JPS6283431A - Refining apparatus for molten aluminum - Google Patents

Refining apparatus for molten aluminum

Info

Publication number
JPS6283431A
JPS6283431A JP22232285A JP22232285A JPS6283431A JP S6283431 A JPS6283431 A JP S6283431A JP 22232285 A JP22232285 A JP 22232285A JP 22232285 A JP22232285 A JP 22232285A JP S6283431 A JPS6283431 A JP S6283431A
Authority
JP
Japan
Prior art keywords
molten
gas
refining
tube
molten metal
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP22232285A
Other languages
Japanese (ja)
Inventor
Jun Kawakiri
川桐 純
Yoshiaki Yokoyama
義明 横山
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Aluminum Co Ltd
Original Assignee
Mitsui Aluminum Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsui Aluminum Co Ltd filed Critical Mitsui Aluminum Co Ltd
Priority to JP22232285A priority Critical patent/JPS6283431A/en
Publication of JPS6283431A publication Critical patent/JPS6283431A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To effectively remove impurities from molten Al, by uniformly and finely dispersing refining gas by a specified short cylindrical rotary tube, at refining molten Al by blowing refining gas therein from bottom part of a treating vessel. CONSTITUTION:Molten Al is poured from an inlet 8 of the treating vessel 1, refining gas is supplied from a porous plug 2 at a treating chamber 11 to perform refining and exhausted from an outlet 7 through an outlet chamber 12. Thereat, the short cylindrical rotary tube 6 is hung into molten Al through a rotary shaft 8 and rotated by a driving means 4. Plural brades 7 are protrudently provided to the tube 6 and an angle of the brade 7 is slanted by 10-45 deg. to the shaft line. It is favorable to adopt about 20-60mm to a height (h) of the tube 6 and about 20-10mm to a length (l) of the blade 7. In this way, refining gas introduced in molten A4l is pervaded into molten metal over a wind range under fine bubble state to effectively remove impurities in molten metal.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明はアルミニウム溶湯の精製処理に関し、更に詳し
くは溶湯中に含まれる水素ガスやアルミニウムあるいは
マグネシウム等の酸化物の非金属介在物等の不純物を効
果的に除去する装置に関する。
[Detailed Description of the Invention] <Industrial Application Field> The present invention relates to the refining treatment of molten aluminum, and more specifically, the present invention relates to the purification treatment of molten aluminum, and more specifically to the purification of impurities such as hydrogen gas and nonmetallic inclusions of oxides such as aluminum or magnesium contained in the molten metal. The present invention relates to a device for effectively removing.

〈従来の技術及びその問題点〉 鋳塊を製造する場合のアルミニウム溶湯には水素ガスや
アルミニウム及びマグネシウムなどの酸化物の非金属介
在物が含まれ゛(−いる。
<Prior art and its problems> Molten aluminum used to produce ingots contains hydrogen gas and nonmetallic inclusions of oxides such as aluminum and magnesium.

水素ガスや非金属介在物等が含まれたよ5のアルミニウ
ム8′湯で鋳塊を製造しl:場合、得られIコ鋳塊及び
この鋳塊により作られた製品が欠陥となる場合がある。
If an ingot is produced using aluminum molten metal containing hydrogen gas or non-metallic inclusions, the resulting ingot and the products made from this ingot may be defective. .

その為アルミニウム溶湯より鋳塊を製造する場合におい
ては溶湯精製処理を施し、これらの水素ガス、非金属介
在物を除去ずろ必要がある。
Therefore, when producing an ingot from molten aluminum, it is necessary to perform a molten metal purification treatment to remove hydrogen gas and nonmetallic inclusions.

従来乙のような水素ガス、非金属介在物などの不純物を
除去するために採用されている方法としては、窒素ガス
やアルゴンガス等の不活性ガスあるいは塩素ガス、フロ
ンガス等の反応性ガスを鉄製あるいは黒鉛パイプ等を介
して吹き込むものである。この方法では吹き込まれろガ
スの気泡が大きく、また溶湯全体に気泡を接触させるこ
とも困難であるため、高い処理効率を得るのは難しい。
Conventionally, methods used to remove impurities such as hydrogen gas and non-metallic inclusions include inert gases such as nitrogen gas and argon gas, or reactive gases such as chlorine gas and chlorofluorocarbon gases. Alternatively, it can be injected through a graphite pipe or the like. In this method, it is difficult to obtain high processing efficiency because the bubbles of the blown gas are large and it is difficult to bring the bubbles into contact with the entire molten metal.

そこで、これらの点を改善するものとして、例えば特公
昭52−36487号公報で示される様に固定子の下端
に回転子を設は両者の間隙から精製用ガスを溶出中へ導
入すると共に前記回転子を高速で回転させると4とによ
り導入されろガスを徹細なガス泡に細分して溶湯と接触
させる方法及び装置がある。
Therefore, in order to improve these points, for example, as shown in Japanese Patent Publication No. 52-36487, a rotor is installed at the lower end of the stator, and the gas for purification is introduced into the elution process from the gap between the two, and the rotation There is a method and apparatus in which the gas introduced by rotating the child at high speed is subdivided into fine gas bubbles and brought into contact with the molten metal.

乙の方法によれば処理効率の点では十分満足できる結宋
が得られるが、固定子と回転子を−・体に構成する必要
があること、更には固定子と回転子の間を適正な間隙に
保持j7なければならないこと等構造が複雑なものとな
る。
According to method B, a sufficiently satisfactory result can be obtained in terms of processing efficiency, but it is necessary to configure the stator and rotor as a body, and furthermore, it is necessary to ensure that the space between the stator and rotor is properly adjusted. The structure becomes complicated as it must be held in the gap.

また固定子、回転子などの消耗が激しいため、これらの
取換え作業が極めて煩雑になるといった問題が存在する
In addition, there is a problem in that the stator, rotor, etc. are subject to rapid wear and tear, making the task of replacing them extremely complicated.

又類似の方法ではあるが、特開昭58−144438号
公報に示さiする様な槽下部のノズルあるいはガス吹き
込みパイプ、又は回転軸の内部より導入されt:ガスを
回転軸下端に設けtニガス滞留部に滞留させ、乙の滞留
したガスを回転子の回転によって溶湯中に分散させる方
法及び装置も提案されている。
In a similar method, gas is introduced from the nozzle or gas blowing pipe at the bottom of the tank, or from the inside of the rotating shaft, as shown in Japanese Patent Application Laid-Open No. 58-144438. A method and device have also been proposed in which the gas is allowed to remain in the stagnation part and is dispersed into the molten metal by rotation of a rotor.

この方法に、1t1ばノズル及びパイプあるいは回転軸
よりガス滞留部に導入されtニガペがこのガス滞留部に
於いてノiス同志の合体を牛し、その為に徹細な気泡と
じ−(溶湯中((均 分散きljイ、と、!: Il 
9・Ilしい。またガスをバ1シ悄さ得る為の回転軸の
1〜端の回転子の形状が複雑になるといつ間!/flも
存在4ろ、1〈問題点を解決−4ろ為の手段〉 本発明(1F述の諸問題ろ・解lJ4−<J為に、アル
ε二一つl、溶湯内(と導入さ第1j:精製用ガスをi
+PI411111′気泡状のト((溶出中11.11
;b囲((行き渡らせる為:(、精製用ガスの攪拌羽根
に1゛人をなしl二もの−(あり、その要旨はアルミ−
ラム溶湯の人11と出11とをそわぞれに有する処理槽
の底部に$h製用ガス供給パイプを直接的にあるいはポ
ーラスプラグを介し−C開口せしめ、かつ処理槽−11
部より吊設しl1回転軸の下端に連設した短円筒状回転
筒をl−、配積製用ガスの供給部より1.を所要間隔l
′yかせl臼i装置となし、かつ同回転筒の外周面に同
回転筒の軸線と10〜45°傾斜した複数個の羽根が突
設された乙とを特徴とするアルミニウム溶湯の精製装置
である。
In this method, the gas is introduced into the gas retention area from the nozzle and pipe or the rotating shaft, and in this gas retention area, the gas is introduced into the gas retention area. Medium ((uniform dispersion lj,!:
9.I want to do it. Also, when the shape of the rotor from the first to the end of the rotating shaft to get the gas to flow becomes complicated! /fl also exists 4, 1 <Means for solving the problems - 4)> The present invention (1 Part 1j: Refining gas i
+PI411111'bubble ((during elution 11.11
; b Surrounding ((To distribute the gas: (, one person is placed on the stirring blade of the refining gas, and two people are placed on the agitation blade.
A $h gas supply pipe is opened directly or through a porous plug at the bottom of the processing tank, which has a ram molten metal outlet 11 and an outlet 11, respectively, and the processing tank 11
A short cylindrical rotary cylinder suspended from the l1 rotation shaft and connected to the lower end of the l1 rotary shaft is connected to the l- and 1. the required interval l
An apparatus for refining molten aluminum, characterized by a skein mortar device, and a plurality of blades protruding from the outer circumferential surface of the rotary cylinder at an angle of 10 to 45 degrees with respect to the axis of the rotary cylinder. It is.

なお上記本発明装置に於いて、回転筒の外周面に突設す
る羽根を、軸線と10〜45°の角度をもっ−(傾斜さ
せる様にしたのは、回転筒の下から上昇j7て来る精製
用ガスを出来る限り処理槽下方へ撹散させる為゛(あり
、その為には少なくとも10°は#A斜さセなければ下
向きの成分が生しず、−・方45°を越えれば全体的な
攪拌力が弱まるから−Cある。。
In the device of the present invention, the blades protruding from the outer circumferential surface of the rotary cylinder are inclined at an angle of 10 to 45 degrees with respect to the axis. In order to disperse the refining gas as far down as possible into the processing tank, the angle must be at least 10° to avoid the formation of downward components, and if it exceeds 45°, the whole -C because the stirring power is weakened.

乙の様に羽根を傾斜せしめるのは精製ガスを下向きに撹
散させる為であるの−C1該羽根の傾斜方向と回転軸の
回転方向については一定の関係がある事は勿論である 〈実施例及び作用〉 以下本発明装置を、その実施例を示す図面を参酌(7乍
ら詳述する。
The reason why the blades are tilted as in B is to disperse the purified gas downward.-C1 It goes without saying that there is a certain relationship between the direction of inclination of the blades and the direction of rotation of the rotating shaft. and Operation> The apparatus of the present invention will be described in detail below with reference to the drawings showing the embodiments thereof.

第1図は本発明装置の一実施例を示し、処理槽(1)の
底部に取付けら1またポーラスプラグ(2)に、精製ガ
ス供給パイプ(3)か連通され、処理槽(1)内に精製
ガスを導入する様になっている。この処理槽(1)内に
上部に駆動手段(4)を有する回転軸(5)が吊設され
、その下端に回転筒(6)が取付けられており、その詳
細は第2図及び第3図に示す様な形状であり、回転筒(
6)の外周には羽根(7)が複数個突設されている。
Fig. 1 shows an embodiment of the present invention apparatus, which is installed at the bottom of the processing tank (1) and connected to a porous plug (2) and a purified gas supply pipe (3) inside the processing tank (1). Purified gas will be introduced into the area. A rotating shaft (5) having a driving means (4) at the upper part is suspended in the treatment tank (1), and a rotating cylinder (6) is attached to the lower end of the shaft. The shape is as shown in the figure, and the rotating cylinder (
A plurality of blades (7) are provided protruding from the outer periphery of 6).

回転軸(5)上方の駆動手段(4)は電動機やエアーモ
ータ等によって回転さ第1、それによって回転軸(5)
及び回転筒(6)が回転(7槽底部のポーラスプラグ(
2)より吹き込まねた精製用ガスを溶出中へ均一微細に
分散させる。
The driving means (4) above the rotating shaft (5) is first rotated by an electric motor, an air motor, etc., and thereby the rotating shaft (5)
and the rotating cylinder (6) rotates (the porous plug at the bottom of the tank (7)
2) Uniformly and finely disperse the purification gas blown into the elution medium.

本発明で用いる回転筒(6)外周の羽根(7)は槽底部
のポーラスプラグ、[り吹き込まねた精製用ガスの微細
気泡を十分に溶出中に分散させるために(よその数は4
〜8L!J所又乙の羽根の角度はI’、 l[! I/
た様に軸線に対し10〜45°の範囲が好ましい。更に
望ましくは回転筒の高さ)1を20〜60IIIIIl
1羽根の長さlを20〜10nII11とムるようにす
ることが好ましい。
The rotary cylinder (6) used in the present invention has blades (7) on the outer periphery of the porous plug at the bottom of the tank.
~8L! The angle of the blade of J Tokoro Mata Otsu is I', l [! I/
As mentioned above, a range of 10 to 45 degrees with respect to the axis is preferable. More preferably, the height of the rotating cylinder) 1 is 20 to 60III
It is preferable that the length l of one blade is 20 to 10 nII11.

なお回転筒(6)の形状としては、第2図に示す様なも
のの他に、第4図に示す様に下部になるにつれ順次その
径が人となる様な構成のものもあり、この様になす事に
より精製用ガスをより効率良く下方向へ送る事が出来る
ものである。
In addition to the shape of the rotating cylinder (6) shown in Fig. 2, there is also one in which the diameter gradually becomes larger towards the bottom as shown in Fig. 4. By doing this, refining gas can be sent downward more efficiently.

図中、(8)は溶湯人F1、(9)ば溶湯出[−1、(
10)は処理槽(1)内に設けられる仕切り板であり、
乙の(1切り板(10)に、lり処理槽(1)は処理室
(11)と出[−1室(]2)とに分割されており、同
仕切り板(10)は精製用ガスの微細気泡に捕捉された
水素ガスや非金属介在物等の懸濁粒子及び懸濁状杓子か
浮上しててきlニドロスが浮−1,(7ないうらに、溶
1易出[−1(11)へ流れるのを防いている。
In the figure, (8) is the molten metal F1, (9) is the molten metal [-1, (
10) is a partition plate provided in the processing tank (1),
On the first cutting plate (10), the processing tank (1) is divided into a processing chamber (11) and an output chamber (2), and the partition plate (10) is used for refining. Suspended particles such as hydrogen gas and non-metallic inclusions trapped in gas microbubbles and suspended particles floated to the surface. This prevents the flow to (11).

処理槽(])の大きさ、特に処理室(+ 1)の大きさ
及び回転軸子端の回転筒(6)の大きさは槽底部より吹
き込よilるガスが処理室(11)内の溶湯全体に分散
するように定めればよく、比較的高範囲の・1法のもの
を用いることができる。−例として水空気モデA実験の
結果によれば処理室(11)の有効直径と回転羽根との
直径比をに02〜06程度に、又回転羽根の直径と槽底
部のノズルとの直径比は1:12〜06程度にとれば充
分である。
The size of the processing tank (]), especially the size of the processing chamber (+1) and the size of the rotating cylinder (6) at the end of the rotating shaft, are such that the gas blown from the bottom of the tank will not flow into the processing chamber (11). It is only necessary to set it so that it is dispersed throughout the molten metal, and it is possible to use a method having a relatively high range. - For example, according to the results of the water-air model A experiment, the diameter ratio between the effective diameter of the treatment chamber (11) and the rotating blade is approximately 02 to 06, and the diameter ratio between the rotating blade and the nozzle at the bottom of the tank is approximately 02 to 06. It is sufficient to set the ratio to about 1:12 to 06.

乙とて処理室(11)の有効直径とは処理室(11)の
断面形状が円の場合はその直径、正方形の場合はその−
・辺の長さ、長方形の場合は短辺の長さをいう。又回転
羽根及びノズルのr&径とはそilそれの円周で最も長
い部分をいう。
The effective diameter of the processing chamber (11) is the diameter if the cross-sectional shape of the processing chamber (11) is circular, and the diameter if it is square.
・Length of the side, in the case of a rectangle, the length of the short side. Also, the r&diameter of the rotating blade and nozzle refers to the longest part of its circumference.

次に第5図及び第す図はそれぞれ精製用ノJス吹き込み
[Iを2個としt:例及び回転筒を2個した例を示しア
ルミニウム溶出の臘や含、1れろ水素ガスあるいは非金
属介在物の観に応1しこの第5図や第6図の様な方式を
採用する事もある。
Next, Figures 5 and 3 show an example in which two rotating cylinders are used for refining gas injection [I and two rotating cylinders, respectively], and the results are shown in Figures 5 and 5 respectively. Depending on the view of inclusions, methods such as those shown in Figures 5 and 6 may be adopted.

次に本発明装置を用いて行なっl:精製処理試験の結果
を示す。
Next, the results of a purification test conducted using the apparatus of the present invention are shown.

第1図に示した装置を用いて純アルミニウムの連続処理
を行な−)た回転筒は第2図に示した、Lうな形状のも
のである。即ら、直径が250mmで羽根の高さl)を
50mmとし羽根の角唯は10’で6個の羽根を設はノ
コ。回転軸や回転筒等はずへて黒鉛で作製した。−力積
製用ガスを回転筒の1a上に位置するようにノズルを設
けた。この用台回転筒とノズルとの間隙を50InIn
とl、 1.: 、処理槽は鋼板製外殻の内側に断熱ボ
ードを内張し、唄にその内側に高アルミナ質レンガを内
張しt:直方体形状のものを用い、その出口側には仕切
り板を配置した。まt:回転軸はその回転軸中心線が処
理室の中央1こくるように配置した。この様な装置に前
記純アルミニウム溶湯を5000kg/hrの割合て連
続的に供給し、回転軸を30Or、 p、 mの速度で
回転し合計201−ンの溶出を処理した。精製用ガスと
してはアノLゴン90vo 1%と塩素10vo 1%
との混合ガスを用い、]Om’/hrの割合で供給した
The rotary cylinder used for continuous processing of pure aluminum using the apparatus shown in FIG. 1 is L-shaped as shown in FIG. That is, the diameter is 250 mm, the height of the blade is 50 mm, the angle of the blade is 10', and 6 blades are installed. The rotating shaft, rotating cylinder, etc. were removed and made of graphite. - A nozzle was provided so that the impulse-producing gas was positioned above the rotating cylinder 1a. The gap between this rotary cylinder and the nozzle is 50 InIn.
and l, 1. The treatment tank has a steel plate shell lined with a heat insulating board, and the inside is lined with high alumina bricks. A rectangular parallelepiped-shaped tank is used, and a partition plate is placed on the outlet side. did. Mat: The rotating shaft was arranged so that the center line of the rotating shaft was one point in the center of the processing chamber. The pure aluminum molten metal was continuously supplied to such an apparatus at a rate of 5000 kg/hr, and the rotating shaft was rotated at a speed of 30 Or, p, m, to process a total of 201 tons of elution. Purification gases include Ano Lgon 90vo 1% and chlorine 10vo 1%
A mixed gas was used and was supplied at a rate of ]Om'/hr.

以にの様な処理を行なう前と行なっt:後の溶湯につい
てサンプリングを行ない、水素ガス量、ナ)・リウム呈
及び非金属介在物の濃度を測定した。
Sampling was performed on the molten metal before and after the above-mentioned treatments, and the amount of hydrogen gas, the concentration of sodium and lithium, and the concentration of nonmetallic inclusions were measured.

以上の結果を第1表に示す。The above results are shown in Table 1.

〈発明の効果〉 以上の構成を有する本発明装置では槽底部のノズルある
いはポーラスプラグより吹き込まれた精製用ガスは回転
軸の回転(こより回転筒の底部てガス同志で合体するこ
となく、槽底部に向い乱流状態を作る。この為精製用ガ
スが溶出中に均一に微細分散するとともにかつ溶出と気
泡との接触時間を長くすることができ、溶出中に存在す
る水素ガスあるいは非金属介在物の除去効率を高めるも
のである。又槽底部のノズルあるいはポーラスーツ°ラ
グと回転筒の間隙を20〜100III11の軛囲内に
保つ乙とにより更に除去効率を高めることもできる。j
7かも全体の構造が非常に簡単なので製作及び取替も容
易である。
<Effects of the Invention> In the device of the present invention having the above configuration, the purification gas blown from the nozzle or porous plug at the bottom of the tank is transferred to the bottom of the tank by the rotation of the rotating shaft (through the rotation of the rotating shaft), the gases do not coalesce together at the bottom of the rotating cylinder. This creates a turbulent flow state for the purification gas to be dispersed uniformly and finely during the elution, and the contact time between the elution and the bubbles can be extended, eliminating hydrogen gas or non-metallic inclusions present during the elution. The removal efficiency can be further increased by keeping the gap between the nozzle at the bottom of the tank or the polar suit lug and the rotating cylinder within a range of 20 to 100 mm.
7. Since the overall structure is very simple, it is easy to manufacture and replace.

従ってアルミニウムの溶出の精製には非常に慢れた効果
を発揮する。
Therefore, it is extremely effective in purifying aluminum elution.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明装置の一実施例の説明図、第2図及び第
3図はそれぞれ回転筒部分の正面図及び斜視図、第4図
は回転筒の他の形態を示す斜視図、第5図及び第6図は
それぞれ本発明装置に他の実施例を示す説明図。 図中、 (1)処理槽 (5)回転軸 (6)回転筒 (7)羽根 特許出願人 三井アルミニウム工業株式会社代 理 人
 H吉 教晴
FIG. 1 is an explanatory diagram of one embodiment of the device of the present invention, FIGS. 2 and 3 are a front view and a perspective view of the rotary cylinder portion, respectively, and FIG. 4 is a perspective view showing another form of the rotary cylinder. 5 and 6 are explanatory diagrams showing other embodiments of the apparatus of the present invention, respectively. In the diagram: (1) Treatment tank (5) Rotating shaft (6) Rotating tube (7) Vane Patent applicant Mitsui Aluminum Industries Co., Ltd. Agent Noriharu H.

Claims (1)

【特許請求の範囲】[Claims] 1、アルミニウム溶湯の入口と出口とをそれぞれに有す
る処理槽の底部に精製用ガス供給パイプを直接的にある
いはポーラスプラグを介して開口せしめ、かつ処理槽上
部より吊設した回転軸の下端に連設した短円筒状回転筒
を上記精製用ガスの供給部よりは所要間隔浮かせた位置
となし、かつ同回転筒の外周面に同回転筒の軸線と10
〜45°傾斜した複数個の羽根が突設されたことを特徴
とするアルミニウム溶湯の精製装置。
1. A refining gas supply pipe is opened directly or through a porous plug at the bottom of the processing tank, which has an inlet and an outlet for molten aluminum, and is connected to the lower end of a rotating shaft suspended from the top of the processing tank. The installed short cylindrical rotating tube is placed a required distance above the purification gas supply section, and the outer circumferential surface of the rotating tube has a 10-degree angle with the axis of the rotating tube.
A molten aluminum refining device characterized by a plurality of protruding blades tilted at ~45°.
JP22232285A 1985-10-04 1985-10-04 Refining apparatus for molten aluminum Pending JPS6283431A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22232285A JPS6283431A (en) 1985-10-04 1985-10-04 Refining apparatus for molten aluminum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22232285A JPS6283431A (en) 1985-10-04 1985-10-04 Refining apparatus for molten aluminum

Publications (1)

Publication Number Publication Date
JPS6283431A true JPS6283431A (en) 1987-04-16

Family

ID=16780536

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22232285A Pending JPS6283431A (en) 1985-10-04 1985-10-04 Refining apparatus for molten aluminum

Country Status (1)

Country Link
JP (1) JPS6283431A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996016193A1 (en) * 1994-11-24 1996-05-30 Aluminium Pechiney Device for degassing and separating the inclusions in a liquid metal bath

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996016193A1 (en) * 1994-11-24 1996-05-30 Aluminium Pechiney Device for degassing and separating the inclusions in a liquid metal bath
FR2727432A1 (en) * 1994-11-24 1996-05-31 Pechiney Aluminium DEVICE FOR DEGASING AND SEPARATION OF INCLUSIONS IN A LIQUID METAL BATH

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