JP4123740B2 - Molten metal processing equipment - Google Patents
Molten metal processing equipment Download PDFInfo
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- JP4123740B2 JP4123740B2 JP2001191057A JP2001191057A JP4123740B2 JP 4123740 B2 JP4123740 B2 JP 4123740B2 JP 2001191057 A JP2001191057 A JP 2001191057A JP 2001191057 A JP2001191057 A JP 2001191057A JP 4123740 B2 JP4123740 B2 JP 4123740B2
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- molten metal
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【0001】
【産業上の利用分野】
本発明は、溶融金属中の溶存ガスや非金属介在物粒子を不活性ガスなどの吹き込みにより除去する装置に関する。
【0002】
【従来の技術】
溶融金属中に含まれる溶存ガスや介在物は、欠陥の原因となるので、鋳造の前に溶融金属中の溶存ガスや介在物の除去が行われる。
例えば、アルミニウムあるいはアルミニウム合金を鋳造する場合、溶融金属中に含有されている水素ガスや、酸化物等の非金属介在物を除去するために、不活性ガスなどを吹き込んで、不活性ガス等の気泡に溶存ガスや非金属介在物を付着させることによって、溶存ガスや非金属介在物を除去する溶湯処理が行われている。特に近年の要求鋳造品質の向上に伴い、従来問題とされなかったレベルの含有ガスおよび非金属介在物の除去が必要とされるようになってきている。
【0003】
溶存ガスや非金属介在物の除去を効率的に行うためには、気泡の表面積を大きくする必要がある。気泡の表面積をできるだけ大きくするためには、気泡をできるだけ細かく分散させることが必要である。
従来の溶湯処理装置は、溶湯保持槽内に配置され内部に軸方向に伸びる気体通気路を有する垂直回転軸と、この垂直回転軸の先端に設けられ、かつ底面あるいは側面に前記気体通気路とつながった気体吹き出し口が設けられた回転体からなるものである。溶融金属中に注入された気泡を細かく分散させるために、上記回転体の形状を工夫したり、回転軸の回転数をより高めたりしている。
【0004】
【発明が解決しようとする課題】
しかし、回転軸を高速に回転させると、溶融金属に回転軸を中心に渦が発生し、溶融金属表面に浮上した溶存ガスや非金属介在物が巻き込まれてしまうため、軸の回転数を過度に高めることはできない。
溶融金属に渦を発生させない方法として、溶融金属処理槽の側壁等に邪魔板を設ける方法もあるが、邪魔板を設けると吹き込まれた気泡が溶融金属に行き渡らない部分ができてしまう。また、邪魔板と溶融金属の旋回流が衝突し、溶融金属表面が波うってしまい表面酸化の量が増えるという弊害がある。
本発明は、このような問題を解消すべく案出されたものであり、回転体を高速に回転させても渦が発生することがない溶融金属処理装置を提供することを目的とする。
【0005】
【課題を解決するための手段】
本発明の溶融金属処理装置は、その目的を達成するため、金属溶湯保持槽と、この溶湯保持槽内に配置され内部に軸方向に伸びる気体通気路を有する垂直回転軸と、この垂直回転軸の先端に設けられ、かつ底面または側面のいずれかまたは双方に前記気体通気路と連なった気体吹出口が設けられた回転体と、前記垂直回転軸を覆うとともにこの回転軸先端の前記回転体をも覆う非回転の旋回流発生防止カバーを備えたものである。
【0006】
【模擬実験】
まず、水素ガスおよび非金属介在物の除去効果を阻害するプロセスを知り、非回転の旋回流発生防止カバーの渦発生防止効果を知るために、アルミニウム溶湯の代わりに観察が容易な水モデルを採用した。
溶融金属槽2に模した、内径700mmの透明塩ビ製の処理槽に深さが700mmになるように水を入れて実験を行った。なお、酸化皮膜に擬して水と同程度の比重を有する微小プラスチック系樹脂片(5×10×1mm)6を水中に混入させておいた。
【0007】
気泡発生のために、黒鉛製の外径75mmの回転軸3と、その下端に外径が230mmで厚さが60mmの回転羽根が一体化した回転体4を使用した。なお、この回転軸4の中央部には中空(内径10mm)の不活性ガス進入孔が軸方向に貫通されており、回転羽根の下面には、その外周に向けて幅30mmで深さ10mmの加工溝が中心より外周に向けて6箇所で放射状に設けられている。
このような回転体4を、回転軸部が500mm、回転羽根部が50mm、全体で550mmになる深さで水中に浸漬し、回転数を変えつつ、Arガス量を20L/分で一定にして吹き込み、渦流の発生状況および水の挙動を観察した。
【0008】
旋回流発生防止カバーは、内径80mm、外径100mmで浸漬深さを可変できる透明塩ビ製の丸パイプ状の本体部分と、必要に応じて回転羽根を覆う同じく塩ビ製の付け足しカバー部分からなるもので、取り付けは、処理装置本体の非回転部に固定する。
【0009】
旋回流発生防止カバーの取り付け深さを変え、回転体4の回転速度0から500rpm間で変動させて、上記渦流の発生状況および水の挙動を観察した。
回転数と渦流の関係を図3に示す。なお、図中、(a)は旋回流発生防止カバーなしの従来法、(b)は水面から50mmの位置まで覆ったもの、(c)、(d)は同じく200mm、500mmまで覆ったもの、さらに(e)は回転体4まで覆ったものである。
【0010】
図からもわかるように、回転軸の湯面付近に形成される渦流の深さは、ほぼ回転数に比例して増大している。ただし、従来法の場合では、例えば500rpm時の渦流深さが20mmであったのに対し、旋回流発生防止カバーを設けた本発明法では、各実験例とも5mm以下になっており、大幅な発生防止効果が確認された。
また、その際、この旋回流発生防止カバーは、浸漬深さが深いほど効果があり、特に気泡を発生する回転体まで覆う場合に顕著な効果が得られている。
【0011】
従来法の場合は、気泡に付着した酸化皮膜に仮定した疑似介在物は水と同調し旋回した後、一旦は浮上するものの、その後は回転軸の水面付近に発生した渦流に巻き込まれ、再度、水中に戻される様子が確認された。
これに対して、旋回流発生防止カバーを使用して、渦流をほとんど発生させない本発明方法の場合では、旋回流や渦流等の水の流動は該旋回流発生防止カバー内に留められ、カバーの外の処理槽内にある水のほとんどは流動することがなかった。
回転体4から吹き出されたガスが乱流となって微細気泡と擦れあいながら疑似介在物と付着し浮上していくことが観察された。
なお、当然ではあるが、一旦浮上した疑似介在物のプラスチック片が再び水中に還流されることは観察されなかった。
【0012】
【実施例】
実施例1
上記水モデル実験で得られた知見を基に、溶融アルミニウム合金中の水素ガスおよび酸化皮膜の除去を主体とした旋回流発生防止カバーの設置効果を確認した。
図4に示すような、内径700mmで深さ700mmの保温機能を有した鋳鉄製坩堝に620kgのSi含有量6.5〜7.5質量%の鋳造用Al−Si合金溶湯を入れ(ちなみに溶湯深さは約700mmになっている。)、溶湯温度を730℃に保持した。回転体としては水モデル実験で用いたものと同じ材質・形状のものを使用し、溶湯面から550mmの深さ位置で回転数400rpmで統一して回転させつつ、20リットル/分でArガスを吹き込んで上記溶融アルミニウム合金を処理した。
【0013】
旋回流発生防止カバーとして、肉厚10mmの黒鉛製で、この旋回流発生防止カバーの内周と回転軸の外周から構成される所定の間隙幅を確保するために、種々の内径のものを準備した。一方、該旋回流発生防止カバーの浸漬深さに関しては、任意の長さに調整できるように可動式とした。
まずこの実施例では、図4中8で示す旋回流発生防止カバーを、回転軸3との間隔を10mmに統一し、浸漬深さを変えて取り付け、ガス吹き込み処理を行った。
【0014】
処理後、溶融アルミニウム合金中の水素ガス含有量および表面に形成された酸化物量を測定し、処理前、処理後および従来法の結果と比較した。
なお、処理後の分析は、処理装置を鋳鉄製の坩堝から脱着後、静かに攪拌してから3分間の養静時間を経た後に試料採取し、分析手段としては、水素ガス量はランズレー法を、また介在物を代表した酸化皮膜量はOlin-Fritテスト法を採用した。その結果を、図5に示す。
【0015】
実施例2
図4中8で示す旋回流発生防止カバーを、浸漬深さを250mmに統一し、回転軸と当該旋回流発生防止カバーの間隔を変えて取り付け、他は実施例1と同じ条件でガス吹き込み処理を行った。その後、実施例1と同様に、溶融アルミニウム合金中の水素ガス含有量および表面の酸化物量を測定した。
その結果を、図6に示す。
【0016】
図5、図6に示す結果からわかるように、溶融アルミニウム合金中の水素ガス含有量は、処理前に比べ、処理後は従来法および本発明法の両者とも半減あるいはそれ以下までに減少している。旋回流発生防止カバーの設置により、従来よりも水素ガス含有量は減少しており、しかも、旋回流発生防止カバーの設置効果を高めるためには、回転軸をより深く覆うことが好ましく、また、回転軸との間隔を小さくして設置することが好ましい。
【0017】
溶湯処理後の溶融アルミニウム合金中の酸化皮膜量は、従来法は、処理前に比べて多くなっているのに対し、本発明法の場合、いずれの条件設定下でも大幅な改善効果が確認された。
そして、酸化皮膜量に関する旋回流発生防止カバーの設置の設置効果は、該カバーの浸漬深さを深くするほど高く、回転体まで覆うことにより顕著になっている。また、酸化皮膜量に関しても、回転軸との間隔を小さくして設置することが好ましい。
なお、従来法で処理前よりも酸化皮膜量が増えている現象は、もともと湯面上にあった酸化皮膜が処理装置の回転に伴った溶融アルミニウムの旋回流に巻き込まれて溶湯中にはいり、新たに溶湯面上に形成された酸化皮膜等が渦流により巻き戻されたことが起因しているものと思われる。
【0018】
【発明の効果】
以上に説明したように、内部に軸方向に伸びる気体通気路を有する垂直回転軸と、この垂直回転軸の先端に設けられ、かつ底面または側面のいずれかに前記気体通気路と連なった気体吹出口が設けられた回転体を溶融金属中で回転させて、溶融金属を処理する際、前記垂直回転軸を、非回転の旋回流発生防止カバーで覆うことにより、溶融金属に旋回渦流の発生を防ぎ、含有ガスと非金属介在物の効率的除去と溶融金属自身の酸化を防ぐことができる溶融金属処理装置を提供することができ、特にアルミニウム合金等の高品質化に資することができる。
【図面の簡単な説明】
【図1】 従来の溶湯処理装置
【図2】 水モデル実験装置
【図3】 水モデル実験による渦流発生状況を示したグラフ
【図4】 本発明の溶湯処理装置の概念図
【図5】 旋回流発生防止カバーの漬浸深さによる溶湯中の水素ガス含有量および酸化皮膜形成量の変化を示すグラフ
【図6】 旋回流発生防止カバーの回転軸との間隔の違いによる溶湯中の水素ガス含有量および酸化皮膜形成量の変化を示すグラフ
【符号の説明】
1:溶融金属、 2:溶融金属槽、 3:回転軸、 4:回転体、
5:ガス吹き出し口、 6:プラスチック片、 7:モーター、
8:旋回流発生防止カバー[0001]
[Industrial application fields]
The present invention relates to an apparatus for removing dissolved gas and non-metallic inclusion particles in molten metal by blowing an inert gas or the like.
[0002]
[Prior art]
Since the dissolved gas and inclusions contained in the molten metal cause defects, the dissolved gas and inclusions in the molten metal are removed before casting.
For example, when casting aluminum or an aluminum alloy, in order to remove non-metallic inclusions such as hydrogen gas and oxides contained in the molten metal, an inert gas or the like is blown to remove the inert gas or the like. A molten metal treatment for removing dissolved gas and non-metallic inclusions is performed by attaching dissolved gas and non-metallic inclusions to the bubbles. In particular, with the recent improvement in required casting quality, it has become necessary to remove contained gases and non-metallic inclusions at levels not previously considered as problems.
[0003]
In order to efficiently remove dissolved gas and non-metallic inclusions, it is necessary to increase the surface area of the bubbles. In order to increase the surface area of the bubbles as much as possible, it is necessary to disperse the bubbles as finely as possible.
A conventional molten metal processing apparatus includes a vertical rotation shaft having a gas ventilation path disposed in a molten metal holding tank and extending in the axial direction inside, a gas rotation path provided at a tip of the vertical rotation shaft, and the gas ventilation path on a bottom surface or a side surface. It consists of a rotating body provided with a connected gas outlet. In order to finely disperse the bubbles injected into the molten metal, the shape of the rotating body is devised or the rotational speed of the rotating shaft is further increased.
[0004]
[Problems to be solved by the invention]
However, if the rotating shaft is rotated at a high speed, a vortex is generated in the molten metal around the rotating shaft, and dissolved gas and non-metallic inclusions floating on the surface of the molten metal are entrained. It cannot be increased.
As a method of preventing the vortex from being generated in the molten metal, there is a method of providing a baffle plate on the side wall or the like of the molten metal treatment tank. However, if the baffle plate is provided, a portion where the blown bubbles do not reach the molten metal is formed. In addition, the baffle plate and the swirling flow of the molten metal collide, and the molten metal surface undulates, increasing the amount of surface oxidation.
The present invention has been devised to solve such a problem, and an object thereof is to provide a molten metal processing apparatus in which vortices are not generated even when a rotating body is rotated at a high speed.
[0005]
[Means for Solving the Problems]
In order to achieve the object, the molten metal processing apparatus of the present invention has a molten metal holding tank, a vertical rotating shaft that is disposed in the molten metal holding tank and has a gas vent passage extending axially therein, and the vertical rotating shaft. A rotating body provided at a tip of the gas outlet and provided with a gas blowout opening connected to the gas ventilation path on either or both of the bottom surface and the side surface, and covering the vertical rotating shaft and the rotating body at the tip of the rotating shaft. A non-rotating swirl flow generation prevention cover is also provided.
[0006]
[Simulation experiment]
First, in order to know the process that hinders the removal effect of hydrogen gas and non-metallic inclusions, and to know the vortex generation prevention effect of the non-rotating swirl flow prevention cover, a water model that is easy to observe is adopted instead of molten aluminum did.
An experiment was conducted by putting water into a transparent PVC treatment tank having an inner diameter of 700 mm, which is similar to the
[0007]
In order to generate bubbles, a rotating
Such a rotating
[0008]
The swirl flow prevention cover consists of a transparent PVC round pipe-shaped body part with an inner diameter of 80 mm and an outer diameter of 100 mm, which can be varied in immersion depth, and an additional PVC-made cover part covering the rotating blades as necessary. The attachment is fixed to the non-rotating part of the processing apparatus main body.
[0009]
The installation depth of the swirl flow generation prevention cover was changed, and the rotation speed of the rotating
FIG. 3 shows the relationship between the rotational speed and the vortex flow. In the figure, (a) is a conventional method without a swirl flow generation prevention cover, (b) is a cover up to a position of 50 mm from the water surface, (c) and (d) are also covered up to 200 mm and 500 mm, Furthermore, (e) covers the rotating
[0010]
As can be seen from the figure, the depth of the vortex formed near the surface of the rotating shaft increases substantially in proportion to the rotational speed. However, in the case of the conventional method, for example, the vortex depth at 500 rpm was 20 mm, but in the method of the present invention provided with the swirl flow generation prevention cover, each experimental example was 5 mm or less, which The prevention effect was confirmed.
Further, at this time, the swirl flow generation prevention cover is more effective as the immersion depth is deeper, and is particularly effective when covering the rotating body that generates bubbles.
[0011]
In the case of the conventional method, the pseudo inclusions assumed in the oxide film adhering to the bubbles swirl in synchronism with water and then float once, but after that, they are caught in the vortex generated near the water surface of the rotating shaft, and again, It was confirmed that it was returned to the water.
On the other hand, in the case of the method of the present invention in which the swirl flow generation prevention cover is used and the vortex flow is hardly generated, the water flow such as the swirl flow and the vortex flow is retained in the swirl flow generation prevention cover. Most of the water in the outside treatment tank did not flow.
It was observed that the gas blown out from the
Of course, it was not observed that the pseudo-inclusion plastic piece that once floated returned to the water again.
[0012]
【Example】
Example 1
Based on the knowledge obtained in the water model experiment, the installation effect of the swirl flow prevention cover mainly confirming the removal of hydrogen gas and oxide film in the molten aluminum alloy was confirmed.
As shown in FIG. 4, a cast iron crucible having an inner diameter of 700 mm and a depth of 700 mm and having a heat retaining function is charged with 620 kg of an Si-containing Al-Si alloy molten metal having a Si content of 6.5 to 7.5 mass% (by the way, the molten metal). The depth is about 700 mm.) The molten metal temperature was kept at 730 ° C. As the rotating body, the same material and shape as those used in the water model experiment were used, and Ar gas was supplied at 20 liters / minute while rotating uniformly at a rotational speed of 400 rpm at a depth of 550 mm from the molten metal surface. The molten aluminum alloy was treated by blowing.
[0013]
A swirl flow prevention cover made of graphite with a thickness of 10 mm is prepared with various inner diameters to ensure a predetermined gap width composed of the inner periphery of the swirl flow generation prevention cover and the outer periphery of the rotating shaft. did. On the other hand, the immersion depth of the swirl flow generation prevention cover is movable so that it can be adjusted to an arbitrary length.
First, in this example, the swirl flow generation prevention cover indicated by 8 in FIG. 4 was attached at a distance of 10 mm from the
[0014]
After the treatment, the hydrogen gas content in the molten aluminum alloy and the amount of oxide formed on the surface were measured and compared with the results of the treatment before, after the treatment, and the conventional method.
The analysis after the treatment was carried out after removing the treatment device from the cast iron crucible, and after gently stirring for 3 minutes, taking a sample, and as an analysis means, the amount of hydrogen gas was calculated using the Lansley method. In addition, the Olin-Frit test method was used for the amount of oxide film representing inclusions. The result is shown in FIG.
[0015]
Example 2
The swirl flow generation prevention cover indicated by 8 in FIG. 4 is attached by changing the distance between the rotating shaft and the swirl flow generation prevention cover by unifying the immersion depth to 250 mm and performing the gas blowing process under the same conditions as in the first embodiment. Went. Thereafter, in the same manner as in Example 1, the hydrogen gas content and the surface oxide amount in the molten aluminum alloy were measured.
The result is shown in FIG.
[0016]
As can be seen from the results shown in FIGS. 5 and 6, the hydrogen gas content in the molten aluminum alloy is reduced to half or less in both the conventional method and the method of the present invention after the treatment, compared to before the treatment. Yes. Due to the installation of the swirl flow generation prevention cover, the hydrogen gas content is reduced as compared with the prior art, and in order to enhance the installation effect of the swirl flow generation prevention cover, it is preferable to cover the rotating shaft deeper, It is preferable to install with a small distance from the rotating shaft.
[0017]
The amount of oxide film in the molten aluminum alloy after molten metal treatment is larger than that before treatment in the conventional method, whereas in the case of the method of the present invention, a significant improvement effect is confirmed under any condition setting. It was.
And the installation effect of installation of the swirl | flow generation | occurrence | production prevention cover regarding the amount of oxide films becomes so high that the immersion depth of this cover is deepened, and becomes remarkable by covering even a rotary body. In addition, regarding the amount of the oxide film, it is preferable to install it with a small distance from the rotating shaft.
In addition, the phenomenon that the amount of oxide film increased by the conventional method than before treatment is that the oxide film originally on the molten metal surface is caught in the swirling flow of molten aluminum accompanying the rotation of the treatment device, and enters the molten metal, This is probably because the oxide film newly formed on the molten metal surface was rewound by eddy current.
[0018]
【The invention's effect】
As described above, a vertical rotation shaft having a gas ventilation path extending in the axial direction inside, and a gas blower provided at the tip of the vertical rotation shaft and connected to the gas ventilation path on either the bottom surface or the side surface. When processing the molten metal by rotating the rotating body provided with the outlet in the molten metal, the vertical rotating shaft is covered with a non-rotating swirl flow prevention cover, thereby generating swirl vortex in the molten metal. Therefore, it is possible to provide a molten metal processing apparatus capable of preventing, efficiently removing contained gases and non-metallic inclusions and preventing oxidation of the molten metal itself, and can contribute particularly to the improvement of quality of aluminum alloys and the like.
[Brief description of the drawings]
[Fig. 1] Conventional molten metal processing equipment [Fig. 2] Water model experimental device [Fig. 3] Graph showing the eddy current generation state by water model experiment [Fig. 4] Conceptual diagram of molten metal processing device of the present invention [Fig. Graph showing changes in hydrogen gas content and oxide film formation amount in the molten metal depending on the immersion depth of the flow prevention cover [Fig. 6] Hydrogen gas in the molten metal due to the difference in the distance from the rotating shaft of the swirl prevention cover Graph showing changes in content and oxide film formation amount [Explanation of symbols]
1: molten metal, 2: molten metal tank, 3: rotating shaft, 4: rotating body,
5: Gas outlet, 6: Plastic piece, 7: Motor,
8: Swirl flow prevention cover
Claims (1)
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JP2001191057A JP4123740B2 (en) | 2001-06-25 | 2001-06-25 | Molten metal processing equipment |
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JP2001191057A JP4123740B2 (en) | 2001-06-25 | 2001-06-25 | Molten metal processing equipment |
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CN104988343B (en) * | 2015-08-12 | 2017-03-08 | 北京科技大学 | A kind of air cooling multitube stirring prepares the device and method of light alloy semisolid slurry |
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