JP7109014B2 - Air bubble disperser and impeller - Google Patents

Air bubble disperser and impeller Download PDF

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JP7109014B2
JP7109014B2 JP2022513819A JP2022513819A JP7109014B2 JP 7109014 B2 JP7109014 B2 JP 7109014B2 JP 2022513819 A JP2022513819 A JP 2022513819A JP 2022513819 A JP2022513819 A JP 2022513819A JP 7109014 B2 JP7109014 B2 JP 7109014B2
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impeller
air bubble
blade
molten metal
tip
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JPWO2021205623A1 (en
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藍礼 鈴木
卓也 山本
将也 繁光
諒輔 谷口
保生 石渡
セルゲイ コマロフ
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Tohoku University NUC
Nippon Light Metal Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D1/00Treatment of fused masses in the ladle or the supply runners before casting
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D21/00Casting non-ferrous metals or metallic compounds so far as their metallurgical properties are of importance for the casting procedure; Selection of compositions therefor
    • B22D21/02Casting exceedingly oxidisable non-ferrous metals, e.g. in inert atmosphere
    • B22D21/04Casting aluminium or magnesium
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B21/00Obtaining aluminium
    • C22B21/06Obtaining aluminium refining

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  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
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Description

本発明は、金属溶湯に精製ガスを吹き込む気泡分散装置およびインペラーに関する。 TECHNICAL FIELD The present invention relates to a bubble dispersing device and an impeller for blowing refined gas into molten metal.

アルミニウム又はアルミニウム合金の溶湯には、アルカリ金属,アルミニウムカーバイド,水素ガス,炉材の微粉等の不純物が含まれている。比重の軽い不純物は、溶湯中に塩素,窒素,Arガス等の精製ガスを微細気泡として吹き込むことにより浮上ささて分離する。精製ガス吹込みに際し、溶湯中に渦流を発生させながら精製ガスを吹き込むと、吹き込まれた精製ガスは微細気泡となって溶湯中に効率よく分散し、処理効率を向上させる。 Molten aluminum or aluminum alloy contains impurities such as alkali metals, aluminum carbide, hydrogen gas, and fine powder of furnace materials. Impurities with a low specific gravity are floated and separated by blowing refined gas such as chlorine, nitrogen, or Ar gas into the molten metal as fine bubbles. At the time of blowing the purified gas, if the purified gas is blown into the molten metal while generating a whirlpool, the blown purified gas becomes fine bubbles and is efficiently dispersed in the molten metal, thereby improving the treatment efficiency.

たとえば、特許文献1には、精製ガス用の貫通孔を開け、先端にインペラーを固着した回転軸を備えた気泡分散装置が開示されている。この気泡分散装置によると、インペラーによって溶湯中に渦流が発生する。インペラーの上方には円筒形のスカート部を備えた被覆体が設けられており、インペラーと被覆体の間に浸入した溶湯は、インペラーの回転によって押し出され、溶湯循環流となって溶湯容器内を循環する。精製ガスは、インペラーの底面に設けられた開口部から溶湯中に吹き出され、微細気泡として溶湯循環流に乗って溶湯全体に万遍なく分散される。特許文献1の気泡分散装置では、被覆体のスカート部の下端がインペラーの上面よりも高い位置に形成されている。このような構成とすることで、インペラーと被覆体間に浸入する溶湯量が十分に確保されることで、溶湯循環流が安定化し、溶湯に対する微細気泡の分散性が向上するので、アルミニウム又はアルミニウム合金溶湯を効率よく精製することができる。 For example, Patent Literature 1 discloses a bubble dispersion device provided with a rotary shaft having a through hole for purified gas and an impeller fixed to the tip. According to this air bubble dispersing device, the impeller generates a vortex in the molten metal. A cover with a cylindrical skirt is provided above the impeller, and the molten metal that has entered between the impeller and the cover is pushed out by the rotation of the impeller, forming a circulating flow of molten metal that flows through the container. Circulate. The purified gas is blown out into the molten metal from an opening provided in the bottom surface of the impeller, and is evenly dispersed throughout the molten metal as fine bubbles on the circulating flow of the molten metal. In the bubble dispersion device of Patent Document 1, the lower end of the skirt portion of the cover is formed at a position higher than the upper surface of the impeller. With such a configuration, a sufficient amount of molten metal that enters between the impeller and the coating is ensured, thereby stabilizing the molten metal circulation flow and improving the dispersibility of fine bubbles in the molten metal. It is possible to efficiently refine the molten alloy.

特開2000-309829号公報Japanese Patent Application Laid-Open No. 2000-309829

インペラーの底面の開口部から吹き出された精製ガスは、インペラーの回転により発生する斜め下方への吐出流によって溶湯中に流される。このとき、インペラーの下端部の外周部(羽根の先端部が通過する部分)が、精製ガスの気泡が効率的に分断される分断領域となり、精製ガスが分断領域を通過する際に、細かく分断される。しかしながら、インペラーの羽根の径方向寸法が大きい場合には、精製ガスの一部が、インペラーの中心部寄りで羽根の基端部間の隙間を通過し、分断領域を通過せずに上方に抜けてしまうため、大きな気泡として残ってしまう場合があった。つまり、気泡の分散効率は改善の余地が残されている。 The purified gas blown out from the opening in the bottom surface of the impeller is flowed into the molten metal by the obliquely downward discharge flow generated by the rotation of the impeller. At this time, the outer periphery of the lower end of the impeller (the part through which the tips of the blades pass) becomes a dividing area where the bubbles of the purified gas are efficiently divided. be done. However, when the radial dimension of the impeller blades is large, part of the purified gas passes through the gap between the base ends of the blades near the center of the impeller and escapes upward without passing through the dividing region. As a result, large bubbles may remain. In other words, there is still room for improvement in the bubble dispersion efficiency.

そこで、本発明は上記問題に鑑みてなされたものであり、気泡を効率的に分断できる気泡分散装置およびインペラーを提供することを目的とする。 Accordingly, the present invention has been made in view of the above problems, and an object of the present invention is to provide an air bubble dispersing device and an impeller capable of efficiently dividing air bubbles.

このような課題を解決するための第一の本発明は、金属溶湯に精製ガスを吹き込む気泡分散装置において、前記精製ガスを供給する貫通孔を備えた回転軸と、前記回転軸の下端に取り付けられるインペラーとを備えている。前記インペラーは、前記貫通孔に連通するガス噴出孔を有する中心胴部と、前記インペラーの周方向に等間隔に配置されるとともに前記インペラーの軸方向に対して傾斜した複数の羽根部と、隣り合う前記羽根部間の隙間を覆う気泡誘導部とを備え、前記気泡誘導部の上面は、前記羽根部の基端部寄りが高く、前記羽根部の先端部寄りが低くなるように傾斜していることを特徴とする。 A first invention for solving such problems is a bubble dispersion device for blowing a refined gas into a molten metal, wherein a rotating shaft having a through hole for supplying the refined gas and attached to the lower end of the rotating shaft with an impeller that is The impeller includes a central body portion having gas ejection holes communicating with the through holes, a plurality of blade portions arranged at equal intervals in the circumferential direction of the impeller and inclined with respect to the axial direction of the impeller, and a plurality of blade portions adjacent to each other. and a bubble guiding portion that covers the gap between the blades that are aligned with each other, and the upper surface of the bubble guiding portion is inclined so that the base end side of the blade portion is higher and the tip side of the blade portion is lower. It is characterized by

本発明に係る気泡分散装置によれば、ガス噴出孔から噴出された精製ガスが、気泡誘導部によって羽根部の先端部に流される。羽根部の先端部が通過する気泡の分断領域では、精製ガスの気泡が効率的に分断される。これによって、細かく分断された気泡を溶湯内に効率的に分散させることができる。さらに、インペラーの回転に伴い、溶湯が気泡誘導部の上面に沿って流れて整流されるため、インペラーの外周部から斜め下方に向かって発生する吐出流の吐出量が大きくなる。これによって、溶湯内に循環流が発生し、精製ガスが溶湯の全体に渡って広がる。 According to the air bubble dispersion device of the present invention, the purified gas ejected from the gas ejection holes is caused to flow to the tip portion of the blade portion by the air bubble guide portion. In the bubble dividing region through which the tip of the blade passes, the bubbles of the purified gas are efficiently divided. As a result, finely divided air bubbles can be efficiently dispersed in the molten metal. Further, as the impeller rotates, the molten metal flows along the upper surface of the air bubble guiding portion and is straightened, so that the discharge amount of the discharge flow generated obliquely downward from the outer peripheral portion of the impeller increases. This creates a circulating flow within the melt and the purified gas spreads throughout the melt.

また、本発明に係る気泡分散装置においては、前記気泡誘導部の外側端部は、前記羽根部の先端よりも基端部側に位置しているものが好ましい。このような構成によれば、ガス噴出孔から噴出された精製ガスは、気泡誘導部によって羽根部の先端部の分断領域に流された後、浮上し始め、羽根部の先端部に衝突するので、より一層効率的に分断される。 Further, in the air bubble dispersion device according to the present invention, it is preferable that the outer end of the air bubble guiding portion is positioned closer to the base end than the tip of the blade portion. According to such a configuration, the purified gas ejected from the gas ejection hole is flowed by the air bubble guiding portion to the divided region of the tip portion of the blade portion, and then begins to float and collide with the tip portion of the blade portion. , is more efficiently decoupled.

さらに、本発明に係る気泡分散装置においては、前記気泡誘導部の底面は、前記羽根部の底面と面一であるものが好ましい。このような構成によれば、ガス噴出孔から噴出された精製ガスは、羽根部と気泡誘導部の底面に沿って外周側に円滑に流される。
また、本発明に係る気泡分散装置においては、前記羽根部の側面のうち回転方向前方の側面は、斜め下方を向いて傾斜しているものが好ましい。このような構成によれば、溶湯が羽根部によって下方に付勢され、溶湯容器内に循環流が発生する。
Furthermore, in the air bubble dispersion device according to the present invention, it is preferable that the bottom surface of the air bubble guiding portion is flush with the bottom surface of the blade portion. According to such a configuration, the purified gas ejected from the gas ejection holes smoothly flows to the outer peripheral side along the bottom surfaces of the vane portion and the bubble guide portion.
Further, in the air bubble dispersing device according to the present invention, it is preferable that the side surface of the blade portion, which is forward in the rotation direction, is slanted obliquely downward. With such a configuration, the molten metal is urged downward by the vanes, and a circulating flow is generated in the molten metal container.

前記課題を解決するための第二の本発明は、金属溶湯に精製ガスを吹き込む気泡分散装置に用いられるインペラーである。前記精製ガスを下面から供給するガス噴出孔を有する中心胴部と、前記インペラーの周方向に等間隔に配置されるとともに前記インペラーの軸方向に対して傾斜した複数の羽根部と、隣り合う前記羽根部間の隙間を覆う気泡誘導部とを備え、前記気泡誘導部の上面は、前記羽根部の基端部寄りが高く、前記羽根部の先端部寄りが低くなるように傾斜していることを特徴とする。 A second aspect of the present invention for solving the above-mentioned problems is an impeller used in a bubble dispersing device for blowing refined gas into molten metal. A central body portion having gas ejection holes for supplying the purified gas from the bottom surface, a plurality of blade portions arranged at equal intervals in the circumferential direction of the impeller and inclined with respect to the axial direction of the impeller, and the adjacent and a bubble guiding portion that covers a gap between the blades , and the upper surface of the bubble guiding portion is inclined so that the base end side of the blade portion is higher and the blade tip portion side is lower. characterized by

本発明に係るインペラーを回転軸の下端部に取り付けて、精製ガスを供給しながら溶湯内で回転させると、請求項1に係る発明と同様に、ガス噴出孔から噴出された精製ガスが、気泡誘導部によって羽根部の先端部に流される。羽根部の先端部が通過する気泡の分断領域では、精製ガスの気泡が効率的に分断される。これによって、細かく分断された気泡を溶湯内に効率的に分散させることができる。さらに、インペラーの回転に伴い、溶湯が気泡誘導部の上面に沿って流れて整流されるため、インペラーの外周部から斜め下方に向かって発生する吐出流の吐出量が大きくなる。これによって、溶湯内に循環流が発生し、精製ガスが溶湯の全体に渡って広がる。 When the impeller according to the present invention is attached to the lower end of the rotating shaft and is rotated in the molten metal while supplying the purified gas, the purified gas ejected from the gas ejection holes forms bubbles in the same manner as in the invention according to claim 1. It is flowed to the tips of the blades by the guide section. In the bubble dividing region through which the tip of the blade passes, the bubbles of the purified gas are efficiently divided. As a result, finely divided air bubbles can be efficiently dispersed in the molten metal. Further, as the impeller rotates, the molten metal flows along the upper surface of the air bubble guiding portion and is straightened, so that the discharge amount of the discharge flow generated obliquely downward from the outer peripheral portion of the impeller increases. This creates a circulating flow within the melt and the purified gas spreads throughout the melt.

本発明に係るインペラーにおいては、前記気泡誘導部の外側端部は、前記羽根部の先端よりも基端部側に位置しているものが好ましい。さらに、前記気泡誘導部の底面は、前記羽根部の底面と面一であるものが好ましい。また、前記羽根部の側面のうち回転方向前方の側面は、斜め下方を向いて傾斜しているものが好ましい。このような構成によれば、請求項2乃至に係る発明と同様の作用効果を得られる。
In the impeller according to the present invention, it is preferable that the outer ends of the air bubble guiding portions are positioned closer to the base end than the tips of the blades. Further, it is preferable that the bottom surface of the air bubble guiding portion is flush with the bottom surface of the blade portion. Further, it is preferable that the side surface of the blade portion, which is forward in the rotation direction, is slanted obliquely downward. According to such a configuration, it is possible to obtain the same effects as those of the second to fourth aspects of the invention.

本発明によれば、溶湯内の気泡を効率的に分断することができる。 According to the present invention, bubbles in molten metal can be efficiently divided.

本発明の実施形態に係るインペラーを示した平面図である。It is a top view showing the impeller concerning the embodiment of the present invention. 本発明の実施形態に係るインペラーを示した正面図である。It is a front view showing an impeller according to an embodiment of the present invention. 本発明の実施形態に係るインペラーを示した底面図である。It is a bottom view showing the impeller according to the embodiment of the present invention. 本発明の実施形態に係るインペラーを斜め上方から示した斜視図である。It is the perspective view which showed the impeller which concerns on embodiment of this invention from diagonally upward. 本発明の実施形態に係るインペラーを斜め下方から示した斜視図である。It is the perspective view which showed the impeller which concerns on embodiment of this invention from diagonally downward. 図1AのA-A線断面図である。FIG. 1B is a cross-sectional view taken along line AA of FIG. 1A; 図1AのB-B線断面図である。FIG. 1B is a cross-sectional view taken along line BB of FIG. 1A; 本発明の実施形態に係るインペラーの形状を説明するための斜視図である。It is a perspective view for explaining the shape of the impeller according to the embodiment of the present invention. 本発明の実施形態に係る気泡分散装置を示した分解斜視図である。1 is an exploded perspective view showing an air bubble dispersion device according to an embodiment of the present invention; FIG. 本発明の実施形態に係る気泡分散装置を示した側面図である。1 is a side view showing a bubble dispersion device according to an embodiment of the present invention; FIG. 本発明の実施形態に係る気泡分散装置の使用状態を示した側面図である。It is the side view which showed the use condition of the air-bubble dispersion apparatus which concerns on embodiment of this invention.

本発明の実施形態に係る気泡分散装置およびインペラーについて、図面を参照しながら詳細に説明する。図8に示すように、気泡分散装置1は、金属の溶湯Mに微細気泡として精製ガスを吹き込み、不純物を浮上させ分離する装置である。金属は、例えばアルミニウムまたはアルミニウム合金である。図6および図7にも示すように、本実施形態に係る気泡分散装置1は、回転軸10とインペラー20とを備えている。 A bubble dispersion device and an impeller according to embodiments of the present invention will be described in detail with reference to the drawings. As shown in FIG. 8, the bubble dispersing device 1 is a device for blowing refined gas as fine bubbles into molten metal M to float and separate impurities. The metal is for example aluminum or an aluminum alloy. As also shown in FIGS. 6 and 7, the air bubble dispersion device 1 according to this embodiment includes a rotating shaft 10 and an impeller 20. As shown in FIG.

回転軸10は、金属溶湯による浸食に耐え得る、耐熱性に優れたグラファイト,セラミックス等にて形成されている。回転軸10は、軸方向に延びる貫通孔11を備えている。貫通孔11は、精製ガスを供給するための流路であり、回転軸10の全長に渡って形成されている。回転軸10の下端部には、インペラー20の雌ネジ部25に螺合する雄ネジ部12が形成されている。雄ネジ部12は、回転軸10をインペラー20に対してインペラー20の回転方向に回すとインペラー20の雌ネジ部25に締め付けられる向きになっている。 The rotating shaft 10 is made of graphite, ceramics, or the like, which has excellent heat resistance and can withstand erosion by molten metal. The rotating shaft 10 has a through hole 11 extending in the axial direction. The through-hole 11 is a channel for supplying purified gas, and is formed over the entire length of the rotating shaft 10 . A male threaded portion 12 that is screwed into a female threaded portion 25 of the impeller 20 is formed at the lower end of the rotating shaft 10 . The male threaded portion 12 is oriented to be tightened by the female threaded portion 25 of the impeller 20 when the rotary shaft 10 is rotated with respect to the impeller 20 in the rotational direction of the impeller 20 .

インペラー20は、回転軸10と同じ材質に形成されており、回転軸10の下端に取り付けられる。図1乃至図4に示すように、インペラー20は、中心胴部21と羽根部22と気泡誘導部23とを備えている。中心胴部21は、インペラー20の回転中心に位置し上下方向に延在している。中心胴部21には、貫通孔11に連通するガス噴出孔24が形成されている。ガス噴出孔24は、中心胴部21を上下方向に貫通している。ガス噴出孔24の上端部は、拡径しており、内周面に雌ネジ部25が形成されている。雌ネジ部25には、回転軸10の雄ネジ部12が螺合する。 The impeller 20 is made of the same material as the rotating shaft 10 and attached to the lower end of the rotating shaft 10 . As shown in FIGS. 1 to 4, the impeller 20 includes a central body portion 21, blade portions 22, and air bubble guide portions 23. As shown in FIGS. The central trunk portion 21 is positioned at the center of rotation of the impeller 20 and extends vertically. A gas ejection hole 24 communicating with the through hole 11 is formed in the center body portion 21 . The gas ejection holes 24 vertically penetrate the central body portion 21 . The upper end portion of the gas ejection hole 24 is enlarged in diameter, and a female screw portion 25 is formed on the inner peripheral surface. The male threaded portion 12 of the rotary shaft 10 is screwed into the female threaded portion 25 .

羽根部22は、溶湯Mを攪拌するものであって、中心胴部21の周囲に複数設けられている。羽根部22は、周方向に等間隔に配置され、中心胴部21から外方に向かって放射状に延在している。羽根部22は、上面22aと下面22bがインペラー20の軸部中心に所定角度(本実施形態では30°)オフセットしている。上面22aと下面22bは共に水平である。上面22aと下面22aを繋ぐ先端面22cと両側面22d,22eがそれぞれ傾斜している。先端面22cを正面から見た状態で、先端面22cの幅方向中間部を結ぶ(縦方向に延在する)中心線は、インペラー20の軸方向に対して傾斜している。一方の側面22dは斜め上方を向き、他方の側面22eは斜め下方を向いている。羽根部22の傾斜角(先端面22cの中心線とインペラー20の軸方向との傾斜角)は、溶湯Mに与える推力とインペラー20の回転に必要な駆動力を考慮して、30~60°の範囲であることが好ましい。 The blades 22 stir the molten metal M and are provided in plurality around the central body 21 . The blades 22 are arranged at equal intervals in the circumferential direction and radially extend outward from the central body 21 . The blade portion 22 has an upper surface 22a and a lower surface 22b offset from the center of the shaft portion of the impeller 20 by a predetermined angle (30° in this embodiment). Both the upper surface 22a and the lower surface 22b are horizontal. A tip surface 22c connecting the upper surface 22a and the lower surface 22a and both side surfaces 22d and 22e are inclined. A center line (extending in the vertical direction) connecting the widthwise intermediate portions of the tip end face 22c is inclined with respect to the axial direction of the impeller 20 when the tip end face 22c is viewed from the front. One side surface 22d faces obliquely upward, and the other side surface 22e faces obliquely downward. The angle of inclination of the vanes 22 (the angle of inclination between the center line of the tip surface 22c and the axial direction of the impeller 20) is 30 to 60°, taking into consideration the thrust applied to the molten metal M and the driving force required to rotate the impeller 20. is preferably in the range of

気泡誘導部23は、ガス噴出孔24から噴出された精製ガスを羽根部22の先端部側に誘導する。気泡誘導部23は、周方向に隣り合う羽根部22,22間の隙間を、羽根部22の基端部から先端側に向かって所定長さで覆っている。気泡誘導部23は、6枚の羽根部22,22・・に対応して6か所に設けられている。気泡誘導部23の先端部(外側端部)は、羽根部の先端よりも基端部側に入った部分に位置している。気泡誘導部23の上面は、羽根部22の基端部寄りが高く、羽根部22の先端部寄りが低くなるように傾斜している。気泡誘導部23の基端部の上端は、羽根部22の上面と同じ高さとなっている。気泡誘導部23の底面は、羽根部22の底面と面一になっている。6つの気泡誘導部23,23・・を仮想的に結ぶと円錐台状(図5参照)になる。つまり、インペラー20は、図5に示すように、中心胴部21と羽根部22とを備えた形状に、円錐台23aを組み合わせて成る形状である。 The bubble guiding portion 23 guides the purified gas ejected from the gas ejection hole 24 to the tip portion side of the blade portion 22 . The air bubble guiding portion 23 covers the gap between the blade portions 22, 22 adjacent in the circumferential direction by a predetermined length from the base end portion of the blade portion 22 toward the tip side. The bubble guide portions 23 are provided at six locations corresponding to the six blade portions 22, 22, . . . . The tip (outer end) of the air bubble guiding portion 23 is positioned closer to the base end than the tip of the blade. The upper surface of the air bubble guiding portion 23 is inclined so that the base end side of the blade portion 22 is higher and the tip end portion side of the blade portion 22 is lower. The upper end of the base end portion of the air bubble guiding portion 23 is at the same height as the upper surface of the blade portion 22 . The bottom surface of the bubble guide portion 23 is flush with the bottom surface of the blade portion 22 . Virtually connecting the six bubble guiding portions 23, 23, . . . forms a truncated cone (see FIG. 5). That is, as shown in FIG. 5, the impeller 20 has a shape in which a truncated cone 23a is combined with a shape including a central body portion 21 and blade portions 22. As shown in FIG.

回転軸10にインペラー20を固着するに際し、回転軸10の雄ネジ部12をインペラー20の雌ネジ部25に螺合する。雄ネジ部12のねじ込みに伴って回転軸10の雄ネジ部12の基端部の周囲の面がインペラー20の上面に押し付けられるので、インペラー20は隙間なく回転軸10に密着する。また、雄ネジ部12は、インペラー20が回転すると締まるように形成されているので、運転中にネジが緩むことなく強固にインペラー20と圧着できる。 When fixing the impeller 20 to the rotating shaft 10 , the male threaded portion 12 of the rotating shaft 10 is screwed into the female threaded portion 25 of the impeller 20 . As the male threaded portion 12 is screwed in, the surface around the base end of the male threaded portion 12 of the rotating shaft 10 is pressed against the upper surface of the impeller 20 , so the impeller 20 is in close contact with the rotating shaft 10 without a gap. Further, since the male threaded portion 12 is formed so as to be tightened when the impeller 20 rotates, the impeller 20 can be firmly crimped without loosening during operation.

気泡分散装置1を溶湯容器2に貯められた溶湯Mに浸漬してインペラー20を回転させるとき、羽根部22によって推力が付与された溶湯Mは、溶湯容器2内に送り出される。このとき、溶湯Mは、羽根部22によって下方に付勢されるとともに気泡誘導部23の上面に沿って整流され、インペラー20の外周部の下部から外側斜め下方に向かって送り出される。気泡誘導部23の上面で整流されたことで、送り出される溶湯Mの吐出流の吐出量は大きくなるので、溶湯容器2内に循環流が発生する。 When the air bubble dispersion device 1 is immersed in the molten metal M stored in the molten metal container 2 and the impeller 20 is rotated, the molten metal M to which the impeller 20 is applied with thrust is sent into the molten metal container 2 . At this time, the molten metal M is urged downward by the vanes 22 and rectified along the upper surface of the air bubble guiding portion 23, and is sent out obliquely downward from the lower portion of the outer peripheral portion of the impeller 20. As shown in FIG. Since the discharged flow of the molten metal M is rectified by the upper surface of the air bubble guiding portion 23 , the discharge amount of the discharged molten metal M is increased, so that a circulating flow is generated in the molten metal container 2 .

ガス噴出孔24から噴出された精製ガスの気泡Gは、気泡誘導部23の底部を含むインペラー20の底面によって羽根部22の先端部に流される。羽根部22の先端部は周速が早く、羽根部22の先端角部が気泡をかき切る。つまり、羽根部22の先端部が通過する部分が気泡Gの分断領域となる。分断領域では、精製ガスの気泡Gが効率的に分断されるが、本実施形態では、気泡誘導部23を設けたことで分断領域に気泡Gを誘導するので、気泡Gを効率的に分断させることができる。気泡Gが細かく分断されることで、その表面積が増加し、溶湯Mの脱不純物反応が促進される。 The bubbles G of the purified gas ejected from the gas ejection holes 24 are flowed to the tip portions of the blade portions 22 by the bottom surface of the impeller 20 including the bottom portion of the bubble guide portion 23 . The peripheral speed of the tip of the blade 22 is high, and the corner of the tip of the blade 22 cuts through the air bubbles. That is, the portion through which the tip of the blade portion 22 passes becomes the division region of the air bubble G. As shown in FIG. In the dividing region, the bubbles G of the purified gas are efficiently divided, but in the present embodiment, the bubbles G are guided to the dividing region by providing the bubble guiding portion 23, so that the bubbles G are efficiently divided. be able to. By finely dividing the bubbles G, the surface area thereof increases, and the impurity removal reaction of the molten metal M is promoted.

また、気泡誘導部23の外側端部は、羽根部22の先端よりも基端部側に位置しているので、気泡Gが分断領域に誘導されやすい。具体的には、ガス噴出孔24から噴出された精製ガスの気泡Gの大部分は、気泡誘導部23の底面に沿って気泡誘導部23の外側端部に流された後、浮上し始め、分断領域において羽根部22の先端角部に衝突するので、より一層効率的に分断される。さらに、気泡誘導部23の底面は、羽根部22の底面と面一であるので、気泡Gは、羽根部22と気泡誘導部23の底面に沿って外周側に円滑に流される。 In addition, since the outer end of the air bubble guiding portion 23 is positioned closer to the base end than the tip of the blade portion 22, the air bubbles G are easily guided to the dividing region. Specifically, most of the bubbles G of the purified gas ejected from the gas ejection holes 24 flow along the bottom surface of the bubble guide portion 23 to the outer end of the bubble guide portion 23, and then start to float. Since it collides with the tip corners of the blades 22 in the splitting region, it is split more efficiently. Furthermore, since the bottom surface of the air bubble guiding portion 23 is flush with the bottom surface of the blade portion 22 , the air bubbles G are smoothly flowed along the bottom surfaces of the blade portion 22 and the air bubble guiding portion 23 to the outer peripheral side.

以上のように、分断領域で効率的に分断された気泡Gは、溶湯Mの循環流によって、溶湯Mの全体に渡って分散される。 As described above, the bubbles G efficiently divided in the dividing region are dispersed throughout the molten metal M due to the circulating flow of the molten metal M.

また、本発明に係る気泡分散装置1およびインペラー20においては、気泡誘導部23によって、気泡Gがインペラー20の外周部に誘導されるので、従来のように被覆体を設ける必要がない。したがって、気泡分散装置1の構成部品を減らすことができ、製造コストを軽減することができる。 In addition, in the air bubble dispersion device 1 and the impeller 20 according to the present invention, the air bubble guiding portion 23 guides the air bubbles G to the outer peripheral portion of the impeller 20, so there is no need to provide a cover as in the prior art. Therefore, it is possible to reduce the number of components of the air bubble dispersion device 1 and reduce the manufacturing cost.

以上本発明の実施形態について説明したが、本発明は、その趣旨に反しない範囲において適宜設計変更が可能である。例えば、前記実施形態では、気泡誘導部23の上面の傾斜面は平面状であるが、曲面状としてもよい。このような構成によれば、溶湯Mの流れをより一層円滑にできる場合がある。 Although the embodiments of the present invention have been described above, the present invention can be appropriately modified in design within the scope of the invention. For example, in the above-described embodiment, the inclined surface of the upper surface of the air bubble guiding portion 23 is flat, but it may be curved. With such a configuration, the molten metal M may flow more smoothly.

また、前記実施形態では、気泡誘導部23の底面は、羽根部22の底面と面一であるが、たとえば、気泡誘導部23の底面が一段高くなるように段差を設けてもよい。このような構成によれば、気泡Gを気泡誘導部23の外側端部の羽根部22,22間の隙間に誘導でき、分断効率をより一層高めることができる。 Further, in the above-described embodiment, the bottom surface of the air bubble guiding portion 23 is flush with the bottom surface of the blade portion 22, but for example, a step may be provided so that the bottom surface of the air bubble guiding portion 23 is one step higher. According to such a configuration, the air bubble G can be guided to the gap between the blade portions 22, 22 at the outer end portion of the air bubble guiding portion 23, and the dividing efficiency can be further enhanced.

前記実施形態では、気泡分散装置1は、回転軸10が垂直になるように、溶湯Mに浸漬しているが、これに限定されるものではない。溶湯容器2の形状に応じて、回転軸10が斜めになるように、気泡分散装置1を配置してもよい。このような構成によれば、溶湯Mの循環流が発生しやすくなる場合がある。 In the above embodiment, the air bubble dispersion device 1 is immersed in the molten metal M so that the rotating shaft 10 is vertical, but it is not limited to this. Depending on the shape of the molten metal container 2, the air bubble dispersion device 1 may be arranged so that the rotating shaft 10 is inclined. According to such a configuration, a circulating flow of the molten metal M may easily occur.

1 気泡分散装置
10 回転軸
11 貫通孔
20 インペラー
21 中心胴部
22 羽根部
23 気泡誘導部
24 ガス噴出孔
G 気泡
M 溶湯
REFERENCE SIGNS LIST 1 air bubble dispersing device 10 rotating shaft 11 through hole 20 impeller 21 central body 22 vane 23 air bubble guide 24 gas ejection hole G air bubble M molten metal

Claims (8)

金属溶湯に精製ガスを吹き込む気泡分散装置において、
前記精製ガスを供給する貫通孔を備えた回転軸と、前記回転軸の下端に取り付けられるインペラーとを備え、
前記インペラーは、前記貫通孔に連通するガス噴出孔を有する中心胴部と、前記インペラーの周方向に等間隔に配置されるとともに前記インペラーの軸方向に対して傾斜した複数の羽根部と、隣り合う前記羽根部間の隙間を覆う気泡誘導部とを備え、
前記気泡誘導部の上面は、前記羽根部の基端部寄りが高く、前記羽根部の先端部寄りが低くなるように傾斜している
ことを特徴とする気泡分散装置。
In a bubble dispersion device that blows refined gas into molten metal,
A rotating shaft having a through hole for supplying the purified gas, and an impeller attached to the lower end of the rotating shaft,
The impeller includes a central body portion having gas ejection holes communicating with the through holes, a plurality of blade portions arranged at equal intervals in the circumferential direction of the impeller and inclined with respect to the axial direction of the impeller, and a plurality of blade portions adjacent to each other. and a bubble guiding portion that covers the gap between the matching blades,
The air bubble dispersing device, wherein the upper surface of the air bubble guiding portion is inclined so that the base end side of the blade portion is higher and the tip end portion side of the blade portion is lower.
前記気泡誘導部の外側端部は、前記羽根部の先端よりも基端部側に位置している
ことを特徴とする請求項に記載の気泡分散装置。
2. The air bubble dispersion device according to claim 1 , wherein an outer end portion of the air bubble guide portion is positioned closer to the base end portion than the tip of the blade portion.
前記気泡誘導部の底面は、前記羽根部の底面と面一である
ことを特徴とする請求項1に記載の気泡分散装置。
The air bubble dispersion device according to claim 1, wherein the bottom surface of the air bubble guiding portion is flush with the bottom surface of the blade portion.
前記羽根部の側面のうち回転方向前方の側面は、斜め下方を向いて傾斜している
ことを特徴とする請求項1乃至請求項のいずれか一項に記載の気泡分散装置。
The air bubble dispersing device according to any one of claims 1 to 3 , wherein a side surface of the blade portion that is forward in the rotational direction is slanted downward.
金属溶湯に精製ガスを吹き込む気泡分散装置に用いられるインペラーにおいて、
前記精製ガスを下面から供給するガス噴出孔を有する中心胴部と、前記インペラーの周方向に等間隔に配置されるとともに前記インペラーの軸方向に対して傾斜した複数の羽根部と、隣り合う前記羽根部間の隙間を覆う気泡誘導部とを備え、
前記気泡誘導部の上面は、前記羽根部の基端部寄りが高く、前記羽根部の先端部寄りが低くなるように傾斜している
ことを特徴とするインペラー。
In the impeller used in the bubble dispersion device that blows refined gas into the molten metal,
A central body portion having gas ejection holes for supplying the purified gas from the bottom surface, a plurality of blade portions arranged at equal intervals in the circumferential direction of the impeller and inclined with respect to the axial direction of the impeller, and the adjacent and a bubble guiding portion that covers the gap between the blades,
The impeller, wherein the upper surface of the air bubble guiding portion is inclined so that the base end portion of the blade portion is higher and the tip end portion of the blade portion is lower.
前記気泡誘導部の外側端部は、前記羽根部の先端よりも基端部側に位置している
ことを特徴とする請求項に記載のインペラー。
6. The impeller according to claim 5 , wherein an outer end portion of the air bubble guide portion is positioned closer to the base end portion than the tip of the blade portion.
前記気泡誘導部の底面は、前記羽根部の底面と面一である
ことを特徴とする請求項に記載のインペラー。
The impeller according to claim 5 , wherein the bottom surface of the air bubble guiding portion is flush with the bottom surface of the blade portion.
前記羽根部の側面のうち回転方向前方の側面は、斜め下方を向いて傾斜している
ことを特徴とする請求項乃至請求項のいずれか一項に記載のインペラー。
The impeller according to any one of claims 5 to 7 , wherein a side surface of the blade portion, which is forward in the rotational direction, is inclined obliquely downward.
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JP2004162102A (en) 2002-11-12 2004-06-10 Akechi Ceramics Co Ltd Degassing and cleaning apparatus for molten metal
JP2015089957A (en) 2013-11-06 2015-05-11 三井金属鉱業株式会社 Degassing apparatus, degassing method, agitator for molten metal and method for producing the same
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