JPS60190534A - Apparatus for continuous production of high-purity aluminum - Google Patents
Apparatus for continuous production of high-purity aluminumInfo
- Publication number
- JPS60190534A JPS60190534A JP4593584A JP4593584A JPS60190534A JP S60190534 A JPS60190534 A JP S60190534A JP 4593584 A JP4593584 A JP 4593584A JP 4593584 A JP4593584 A JP 4593584A JP S60190534 A JPS60190534 A JP S60190534A
- Authority
- JP
- Japan
- Prior art keywords
- aluminum
- molten
- crucible
- crucibles
- straight line
- 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.)
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- Manufacture And Refinement Of Metals (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は、偏析凝固を利用した高純度アルミニウムの
連続製造装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for continuously producing high-purity aluminum using segregation solidification.
本出願人は、高純度アルミニウムを製造するために、先
に偏析凝固の原理を利用したアルミニウムの精製方法を
提案した。この精製方法は、精製づべきアルミニウムを
溶解した後、この溶融アルミニウムを常にその凝固温度
を越えた温度に加熱保持しておき、この加熱された溶融
アルミニウム中に冷却体を浸漬し、この冷iJj体の表
面温度を上記凝固温度以下に保持し、この冷部体を回転
させて凝固界面近傍に排出された不純物を分散混合りる
ことにより、液相中における凝固界面近傍の不純物濃化
層の厚さを薄くし、その結果上記不純物濃化層での液相
中の温度勾配を急にしながら、冷却体の表面に高純度ア
ルミニウムを晶出させることを特徴とするものでアル(
特開1j)57−82437号)。The present applicant previously proposed an aluminum refining method that utilizes the principle of segregation solidification in order to produce high-purity aluminum. In this refining method, after melting the aluminum to be refined, the molten aluminum is always heated and maintained at a temperature exceeding its solidification temperature, and a cooling body is immersed in the heated molten aluminum. By maintaining the surface temperature of the body below the solidification temperature and rotating this cold body to disperse and mix the impurities discharged near the solidification interface, the impurity concentrated layer near the solidification interface in the liquid phase is It is characterized by crystallizing high-purity aluminum on the surface of the cooling body while reducing the thickness and thereby steepening the temperature gradient in the liquid phase in the impurity-concentrated layer.
JP-A-1J) No. 57-82437).
この発明は、上記の方法を利用して高純度アルミニウム
を連続的に製造するにさいし、精製中に発生づるアルミ
ニウム酸化物を効率よく除去することの可能な装置を提
供することを目的とする。An object of the present invention is to provide an apparatus capable of efficiently removing aluminum oxide generated during refining when high-purity aluminum is continuously produced using the above-described method.
この明細■において、前後とはアルミニウム溶湯の進む
ん向を基準にし、前どは溶解炉で溶解されたアルミニウ
ム溶湯が進む方向(ずなわら第1図右側)を指し、後と
はこれと反対側を指すものとする。また、左右とは前方
に向っていうものとする。In this specification (■), forward and backward refers to the direction in which the molten aluminum advances in the melting furnace (right side of Figure 1), and backward refers to the direction in which the molten aluminum advances in the melting furnace. It shall point to the side. In addition, left and right mean forward.
この発明による高純度アルミニウムの連vc製造装置は
、アルミニウムを溶解するための溶解炉に続いて一列に
並べられた複数個のるつはと、各るつぼ内に1つずつ配
置されており、かつ上下動自在である高純度アルミニウ
ムを晶出さU゛るための回転冷却体とを備えており、隣
り合うるつぼどうしが上端部において連結樋によって連
通状に接続され、溶解炉から最も速いるつぼの上端部に
溶湯排出樋が取付けられ、すべでの連結樋J3よび溶湯
排出樋が、平面から見てるつぼの中心どうしを結ぶ直線
と平行な直線上に位置せられ、溶解炉に最も近いるつぼ
に溶解炉からアルミニウム溶湯が送り込まれるようにな
されているものである。The continuous VC manufacturing apparatus for high-purity aluminum according to the present invention includes a plurality of crucibles arranged in a line following a melting furnace for melting aluminum, one crucible in each crucible, and It is equipped with a rotary cooling body for crystallizing high-purity aluminum that can be moved up and down, and adjacent crucibles are connected in a continuous manner by a connecting gutter at the upper end, so that the upper end of the crucible that is the fastest to move from the melting furnace A molten metal discharge gutter is attached to the melting furnace, and the connecting gutter J3 and the molten metal discharge gutter are located on a straight line parallel to the straight line connecting the centers of the crucibles when viewed from the plane, and melting is carried out in the crucible closest to the melting furnace. Molten aluminum is fed into the furnace from a furnace.
回転冷却体は、その周面に高純度のアルミニウムを晶出
させるために用いる。すなわち、各るつぼ中に溶湯が入
れられた後に回転冷却体を下降させて溶湯中に浸漬し、
これを回転させると、回転冷却体の周面に高純度の初晶
アルミニウムが晶出し、不純物は液相中に排出されるが
、回転冷7.11体を回転さけるど固相ど液相との間に
相対的な運動が生じ、排出された不純物によって凝固界
面近傍に形成された不純物濃化層と他の大部分の液相と
の攪拌混合が効果的に行なわれ、不純物濃化層中の不純
物が液相全体に分散さけられて、不純物濃化層の厚さは
結果的に非常に薄くなる。したがって、精製効率が高く
なつC高純度)アルミニウムを得られる。この回転冷却
体としては、円筒状のものおよび下方に向って漸次小径
とされたテーバ筒状のものなどを用いる。冷却体として
テーパ筒状のものを用いると、冷却体の周面に晶出した
高純度アルミニウムの回収作業が容易になるので一層好
ましい。The rotary cooling body is used to crystallize high-purity aluminum on its circumferential surface. That is, after the molten metal is poured into each crucible, the rotary cooling body is lowered and immersed in the molten metal,
When the rotary cooling body is rotated, high-purity primary aluminum crystallizes on the circumferential surface of the rotary cooling body, and impurities are discharged into the liquid phase. A relative movement occurs between the two, and the impurity concentrated layer formed near the solidification interface by the ejected impurities is effectively stirred and mixed with most of the other liquid phase, and the impurity concentrated layer is The impurities are dispersed throughout the liquid phase, and the thickness of the impurity-concentrated layer becomes very thin as a result. Therefore, high purity aluminum can be obtained with high purification efficiency. As this rotary cooling body, a cylindrical one or a Taber cylindrical one whose diameter becomes gradually smaller toward the bottom are used. It is more preferable to use a tapered cylindrical cooling body as this makes it easier to recover high-purity aluminum crystallized on the circumferential surface of the cooling body.
また冷却体は、その内部に:空気、アルゴンガス、窒素
ガス、空気と水との混合液体等の冷IJI体を送り込む
ことにより冷却される。外部熱源からの加熱によりるつ
ぼ中の溶融アルミニウムに供給される煎出を大きくし、
しかも冷却体によって溶融アルミニウムを冷却して多く
の熱を奪うと、凝固速度が小さくなるとともに、冷却体
と溶融アルミニウムとの間の熱流が大きくなって、凝固
界面近傍の液相中の温度勾配が大きくなる。したがって
、上述した冷却体の回転による効果、ずなわら高純度ア
ルミニウムを得られるという効果は一層向上する。The cooling body is cooled by feeding a cold IJI body such as air, argon gas, nitrogen gas, or a mixed liquid of air and water into the cooling body. increasing the infusion delivered to the molten aluminum in the crucible by heating from an external heat source;
Moreover, if a large amount of heat is removed by cooling the molten aluminum with the cooling body, the solidification rate will decrease, and the heat flow between the cooling body and the molten aluminum will increase, increasing the temperature gradient in the liquid phase near the solidification interface. growing. Therefore, the effect of the rotation of the cooling body mentioned above and the effect of obtaining high-purity aluminum are further improved.
連結樋および排出樋は、アルミニウム溶湯が前方へ進む
場合、回転冷却体が平面がら見て時バ]方向に回転さμ
られるときには、るつぼの中心どうしを結ぶ直線よりも
左側に偏った位置に配置され、回転冷却体が平面から見
て反時計方向に回転させられるときには、るつぼの中心
どうしを結ぶDI線にりも右側に偏った位置に配置され
る。したがって、回転冷却体の回転により生じた遠心力
により高純度アルミニウムの製造作業中に発生したアル
ミニウム酸化物は、連結樋を通つく前りのるつぼに流れ
、JJI出樋を通ってスムーズに除去される。The connecting gutter and the discharge gutter are designed so that when the molten aluminum advances forward, the rotating cooling body rotates in the direction of
When the rotary cooling body is rotated counterclockwise when viewed from a plane, it is placed to the left of the straight line connecting the centers of the crucibles, and to the right of the DI line connecting the centers of the crucibles. It is placed in a position that is biased towards. Therefore, the aluminum oxide generated during the production of high-purity aluminum due to the centrifugal force generated by the rotation of the rotary cooling body flows through the connecting gutter to the crucible before passing through the JJI tap and is smoothly removed. Ru.
このような1OIIIi度アルミニウムの製造装置にお
いて、あらかじめ冷111体を上がさけておき、溶解炉
からるつぼへアルミニウム溶湯を供給して各るつぼ内の
溶湯量が等しくなってから冷却体を下降させて溶湯中に
浸漬し回転さける。そして、各るつぼ中の溶湯■が操業
中不変となるように、溶湯供給ffi d5よび排出室
を調整するとともに、各冷却体の周面に晶出するアルミ
ニウムの石が等しくなるように調整する。冷却体の周面
に晶出するアルミニウム量は、溶湯の温度、冷却体の回
転数、冷却能、浸油時間により適宜変更づ゛ることがで
きる。各るつぼにお()る溶湯中の不純物1I11度は
、溶解炉に近いものから遠ざかるにつれ゛C順次高くな
っている。各冷1]体によって回収されるアルミニウム
の合ii1’ 7′i1の、1ハ給された溶湯の合計■
に対する比(以下、この比を回収率という)を変えるこ
とによって1′1られる全でのアルミニウム中の平均不
純物濃度を変えることができ、回収率が小さいほど上記
平均不純物m度は低くなる。したがって、上記回収率を
所定の値にづ゛ることによって溶解炉から供給される元
の精製すべきアルミニウムよりも高IT! 1.ffの
アルミニウムを1gることかできる。また、回収率を一
定に保った場合には、るつぼの数が多いはど高純度のア
ルミニウムを得ることができる。In such a manufacturing apparatus for 1OIIIi degree aluminum, the cold body is raised in advance, molten aluminum is supplied from the melting furnace to the crucibles, and the amount of molten metal in each crucible becomes equal, and then the cooling body is lowered. Immerse it in molten metal and avoid rotating it. Then, the molten metal supply ffi d5 and the discharge chamber are adjusted so that the molten metal (1) in each crucible remains unchanged during operation, and the aluminum stones crystallized on the circumferential surface of each cooling body are adjusted to be equal. The amount of aluminum crystallized on the circumferential surface of the cooling body can be changed as appropriate depending on the temperature of the molten metal, the rotational speed of the cooling body, the cooling capacity, and the oil immersion time. The impurity 1I11 degree in the molten metal in each crucible increases successively from the one closest to the melting furnace to the further away from the melting furnace. The total amount of aluminum recovered by each cold body ii1'7'i1, the total amount of molten metal fed into the
By changing the ratio to aluminum (hereinafter referred to as recovery rate), the average impurity concentration in the total aluminum can be changed, and the smaller the recovery rate, the lower the above average impurity concentration. Therefore, by setting the above-mentioned recovery rate to a predetermined value, it is possible to obtain a higher IT! 1. It is possible to produce 1 g of ff aluminum. Furthermore, if the recovery rate is kept constant, high purity aluminum can be obtained with a large number of crucibles.
」−述のように、この発明の高純度アルミニウムの連続
vJ造装置によれば、すべての連結樋おJ、び溶湯排出
樋が平面から見てるつぼの中心どうしを結ぶ直線と平行
な直線上に位置させられているので、精製作業中に各る
つぼ内のアルミニウム溶湯中に発生づるアルミニウム酸
化物も、回転冷fJI体の回転により生じた遠心力によ
って、連結樋J3J:び171出樋を通ってスムーズに
除去Jることがでさる。連結樋および排出樋がるつぼの
中心どうしを結ぶ直線上にある場合にはアルミニウム酸
化物はスムーズに前方に流れず、また連結Cmが、平面
から見て隣り合う2つのるつぼに共通づる接線上にある
場合には、一端前方のるつぼへ流れ込/vだものが逆流
Jるおイれがある。なお、この発明の装置によれば、溶
解炉で溶解されて後端のるつぼに供給されたアルミニウ
ム溶湯を、回転体の冷Jil1体の回転により生じる遠
心力によって前方のるつぼへスムーズに送ることができ
、にb純度アルミニウムを連続的にかつ効率よく製造す
ることがぐきる。” - As mentioned above, according to the high-purity aluminum continuous VJ production apparatus of the present invention, all the connection gutter and molten metal discharge gutter are on a straight line parallel to the straight line connecting the centers of the crucible when viewed from the plane. Since the aluminum oxides generated in the molten aluminum in each crucible during the refining work are also passed through the connection gutter J3J and the outlet gutter 171 by the centrifugal force generated by the rotation of the rotating cold fJI body. It can be removed smoothly. If the connecting gutter and the discharge gutter are on a straight line connecting the centers of the crucibles, the aluminum oxide will not flow forward smoothly, and if the connecting gutter Cm is on the tangent line common to two adjacent crucibles when viewed from the plane. In some cases, there is a backflow of something flowing into the crucible at one end in front. According to the device of the present invention, the molten aluminum melted in the melting furnace and supplied to the crucible at the rear end can be smoothly sent to the crucible at the front by the centrifugal force generated by the rotation of the cold body of the rotor. This makes it possible to continuously and efficiently produce high-purity aluminum.
この発明を、以下図面を参照しながら説明り−る。This invention will be explained below with reference to the drawings.
高純度アルミニウムの連続製造装置は、アルミニウムを
溶解する溶解炉(1)に続いて並べられた5つのるつぼ
(2Δ)〜(2E)と、後端のるつぼ(2△)内に配置
された撹拌機〈3)と、他の4つのるつぼ(2B)〜(
2[E )中に1つずつ配置されてiJ3す、かつ上下
動自在である高純度アルミニウムを晶出するだめの回転
冷却体(4)とを備えている。The continuous production equipment for high-purity aluminum consists of a melting furnace (1) that melts aluminum, five crucibles (2Δ) to (2E) lined up next to each other, and a stirring pot located in the crucible (2Δ) at the rear end. machine (3) and the other four crucibles (2B) ~ (
2[E], and rotary cooling bodies (4) for crystallizing high-purity aluminum, which are movable up and down.
隣り合うるつぼ(2A)〜(2[)どうしは、上端部に
J3いて連結樋(5)によって連通状に接続され、後端
のるつぼ(2A)に溶解炉(1)から供給されるりフル
ミニラム溶湯を受りるための・受樋(6)が取付りられ
、前端のるつぼ(21三)の上端部に溶瀉排出側(7)
が取イリ(Jられ、了1べ−(の連結樋(5)、受樋(
6)および溶湯排出1iffi (7)が、平面から見
てるつぼ(2Δ)〜(211= )の中心どうしを結ぶ
直線と平行でがつhhに(−)った直線上に位置させら
れている。Adjacent crucibles (2A) to (2[) are connected in a communicating manner by a connecting gutter (5) at the upper end, and the melting furnace (1) supplies full miniram molten metal to the crucible (2A) at the rear end. A receiving gutter (6) is installed to receive the melted slag discharge side (7) at the upper end of the crucible (213) at the front end.
Connecting gutter (5), receiving gutter (
6) and molten metal discharge 1iffi (7) are located on a straight line with a sharp hh (-) parallel to the straight line connecting the centers of the crucibles (2Δ) to (211= ) when viewed from the plane. .
各るつぼ(2△)〜(2E)の周壁には、上縁から()
形のり欠ぎ(8)が形成され、この切欠き(8)のまわ
りの部分のうち下側J3よび右側において周壁外面に凹
所(9)が設けられている。連結樋(5)は隣り合うる
っぽ(2A)〜(2E)の切欠き(8ンどぅしを連通さ
せるように配置されている。連結樋(5)は横断面()
形で、その前後両端がるっぽ(2Δ)〜(2I:3 )
の外周面に沿うJ:うにアール状となされている。On the peripheral wall of each crucible (2△) to (2E), from the upper edge ()
A shaped notch (8) is formed, and a recess (9) is provided in the outer surface of the peripheral wall on the lower side J3 and on the right side of the portion around this notch (8). The connecting gutter (5) is arranged so that the notches (8 pieces) of the adjacent corners (2A) to (2E) communicate with each other.The connecting gutter (5) has a cross section ()
In shape, both front and rear ends are round (2Δ) ~ (2I:3)
J along the outer circumferential surface of the sea urchin is rounded.
また、連結1ffi (5)の前後両端には切欠き(8
)内に挿入しうるIIl′1人部(1o)が突出状に訛
りられている。そして、連結樋(5)は挿入部(1o〉
が切欠さく8)内にfiti人されるとともに、下側お
よび右側の部分が凹所(9)に嵌め込まれた状rM −
’c ルっぽ(2Δ)〜(2E)に固定されている。受
樋(6)および排出樋(7)のるつぼ(2A>(2E)
への接続端部は連結tilfi(5)と同様な形状とさ
れ、連結樋(5)と同様にしてるつぼ(2A>(2E)
に固定されている。In addition, there are notches (8
) The human part (1o) that can be inserted into the middle part (1o) is accented in a protruding manner. The connecting gutter (5) is connected to the insertion part (1o)
is fitted into the notch (8), and the lower and right parts are fitted into the recess (9).
'c It is fixed at Ruppo (2Δ) ~ (2E). Crucible of receiving gutter (6) and discharge gutter (7) (2A>(2E)
The connecting end to the connecting tilfi (5) has the same shape as the connecting trough (5), and the crucible (2A>(2E)
is fixed.
回転冷却体(4)は下方に向って徐々に細くなりかつ両
端が閉塞された中空のテーパ筒状であり、黒鉛、しラミ
ックス等からつくられている。また、回転冷却体(4)
は中空回転軸(12)の下端に取付けられており、その
内部には、中空回転軸(12)内に配置された冷却流体
供給管(図丞略)から冷却流体が供給されるようになっ
ている。The rotary cooling body (4) has a hollow tapered cylindrical shape that gradually becomes thinner toward the bottom and is closed at both ends, and is made of graphite, shiramix, or the like. In addition, the rotary cooling body (4)
is attached to the lower end of the hollow rotating shaft (12), and cooling fluid is supplied to the inside thereof from a cooling fluid supply pipe (not shown) arranged inside the hollow rotating shaft (12). ing.
このような構成の高純度アルミニウムの連続製造装置に
おいて、溶解炉(1)内で溶融せられた精製リーベきア
ルミニウムは、各るつぼ(2Δ)〜(2[)に送り込ま
れる。この溶融アルミニウムに、Fe、Si、Ctll
MCIなどの共晶不純物の他に丁’ z VN Zrな
どのアルミニウムと包晶を生成する不純物(以下包晶不
純物という)が含まれている場合、左端のるつぼ(2A
)において、溶湯中にホウ素を添加して撹拌機(3)で
攪]1!覆ると、ホウ素がTi1■、Zr等の包晶不純
物と反応してTtB2、VB2 、Zr B2等の不溶
性金属ホウ化物が生成する。In the continuous manufacturing apparatus for high-purity aluminum having such a configuration, refined rivet aluminum melted in the melting furnace (1) is fed into each of the crucibles (2Δ) to (2[). This molten aluminum contains Fe, Si, Ctll.
In addition to eutectic impurities such as MCI, if impurities that form peritectics with aluminum such as Zr are included (hereinafter referred to as peritectic impurities), the leftmost crucible (2A
), add boron to the molten metal and stir with the stirrer (3)] 1! When covered, boron reacts with peritectic impurities such as Ti1 and Zr to form insoluble metal borides such as TtB2, VB2 and ZrB2.
各るつぼ(2B ) ” (2E ) kl: # 4
:J’ Z>溶湯mが所定量に達したときに、冷却体(
4)を十降さUて溶湯中に浸漬し、その内部に冷却流体
を供給しつつこれを回転させる。すると、回転冷却体(
4)の周面にだ番ノ高@度アルミニウムが晶出する。共
晶不純物および左端のるつぼ(2A)で添加した余剰の
ホウ素は、液相中にJjF出され、冷却体(4)の回転
により生じる遠心ツノによって冷却体(4)から遠さく
ノられる。1、た、溶融アルミニウム中に含まれていた
金属ホウ化物も回転冷却体(4)の回転により生じる遠
心力により回転冷却体(4)から遠ざけられるので、回
転冷却体(4)の周面に晶出した”アルミニウムに金属
ホウ化物が含まれることはなくなる。こうして、溶解炉
(1)から供給される元の精製リベきアルミニウムより
も高純度のアルミニウムが得られる。Each crucible (2B)” (2E) kl: #4
:J'Z>When the molten metal m reaches a predetermined amount, the cooling body (
4) is lowered ten times and immersed in the molten metal, and is rotated while supplying cooling fluid to the inside. Then, the rotating cooling body (
4) High-grade aluminum crystallizes on the surrounding surface. The eutectic impurities and the excess boron added in the crucible (2A) on the left end are ejected into the liquid phase and are removed from the cooling body (4) by the centrifugal horn generated by the rotation of the cooling body (4). 1. Metal borides contained in the molten aluminum are also moved away from the rotary cooling body (4) by the centrifugal force generated by the rotation of the rotary cooling body (4), so that the metal borides contained in the molten aluminum are moved away from the rotary cooling body (4), so that they are The crystallized "aluminum" no longer contains metal borides. In this way, aluminum of higher purity than the original purified aluminum supplied from the melting furnace (1) is obtained.
また、回転冷却体(4)が回転することにより生ずる遠
心力にJ:す、精製作業中に各るつぼ(2B)〜(2F
)中で生じたアルミニウム酸化物は連結樋(5)を通っ
て前端のるつぼ(2F)にスムーズに送られ、JJI出
6im (7)を通って除去される。In addition, due to the centrifugal force generated by the rotation of the rotary cooling body (4), each crucible (2B) to (2F) is
) is smoothly sent to the front end crucible (2F) through the connecting trough (5) and removed through the JJI outlet (7).
図面はこの発明の実施例を示し、第1図は垂直縦断面図
、第2図は一部省略平面図、第3図は第2図の部分拡大
図、第4図は第3図のIV −IV線にそう断面図、第
5図はるつぼと連結樋との接続状態を示す分解斜視図で
ある。
(1)・・・溶解炉、(2B)〜(2E)・・・るつぼ
、(4)・・・回転冷月1体、(5)・・・連結樋、(
7)・・・排出樋。
以 上The drawings show an embodiment of the present invention, and FIG. 1 is a vertical longitudinal cross-sectional view, FIG. 2 is a partially omitted plan view, FIG. 3 is a partially enlarged view of FIG. 2, and FIG. 4 is an IV view of FIG. 3. FIG. 5 is an exploded perspective view showing the state of connection between the crucible and the connecting gutter. (1)... Melting furnace, (2B) to (2E)... Crucible, (4)... 1 rotating cold moon, (5)... Connecting gutter, (
7)...Discharge gutter. that's all
Claims (1)
列に並べられた複数個のるつぼ(2B)〜(2[三)と
、各るつぼ(2B)〜(2F)内に1つずつ配置されて
おり、かつ上下動自在である高純度アルミニウムを晶出
させるための回転冷2J1体(4)とを備えており、隣
り合うるつぽ(2B)〜(2F)どうしが上端部におい
(連結(通く5)によって連通状に接続され、溶解炉(
1)から最も遠いるつぼ(2F)の上端部に溶湯jJl
出(通(7)が取イリけられ、すべての連結樋(5)
J3よび溶湯排出樋(7)が、平面から見てるつぼ(2
B)〜(2E)の中心どうしを結ぶ直線と平行な直線上
に位置させられ、溶解炉(1)に最も近いるつぼ(2B
)に溶解炉(1)からアルミニウム溶湯が送り込まれる
ようになされている、高純度アルミニウムの連続製T;
1装置。A melting furnace (1) for melting aluminum is followed by a plurality of crucibles (2B) to (2[3) arranged in a row, and one crucible is placed in each crucible (2B) to (2F). It is equipped with a rotary cooling 2J body (4) for crystallizing high-purity aluminum that can be moved up and down, and adjacent crucibles (2B) to (2F) are connected to each other at their upper ends. (through 5) and are connected in a continuous manner through the melting furnace (
Molten metal jJl is placed at the upper end of the crucible (2F) farthest from 1).
The outlet (7) has been removed and all connecting gutters (5) have been removed.
J3 and the molten metal discharge gutter (7) are connected to the crucible (2) when viewed from above.
The crucible (2B) that is located on a straight line parallel to the straight line connecting the centers of
) is a continuous production T made of high-purity aluminum, into which molten aluminum is fed from a melting furnace (1);
1 device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4593584A JPS60190534A (en) | 1984-03-09 | 1984-03-09 | Apparatus for continuous production of high-purity aluminum |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4593584A JPS60190534A (en) | 1984-03-09 | 1984-03-09 | Apparatus for continuous production of high-purity aluminum |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60190534A true JPS60190534A (en) | 1985-09-28 |
JPS6147890B2 JPS6147890B2 (en) | 1986-10-21 |
Family
ID=12733123
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4593584A Granted JPS60190534A (en) | 1984-03-09 | 1984-03-09 | Apparatus for continuous production of high-purity aluminum |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60190534A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001107154A (en) * | 1999-09-03 | 2001-04-17 | Norsk Hydro Asa | Device for treating liquid |
CN111549236A (en) * | 2019-02-28 | 2020-08-18 | 宁波锦越新材料有限公司 | Linkage piece of purifying and crystallizing device for ultra-high-purity aluminum |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07250781A (en) * | 1994-03-16 | 1995-10-03 | Toto Ltd | Sterilizing device of portable private parts flushing device |
-
1984
- 1984-03-09 JP JP4593584A patent/JPS60190534A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001107154A (en) * | 1999-09-03 | 2001-04-17 | Norsk Hydro Asa | Device for treating liquid |
CN111549236A (en) * | 2019-02-28 | 2020-08-18 | 宁波锦越新材料有限公司 | Linkage piece of purifying and crystallizing device for ultra-high-purity aluminum |
Also Published As
Publication number | Publication date |
---|---|
JPS6147890B2 (en) | 1986-10-21 |
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