped sleeves having the same size as that used in Example 1 was molded at a molding pressure of 2500 tons using a direct oil press. A basic mortar having a thickness of 2 mm was applied to the back surface and the circumferential end surface of the obtained arc-shaped sleeve (expansion allowance) to form a reflux tube and a lower structure main body in the same manner as in Example 1, and dipping A tube was attached to complete the substructure.

上記で得られた下部構造を備えたRH式真空脱ガス装置を使って、溶鋼の二次精錬で実機操業した。その結果、350チャージを過ぎても環流管の管路にひび割れや亀裂が入ることはなかったが、480チャージのところで環流管の管路における円弧状スリーブの内壁面の残厚が少なくなり、2つの管路の中心点を結んだ仮想線分Lを挟んで両方向におよそ45°の中心角度を有した部分に損耗が確認され、操業を中止した。   Using the RH vacuum degassing apparatus having the substructure obtained above, the actual operation was performed by secondary refining of molten steel. As a result, cracks and cracks did not occur in the conduit of the reflux tube even after 350 charges, but the remaining thickness of the inner wall surface of the arc-shaped sleeve in the conduit of the reflux tube decreased at 480 charges. Wear was confirmed in a portion having a central angle of about 45 ° in both directions across an imaginary line segment L connecting the central points of two pipes, and the operation was stopped.

[実施例5]
実施例1で使用したものと同じサイズの円弧状スリーブをAl23−MgOのプレキャスト品にかえた以外は実施例1と同様にして、下部構造を完成させた。
[Example 5]
The substructure was completed in the same manner as in Example 1 except that the arc-shaped sleeve having the same size as that used in Example 1 was replaced with a precast product of Al 2 O 3 —MgO.

得られた下部構造を備えたRH式真空脱ガス装置を使って、実施例1と同様に実機操業したところ、350チャージを過ぎても環流管の管路にひび割れや亀裂が入ることはなかったが、380チャージのところで、円弧状スリーブの内壁面の残厚が少なくなり、2つの管路の中心点を結んだ仮想線分Lを挟んで両方向におよそ45°の中心角度を有した部分にひび割れや亀裂が確認され、操業を中止した。   Using the RH-type vacuum degassing apparatus having the obtained substructure, the actual machine was operated in the same manner as in Example 1. As a result, cracks and cracks did not enter the conduit of the reflux pipe even after 350 charges. However, at the 380 charge, the remaining thickness of the inner wall surface of the arc-shaped sleeve is reduced, and a portion having a central angle of about 45 ° in both directions across the virtual line segment L connecting the center points of the two pipes. Cracks and cracks were confirmed, and the operation was stopped.

[実施例6]
実施例1と同様にして成形した内径φ700mm×外径φ1090mm×高さ1040mmの円筒形の成形品を縦方向3つに切断して横断面が120°の中心角度を有した円弧状スリーブを得た。得られた円弧状スリーブの2つを用いて、背面と周方向の端面とにそれぞれ厚さ2mmで塩基性のモルタルを塗布した(膨張代)。そして、環流管P2を形成する円弧状スリーブの周方向の両端部について、図3に示す線分LとA2とのなす角度mO22を50°とし、もう一方の線分LとB2とのなす角mO22を70°として配置した。また、環流管P1を形成する円弧状スリーブの周方向の両端部についても同様に、線分LとA1とのなす角度mO11を50°とし、もう一方の線分LとB1とのなす角mO11を70°として配置した。これら以外は実施例1と同様にして環流管及び下部構造本体を形成し、浸漬管を取り付けて下部構造を完成させた。
[Example 6]
A cylindrical molded product having an inner diameter φ700 mm × outer diameter φ1090 mm × height 1040 mm formed in the same manner as in Example 1 was cut into three longitudinal directions to obtain an arc-shaped sleeve having a central angle of 120 ° in cross section. It was. Using two of the obtained arc-shaped sleeves, basic mortar with a thickness of 2 mm was applied to the back surface and the end surface in the circumferential direction, respectively (expansion allowance). Then, at both ends in the circumferential direction of the arc-shaped sleeve forming the reflux pipe P 2 , the angle mO 2 A 2 formed by the line segment L and A 2 shown in FIG. It was placed an angle mO 2 B 2 and B 2 as 70 °. Similarly, at both ends in the circumferential direction of the arc-shaped sleeve forming the reflux pipe P 1 , the angle mO 1 A 1 formed by the line segment L and A 1 is set to 50 °, and the other line segments L and B The angle mO 1 B 1 formed with 1 was set to 70 °. Except for these, a reflux tube and a lower structure main body were formed in the same manner as in Example 1, and a dip tube was attached to complete the lower structure.

上記で得られた下部構造を備えたRH式真空脱ガス装置を使って、実施例1と同様に実機操業したところ、550チャージのところで下部構造本体を形成する側壁煉瓦の残厚が少なくなり、操業を中止した。このとき、2つの環流管ともに、管路を形成する環流管本体と円弧状スリーブの内壁面にはいずれもひび割れや亀裂は確認されず、真空脱ガス装置自体の寿命まで特段の補修等を要さずに使用することも可能である。   Using the RH-type vacuum degassing apparatus having the lower structure obtained above, and operating the actual machine in the same manner as in Example 1, the remaining thickness of the side wall bricks forming the lower structure body at 550 charges is reduced. The operation was stopped. At this time, neither of the two recirculation tubes is confirmed to have cracks or cracks on the inner surface of the recirculation tube main body and the arc-shaped sleeve forming the pipe, and special repairs are required until the life of the vacuum degassing device itself. It is also possible to use it.

[比較例1]
円弧状スリーブを配設せずに、2つの環流管ともにAl23−MgO系キャスタブルを流し込んで管路を形成した以外は実施例1と同様にして、下部構造を完成させた。得られた下部構造を備えたRH式真空脱ガス装置を使って、溶鋼の二次精錬で実機操業したところ、350チャージのところで両方の環流管ともに股部付近で管路に複数の亀裂が確認され、なかでも、2つの管路の中心点を結んだ仮想線分Lを挟んで両方向におよそ45°の中心角度を有したところには比較的大きな亀裂が入ったことから、操業を中止した。
[Comparative Example 1]
The substructure was completed in the same manner as in Example 1, except that the Al 2 O 3 —MgO-based castable was poured into the two reflux tubes without forming the arc-shaped sleeve. Using the RH-type vacuum degassing device with the obtained substructure, the actual machine was operated by secondary refining of molten steel. At 350 charge, both cracked pipes were confirmed to have multiple cracks near the crotch. In particular, the operation was stopped because there was a relatively large crack at the center angle of about 45 ° in both directions across the virtual line segment L connecting the center points of the two pipes. .

[比較例2]
内径φ700mm×外径φ1090mm×高さ1040mmの円筒形の成形品を縦方向に分割せずに、円筒形スリーブのままで管路を形成するようにした。すなわち、上記円筒形スリーブの背面に厚さ2mmで塩基性のモルタルを塗布し(膨張代)、鉄皮からなる外枠にそのまま配置して2つの環流管を形成した以外は実施例1と同様にして、下部構造を完成させた。
[Comparative Example 2]
A cylindrical molded product having an inner diameter of 700 mm, an outer diameter of 1090 mm, and a height of 1040 mm was not divided in the vertical direction, and a pipe line was formed as it was with a cylindrical sleeve. That is, the same as in Example 1 except that a basic mortar having a thickness of 2 mm was applied to the back surface of the cylindrical sleeve (expansion allowance), and was arranged as it was on the outer frame made of iron skin to form two reflux tubes. Thus, the substructure was completed.

上記で得られた下部構造を備えたRH式真空脱ガス装置を使って、実施例1と同様に実機操業したところ、350チャージを過ぎても環流管の管路にひび割れや亀裂が入ることはなかったが、430チャージのところで円筒状スリーブの複数個所にランダムに長手方向に向かった亀裂が顕在化し、操業を中止した。   Using the RH-type vacuum degassing apparatus having the substructure obtained above, the actual machine was operated in the same manner as in Example 1. As a result, cracks and cracks could enter the pipe of the reflux tube even after 350 charges. Although there were no cracks, the cracks randomly oriented in the longitudinal direction became apparent at a plurality of locations on the cylindrical sleeve at 430 charges, and the operation was stopped.

上記実施例及び比較例の内容をまとめると以下の表1のとおりである。   The contents of the examples and comparative examples are summarized in Table 1 below.

Figure 2013082969
Figure 2013082969

1:下部構造、2:下部構造本体、3:環流管、4:管路(環流管)、5:浸漬管、6:フランジ(環流管)、7:フランジ(浸漬管)、8:フランジ(下部構造本体)、9:環流管本体、10:円弧状スリーブ、11:管路(浸漬管)、12:浸漬管本体、13:敷き煉瓦、14:槽底、15:側壁煉瓦、16:鉄皮。 1: lower structure, 2: lower structure main body, 3: reflux pipe, 4: pipe (circulation pipe), 5: dip pipe, 6: flange (reflux pipe), 7: flange (dip pipe), 8: flange ( Lower structure main body), 9: Circulating pipe main body, 10: Arc-shaped sleeve, 11: Pipe line (dip tube), 12: Dip pipe main body, 13: Laying brick, 14: Tank bottom, 15: Side wall brick, 16: Iron leather.

Claims (4)

溶融金属の通過する管路を有した環流管を2つ備えた真空脱ガス装置の下部構造であって、
前記各環流管は、環流管本体と横断面が90°以上180°以下の中心角度を有した円弧状のスリーブとを備えると共に、これらが互いに相補的な形状を有して環流管本体の一部に円弧状スリーブが嵌め合わされ、環流管本体の内壁面と円弧状スリーブの内壁面とによって管路を形成しており、かつ、
2つの環流管の横断面において、一方の環流管P1の管路の中心点O1と他方の環流管P2の管路の中心点O2とを結んで仮想線分Lとしたとき、環流管P1に配設された円弧状スリーブS1の周方向における両方の端部は、いずれも仮想線分Lを基準にして中心点O1における角度が45°以上となる位置に存在すると共に、環流管P2に配設された円弧状スリーブS2の周方向における両方の端部は、いずれも仮想線分Lを基準にして中心点O2における角度が45°以上となる位置に存在することを特徴とする、真空脱ガス装置の下部構造。
A substructure of a vacuum degassing apparatus having two reflux tubes each having a conduit through which molten metal passes,
Each of the reflux tubes includes a reflux tube body and an arcuate sleeve having a central angle of 90 ° to 180 ° in cross section, and these have complementary shapes to each other. An arc-shaped sleeve is fitted to the portion, and a pipe line is formed by the inner wall surface of the reflux tube body and the inner wall surface of the arc-shaped sleeve; and
In cross-section of the two reflux condenser, when a virtual line L by connecting one of the center point of the reflux condenser P 1, line O 1 and the other with the central point O 2 of the conduit reflux condenser P 2, Both ends in the circumferential direction of the arc-shaped sleeve S 1 disposed in the reflux pipe P 1 are present at positions where the angle at the center point O 1 is 45 ° or more with respect to the virtual line segment L. At the same time, both ends in the circumferential direction of the arc-shaped sleeve S 2 disposed in the reflux pipe P 2 are at positions where the angle at the center point O 2 is 45 ° or more with respect to the virtual line segment L. A substructure of a vacuum degassing apparatus, characterized in that it exists.
前記環流管本体との間に膨張吸収材を介在させて円弧状スリーブが嵌め合わされている、請求項1に記載の真空脱ガス装置の下部構造。   The substructure of the vacuum degassing apparatus according to claim 1, wherein an arc-shaped sleeve is fitted with an expansion absorbent between the reflux tube body. 前記円弧状スリーブが少なくとも厚さ70mmを有する、請求項1又は2に記載の真空脱ガス装置の下部構造。   The lower structure of the vacuum degassing apparatus according to claim 1 or 2, wherein the arc-shaped sleeve has a thickness of at least 70 mm. 前記円弧状スリーブが静水圧加圧成形によって得られたものである、請求項1〜3のいずれかに記載の真空脱ガス装置の下部構造。   The lower structure of the vacuum degassing apparatus according to any one of claims 1 to 3, wherein the arc-shaped sleeve is obtained by hydrostatic pressure molding.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101794594B1 (en) * 2016-05-26 2017-11-07 주식회사 포스코 Apparatus for molten metal treatment

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JPS60162721A (en) * 1984-02-02 1985-08-24 Tokyo Yogyo Co Ltd Reflux pipe
JPH0820815A (en) * 1994-07-08 1996-01-23 Shinagawa Refract Co Ltd Method for repairing circulating flow tube of vacuum degassing apparatus
JPH1030118A (en) * 1996-07-17 1998-02-03 Nkk Corp Method for preventing float-up of bedded brick in vacuum degassing vessel and device therefor
JP2007197780A (en) * 2006-01-27 2007-08-09 Jfe Steel Kk Structure of circular-flowing tube brick in rh-vacuum degassing apparatus

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* Cited by examiner, † Cited by third party
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JPS60162721A (en) * 1984-02-02 1985-08-24 Tokyo Yogyo Co Ltd Reflux pipe
US4595178A (en) * 1984-02-02 1986-06-17 Tokyo Yogyo Kabushiki Kaisha Leg for vacuum tank for refining molten steel
JPH0820815A (en) * 1994-07-08 1996-01-23 Shinagawa Refract Co Ltd Method for repairing circulating flow tube of vacuum degassing apparatus
JPH1030118A (en) * 1996-07-17 1998-02-03 Nkk Corp Method for preventing float-up of bedded brick in vacuum degassing vessel and device therefor
JP2007197780A (en) * 2006-01-27 2007-08-09 Jfe Steel Kk Structure of circular-flowing tube brick in rh-vacuum degassing apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101794594B1 (en) * 2016-05-26 2017-11-07 주식회사 포스코 Apparatus for molten metal treatment

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