JP2008224049A - Rotating body for stirring molten bath - Google Patents

Rotating body for stirring molten bath Download PDF

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JP2008224049A
JP2008224049A JP2007058376A JP2007058376A JP2008224049A JP 2008224049 A JP2008224049 A JP 2008224049A JP 2007058376 A JP2007058376 A JP 2007058376A JP 2007058376 A JP2007058376 A JP 2007058376A JP 2008224049 A JP2008224049 A JP 2008224049A
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gas
rotor
molten metal
rotating body
inert gas
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Masashi Terayama
正志 寺山
Kenichiro Shimizu
健一郎 清水
Shigeyuki Hamayoshi
繁幸 濱吉
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Proterial Ltd
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Hitachi Metals Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a rotating body for stirring molten bath capable of stabilizing a bubble releasing amount to the molten bath, and keeping high fine dispersibility of bubbles, even when dispersion is found in an inert gas supply amount, and preventing change in degassing performance and slag eliminating performance with time. <P>SOLUTION: In this rotating body for stirring molten bath, constituted by fixing a disc-shaped rotor 2 to a lower portion of a hollow pipe-shaped shaft 1 having an inert gas introduction hole 11, the inside of the rotor is provided with a gas storing portion 21 opened at its bottom surface and storing an insert gas, an outer peripheral edge portion of the rotor is provided with groove-shaped recessed portions 22 and projecting portions 23 held between the recessed portions in adjacent to each other, and a plurality of gas jetting ports 24 are formed on the recessed portions in a state of being communicated with the gas storing portion. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、アルミニウム合金等の溶湯中に窒素やアルゴンガスのような不活性ガスを気泡状態に放出して、溶湯中の水素などのガスや酸化物などの不純物を除去する溶湯攪拌用回転体に関する。   The present invention relates to a rotating body for stirring a molten metal that releases inert gas such as nitrogen or argon gas into a molten metal such as an aluminum alloy to remove impurities such as gas such as hydrogen or oxide in the molten metal. About.

アルミニウム合金等の溶湯では、溶湯中の不純物や水素ガスなどを浮遊させて除去するために、溶湯を攪拌しつつ、窒素やアルゴンガスなどの不活性ガスを溶湯中でバブリングさせて、気泡を微細化させるとともに溶湯中に均一に分散させる溶湯攪拌用回転体が用いられている。   In a molten metal such as an aluminum alloy, in order to float and remove impurities and hydrogen gas in the molten metal, bubbles are made fine by bubbling an inert gas such as nitrogen or argon gas in the molten metal while stirring the molten metal. A rotating body for molten metal stirring is used that is made uniform and uniformly dispersed in the molten metal.

例えば特許文献1には、アルミニウム溶湯中に精製用ガスを導入し、かつ溶湯中に設置された回転子を回転させることによって、ガスを溶湯中に微細に分散させて、溶湯を精製する方法において、ガスを溶湯内で回転子の下端に形成されかつ下面が開放されているガス滞留部に一旦滞留させるとともに、回転子を回転させるアルミニウム溶湯の精製処理方法が記載されている。ガス滞留部は上面および側面が壁部材によって密閉され下面が開放されたお椀型すなわち側面下広がりの円錐台状で、壁部材の側面下端に切欠きを設けることが記載されている。   For example, Patent Document 1 discloses a method for purifying a molten metal by introducing a purification gas into a molten aluminum and rotating a rotor installed in the molten metal to finely disperse the gas in the molten metal. In addition, there is described a method for refining molten aluminum in which a gas is temporarily retained in a gas retaining portion formed at the lower end of the rotor in the molten metal and having an open lower surface, and the rotor is rotated. It is described that the gas retaining portion is a bowl shape whose upper surface and side surfaces are sealed by a wall member and whose lower surface is opened, that is, a truncated conical shape spreading under the side surface, and a notch is provided at the lower end of the side surface of the wall member.

特許文献2には、気体供給路を内部に有する垂直回転軸の下端に、気泡微細化分散用回転体を取付け、気体供給路の下端が回転体の底面に開口させられ、回転体の底面に気体供給路の開口部から周縁に至る複数の溝が放射状に設けられ、回転体の周面における各溝の開口の間に、下端部が回転体の底面周縁部に開口した凹所を設けた溶湯攪拌用回転体が記載されている。   In Patent Document 2, a bubble refining and rotating body is attached to the lower end of a vertical rotation shaft having a gas supply path therein, and the lower end of the gas supply path is opened at the bottom surface of the rotating body. A plurality of grooves extending from the opening of the gas supply path to the periphery are provided radially, and a recess having a lower end opened at the periphery of the bottom surface of the rotating body is provided between the openings of the grooves on the peripheral surface of the rotating body. A rotating body for molten metal stirring is described.

特許文献3には、内部に長さ方向に伸びる気体通路を有しておりかつ液体中に配置される垂直回転軸と、回転軸の下端に設けられた気泡放出分散用回転体とより構成されており、液体中に、微細化された気泡状態で気体を放出し、液体全体に分散させる装置において、回転体が、周面に回転軸の気体通路と連なった気体吹出口が円周方向において複数形成されている円板状本体と、円板状本体の周面に取付けられたリング状多孔質体とよりなる気泡放出分散装置が記載されている。   Patent Document 3 includes a vertical rotation shaft that has a gas passage extending in the lengthwise direction and is disposed in a liquid, and a bubble discharge / dispersion rotator provided at the lower end of the rotation shaft. In a device that discharges gas in the form of fine bubbles in the liquid and disperses it throughout the liquid, the rotating body has a gas outlet that is connected to the gas passage of the rotating shaft on the circumferential surface in the circumferential direction. There is described a bubble discharge / dispersion device comprising a plurality of disk-shaped main bodies and a ring-shaped porous body attached to the peripheral surface of the disk-shaped main body.

特開昭58−144438号公報JP 58-144438 A 特公昭61−40737号公報Japanese Patent Publication No. 61-40737 特開平4−308047号公報Japanese Patent Laid-Open No. 4-308047

特許文献1は不活性ガスをお椀型のガス滞留部に蓄えるため、不活性ガスの供給量にばらつきが生じても溶湯への気泡放出量は大きく変動せず良好である。しかしながら、ガス滞留部の下面の開放部から気泡が放出される構造では気泡の微細分散化は十分であるといえない。   In Patent Document 1, since inert gas is stored in a bowl-shaped gas retention part, even if variations in the supply amount of inert gas occur, the amount of bubbles released into the molten metal does not vary greatly, which is good. However, it cannot be said that the fine dispersion of the bubbles is sufficient in the structure in which the bubbles are released from the open portion on the lower surface of the gas retention portion.

特許文献2は垂直回転軸の下端から溶湯中に放出される不活性ガスの気泡を、回転体の底面に設けた放射状溝と底面周縁部に開口した凹所による機械的な剪断作用で微細、分散させる。これは不活性ガスの供給量にばらつきが発生すると、気泡微細分散化能力が低下し、期待される脱ガス性能や除滓性能が得られ難い。   Patent Document 2 discloses that the inert gas bubbles released from the lower end of the vertical rotation shaft into the molten metal are fine by a mechanical shearing action by a radial groove provided in the bottom surface of the rotating body and a recess opened in the peripheral edge of the bottom surface. Disperse. This is because if the supply amount of the inert gas varies, the ability to finely disperse the bubbles decreases, and it is difficult to obtain the expected degassing performance and degassing performance.

特許文献3は長期間の使用により多孔質体の気孔が徐々に塞がり気孔率が低下して、溶湯への不活性ガスの単位時間当たりの供給量が低下する。また不活性ガスが回転体中に設けた細い孔径の気体吹出口を通過することから、不活性ガスの供給量を多くするためには供給圧を高く設定する必要がある。不活性ガスの供給量を多くした場合、多孔質体を通過した後にガスが大きな気泡となって発生し脱ガス性能や除滓性能の低下を招きやすい。   In Patent Document 3, the pores of the porous body are gradually blocked by long-term use, the porosity is lowered, and the supply amount of inert gas per unit time to the molten metal is lowered. Further, since the inert gas passes through the gas outlet having a small hole diameter provided in the rotating body, it is necessary to set the supply pressure high in order to increase the supply amount of the inert gas. When the supply amount of the inert gas is increased, the gas is generated as large bubbles after passing through the porous body, and the degassing performance and the degassing performance are likely to be deteriorated.

本発明は、不活性ガスの供給量にばらつきが生じた場合にも、溶湯への気泡放出量が安定しておりかつ気泡の微細分散化能力が高く維持され、脱ガス性能と除滓性能に経年変化をきたさない溶湯攪拌用回転体を提供することを課題とする。   In the present invention, even when the supply amount of the inert gas varies, the amount of bubbles released to the molten metal is stable, and the ability to finely disperse the bubbles is maintained high. It is an object of the present invention to provide a rotating body for molten metal stirring that does not change over time.

本発明は、不活性ガス導入孔を有する中空管状のシャフトの下部に円盤状のロータを固定した溶湯攪拌用回転体において、ロータの内側に底面が開口してなり不活性ガスが滞留するガス滞留部と、ロータの外周縁部に溝状の凹部と隣り合う凹部同士間に挟まれてなる突起部と、該凹部にガス滞留部と連通する複数のガス噴出口を設けたことを特徴とする。   The present invention relates to a molten metal stirring rotator in which a disc-shaped rotor is fixed to a lower portion of a hollow tubular shaft having an inert gas introduction hole, and a gas retention in which an inert gas is retained by opening a bottom surface inside the rotor. And a plurality of gas jets communicating with the gas retention portion in the concave portion, and a projection portion sandwiched between the groove-shaped concave portion and the adjacent concave portion at the outer peripheral edge portion of the rotor. .

本発明において、前記凹部に設けたガス噴出口に加えて、さらに突起部にガス滞留部と連通する複数のガス噴出口を設けたことを特徴とする。また前記凹部に形成したガス噴出口および突起部に形成したガス噴出口が丸孔またはスリットの形状に形成されてなることを特徴とする。   In the present invention, in addition to the gas jet port provided in the concave portion, a plurality of gas jet ports communicating with the gas retention portion are further provided in the protrusion. Further, the gas jet port formed in the recess and the gas jet port formed in the projection are formed in the shape of a round hole or a slit.

前記凹部および突起部にガス噴出口を形成した場合、凹部に設けた複数のガス噴出口の開口面積の総和が、突起部に設けた複数のガス噴出口の開口面積の総和より大きいことを特徴とする。前記ロータの開口した底面部の下端に逆凹状の切欠き部を設けたことを特徴とする。   When gas outlets are formed in the recess and the protrusion, the sum of the opening areas of the plurality of gas outlets provided in the recess is larger than the sum of the opening areas of the plurality of gas outlets provided in the protrusion. And A reverse concave notch is provided at the lower end of the open bottom of the rotor.

前記凹部に、または凹部および突起部にガス噴出口が丸孔で形成されている場合、その丸孔の最大直径が前記シャフトの不活性ガス導入孔の最小直径より小さいことを特徴とする。また、前記凹部に、または凹部および突起部にガス噴出口がスリットで形成されている場合、そのスリットの最大幅寸法が5mm以下であることを特徴とする。さらに、前記ロータの最大高さ寸法が、ロータの最大外径の1/4〜1/2の範囲内であることを特徴とする。   In the case where the gas outlet is formed as a round hole in the recess or in the recess and the protrusion, the maximum diameter of the round hole is smaller than the minimum diameter of the inert gas introduction hole of the shaft. Moreover, when the gas ejection port is formed in the said recessed part or the recessed part and the projection part with the slit, the maximum width dimension of the slit is 5 mm or less, It is characterized by the above-mentioned. Furthermore, the maximum height dimension of the rotor is within a range of 1/4 to 1/2 of the maximum outer diameter of the rotor.

本発明は、ロータの内側に底面が開口し不活性ガスが滞留するガス滞留部を設け、これに不活性ガス導入孔から供給される不活性ガスを一旦蓄える。この蓄えられた不活性ガスが、ロータの外周縁部の溝状の凹部、または溝状の凹部と隣り合う凹部同士間に挟まれてなる突起部に設けたガス滞留部と連通する小さい開口面積の複数のガス噴出口を通して溶湯内に小さな気泡として微細化して分散放出される。この構成により、不活性ガスの供給量にばらつきが生じた場合でも、ガス滞留部があるため安定しており、溶湯内へ微細化した気泡を確実に分散させることができる。   In the present invention, a gas retention portion in which the bottom surface is opened inside the rotor and the inert gas is retained is provided, and the inert gas supplied from the inert gas introduction hole is temporarily stored therein. A small opening area through which the stored inert gas communicates with a groove-like recess in the outer peripheral edge of the rotor, or a gas retention part provided in a protrusion sandwiched between adjacent recesses. The gas is finely dispersed as small bubbles into the molten metal through a plurality of gas outlets. With this configuration, even when the supply amount of the inert gas varies, there is a gas retention portion, which is stable, and the finely divided bubbles can be reliably dispersed in the molten metal.

ガス噴出口から放出される不活性ガスの小さな気泡は、ロータの外周縁部に設けた溝状の凹部や突起部で剪断され更に微細化される。剪断作用による微細化を最大限に発揮させるために、ガス噴出口は奥行の三面を壁面に囲まれた凹部に設けることが好ましい。不活性ガスの供給量と各ガス噴出口の開口面積を総和した面積のバランスを考慮して、ガス噴出口から出るガス量が足りずロータ底面の開口部から大きな気泡となって溶湯内に漏れ出ることが想定される場合、ロータの凹部以外に突起部にもガス噴出口を設ける。凹部と突起部の両者にガス噴出口を設ける場合、ロータの外周縁部の凹部に設けた複数のガス噴出口の開口面積の総和が、突起部に設けた複数のガス噴出口の開口面積の総和より大きくすることにより、剪断作用効果が大きくなるので好ましい。   The small bubbles of the inert gas discharged from the gas outlet are sheared and further refined by a groove-like recess or protrusion provided in the outer peripheral edge of the rotor. In order to maximize the miniaturization due to the shearing action, it is preferable to provide the gas outlet in a recess surrounded by three wall surfaces in the depth. Considering the balance between the amount of inert gas supplied and the total area of the gas outlets, the amount of gas coming out of the gas outlets is insufficient and leaks into the melt as large bubbles from the opening at the bottom of the rotor. In the case where it is assumed that the gas jetting exits, a gas ejection port is provided in the protrusion in addition to the recess of the rotor. When providing gas outlets in both the recesses and the protrusions, the sum of the opening areas of the gas outlets provided in the recesses on the outer peripheral edge of the rotor is equal to the opening area of the gas outlets provided in the protrusions. By making it larger than the total, the shearing effect is increased, which is preferable.

また仮に不活性ガスがロータ底面の開口部から大きな気泡となって溶湯内に漏れ出た場合でも、脱ガス性能や除滓性能を大きく低下させないために、ロータの底面部の下端に逆凹状の切欠き部を複数設ける。この切欠き部による溶湯の剪断作用で、ロータ底面の開口部から出る比較的大きな気泡の微細、分散化ができる。   In addition, even if the inert gas leaks into the molten metal as a large bubble from the opening at the bottom of the rotor, a reverse concave shape is formed at the lower end of the bottom of the rotor so as not to greatly reduce the degassing performance or the degassing performance. Provide multiple notches. By the shearing action of the molten metal by this notch, relatively large bubbles coming out from the opening at the bottom of the rotor can be made fine and dispersed.

ガス噴出口が丸孔に形成されてなる場合、その丸孔の最大直径が前記シャフトの不活性ガス導入孔の最小直径より小さいこと、またガス噴出口がスリットで形成されてなる場合、そのスリットの最大幅寸法が5mm以下であるのが気泡の微細分散のために好ましい。また、ロータの最大高さ寸法が、ロータの最大外径の1/4〜1/2の範囲内であるのが構造上好ましい。   When the gas outlet is formed in a round hole, the maximum diameter of the round hole is smaller than the minimum diameter of the inert gas introduction hole of the shaft, and when the gas outlet is formed with a slit, the slit The maximum width dimension of 5 mm or less is preferable for fine dispersion of bubbles. Further, the maximum height dimension of the rotor is preferably in the range of 1/4 to 1/2 of the maximum outer diameter of the rotor.

また脱ガス性能と除滓性能を安定的に発揮させるために、溶湯攪拌用回転体の構成部材であるロータおよびシャフトを溶湯中でも形状変化が起きないセラミックスで形成するのが望ましい。なかでも窒化ケイ素、サイアロンが好ましい。   In order to stably exhibit the degassing performance and the degassing performance, it is desirable to form the rotor and the shaft, which are constituent members of the molten metal stirring rotor, with ceramics that do not change its shape even during the molten metal. Of these, silicon nitride and sialon are preferred.

図1は本発明の溶湯攪拌用回転体の実施例を示す一部断面図である。図2は図1のロータの平面図である。本発明実施例の溶湯攪拌用回転体は、中空管状のセラミックス製シャフト1の下部に、円盤状のセラミックス製ロータ2を螺合固定して構成される。   FIG. 1 is a partial cross-sectional view showing an embodiment of a rotating body for molten metal stirring according to the present invention. FIG. 2 is a plan view of the rotor of FIG. The rotating body for molten metal stirring according to the embodiment of the present invention is configured by screwing and fixing a disk-shaped ceramic rotor 2 to a lower portion of a hollow tubular ceramic shaft 1.

シャフト1は、窒化ケイ素を主成分とする焼結体からなり、その内部に窒素やアルゴンガスなどの不活性ガスを供給するための中空の不活性ガス導入孔11を有する。不活性ガス導入孔11の下端の開口部を経てロータ2のガス滞留部21の空間内に不活性ガスが供給される。シャフト1の下部にロータ2と接合するための雄ねじ部を形成する。窒化ケイ素を主成分とする焼結体は、相対密度99.4%、常温における熱伝導率55W/(m・K)、常温における4点曲げ強度905MPaである。   The shaft 1 is made of a sintered body mainly composed of silicon nitride, and has a hollow inert gas introduction hole 11 for supplying an inert gas such as nitrogen or argon gas therein. The inert gas is supplied into the space of the gas retention portion 21 of the rotor 2 through the opening at the lower end of the inert gas introduction hole 11. A male screw portion for joining to the rotor 2 is formed in the lower portion of the shaft 1. The sintered body mainly composed of silicon nitride has a relative density of 99.4%, a thermal conductivity at room temperature of 55 W / (m · K), and a four-point bending strength at room temperature of 905 MPa.

ロータ2は、シャフト1同様に窒化ケイ素を主成分とする焼結体からなり、ロータ2の上面の中央孔部12にシャフト1と接合するための雌ねじ部13を形成する。ロータ2の内側に底面が開口した逆凹状の不活性ガスが滞留する空間であるガス滞留部21を形成する。ロータ2の外周縁部に溝状の凹部22と、隣り合うこれら凹部22同士間に挟まれて半径方向に突出してなる突起部23を円周方向45度間隔毎に8個設けた。   Like the shaft 1, the rotor 2 is made of a sintered body containing silicon nitride as a main component, and a female screw portion 13 for joining the shaft 1 is formed in the central hole portion 12 on the upper surface of the rotor 2. A gas retention portion 21, which is a space in which a reverse concave inert gas whose bottom surface is opened, is retained inside the rotor 2. On the outer peripheral edge of the rotor 2, groove-like recesses 22 and eight protrusions 23 sandwiched between the adjacent recesses 22 and projecting in the radial direction are provided every 45 degrees in the circumferential direction.

ロータ2の凹部22に、ガス滞留部21と連通する直径5mmの丸孔のガス噴出口24を穿孔した。凹部22一箇所あたりガス噴出口24を5個づつ設けた。また、ロータ2の突出部23に、ガス滞留部21と連通する直径5mmの丸孔のガス噴出口25を穿孔した。突出部23一箇所あたりガス噴出口25を3個づつ設けた。   A gas outlet 24 having a round hole with a diameter of 5 mm communicating with the gas retention part 21 was drilled in the recess 22 of the rotor 2. Five gas outlets 24 were provided for each recess 22. Further, a round gas outlet 25 having a diameter of 5 mm communicating with the gas retention part 21 was drilled in the protruding part 23 of the rotor 2. Three gas outlets 25 were provided for each protrusion 23.

ロータ2の開口した底面部26の下端に逆凹状の切欠き部27を設けた。底面部26は凹部22および突出部23の底面で構成されるが、切欠き部27は凹部22の底面に設けた。   A reverse concave cutout 27 is provided at the lower end of the open bottom surface 26 of the rotor 2. The bottom surface portion 26 is constituted by the bottom surface of the concave portion 22 and the protruding portion 23, but the notch portion 27 is provided on the bottom surface of the concave portion 22.

ロータ2の最大高さ(ロータの最底面から最上面までの寸法)が96mm、ロータ2の最大外径(対向する突起部の先端間の長さ)が240mmである。ガス噴出口24およびガス噴出口25の丸孔の最大直径5mmは、シャフト1の不活性ガス導入孔11の最小直径50mmより小さくした。また、凹部22に設けたガス噴出口24の開口面積を総和した面積は、突起部23に設けたガス噴出口25の開口面積を総和した面積に比べて大きくした。   The maximum height of the rotor 2 (dimension from the bottom surface to the top surface of the rotor) is 96 mm, and the maximum outer diameter of the rotor 2 (the length between the tips of the opposing protrusions) is 240 mm. The maximum diameter 5 mm of the round holes of the gas outlet 24 and the gas outlet 25 was made smaller than the minimum diameter 50 mm of the inert gas introduction hole 11 of the shaft 1. Further, the total area of the opening areas of the gas outlets 24 provided in the recesses 22 was made larger than the total area of the opening areas of the gas outlets 25 provided in the protrusions 23.

このように構成した本発明実施例の溶湯攪拌用回転体を680℃のアルミニウム溶湯中に浸漬し、シャフトを駆動装置によって高速回転させるとともに、不活性ガス導入孔から不活性ガスを供給して、溶湯中の不純物などを浮遊させるための回転攪拌に供したところ、気泡の微細化分散効果が十分に得られた。また、不活性ガスの供給量にばらつきが生じた場合にも、溶湯への気泡放出量が安定しておりかつ気泡の微細分散化能力が高く維持されることが確認できた。   The molten metal stirring rotator according to the embodiment of the present invention thus configured is immersed in molten aluminum at 680 ° C., the shaft is rotated at a high speed by a driving device, and an inert gas is supplied from an inert gas introduction hole. When subjected to rotary stirring for floating impurities in the molten metal, the effect of finely dispersing bubbles was sufficiently obtained. It was also confirmed that the amount of bubbles released to the molten metal was stable and the ability to finely disperse the bubbles was maintained even when the supply amount of the inert gas varied.

本発明の溶湯攪拌用回転体によれば、不活性ガスの供給量にばらつきが生じた場合にも、溶湯への気泡放出量が安定しておりかつ気泡の微細分散化能力が高く維持され、脱ガス性能と除滓性能に経年変化をきたさない。   According to the molten metal stirring rotator of the present invention, even when the amount of inert gas supplied varies, the amount of bubbles released to the molten metal is stable and the ability to finely disperse the bubbles is maintained high. There is no secular change in degassing performance and removal performance.

本発明の溶湯攪拌用回転体の実施例を示す一部断面図である。It is a partial cross section figure which shows the Example of the rotary body for molten metal stirring of this invention. 図1のロータの平面図である。It is a top view of the rotor of FIG.

符号の説明Explanation of symbols

1 シャフト、 2 ロータ、 11 不活性ガス導入孔、 12 中央孔部、
13 ねじ部、 21 ガス滞留部、 22 凹部、 23 突起部、
24 ガス噴出口、 25 ガス噴出口、 26 底面部、 27 切欠き部
1 shaft, 2 rotor, 11 inert gas introduction hole, 12 central hole,
13 thread part, 21 gas retention part, 22 recessed part, 23 protrusion part,
24 gas outlet, 25 gas outlet, 26 bottom face, 27 notch

Claims (8)

不活性ガス導入孔を有する中空管状のシャフトの下部に円盤状のロータを固定した溶湯攪拌用回転体において、ロータの内側に底面が開口してなり不活性ガスが滞留するガス滞留部と、ロータの外周縁部に溝状の凹部と隣り合う凹部同士間に挟まれてなる突起部と、該凹部にガス滞留部と連通する複数のガス噴出口を設けたことを特徴とする溶湯攪拌用回転体。 In a rotating body for molten metal stirring in which a disk-shaped rotor is fixed to a lower part of a hollow tubular shaft having an inert gas introduction hole, a gas retaining portion in which a bottom surface is opened inside the rotor and inert gas is retained, and the rotor Rotation for molten metal agitation characterized in that a groove-shaped recess and a protrusion sandwiched between adjacent recesses are provided on the outer peripheral edge of the gas and a plurality of gas jets communicating with the gas retention portion are provided in the recess. body. 前記突起部にガス滞留部と連通する複数のガス噴出口を設けたことを特徴とする請求項1に記載の溶湯攪拌用回転体。 The rotating body for molten metal stirring according to claim 1, wherein a plurality of gas outlets communicating with the gas retention portion are provided in the protrusion. 前記ガス噴出口が丸孔またはスリットの形状に形成されてなることを特徴とする請求項1または2に記載の溶湯攪拌用回転体。 3. The molten metal agitating rotator according to claim 1, wherein the gas outlet is formed in the shape of a round hole or a slit. 前記凹部に設けた複数のガス噴出口の開口面積の総和が、前記突起部に設けた複数のガス噴出口の開口面積の総和より大きいことを特徴とする請求項2に記載の溶湯攪拌用回転体。 The rotation for melt stirring according to claim 2, wherein the sum of the opening areas of the plurality of gas jets provided in the recess is larger than the sum of the opening areas of the gas jets provided in the protrusion. body. 前記ロータの開口した底面部の下端に逆凹状の切欠き部を設けたことを特徴とする請求項1〜4のいずれかに記載の溶湯攪拌用回転体。 The rotating body for molten metal stirring according to any one of claims 1 to 4, wherein a reverse concave cutout is provided at the lower end of the bottom surface of the rotor. 前記ガス噴出口が丸孔で形成されてなり、その丸孔の最大直径が前記シャフトの不活性ガス導入孔の最小直径より小さいことを特徴とする請求項1、2、4、5のいずれかに記載の溶湯攪拌用回転体。 6. The gas jet nozzle according to claim 1, wherein the gas outlet is formed by a round hole, and the maximum diameter of the round hole is smaller than the minimum diameter of the inert gas introduction hole of the shaft. The rotating body for molten metal stirring described in 1. 前記ガス噴出口がスリットで形成されてなり、そのスリットの最大幅寸法が5mm以下であることを特徴とする請求項1、2、4、5のいずれかに記載の溶湯攪拌用回転体。 The molten metal stirring rotator according to any one of claims 1, 2, 4, and 5, wherein the gas ejection port is formed by a slit, and the maximum width of the slit is 5 mm or less. 前記ロータの最大高さ寸法が、ロータの最大外径の1/4〜1/2の範囲内であることを特徴とする請求項1に記載の溶湯攪拌用回転体。 2. The molten metal agitating rotor according to claim 1, wherein the maximum height of the rotor is within a range of [1/4] to [1/2] of the maximum outer diameter of the rotor.
JP2007058376A 2007-03-08 2007-03-08 Rotating body for stirring molten bath Pending JP2008224049A (en)

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