JP2008036661A - Tundish - Google Patents

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JP2008036661A
JP2008036661A JP2006211905A JP2006211905A JP2008036661A JP 2008036661 A JP2008036661 A JP 2008036661A JP 2006211905 A JP2006211905 A JP 2006211905A JP 2006211905 A JP2006211905 A JP 2006211905A JP 2008036661 A JP2008036661 A JP 2008036661A
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pouring
chamber
molten metal
tundish
pouring chamber
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JP4387385B2 (en
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Toshiyuki Kobayashi
利行 小林
Hiroaki Sakai
宏明 酒井
Takehiro Nakaoka
威博 中岡
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Kobe Steel Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a tundish with a simple structure which does not disturb the flow of molten metal as far as possible in such a manner that the floating-up and separation of non-metallic inclusions can be promoted. <P>SOLUTION: In the tundish, a plurality of communication passages 4 each having a longitudinal direction are provided. The communication passages 4a(4b) have at least one cross part being a cross point α or a cross line mutually crossing in the tangential direction of the outer circumferential faces of the communication passages 4a(4b) in the parts AA(BB) at which the communication passages 4a(4b) are connected with a molten metal pouring chamber 5, and also the direction in which elongated faces A(B) obtained by elongating the outer circumferential faces along the longitudinal direction of the communication passages 4a(4b) go from a receiving chamber 3 to the molten metal pouring chamber 5. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、溶融金属を鋳型内に注湯する際に用いられる溶融金属の容器であるタンディッシュに関する。   The present invention relates to a tundish, which is a molten metal container used when pouring molten metal into a mold.

従来、タンディッシュ内に受容した溶融金属中に存在する非金属介在物の分離除去において、CaO系耐火物からなる複数の板に非金属介在物を付着吸収させる構成を有した溶融金属の清浄化方法が知られている(例えば、特許文献1参照)。この溶融金属の清浄化方法は、タンディッシュ内にCaO系耐火物からなる複数の板を交互に配置して、これらCaO系耐火物の板の間を通過する溶融金属の流速を速くして流れに発生する乱れを大きくし、さらにCaO系耐火物近傍を溶融金属が通過する時間を長くとることにより、非金属系介在物のCaO系耐火物への付着吸収を促進しようとする方法である。   Conventionally, in the separation and removal of non-metallic inclusions present in the molten metal received in the tundish, cleaning of the molten metal having a configuration in which non-metallic inclusions are adhered and absorbed on a plurality of plates made of CaO-based refractory. A method is known (see, for example, Patent Document 1). In this molten metal cleaning method, a plurality of plates made of CaO-based refractories are alternately arranged in a tundish, and the flow rate of molten metal passing between the plates of these CaO-based refractories is increased. This is a method of promoting adhesion and absorption of non-metallic inclusions to the CaO refractory by increasing the turbulence to be generated and taking a longer time for the molten metal to pass through the vicinity of the CaO refractory.

また、溶融金属を旋回槽に受容し、この溶融金属を水平旋回させて非金属介在物を浮上分離するタンディッシュに係る技術が知られている(例えば、特許文献2参照)。この非金属介在物を浮上分離する技術は、溶融金属を充填した旋回槽に移動磁場を印加して水平旋回による遠心力を溶融金属に与え、溶融金属と非金属介在物との比重差により非金属介在物を旋回槽中心に集め、衝突、吸着、凝集合体を促進することにより非金属介在物を浮上分離するという技術である。   A technique related to tundish is also known in which molten metal is received in a swirl tank and non-metallic inclusions are floated and separated by horizontally swirling the molten metal (see, for example, Patent Document 2). This technology for levitating and separating non-metallic inclusions applies a moving magnetic field to a swirling tank filled with molten metal to apply a centrifugal force due to horizontal swirling to the molten metal, and the non-metallic inclusions are caused by a difference in specific gravity between the molten metal and non-metallic inclusions. This is a technique in which metal inclusions are collected at the center of a swirl tank, and nonmetallic inclusions are floated and separated by promoting collision, adsorption, and aggregation.

また、溶融金属を回流槽に受容し、この溶融金属を水平旋回させるとともに回流槽に不活性ガスを流して非金属介在物を浮上分離するタンディッシュに係る技術も知られている(例えば、特許文献3参照)。この非金属介在物を浮上分離する技術は、溶融金属を回流槽に受容する際に、水平一方向成分を有する角度の吐出孔を少なくとも1つ備えたロングノズル内から溶融金属を回流槽に導入し、このロングノズル内に不活性ガスを流しつつ、溶融金属を回流槽の旋回中心から離れた底面近傍位置で回流槽の接線方向に吐出することにより、溶融金属に遠心力を付与して非金属介在物を回流槽中心に集めると同時に、不活性ガスの気泡を回転中心部に集中させることによって、溶融金属中の非金属介在物をガス気泡に凝集・合体させて非金属介在物を浮上分離するという技術である。   Also known is a technique relating to a tundish that receives molten metal in a circulating tank, horizontally swirls the molten metal, and flows non-metallic inclusions by flowing an inert gas through the circulating tank (for example, patents). Reference 3). This technology for floating and separating non-metallic inclusions introduces molten metal from the inside of a long nozzle having at least one discharge hole with an angle having a horizontal unidirectional component into the circulation tank when the molten metal is received in the circulation tank. In addition, while flowing an inert gas into the long nozzle, the molten metal is discharged in the tangential direction of the circulating tank at a position near the bottom surface away from the swirling center of the circulating tank, thereby imparting centrifugal force to the molten metal and non- At the same time as collecting metal inclusions in the center of the circulation tank, the bubbles of inert gas are concentrated in the center of the rotation, thereby aggregating and coalescing the nonmetallic inclusions in the molten metal into the gas bubbles and floating the nonmetallic inclusions. It is a technique of separation.

特開平05−50193号公報Japanese Patent Laid-Open No. 05-50193 特開平06−597号公報Japanese Patent Laid-Open No. 06-597 特開平07−290210号公報JP 07-290210 A

しかしながら、特許文献1に記載されたCaO系耐火物からなる複数の板に非金属介在物を付着吸収させる溶融金属の清浄化方法においては、長期の連続使用により非金属系介在物のCaO系耐火物で形成された板への付着吸収が累積し、適切な板の間隔を維持できなくなる場合がある。よって、この構成では溶融金属を流す予備経路が確保されていないため、一つの経路を使用することができなくなることにより、操業を停止しなければならないという問題がある。また、この方法は積極的に乱流を発生させるために非金属系介在物の混合が促進され、タンディッシュ内での非金属系介在物の浮上分離の面においては、浮上率の低下をまねくことになる。   However, in the method of cleaning molten metal in which non-metallic inclusions are adhered and absorbed on a plurality of plates made of CaO-based refractories described in Patent Document 1, non-metallic inclusions of CaO-based refractory can be obtained by long-term continuous use. Adhesion absorption to the board formed with a thing accumulates, and it may become impossible to maintain an appropriate board interval. Therefore, in this configuration, since a preliminary path for flowing molten metal is not secured, there is a problem that the operation must be stopped because one path cannot be used. In addition, since this method actively generates turbulent flow, mixing of non-metallic inclusions is promoted, and in terms of floating separation of non-metallic inclusions in the tundish, it leads to a decrease in the floating rate. It will be.

一方、特許文献2に記載された溶融金属を水平旋回させて非金属介在物を浮上分離する技術においては、旋回槽内で発生した溶融金属の流速の旋回成分が浮上槽内まで達し、浮上槽内での溶融金属の流れが乱れることによって、浮上槽内での非金属介在物の浮上が阻害される場合がある。また、浮上槽に設けられた注湯ノズルが複数の場合には、浮上槽内での不均一な流速分布のために、各注湯ノズル出口での溶融金属の流量が不均一となることもある。ならびに、本技術は、移動磁場発生装置が必要であり、コストの増大、装置の複雑化をまねくことも考えられる。   On the other hand, in the technology for horizontally swirling the molten metal described in Patent Document 2 to float and separate non-metallic inclusions, the swirl component of the flow rate of the molten metal generated in the swirl tank reaches the inside of the float tank, and the float tank The flow of molten metal in the inside may be disturbed, and the floating of non-metallic inclusions in the floating tank may be hindered. In addition, when there are a plurality of pouring nozzles provided in the levitation tank, the flow rate of the molten metal at each pouring nozzle outlet may become non-uniform due to the non-uniform flow velocity distribution in the levitation tank. is there. In addition, the present technology requires a moving magnetic field generator, which may increase cost and make the device complicated.

また、特許文献3に記載された溶融金属を水平旋回させるとともに回流槽に不活性ガスを流して非金属介在物を浮上分離する技術においては、特許文献2に記載された技術と同様、回流槽内で発生した溶融金属の流速の旋回成分が整流槽内まで達し、整流槽内での溶融金属の流れが乱れることによって、整流槽内での非金属介在物の浮上が阻害される場合がある。また、整流槽に設けられた注湯ノズルが複数の場合には、整流槽内での不均一な流速分布のために、各注湯ノズル出口での溶融金属の流量が不均一となることもある。ならびに、本技術は、回流槽の旋回中心から離れた位置にロングノズルを配置するため、構造上十分な強度を持たせたロングノズルが必要であり、また、不活性ガスの注入装置も必要となるので、コストの増大、装置の複雑化をまねくことも考えられる。   Further, in the technology for horizontally rotating the molten metal described in Patent Document 3 and flowing the inert gas into the circulation tank to float and separate non-metallic inclusions, as in the technique described in Patent Document 2, the circulation tank The swirl component of the flow rate of the molten metal generated inside reaches the inside of the rectifying tank, and the flow of the molten metal in the rectifying tank is disturbed, which may hinder the rise of nonmetallic inclusions in the rectifying tank. . In addition, when there are a plurality of pouring nozzles provided in the rectifying tank, the flow rate of the molten metal at each pouring nozzle outlet may become non-uniform due to the uneven flow velocity distribution in the rectifying tank. is there. In addition, since the long nozzle is disposed at a position away from the swivel center of the circulation tank in the present technology, a long nozzle having a sufficient structure is required, and an inert gas injection device is also required. Therefore, it can be considered that the cost is increased and the apparatus is complicated.

本発明は、上記実情に鑑みてなされたものであって、その目的は、非金属介在物の浮上分離を促進できるように溶融金属の流れをできるだけ乱さず、かつ簡易な構造のタンディッシュを提供することにある。   The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a tundish having a simple structure without disturbing the flow of molten metal as much as possible so as to promote floating separation of nonmetallic inclusions. There is to do.

課題を解決するための手段及び効果Means and effects for solving the problems

本発明に係るタンディッシュは、取鍋から溶融金属を受容する受容室と、前記溶融金属を鋳型に注湯する注湯室と、前記受容室と前記注湯室とを連通して前記溶融金属を前記受容室から前記注湯室に流すための連通路とを備えたタンディッシュに関する。そして、本発明に係るタンディッシュは、上記目的を達成するために以下のようないくつかの特徴を有している。すなわち、本発明のタンディッシュは、以下の特徴を単独で、若しくは、適宜組み合わせて備えている。   The tundish according to the present invention includes a receiving chamber for receiving molten metal from a ladle, a pouring chamber for pouring the molten metal into a mold, and the molten metal by communicating the receiving chamber and the pouring chamber. It relates to a tundish provided with a communication passage for flowing the water from the receiving chamber to the pouring chamber. The tundish according to the present invention has the following features in order to achieve the above object. That is, the tundish of the present invention has the following features alone or in combination as appropriate.

上記目的を達成するための本発明に係るタンディッシュにおける第1の特徴は、前記連通路は、長手方向を有し複数設けられ、前記連通路が前記注湯室に接続する部分における前記連通路の外周面の接線方向であって、且つ前記連通路の長手方向に沿って前記外周面を延長した複数の延長面が、前記受容室から前記注湯室に向かう方向で互いに交差する交差点又は交差線である少なくとも1つの交差部を有していることである。   The first feature of the tundish according to the present invention for achieving the above object is that the communication passage is provided in a plurality having a longitudinal direction, and the communication passage is in a portion where the communication passage is connected to the pouring chamber. A plurality of extended surfaces extending in the tangential direction of the outer peripheral surface and extending along the longitudinal direction of the communication passage intersect each other in the direction from the receiving chamber toward the pouring chamber. Having at least one intersection that is a line.

この構成によると、連通路が長手方向を有さない場合に比較して、取鍋から受容された溶融金属の連通路内での流速が落とされる効果は大きく、よって、この連通路を経由して注湯室内に導入された溶融金属流の乱れを連通路が長手方向を有さない場合に比較して、溶融金属の流速をより小さくできる。また、さらに連通路が複数設けられることにより、例えば、連通路の総断面積を等しくした場合、連通路が1つの場合に比較して溶融金属の連通路壁への接触総面積が大きくなり圧損抵抗が大きくなるので、連通路が1つの場合に比較して溶融金属の連通路内での流速が落とされる効果は大きく、よって、連通路が長手方向を有し、かつ複数設けられることにより、この連通路を経由して注湯室内に導入される溶融金属流の注湯室内での乱れをより小さくできる。   According to this configuration, compared to the case where the communication path does not have a longitudinal direction, the effect of reducing the flow velocity in the communication path of the molten metal received from the ladle is large. Thus, the molten metal flow rate introduced into the molten metal chamber can be made smaller than the case where the communication path does not have a longitudinal direction. Further, by providing a plurality of communication passages, for example, when the total cross-sectional area of the communication passages is made equal, the total contact area of the molten metal with the communication passage walls becomes larger than in the case of one communication passage, resulting in pressure loss. Since the resistance increases, the effect of reducing the flow velocity of the molten metal in the communication path compared to the case where there is one communication path is large. Therefore, the communication path has a longitudinal direction and a plurality of communication paths are provided. The turbulence in the pouring chamber of the molten metal flow introduced into the pouring chamber via this communication path can be further reduced.

さらに、連通路が複数設けられることにより、例えば、1本の連通路が閉塞した場合でも、残りの連通路を使用することができるので、1本の連通路が閉塞したことによる操業の停止を避けることもできる。また、例えば、特許文献2に記載された移動磁場発生装置や、特許文献3に記載された不活性ガスの注入装置等の追加装置を有さないのでコストも抑えられ、構造も簡易なものとなる。   Furthermore, by providing a plurality of communication paths, for example, even when one communication path is blocked, the remaining communication paths can be used, so that the operation is stopped due to the blockage of one communication path. It can also be avoided. In addition, for example, since there is no additional device such as a moving magnetic field generator described in Patent Document 2 or an inert gas injection device described in Patent Document 3, the cost can be suppressed and the structure can be simplified. Become.

ここで、前記連通路が前記注湯室に接続する部分における前記連通路の外周面の接線方向であって、且つ前記連通路の長手方向に沿って前記外周面を延長した複数の延長面が、前記受容室から前記注湯室に向かう方向で互いに交差する交差点又は交差線である少なくとも1つの交差部を有するとは、複数の連通路を通過して注湯室内に導入された広がりを持って流れる溶融金属流が、注湯室内の壁面に衝突する前に、その流れの少なくとも一部は合流し1つの大きな流れとなることである。これにより、1つの大きな流れとなった溶融金属流は、注湯室内の水平面上で対称な流動を実現する。溶融金属の複数の流れがそれぞれ単独に注湯室内の壁面に衝突して分散し、その後、互いに衝突して干渉しあう場合に比較して、溶融金属の流れの乱れを抑制することができ、よって溶融金属中に存在する非金属介在物の浮上率を高め、非金属介在物の浮上分離を促進できる。   Here, there are a plurality of extension surfaces extending in the tangential direction of the outer peripheral surface of the communication passage at a portion where the communication passage is connected to the pouring chamber, and extending the outer peripheral surface along the longitudinal direction of the communication passage. And having at least one intersection that is an intersection or a crossing line that intersect each other in the direction from the receiving chamber to the pouring chamber has a spread introduced into the pouring chamber through a plurality of communication passages. Before the molten metal flow that flows in this way collides with the wall surface in the pouring chamber, at least a part of the flow merges into one large flow. Thereby, the molten metal flow which became one big flow implement | achieves a symmetrical flow on the horizontal surface in a pouring chamber. Compared to the case where a plurality of flows of molten metal individually collide and disperse against the wall surface of the pouring chamber and then collide with each other and interfere with each other, the turbulence of the flow of molten metal can be suppressed, Therefore, the floating rate of the nonmetallic inclusions present in the molten metal can be increased, and the floating separation of the nonmetallic inclusions can be promoted.

また、本発明に係るタンディッシュにおける第2の特徴は、前記交差部は、複数の前記延長面が、前記受容室から前記注湯室に向かう方向で最初に互いに交差する交差点又は交差線である第1交差部であり、前記第1交差部が、前記注湯室内にあるように、前記連通路が設けられることである。   Further, a second feature of the tundish according to the present invention is that the intersecting portion is an intersection or intersecting line where a plurality of the extension surfaces first intersect with each other in a direction from the receiving chamber toward the pouring chamber. It is a 1st crossing part, and the said communication path is provided so that the said 1st crossing part may exist in the said pouring chamber.

この構成によると、上記第1交差部が注湯室外にある場合に比べて、連通路を通過して注湯室内に導入された広がりを持って流れる溶融金属流が注湯室内の壁面に衝突する前に合流する割合は大きくなる。よって、複数の溶融金属流は、互いに合流してより大きな1つの流れとなる。また、逆に、溶融金属の複数の流れがそれぞれまず単独に注湯室内の壁面に衝突して分散する溶融金属流の割合は小さくなる。よって、複数の単独の溶融金属流が互いに衝突して干渉しあう割合が小さくなる。したがって、溶融金属流の衝突による注湯室内での溶融金属流の乱れを抑制する効果が大きくなる。これにより、溶融金属中に存在する非金属介在物の浮上率を高め、非金属介在物の浮上分離を促進できる。   According to this configuration, compared with the case where the first intersecting portion is outside the pouring chamber, the molten metal flow that flows through the communication path and that is introduced into the pouring chamber collides with the wall surface in the pouring chamber. The rate of merging before it increases. Accordingly, the plurality of molten metal flows merge with each other to form one larger flow. On the contrary, the ratio of the molten metal flow in which the plurality of flows of the molten metal each first impinge on the wall surface in the pouring chamber and disperse becomes small. Therefore, the rate at which a plurality of single molten metal flows collide with each other and interfere with each other is reduced. Therefore, the effect of suppressing the turbulence of the molten metal flow in the pouring chamber due to the collision of the molten metal flow is increased. Thereby, the floating rate of the nonmetallic inclusions present in the molten metal can be increased, and the floating separation of the nonmetallic inclusions can be promoted.

また、本発明に係るタンディッシュにおける第3の特徴は、複数の前記延長面が、前記連通路が前記注湯室に接続する前記注湯室の接続壁面に対向する前記注湯室の対向壁面の法線に対して互いに線対称となるように、前記連通路が設けられることである。   Further, a third feature of the tundish according to the present invention is that the plurality of extending surfaces are opposed to the pouring wall facing the connecting wall of the pouring chamber where the communication path connects to the pouring chamber. The communication path is provided so as to be symmetrical with respect to the normal line.

この構成によると、複数形成される溶融金属の流れを合成した溶融金属流の合成成分は上記対向壁面に対してほぼ直角方向の成分となる。つまり、溶融金属の全体的な流れとして、上記対向壁面に衝突した溶融金属流は上記対向壁面に対してほぼ直角に衝突し、ほぼ均等に周囲に分散していくことになる。ここで、例えば、上記の対向壁面が水平面に対して垂直ではなく受容室から注湯室に向かって斜め上方に傾いて形成されている場合であっても、溶融金属流がこの斜め上方に傾いた対向壁面に衝突後、その多くが対向壁面に沿って上方に流れることなく、ほぼ均等に周囲に分散していく。したがって、このように対向壁面が水平面に対して垂直ではなく受容室から注湯室に向かって斜め上方に傾いて形成されている場合であっても、非金属介在物が浮上、滞留して形成された注湯室内の表面層を攪拌するというような、非金属介在物の除去率の低下を招く流れを抑制することができる。   According to this configuration, the synthesized component of the molten metal flow obtained by synthesizing the plurality of molten metal flows is a component in a direction substantially perpendicular to the opposing wall surface. That is, as the entire flow of the molten metal, the molten metal flow colliding with the opposing wall surface collides with the opposing wall surface at a substantially right angle, and is distributed almost uniformly around the periphery. Here, for example, even when the opposing wall surface is not perpendicular to the horizontal plane but is inclined obliquely upward from the receiving chamber toward the pouring chamber, the molten metal flow is inclined obliquely upward. After colliding with the opposite wall surface, most of them do not flow upward along the opposite wall surface but are distributed almost evenly around. Therefore, even when the opposing wall surface is not perpendicular to the horizontal plane and is inclined obliquely upward from the receiving chamber toward the pouring chamber, the nonmetallic inclusions float and stay. It is possible to suppress a flow that causes a reduction in the removal rate of non-metallic inclusions such as stirring the surface layer in the pouring chamber.

また、本発明に係るタンディッシュにおける第4の特徴は、前記交差部が、前記連通路が前記注湯室に接続する前記注湯室の接続壁面に対して垂直方向に前記注湯室を2等分する垂直対称面上にあるように、前記連通路が設けられることである。   Further, a fourth feature of the tundish according to the present invention is that the intersecting portion has the pouring chamber 2 in a direction perpendicular to a connection wall surface of the pouring chamber where the communication path connects to the pouring chamber. The communication path is provided so as to lie on a vertically symmetric plane that equally divides.

この構成によると、複数の連通路から導入された複数の溶融金属流は、上記注湯室内の水平方向両側に同等の分散スペースが確保されているため、合流後において溶融金属の水平方片側一方への不均一な流れを防止でき、注湯室内の流れの乱れを抑えることができる。よって、溶融金属中に存在する非金属介在物の浮上率を高め、非金属介在物の浮上分離を促進できる。   According to this configuration, since the plurality of molten metal flows introduced from the plurality of communication passages have an equal dispersion space on both sides in the horizontal direction in the pouring chamber, one side of the molten metal on one side of the horizontal side after the merge The uneven flow to the water can be prevented, and the disturbance of the flow in the pouring chamber can be suppressed. Therefore, the floating rate of the nonmetallic inclusions present in the molten metal can be increased, and the floating separation of the nonmetallic inclusions can be promoted.

また、本発明に係るタンディッシュにおける第5の特徴は、前記連通路は、前記連通路が前記注湯室に接続する前記注湯室の接続壁面に対して垂直方向に前記注湯室を2等分する垂直対称面の両側であって対称に設けられることである。   Further, a fifth feature of the tundish according to the present invention is that the communication passage is configured such that the pouring chamber is arranged in a direction perpendicular to a connection wall surface of the pouring chamber connected to the pouring chamber. It is to be provided symmetrically on both sides of a vertically symmetric plane that equally divides.

この構成によると、溶融金属が注湯室に導入される位置で、受容室から注湯室に向かって溶融金属の流れるスペースが左右にほぼ同じスペース確保される。よって、注湯室内での水平方向片側一方への不均一な流れを防止でき、非金属介在物の除去率の低下を抑制することができる。   According to this configuration, at the position where the molten metal is introduced into the pouring chamber, the space through which the molten metal flows from the receiving chamber toward the pouring chamber is ensured to be substantially the same on the left and right. Therefore, a non-uniform flow to one side in the horizontal direction in the pouring chamber can be prevented, and a reduction in the removal rate of nonmetallic inclusions can be suppressed.

また、本発明に係るタンディッシュにおける第6の特徴は、前記連通路は、垂直高さが等しく、かつ水平に設けられることである。   A sixth feature of the tundish according to the present invention is that the communication passages are equal in vertical height and are provided horizontally.

この構成によると、連通路から導入された非金属介在物を含む溶融金属の流れが、注湯室の底面に設けられた注湯出口に直接向かうことを防止でき、非金属介在物を含む溶融金属が最短経路で注湯出口から吐出していくというような、非金属介在物の除去率の低下を抑制することができる。また、非金属介在物が浮上、滞留して形成された注湯室内の表面層に向かう流れも防止でき、この非金属介在物を含む表面層を攪拌するというような、非金属介在物の除去率の低下を招く流れを抑制することができる。   According to this configuration, it is possible to prevent the flow of molten metal including non-metallic inclusions introduced from the communication path from going directly to the pouring outlet provided in the bottom surface of the pouring chamber, and to melt including non-metallic inclusions. It is possible to suppress a decrease in the removal rate of non-metallic inclusions such that the metal is discharged from the pouring outlet through the shortest path. Moreover, the flow toward the surface layer in the pouring chamber formed by non-metallic inclusions floating and staying can be prevented, and the non-metallic inclusions can be removed by stirring the surface layer containing the non-metallic inclusions. A flow that causes a decrease in rate can be suppressed.

また、本発明に係るタンディッシュにおける第7の特徴は、前記注湯室は、底面に前記溶融金属を鋳型に注湯するための複数の注湯出口を有し、複数の前記注湯出口は、前記連通路が前記注湯室に接続する前記注湯室の接続壁面に対して平行な1つの直線上に配置され、前記交差部が、複数の前記注湯出口のうち両端に配置された2つの前記注湯出口から等距離の位置にあるように、前記連通路が設けられることである。   Further, a seventh feature of the tundish according to the present invention is that the pouring chamber has a plurality of pouring outlets for pouring the molten metal into a mold on a bottom surface, and the plural pouring outlets are The communication path is arranged on one straight line parallel to the connecting wall surface of the pouring chamber connected to the pouring chamber, and the intersecting portions are arranged at both ends of the plurality of pouring outlets. The communication path is provided so as to be equidistant from the two pouring outlets.

この構成によると、後段設備の鋳型に注湯される溶融金属の流量をほぼ均一にすることができる。また、給湯出口が複数あるため、例えば、1つの給湯出口以降の設備に清掃等のメンテナンスが必要になった場合でも、残りの給湯出口以降の設備を使用することができるので、設備を完全に停止する必要がなく、生産効率やメンテナンス性にも優れる。   According to this configuration, it is possible to make the flow rate of the molten metal poured into the mold of the subsequent equipment almost uniform. In addition, since there are multiple hot water outlets, for example, when maintenance such as cleaning is required for equipment after one hot water outlet, the equipment after the remaining hot water outlet can be used, so the equipment is completely There is no need to stop, and production efficiency and maintenance are excellent.

以下、本発明を実施するための最良の形態について図面を参照しつつ説明する。本発明に係るタンディッシュは、例えば、製鉄プロセスの連続鋳造に用いるものである。但し、インゴット造塊などのバッチ式の鋳造プロセスでも用いることができる。   Hereinafter, the best mode for carrying out the present invention will be described with reference to the drawings. The tundish according to the present invention is used, for example, for continuous casting in an iron making process. However, it can also be used in batch-type casting processes such as ingot ingot casting.

図1は、本発明の一実施形態に係るタンディッシュ1の縦断面模式図である。本実施形態に係るタンディッシュ1は、取鍋から受容した溶融金属の中に含まれる非金属介在物を浮上分離して除去し、非金属介在物が除去された溶融金属を鋳型に注湯するための鋳造用の容器である。このタンディッシュ1は、取鍋からの溶融金属を受容するための受容ノズル2が設けられこの溶融金属を受容する受容室3と、溶融金属中の非金属介在物を浮上分離し、かつ底面に溶融金属を鋳型に注湯するための注湯出口6が設けられ溶融金属を鋳型に注湯する注湯室5と、受容室3と注湯室5とを連通して溶融金属を受容室3から注湯室5に流すための連通路4とを備える溶解金属の容器である。図1における矢印は、溶融金属の流れ方向を示す。   FIG. 1 is a schematic vertical sectional view of a tundish 1 according to an embodiment of the present invention. The tundish 1 according to this embodiment floats and removes non-metallic inclusions contained in the molten metal received from the ladle, and pours the molten metal from which the non-metallic inclusions are removed into a mold. It is a container for casting. The tundish 1 is provided with a receiving nozzle 2 for receiving the molten metal from the ladle, floats and separates the receiving chamber 3 for receiving the molten metal, and non-metallic inclusions in the molten metal, and on the bottom surface. A pouring outlet 6 for pouring the molten metal into the mold is provided, and the pouring chamber 5 for pouring the molten metal into the mold is communicated with the receiving chamber 3 and the pouring chamber 5 to receive the molten metal. A molten metal container including a communication passage 4 for flowing from the hot water to the pouring chamber 5. The arrows in FIG. 1 indicate the flow direction of the molten metal.

受容室3は、受容ノズル2を介して取鍋からの溶融金属を受容し、連通路4を介して溶融金属を注湯室5に流すためのものであり、受容室3の上部には溶融金属よりも比重が軽いアルミナ系やジルコニア系等の非金属介在物が浮上した非金属介在物層11が形成される。注湯室5は、連通路4を介して溶融金属を受け入れ、注湯出口6を介して溶融金属を後段設備の鋳型に注湯するためのものであり、また、溶融金属の中に含まれる上記非金属介在物を浮上分離し、除去するためのものである。注湯室5の上部には上記の非金属介在物が浮上した非金属介在物層11が形成される。   The receiving chamber 3 is for receiving the molten metal from the ladle through the receiving nozzle 2 and for flowing the molten metal to the pouring chamber 5 through the communication passage 4. A non-metallic inclusion layer 11 is formed in which non-metallic inclusions such as alumina or zirconia having a specific gravity lighter than that of metal are levitated. The pouring chamber 5 is for receiving the molten metal through the communication passage 4 and pouring the molten metal into the mold of the subsequent equipment through the pouring outlet 6 and is included in the molten metal. This is for floating and separating the non-metallic inclusions. A non-metallic inclusion layer 11 in which the non-metallic inclusions are levitated is formed on the top of the pouring chamber 5.

図2は、本発明の一実施形態に係るタンディッシュ1の平断面模式図である。本実施形態に係るタンディッシュ1の連通路4は長手方向を有し、図2に示すように連通路4aと連通路4bとから形成される2本の連通路4を有している。ここで、連通路4は2本に限られることはなく3本等複数設けられていても良い。尚、本実施形態に係る連通路4の流路断面形状は、どちらも円形であるが、連通路4の断面形状は、矩形でも、多角形でも良い。連通路4の断面積は、タンディッシュ1の大きさや鋳込み速度、連通路4の設けられる高さ等によって最適な大きさとするのが望ましい。また、連通路4aが注湯室5に接続する部分AAにおける連通路4aの外周面の接線方向であって、且つ連通路4aの長手方向に沿ってこの外周面を延長した延長面Aと、連通路4bが注湯室5に接続する部分BBにおける連通路4bの外周面の接線方向であって、且つ連通路4bの長手方向に沿ってこの外周面を延長した延長面Bとは、受容室3から注湯室5に向かう方向で最初に互いに交差している。さらに、この交差点αは、注湯室5内に存在し、且つ連通路4が注湯室5に接続する注湯室5の接続壁面に対して垂直方向に注湯室5を2等分する垂直対称面γ上でもある。   FIG. 2 is a schematic plan view of a tundish 1 according to an embodiment of the present invention. The communication path 4 of the tundish 1 according to the present embodiment has a longitudinal direction, and has two communication paths 4 formed of a communication path 4a and a communication path 4b as shown in FIG. Here, the communication path 4 is not limited to two, and a plurality of communication paths 4 such as three may be provided. In addition, although the flow path cross-sectional shape of the communicating path 4 which concerns on this embodiment is both circular, the cross-sectional shape of the communicating path 4 may be a rectangle or a polygon. The cross-sectional area of the communication path 4 is preferably set to an optimum size according to the size of the tundish 1, the casting speed, the height at which the communication path 4 is provided, and the like. Further, an extension surface A extending in the tangential direction of the outer peripheral surface of the communication passage 4a in the portion AA where the communication passage 4a connects to the pouring chamber 5, and extending the outer peripheral surface along the longitudinal direction of the communication passage 4a; An extension surface B that is a tangential direction of the outer peripheral surface of the communication passage 4b in the portion BB where the communication passage 4b is connected to the pouring chamber 5 and that extends the outer peripheral surface along the longitudinal direction of the communication passage 4b. First, they cross each other in the direction from the chamber 3 to the pouring chamber 5. Further, the intersection α is present in the pouring chamber 5 and bisects the pouring chamber 5 in the direction perpendicular to the connecting wall surface of the pouring chamber 5 where the communication passage 4 connects to the pouring chamber 5. It is also on the vertical symmetry plane γ.

尚、上記の連通路4aの外周面を連通路4aの長手方向に沿って延長した延長面Aと、連通路4bの外周面を連通路4bの長手方向に沿って延長した延長面Bとの交差が点となるのは、連通路4a及び連通路4bの断面がいずれも円形であり、よって、延長面A及び延長面Bはいずれも筒状の面となるので、2つの筒状の面が交差する場合、最初は点で交差するからである。ただし、例えば、連通路4a及び連通路4bの断面がいずれも矩形である場合などは、上記の交差は線となる場合もある。   In addition, the extended surface A which extended the outer peripheral surface of said communicating path 4a along the longitudinal direction of the communicating path 4a, and the extended surface B which extended the outer peripheral surface of the communicating path 4b along the longitudinal direction of the communicating path 4b The intersection is a point. Since the cross sections of the communication path 4a and the communication path 4b are both circular, and the extension surface A and the extension surface B are both cylindrical surfaces, the two cylindrical surfaces This is because, at the beginning, they intersect at a point. However, for example, when the cross sections of the communication path 4a and the communication path 4b are both rectangular, the above intersection may be a line.

ここで、交差点αが注湯室5外にある場合に比べて、連通路4a又は連通路4bを通過して注湯室5内に導入された広がりを持って流れる溶融金属流が注湯室5内の壁面に衝突する前に合流する割合は大きくなる。よって、複数の溶融金属流は、互いに合流してより大きな1つの流れとなる。また、逆に、溶融金属の複数の流れがそれぞれまず単独に注湯室5内の壁面に衝突して分散する溶融金属流の割合は小さくなる。よって、複数の単独の溶融金属流が互いに衝突して干渉しあう割合が小さくなる。   Here, as compared with the case where the intersection α is outside the pouring chamber 5, the molten metal flow that flows through the communicating passage 4 a or the communicating passage 4 b and having a spread introduced into the pouring chamber 5 is provided. The ratio of joining before colliding with the wall surface in 5 increases. Accordingly, the plurality of molten metal flows merge with each other to form one larger flow. On the other hand, the ratio of the molten metal flow in which the plurality of flows of molten metal each first impinge on the wall surface in the pouring chamber 5 and disperse becomes small. Therefore, the rate at which a plurality of single molten metal flows collide with each other and interfere with each other is reduced.

さらに、上記垂直対称面γ上で連通路4aからの溶融金属流と、連通路4bからの溶融金属流とが合流するため、合流後の溶融金属流は、垂直対称面γを基準面として対称に分散していく。したがって、溶融金属の流れの乱れをより抑制することができる。   Furthermore, since the molten metal flow from the communication path 4a and the molten metal flow from the communication path 4b merge on the vertical symmetry plane γ, the molten metal flow after merging is symmetric with respect to the vertical symmetry plane γ. Will be dispersed. Therefore, disturbance of the molten metal flow can be further suppressed.

尚、上述する本実施形態において、連通路4aからの溶融金属流と連通路4bからの溶融金属流とは、注湯室5内でほぼ全て合流することになる。ただし、広がりを持って流れる溶融金属流が、注湯室5内の壁面に衝突する前に、その流れの少なくとも一部が合流すれば溶融金属流の乱れを抑制できる。つまり、延長面A及び延長面Bが受容室3から注湯室5に向かう方向で互いに交差すれば良く、交差部は、上記注湯室5内に限られるものではない。   In the above-described embodiment, almost all of the molten metal flow from the communication passage 4 a and the molten metal flow from the communication passage 4 b merge in the pouring chamber 5. However, if at least a part of the flow of the molten metal flow that flows in a wide area joins before the molten metal flow collides with the wall surface in the pouring chamber 5, turbulence of the molten metal flow can be suppressed. That is, the extension surface A and the extension surface B may cross each other in the direction from the receiving chamber 3 toward the pouring chamber 5, and the intersecting portion is not limited to the pouring chamber 5.

また、延長面A及び延長面Bが、連通路4が注湯室5に接続する注湯室5の接続壁面に対向する注湯室5の対向壁面の法線に対して互いに線対称となるように、連通路4が設けられることが好ましい。   Further, the extension surface A and the extension surface B are symmetrical with each other with respect to the normal line of the facing wall surface of the pouring chamber 5 facing the connection wall surface of the pouring chamber 5 where the communication passage 4 connects to the pouring chamber 5. As described above, the communication path 4 is preferably provided.

このように連通路4aと、連通路4bとを配置すると、複数形成される溶融金属の流れを合成した溶融金属流の合成成分は上記対向壁面に対してほぼ直角方向の成分となる。つまり、溶融金属の全体的な流れとして、上記対向壁面に衝突した溶融金属流は上記対向壁面に対してほぼ直角に衝突し、ほぼ均等に周囲に分散していくことになる。ここで、例えば、上記の対向壁面が水平面に対して垂直ではなく受容室3から注湯室5に向かって斜め上方に傾いて形成されている場合であっても、溶融金属流がこの斜め上方に傾いた対向壁面に衝突後、その多くが対向壁面に沿って上方に流れることなく、ほぼ均等に周囲に分散していく。したがって、このように対向壁面が水平面に対して垂直ではなく受容室3から注湯室5に向かって斜め上方に傾いて形成されている場合であっても、非金属介在物が浮上、滞留して形成された注湯室5内の非金属介在物層11を攪拌するというような、非金属介在物の除去率の低下を招く流れを抑制することができる。   When the communication path 4a and the communication path 4b are arranged in this way, a combined component of the molten metal flow obtained by combining a plurality of molten metal flows is a component in a direction substantially perpendicular to the opposing wall surface. That is, as the entire flow of the molten metal, the molten metal flow colliding with the opposing wall surface collides with the opposing wall surface at a substantially right angle, and is distributed almost uniformly around the periphery. Here, for example, even when the facing wall surface is not perpendicular to the horizontal plane but is inclined obliquely upward from the receiving chamber 3 toward the pouring chamber 5, the molten metal flow is obliquely upward. After colliding with the opposing wall surface inclined in the direction, most of it does not flow upward along the opposing wall surface but is distributed almost uniformly around. Therefore, even if the opposing wall surface is not perpendicular to the horizontal plane and is inclined obliquely upward from the receiving chamber 3 toward the pouring chamber 5, non-metallic inclusions float and stay. Thus, it is possible to suppress a flow that causes a reduction in the removal rate of non-metallic inclusions such as stirring the non-metallic inclusion layer 11 in the pouring chamber 5 formed.

また、本実施形態に係るタンディッシュ1の連通路4aと、連通路4bとは、図2に示すように、連通路4が注湯室5に接続する注湯室5の接続壁面に対して垂直方向に注湯室5を2等分する垂直対称面γの両側であって対称に設けられ、また、図1に示すように、どちらも垂直高さが等しく、かつ水平に設けられている。連通路4aと連通路4bとを、このように配置することは、注湯室5内での溶融金属の不均一な流れを防止するために好ましい。しかし、連通路4aと連通路4bとの配置は、これに限られるわけではない。   In addition, the communication path 4 a and the communication path 4 b of the tundish 1 according to the present embodiment are connected to the connection wall surface of the pouring chamber 5 where the communication path 4 connects to the pouring chamber 5 as shown in FIG. 2. Both sides of a vertical symmetry plane γ that bisects the pouring chamber 5 in the vertical direction are provided symmetrically, and as shown in FIG. 1, both have the same vertical height and are provided horizontally. . It is preferable to arrange the communication passage 4 a and the communication passage 4 b in this way in order to prevent a non-uniform flow of molten metal in the pouring chamber 5. However, the arrangement of the communication path 4a and the communication path 4b is not limited to this.

また、注湯室5の底面には、溶融金属を後段設備の鋳型に注湯するための注湯出口6が2つ設けられている。連通路4aと、連通路4bとからの溶融金属流が合流する交差点が、注湯出口6aと、注湯出口6bから等距離の位置になるよう、連通路4aと、連通路4bが設けられている。こうすることにより、注湯出口6aと、注湯出口6bとを介して鋳型に注湯される溶融金属の流量をほぼ均一にすることができる。尚、この注湯出口6は、生産効率やメンテナンス性を考慮して本実施形態のように複数、設けられることが好ましい。ただし、本実施形態のように2つに限られるものでない。   Further, two pouring outlets 6 are provided on the bottom surface of the pouring chamber 5 for pouring molten metal into the mold of the subsequent equipment. The communication path 4a and the communication path 4b are provided so that the intersection where the molten metal flows from the communication path 4a and the communication path 4b join is located at an equal distance from the pouring outlet 6a and the pouring outlet 6b. ing. By carrying out like this, the flow volume of the molten metal poured into a casting_mold | template via the pouring exit 6a and the pouring exit 6b can be made substantially uniform. In addition, it is preferable that a plurality of the pouring outlets 6 are provided as in the present embodiment in consideration of production efficiency and maintainability. However, it is not limited to two like this embodiment.

以下、図1及び図2に示す本発明の一実施形態に係るタンディッシュ1に基づいて行われた溶融金属中に含まれる非金属介在物の浮上分離についての数値解析結果に関して説明する。図3は、受容室3と注湯室5とを連通する連通路4’aと、連通路4’bとを互いに平行に配置し、その他の構成は、上述するタンディッシュ1と同じタンディッシュ30を示す模式図であり、このタンディッシュ30に基づいて行われた数値解析結果を、比較対象として示す。   Hereinafter, the numerical analysis result about the floating separation of the nonmetallic inclusions contained in the molten metal performed based on the tundish 1 according to the embodiment of the present invention shown in FIGS. 1 and 2 will be described. FIG. 3 shows a tundish in which the communication path 4′a and the communication path 4′b communicating with the receiving chamber 3 and the pouring chamber 5 are arranged in parallel to each other, and the other configurations are the same as the tundish 1 described above. 30 is a schematic diagram showing a numerical analysis result based on the tundish 30 as a comparison target.

解析条件は、タンディッシュ1の数値解析も、タンディッシュ30の数値解析も同じ条件とし、100μmの粒子径を有するアルミナ系の非金属介在物粒子の流動解析を実施した。   The analysis conditions were the same for both the numerical analysis of the tundish 1 and the numerical analysis of the tundish 30, and the flow analysis of alumina-based nonmetallic inclusion particles having a particle diameter of 100 μm was performed.

数値解析結果として、本発明の一実施形態に係るタンディッシュ1の解析結果は、浮上粒子の割合が約55%であった。それに対し、2つの連通路が平行に配置されたタンディッシュ30の解析結果は、浮上粒子の割合が約38%であった。よって、タンディッシュ1の解析結果の方が明らかに浮上粒子の割合が高く、つまり浮上分離効率が高くなっている。   As a numerical analysis result, the analysis result of the tundish 1 according to the embodiment of the present invention has a floating particle ratio of about 55%. On the other hand, in the analysis result of the tundish 30 in which the two communication paths are arranged in parallel, the ratio of the floating particles is about 38%. Therefore, the analysis result of the tundish 1 clearly has a higher ratio of floating particles, that is, the floating separation efficiency is high.

以上、本発明の実施形態について説明したが、本発明は上述の実施の形態に限られるものではなく、特許請求の範囲に記載した限りにおいて様々に変更して実施することができるものである。   Although the embodiments of the present invention have been described above, the present invention is not limited to the above-described embodiments, and various modifications can be made as long as they are described in the claims.

例えば、図4は、本発明の他の実施形態に係るタンディッシュ101を示す平断面模式図である。図4に示すタンディッシュ101は、連通路7の形状が上記タンディッシュ1の連通路4と異なる。連通路7aと連通路7bとは、受容室3から注湯室5に向かう方向で最初は互いにほぼ平行となっているが、途中で、連通路7a(7b)が注湯室5に接続する部分AA’(BB’)における連通路7a(7b)の外周面の接線方向に向かうように曲がり、それぞれの延長面A’と延長面B’とは、注湯室5内で交差している(交差点α1)。   For example, FIG. 4 is a schematic plan view showing a tundish 101 according to another embodiment of the present invention. The tundish 101 shown in FIG. 4 is different from the communication path 4 of the tundish 1 in the shape of the communication path 7. The communication passage 7a and the communication passage 7b are initially substantially parallel to each other in the direction from the receiving chamber 3 to the pouring chamber 5, but the communication passage 7a (7b) is connected to the pouring chamber 5 in the middle. The portion AA ′ (BB ′) bends toward the tangential direction of the outer peripheral surface of the communication passage 7 a (7 b), and the extension surface A ′ and the extension surface B ′ intersect in the pouring chamber 5. (Intersection α1).

尚、この交差点α1は、連通路7が注湯室5に接続する注湯室5の接続壁面に対して垂直方向に注湯室5を2等分する垂直対称面γ上でもある。   The intersection α1 is also on a vertical symmetry plane γ that bisects the pouring chamber 5 in the vertical direction with respect to the connecting wall surface of the pouring chamber 5 where the communication passage 7 connects to the pouring chamber 5.

本発明の一実施形態に係るタンディッシュを示す縦断面模式図である。It is a longitudinal cross-sectional schematic diagram which shows the tundish which concerns on one Embodiment of this invention. 本発明の一実施形態に係るタンディッシュを示す平断面模式図である。It is a plane cross-sectional schematic diagram which shows the tundish which concerns on one Embodiment of this invention. 2つの連通路が平行に配置されたことを特徴とする他のタンディッシュを示す平断面模式図である。It is a plane cross-sectional schematic diagram which shows the other tundish characterized by the two communication paths arrange | positioning in parallel. 本発明の他の実施形態に係るタンディッシュを示す平断面模式図である。It is a plane cross-sectional schematic diagram which shows the tundish which concerns on other embodiment of this invention.

符号の説明Explanation of symbols

1 タンディッシュ
2 受容ノズル
3 受容室
4 連通路
5 注湯室
6 注湯出口
11 非金属介在物層
A 連通路4aの外周面の延長面
B 連通路4bの外周面の延長面
α 交差点
γ 注湯室5の垂直対称面
30 連通路が平行な他のタンディッシュ
1 Tundish 2 Receiving nozzle 3 Receiving chamber 4 Communication passage 5 Pouring chamber 6 Pouring outlet 11 Non-metallic inclusion layer A Extension surface of outer peripheral surface of communication passage 4a B Extension surface of outer peripheral surface of communication passage 4b α Intersection γ Note Vertically symmetric surface 30 of hot water chamber 5 Other tundish with parallel passages

Claims (7)

取鍋から溶融金属を受容する受容室と、前記溶融金属を鋳型に注湯する注湯室と、前記受容室と前記注湯室とを連通して前記溶融金属を前記受容室から前記注湯室に流すための連通路とを備えたタンディッシュであって、
前記連通路は、長手方向を有し複数設けられ、
前記連通路が前記注湯室に接続する部分における前記連通路の外周面の接線方向であって、且つ前記連通路の長手方向に沿って前記外周面を延長した複数の延長面が、前記受容室から前記注湯室に向かう方向で互いに交差する交差点又は交差線である少なくとも1つの交差部を有していることを特徴とする、タンディッシュ。
A receiving chamber for receiving molten metal from a ladle, a pouring chamber for pouring the molten metal into a mold, and the receiving chamber and the pouring chamber communicated with each other to allow the molten metal to be poured from the receiving chamber. A tundish with a communication passage for flowing into the chamber,
The communication path has a longitudinal direction and is provided in a plurality.
A plurality of extension surfaces extending in the tangential direction of the outer peripheral surface of the communication passage at a portion where the communication passage connects to the pouring chamber and extending the outer peripheral surface along the longitudinal direction of the communication passage, A tundish characterized by having at least one intersection that is an intersection or an intersection line that intersect each other in a direction from a chamber toward the pouring chamber.
前記交差部は、複数の前記延長面が、前記受容室から前記注湯室に向かう方向で最初に互いに交差する交差点又は交差線である第1交差部であり、
前記第1交差部が、前記注湯室内にあるように、前記連通路が設けられることを特徴とする、請求項1に記載のタンディッシュ。
The intersecting portion is a first intersecting portion in which a plurality of extending surfaces are intersecting points or intersecting lines that first intersect each other in a direction from the receiving chamber toward the pouring chamber,
The tundish according to claim 1, wherein the communication path is provided so that the first intersecting portion is in the pouring chamber.
複数の前記延長面が、前記連通路が前記注湯室に接続する前記注湯室の接続壁面に対向する前記注湯室の対向壁面の法線に対して互いに線対称となるように、前記連通路が設けられることを特徴とする、請求項2に記載のタンディッシュ。   The plurality of extension surfaces are symmetrical with each other with respect to the normal line of the opposing wall surface of the pouring chamber facing the connecting wall surface of the pouring chamber where the communication path is connected to the pouring chamber. The tundish according to claim 2, wherein a communication path is provided. 前記交差部が、前記連通路が前記注湯室に接続する前記注湯室の接続壁面に対して垂直方向に前記注湯室を2等分する垂直対称面上にあるように、前記連通路が設けられることを特徴とする、請求項1乃至請求項3のいずれか1項に記載のタンディッシュ。   The communication path is such that the intersecting portion is on a vertical symmetry plane that bisects the pouring chamber in a direction perpendicular to a connection wall surface of the pouring chamber connected to the pouring chamber. The tundish according to any one of claims 1 to 3, wherein the tundish is provided. 前記連通路は、前記連通路が前記注湯室に接続する前記注湯室の接続壁面に対して垂直方向に前記注湯室を2等分する垂直対称面の両側であって対称に設けられることを特徴とする、請求項1乃至請求項4のいずれか1項に記載のタンディッシュ。   The communication path is provided symmetrically on both sides of a vertical symmetry plane that bisects the pouring chamber in the vertical direction with respect to the connection wall surface of the pouring chamber connected to the pouring chamber. The tundish according to any one of claims 1 to 4, wherein the tundish is characterized. 前記連通路は、垂直高さが等しく、かつ水平に設けられることを特徴とする、請求項1乃至請求項5のいずれか1項に記載のタンディッシュ。   The tundish according to any one of claims 1 to 5, wherein the communication paths have the same vertical height and are provided horizontally. 前記注湯室は、底面に前記溶融金属を鋳型に注湯するための複数の注湯出口を有し、
複数の前記注湯出口は、前記連通路が前記注湯室に接続する前記注湯室の接続壁面に対して平行な1つの直線上に配置され、
前記交差部が、複数の前記注湯出口のうち両端に配置された2つの前記注湯出口から等距離の位置にあるように、前記連通路が設けられることを特徴とする、請求項1乃至請求項6のいずれか1項に記載のタンディッシュ。
The pouring chamber has a plurality of pouring outlets for pouring the molten metal into a mold on the bottom surface,
The plurality of pouring outlets are arranged on one straight line parallel to the connecting wall surface of the pouring chamber where the communication path connects to the pouring chamber.
The communication path is provided so that the intersecting portion is located at an equal distance from two pouring outlets arranged at both ends of the pouring outlets. The tundish according to any one of claims 6 to 7.
JP2006211905A 2006-08-03 2006-08-03 Tundish Expired - Fee Related JP4387385B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017177158A (en) * 2016-03-30 2017-10-05 株式会社神戸製鋼所 Multiple strand tundish for continuous casting
JP2017177159A (en) * 2016-03-30 2017-10-05 株式会社神戸製鋼所 Multiple strand tundish for continuous casting
JP2017177160A (en) * 2016-03-30 2017-10-05 株式会社神戸製鋼所 Multiple strand tundish for continuous casting

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017177158A (en) * 2016-03-30 2017-10-05 株式会社神戸製鋼所 Multiple strand tundish for continuous casting
JP2017177159A (en) * 2016-03-30 2017-10-05 株式会社神戸製鋼所 Multiple strand tundish for continuous casting
JP2017177160A (en) * 2016-03-30 2017-10-05 株式会社神戸製鋼所 Multiple strand tundish for continuous casting

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