JP2662178B2 - Aluminum scrap refining equipment - Google Patents

Aluminum scrap refining equipment

Info

Publication number
JP2662178B2
JP2662178B2 JP35045793A JP35045793A JP2662178B2 JP 2662178 B2 JP2662178 B2 JP 2662178B2 JP 35045793 A JP35045793 A JP 35045793A JP 35045793 A JP35045793 A JP 35045793A JP 2662178 B2 JP2662178 B2 JP 2662178B2
Authority
JP
Japan
Prior art keywords
primary crystal
molten metal
crystal particle
container
pressing
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.)
Expired - Fee Related
Application number
JP35045793A
Other languages
Japanese (ja)
Other versions
JPH07197140A (en
Inventor
貴之 五月女
光弘 大滝
秀明 工藤
利仁 小又
弘一 尾原
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.)
Furukawa Electric Co Ltd
Original Assignee
Furukawa Electric 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 Furukawa Electric Co Ltd filed Critical Furukawa Electric Co Ltd
Priority to JP35045793A priority Critical patent/JP2662178B2/en
Publication of JPH07197140A publication Critical patent/JPH07197140A/en
Application granted granted Critical
Publication of JP2662178B2 publication Critical patent/JP2662178B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、アルミスクラップ、特
にアルミブレージングシートを効率よく精製し得る装置
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for efficiently purifying aluminum scrap, particularly aluminum brazing sheet.

【0002】[0002]

【従来の技術】FeやSi等の元素を含有するアルミス
クラップの効率的精製技術の開発は、資源の有効活用並
びに原料費削減に対する最重要課題である。例えば自動
車用のアルミ製ラジエータの冷媒を通すチューブには、
Al−1wt%Mn合金(JIS−3003等)の芯材にAl−3
wt%Si合金(JIS−4043等)の皮材をクラッドした複合
材が用いられており、その製造過程で圧延材のスリッタ
ー屑等が大量に発生する。このようなアルミスクラップ
は、大半がそのまゝ鋳物用低級地金として再利用されて
いる。この複合材が展伸材の原料に転回できれば原料費
の大幅な低減が計れ、延いては資源の有効活用に繋が
る。
2. Description of the Related Art Development of an efficient technology for refining aluminum scrap containing elements such as Fe and Si is the most important issue for effective utilization of resources and reduction of raw material costs. For example, a tube through which the refrigerant of an aluminum radiator for automobiles passes
Al-3 wt% Mn alloy (JIS-3003 etc.) core material is Al-3
A composite material clad with a skin material of a wt% Si alloy (such as JIS-4043) is used, and in the manufacturing process, a large amount of slitter dust and the like of rolled material is generated. Most of such aluminum scrap is reused as a low-grade ingot for casting. If this composite material can be turned into a raw material for wrought material, the cost of the raw material can be significantly reduced, which in turn leads to effective utilization of resources.

【0003】アルミスクラップの精製方法として結晶分
別法がある。この方法は、先に、本発明者等が提案した
もので(特願平5-202361) 、その要旨は、容器内にアル
ミスクラップ溶湯を保持し、この溶湯の液相線以下、固
相線以上の温度範囲内で、この溶湯のほぼ全域を20℃/
min.以下の速度で冷却して、純化された初晶粒子を生成
させ、前記容器の上方から加圧スタンプを降下させて前
記容器下部に初晶粒子を押圧し、この初晶粒子押圧体を
残部溶湯から分離して回収する方法である。初晶粒子
は、樹枝状を呈し、この樹枝間にトラップされた高濃度
液相金属を初晶粒子押圧体から絞り出す為に、初晶粒子
は2〜15MPa の高圧力をかけて押圧される。
[0003] As a method of purifying aluminum scrap, there is a crystal fractionation method. This method has been previously proposed by the present inventors (Japanese Patent Application No. 5-202361), and the gist of the method is to hold a molten aluminum scrap in a container and to use a solidus line below the liquidus line of the molten metal. Within the above temperature range, almost the entire area of this molten
cooling at a speed of min. or less, to generate purified primary crystal particles, press down the pressure stamp from above the container to press the primary crystal particles to the lower portion of the container, and press the primary crystal particle pressing body. This is a method of separating and collecting the remaining molten metal. The primary crystal particles have a dendritic shape, and the primary crystal particles are pressed by applying a high pressure of 2 to 15 MPa in order to squeeze the high-concentration liquid phase metal trapped between the tree branches from the primary crystal particle pressing body.

【0004】[0004]

【発明が解決しようとする課題】前述の精製方法によ
り、大量のアルミスクラップを処理する場合、初晶粒子
の生成、残部溶湯の排出、初晶粒子の回収に多大な時間
を要した。その上、この方法では初晶粒子の生成と押
圧、それに続く残部溶湯の排出、初晶粒子の回収という
一連の作業を、溶湯保持容器を1か所に置いて行う為に
各々の器具の稼働率並びに生産性が低かった。
When a large amount of aluminum scrap is treated by the above-mentioned refining method, it takes a lot of time to generate primary crystal particles, discharge the remaining molten metal, and collect primary crystal particles. In addition, in this method, a series of operations such as generation and pressing of primary crystal particles, subsequent discharge of the remaining molten metal, and recovery of primary crystal particles are performed by operating each of the instruments so that the molten metal holding container is placed in one place. The rate and productivity were low.

【0005】[0005]

【課題を解決するための手段】本発明は、このような状
況の中で鋭意研究を行いなされたもので、アルミスクラ
ップを効率よく精製する装置を提供することを目的とす
る。即ち、請求項1の発明は、溶湯保持容器内に保持さ
れたアルミスクラップ溶湯を、この溶湯の液相線以下、
固相線以上の温度範囲内で保持して生成させた前記溶湯
中の初晶粒子を、前記溶湯保持容器底部に高圧力で押圧
する初晶粒子押圧器具、初晶粒子押圧体上方の残部溶湯
を前記容器内から排出する残部溶湯排出器具、初晶粒子
押圧体を容器から回収する初晶粒子回収器具からなるア
ルミスクラップの精製装置において、前記の初晶粒子押
圧器具、残部溶湯排出器具、初晶粒子回収器具が順次所
定間隔を開けて設置され、初晶粒子回収器具と初晶粒子
押圧器具との間に、溶湯が供給される前の段階で、溶湯
保持容器を予熱する為の走間炉が配置されており、前記
各々の器具は、前記容器を移送する為のコンベヤの所定
位置に順次配置されていることを特徴とするものであ
る。
SUMMARY OF THE INVENTION The present invention has been intensively studied in such a situation, and an object of the present invention is to provide an apparatus for efficiently purifying aluminum scrap. In other words, the invention of claim 1 is to reduce the aluminum scrap molten metal held in the molten metal holding container to a temperature below the liquidus line of the molten metal.
A primary crystal pressing device that presses the primary crystal particles in the molten metal held and generated within a temperature range equal to or higher than the solidus line to the bottom of the molten metal holding container with a high pressure, and the remaining molten metal above the primary crystal particle pressing body. In the aluminum scrap refining apparatus, comprising: a molten metal discharging device for discharging the molten metal from the container; and a primary crystal particle collecting device for recovering the primary crystal particle pressing body from the container. A crystal particle collecting device is sequentially installed at a predetermined interval, and a gap between the primary crystal particle collecting device and the primary crystal particle pressing device for preheating the molten metal holding vessel at a stage before the molten metal is supplied. A furnace is arranged, and the appliances are sequentially arranged at predetermined positions on a conveyor for transferring the containers.

【0006】この発明において、溶湯保持容器内に保持
されたアルミスクラップ溶湯に、初晶粒子を生成させる
には、前記溶湯を自然冷却して行う他、初晶粒子生成器
具を用いて冷却速度を人為的に制御して行うこともでき
る。請求項2は後者の場合の装置で、その構成は、溶湯
保持容器内に保持されたアルミスクラップ溶湯を、この
溶湯の液相線以下、固相線以上の温度範囲内で所定速度
で冷却して初晶粒子を生成させる初晶粒子生成器具、溶
湯中に生成した初晶粒子を前記溶湯保持容器底部に高圧
力で押圧する初晶粒子押圧器具、初晶粒子押圧体上方の
残部溶湯を前記容器内から排出する残部溶湯排出器具、
初晶粒子押圧体を容器から回収する初晶粒子回収器具か
らなるアルミスクラップの精製装置において、前記の初
晶粒子生成器具、初晶粒子押圧器具、残部溶湯排出器
具、初晶粒子回収器具が順次所定間隔を開けて設置さ
れ、初晶粒子回収器具と初晶粒子生成器具との間に、溶
湯が供給される前の段階で、溶湯保持容器を予熱する為
の走間炉が配置されており、前記各々の器具は、前記容
器を移送する為のコンベヤの所定位置に順次配置されて
いることを特徴とするものである。
In the present invention, in order to generate primary crystal particles in the aluminum scrap molten metal held in the molten metal holding container, the molten metal is naturally cooled, and the cooling rate is reduced by using a primary crystal particle generating device. It can also be controlled artificially. A second aspect of the present invention is an apparatus for the latter case, which is configured to cool the aluminum scrap molten metal held in the molten metal holding vessel at a predetermined speed within a temperature range below the liquidus line and above the solidus line of the molten metal. A primary crystal particle generating device for generating primary crystal particles, a primary crystal particle pressing device for pressing the primary crystal particles generated in the molten metal to the bottom of the molten metal holding container at a high pressure, and the remaining molten metal above the primary crystal particle pressing body. Remaining molten metal discharge device to be discharged from the container,
In an aluminum scrap refining apparatus comprising a primary crystal particle recovery device for recovering a primary crystal particle pressing body from a container, the primary crystal particle generation device, the primary crystal particle pressing device, the remaining molten metal discharge device, and the primary crystal particle recovery device are sequentially arranged. It is installed at a predetermined interval, and between the primary crystal particle collection device and the primary crystal particle generation device, at a stage before the molten metal is supplied, a running furnace for preheating the molten metal holding vessel is arranged. , Each of the devices is sequentially arranged at a predetermined position on a conveyor for transferring the containers.

【0007】初晶粒子生成器具には、溶湯保持容器の外
周に密着配備させて用いる冷却ジャケットや溶湯中に浸
漬させる内部通水型冷却子等がある。溶湯を十分徐冷さ
せるときは、容器に加熱器を配備する。加熱器には、電
磁誘導加熱器が、溶湯の攪拌作用を有し、溶湯の温度及
び濃度分布を均一にできて好ましい。攪拌には、溶湯中
に浸漬して用いるプロペラ式攪拌器も適用される。溶湯
保持容器は、耐熱鋼製の殻にキャスタブル耐火物を内張
りしたもの等、高押圧力に耐えられるものが適用され
る。中でも黒鉛等の離型性に優れたものは特に好まし
い。溶湯保持容器の断面形状は円形、角形等任意であ
る。溶湯保持容器を移送する移送体は、ローラー式コン
ベヤや台車等である。
[0007] Examples of the primary crystal particle generating device include a cooling jacket that is used in close contact with the outer periphery of a molten metal holding container, and an internal water-cooling type cooler that is immersed in the molten metal. When cooling the molten metal sufficiently, a heater is provided in the container. As the heater, an electromagnetic induction heater is preferable because it has a function of stirring the molten metal and can make the temperature and concentration distribution of the molten metal uniform. For the stirring, a propeller type stirrer immersed in a molten metal is also used. As the molten metal holding container, a material capable of withstanding a high pressing force, such as a material in which a castable refractory is lined with a heat-resistant steel shell is applied. Among them, those excellent in releasability such as graphite are particularly preferable. The cross-sectional shape of the molten metal holding container is arbitrary, such as circular or square. A transfer body for transferring the molten metal holding container is a roller type conveyor, a cart, or the like.

【0008】前記請求項1及び請求項2の発明におい
て、溶湯の冷却速度は、20℃/min. 以下が得られる初晶
粒子の純度が高く好ましい。又初晶粒子の押圧力は2M
Pa 未満では初晶粒子にトラップされた高濃度液相金属
を十分に絞り出せず、又15MPa を超えても高濃度液相
金属の絞り出しが飽和する。従って2〜15MPa が適当
である。
In the first and second aspects of the present invention, the cooling rate of the molten metal is preferably 20 ° C./min. Or less. The pressing force of the primary crystal particles is 2M.
If it is less than Pa, the high-concentration liquid metal trapped in the primary crystal particles cannot be sufficiently squeezed out, and if it exceeds 15 MPa, the squeezing of the high-concentration liquid metal will be saturated. Therefore, 2 to 15 MPa is appropriate.

【0009】[0009]

【作用】請求項1の発明では、初晶粒子押圧器具、残部
溶湯排出器具、初晶粒子回収器具が順次所定間隔を開け
て設置され、初晶粒子回収器具と初晶粒子押圧器具との
間に、溶湯が供給される前の段階で、溶湯保持容器を予
熱する為の走間炉が配置されており、前記各々の器具
は、前記容器を移送する為のコンベヤの所定位置に順次
配置されているので、溶湯保持容器を複数個用意し、こ
れを移送体に載せて各々の器具間を移送することによ
り、同時に複数の処理を行うことができ、依って、器具
稼働率並びに生産性が向上する。請求項2の発明は、請
求項1の発明装置に初晶粒子生成器具を付加してアルミ
スクラップ溶湯の冷却速度を人為的に制御できるように
したもので、初晶粒子の高純度化が可能となる。
According to the first aspect of the present invention, the primary crystal particle pressing device, the remaining molten metal discharging device, and the primary crystal particle collecting device are sequentially installed at predetermined intervals, and the primary crystal particle collecting device and the primary crystal particle pressing device are disposed between the primary crystal pressing device and the primary crystal pressing device. In a stage before the molten metal is supplied, a running furnace for preheating the molten metal holding container is arranged, and the respective appliances are sequentially arranged at predetermined positions on a conveyor for transferring the container. Therefore, by preparing a plurality of molten metal holding containers, placing them on a transfer body and transferring between the respective devices, it is possible to perform a plurality of processes at the same time, so that the device operation rate and productivity are improved. improves. According to the second aspect of the present invention, a primary crystal particle generating device is added to the apparatus according to the first aspect of the present invention so that the cooling rate of the aluminum scrap melt can be artificially controlled, so that the primary crystal particles can be highly purified. Becomes

【0010】[0010]

【実施例】以下に本発明を実施例により詳細に説明す
る。 実施例1 図1〜図5は本発明装置を構成する各々の器具及び移動
体の実施例を示すそれぞれ側面図又は平面図である。図
1イ、ロは、初晶粒子生成器具のそれぞれ側面図及び平
面図である。初晶粒子生成器具1は、内部通水型の冷却
ジャケットで、溶湯保持容器2の外周に密着配備されて
いる。溶湯保持容器2は断面円形の耐熱鋼製の殻3に離
型材(黒鉛)4を内張りしたものである。図2は、初晶
粒子押圧器具の側面図である。初晶粒子押圧器具5は、
溶湯中に浸漬する加圧スタンプ6と、それに押圧力を伝
達する油圧シリンダ7から構成されている。交換用加圧
スタンプ23は、レール24上を平行に運搬される。図3
イ、ロは、残部溶湯排出器具の側面図である。残部溶湯
排出器具8は溶湯保持容器2を傾動させる油圧クレーン
9と図示しない残部溶湯貯留槽から構成されている(図
3イ)。油圧クレーン9のフック10を溶湯保持容器2の
外周下部の把手11に掛けて引き上げる(図3ロ)。図4
イ、ロは、初晶粒子回収器具の側面図である。初晶粒子
回収器具12は溶湯保持容器2を両側から挟む軸回転可能
な一対の支持体13からなる(図4イ)。支持体13を軸回
転させて初晶粒子押圧体5を落下させる(図4ロ)。図
5は、移送体の平面図である。この移送体14は、環状の
ローラー式コンベヤである。
The present invention will be described below in detail with reference to examples. Embodiment 1 FIGS. 1 to 5 are side views or plan views, respectively, showing an embodiment of each device and a moving body constituting the apparatus of the present invention. 1A and 1B are a side view and a plan view, respectively, of a primary crystal particle generation device. The primary crystal particle producing device 1 is a cooling jacket of an internal water flow type, and is provided in close contact with the outer periphery of the molten metal holding container 2. The molten metal holding container 2 has a shell 3 made of heat-resistant steel having a circular cross section and a release material (graphite) 4 lined. FIG. 2 is a side view of the primary crystal particle pressing device. The primary crystal particle pressing device 5
It comprises a pressure stamp 6 immersed in the molten metal and a hydraulic cylinder 7 for transmitting a pressing force to the stamp. The replacement pressure stamp 23 is transported in parallel on the rail 24. FIG.
(A) and (b) are side views of the remaining molten metal discharging device. The remaining molten metal discharge device 8 includes a hydraulic crane 9 for tilting the molten metal holding container 2 and a residual molten metal storage tank (not shown) (FIG. 3A). The hook 10 of the hydraulic crane 9 is hung on the handle 11 at the lower part of the outer periphery of the molten metal holding container 2 and pulled up (FIG. 3B). FIG.
(A) and (b) are side views of the primary crystal particle collection device. The primary crystal particle collecting device 12 is composed of a pair of axially rotatable supports 13 sandwiching the molten metal holding container 2 from both sides (FIG. 4A). The support 13 is rotated about its axis to drop the primary crystal pressing body 5 (FIG. 4B). FIG. 5 is a plan view of the transfer body. The transfer body 14 is an annular roller type conveyor.

【0011】図6イ〜ハは初晶粒子生成から残部溶湯排
出までの状況説明図である。初晶粒子生成器具1にて初
晶粒子15が生成され(図6イ)、初晶粒子押圧器具の加
圧スタンプ6にて初晶粒子15が押圧され(図6ロ)、残
部溶湯排出器具で残部溶湯16が排出される(図6ハ)。
FIGS. 6A to 6C are explanatory views of the state from the formation of primary crystal grains to the discharge of the remaining molten metal. The primary crystal particles 15 are generated by the primary crystal particle generation device 1 (FIG. 6A), and the primary crystal particles 15 are pressed by the press stamp 6 of the primary crystal particle pressing device (FIG. 6B), and the remaining molten metal discharge device. Then, the remaining molten metal 16 is discharged (FIG. 6C).

【0012】以下に本発明装置を図を参照して具体的に
説明する。図7は、図1〜5に示した各々の器具及び移
送体にて構成した本発明装置の実施例を示す平面図であ
る。初晶粒子生成器具1、初晶粒子押圧器具5、残部溶
湯排出器具8、初晶粒子回収器具12が、環状のローラー
式コンベヤの移送体14の所定位置に順次設置されて、そ
れぞれ初晶粒子生成ゾーン、初晶粒子押圧ゾーン、残部
溶湯排出ゾーン、初晶粒子回収ゾーンを形成している。
Hereinafter, the apparatus of the present invention will be specifically described with reference to the drawings. FIG. 7 is a plan view showing an embodiment of the apparatus of the present invention constituted by the respective instruments and transfer bodies shown in FIGS. A primary crystal particle generating device 1, a primary crystal pressing device 5, a residual molten metal discharging device 8, and a primary crystal particle collecting device 12 are sequentially installed at predetermined positions of a transfer body 14 of an annular roller type conveyor, and primary crystal particles are respectively provided. A formation zone, a primary crystal particle pressing zone, a residual molten metal discharge zone, and a primary crystal particle recovery zone are formed.

【0013】次に、前記装置を用いてアルミ合金溶湯を
連続的に精製する実施例を図7を参照して説明する。環
状のローラー式コンベヤの移送体14上に7台の溶湯保持
容器(以下容器と略記する)31〜37が配置されている。
そのうち、容器31,32は走間炉17内で予熱されている。
走間炉17で予熱されたあとの容器33には、溶湯18が溶解
炉19から樋20を通して供給される。溶湯18は液相線以上
の温度に加熱されている。次に初晶粒子生成ゾーンがあ
り、ここでは溶湯が保持された容器34が、その外周に冷
却ジャケットの初晶粒子生成器具1が密着配備されて、
液相線以下、固相線以上の温度範囲内で徐冷され、溶湯
中に初晶粒子が生成される。次の初晶粒子押圧ゾーンで
は、初晶粒子が生成した容器35内の溶湯の初晶粒子が加
圧スタンプにより容器35の底部に押圧される。加熱スタ
ンプ6は複数本用いられ、走間炉27内で予熱される。次
の残部溶湯排出ゾーンでは、初晶粒子が押圧された容器
36が、図3に示したように、その把手11に油圧クレーン
9のフック10を掛けて傾動され、内部の残部溶湯が残部
溶湯貯留槽21に排出される。最後の初晶粒子回収ゾーン
では、残部溶湯を排出した容器37が、両側面を図4に示
したように、一対の支持体13で挟持され、軸回転されて
初晶粒子が落下し回収箱22に回収される。初晶粒子が回
収された容器37は、次に走間炉17内に入り予熱される。
予熱を除く5工程は、処理時間が同一に仕組まれてお
り、処理が終了するとコンベヤのローラーが自動回転し
て、各々の容器31〜37は次の処理を受ける。
Next, an embodiment of continuously refining a molten aluminum alloy using the above-mentioned apparatus will be described with reference to FIG. Seven molten metal holding containers (hereinafter abbreviated as containers) 31 to 37 are arranged on a transfer body 14 of an annular roller type conveyor.
The containers 31 and 32 are preheated in the running furnace 17.
The molten metal 18 is supplied from the melting furnace 19 through the gutter 20 to the container 33 that has been preheated in the running furnace 17. The molten metal 18 is heated to a temperature higher than the liquidus line. Next, there is a primary crystal particle generation zone. In this case, the container 34 holding the molten metal, the primary crystal particle generation device 1 of the cooling jacket is closely mounted on the outer periphery thereof,
Slow cooling is performed within the temperature range below the liquidus line and above the solidus line, and primary crystal particles are generated in the molten metal. In the next primary crystal particle pressing zone, the primary crystal particles of the molten metal in the container 35 in which the primary crystal particles have been generated are pressed against the bottom of the container 35 by the pressure stamp. A plurality of heating stamps 6 are used, and are preheated in the running furnace 27. In the next remaining molten metal discharge zone, the container where the primary crystal particles were pressed
As shown in FIG. 3, the hook 36 of the hydraulic crane 9 is hung on the handle 11 and tilted, and the remaining molten metal inside is discharged to the remaining molten metal storage tank 21. In the last primary crystal recovery zone, a container 37 from which the remaining molten metal has been discharged is sandwiched between a pair of supports 13 as shown in FIG. Collected at 22. The container 37 in which the primary crystal particles have been recovered enters the traveling furnace 17 and is preheated.
The processing time is the same for the five processes except for preheating, and when the process is completed, the conveyor rollers are automatically rotated, and each of the containers 31 to 37 undergoes the next process.

【0014】この装置によれば、全ての処理器具を常時
稼働させることができる。生産性も用いる容器数に応じ
て増大する。いずれの処理も操作が簡単なので、容器の
移送を含め容易に自動化できる。
According to this apparatus, all the processing tools can be operated at all times. Productivity also increases with the number of containers used. Both processes are easy to operate, and can be easily automated, including the transfer of containers.

【0015】前記装置を用いて、Al−3wt%Si−1wt%
Mn合金のブレージングシートスクラップを10トン精製
した。一連の操作は自動化して、従来と同じ2人作業と
した。Al−0.9wt%Si−0.9wt%Mn組成の精製物が5
トン得られた。処理時間は従来のほぼ1/4に短縮され
た。この精製物を展伸材の原料にブレンドして用いた
が、バージン原料のみを用いた場合と同等品質の製品が
得られた。
Using the above apparatus, Al-3wt% Si-1wt%
10 tons of Mn alloy brazing sheet scrap was purified. A series of operations was automated, and the same two-person operation as before was performed. The purified product with the composition of Al-0.9wt% Si-0.9wt% Mn is 5
T got. The processing time has been reduced to almost 1/4 of the conventional one. This refined product was blended with the raw material of the wrought material and used, but a product of the same quality as when only the virgin raw material was used was obtained.

【0016】以上、Si及びMnを含有するアルミスク
ラップを精製する場合について説明したが、本発明装置
は他の合金元素を含有するアルミスクラップの精製に適
用しても同様の効果が得られる。又アルミスクラップ溶
湯の徐冷を初晶粒子生成器具(冷却ジャケット)を用い
て行ったが、自然冷却させて行うことも可能である。
Although the case where aluminum scrap containing Si and Mn is purified has been described above, the same effect can be obtained by applying the apparatus of the present invention to the purification of aluminum scrap containing another alloy element. In addition, although the slow cooling of the aluminum scrap melt was performed using a primary crystal particle generation device (cooling jacket), it may be performed by natural cooling.

【0017】[0017]

【効果】以上述べたように、本発明装置によれば、アル
ミスクラップ、特にアルミブレージングシートのスクラ
ップを効率よく精製でき、スクラップの大量処理が可能
となり、工業上顕著な効果を奏する。
As described above, according to the apparatus of the present invention, aluminum scrap, particularly scrap of aluminum brazing sheet, can be efficiently purified, and a large amount of scrap can be processed, which has a remarkable industrial effect.

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

【図1】本発明を構成する初晶粒子生成器具の実施例を
示す側面図及び平面図である。
FIG. 1 is a side view and a plan view showing an embodiment of a primary crystal particle producing device constituting the present invention.

【図2】本発明を構成する初晶粒子押圧器具の実施例を
示す側面図である。
FIG. 2 is a side view showing an embodiment of a primary crystal particle pressing device constituting the present invention.

【図3】本発明を構成する残部溶湯排出器具の実施例を
示す側面図である。
FIG. 3 is a side view showing an embodiment of a residual molten metal discharging device constituting the present invention.

【図4】本発明を構成する初晶粒子回収器具の実施例を
示す側面図である。
FIG. 4 is a side view showing an embodiment of a primary crystal particle collecting device constituting the present invention.

【図5】本発明を構成する移送体の実施例を示す平面図
である。
FIG. 5 is a plan view showing an embodiment of a transfer body constituting the present invention.

【図6】本発明における初晶粒子生成から残部溶湯排出
までの状況説明図である。
FIG. 6 is an explanatory diagram of the situation from generation of primary crystal particles to discharge of the remaining molten metal in the present invention.

【図7】本発明装置の実施例を示す平面図である。FIG. 7 is a plan view showing an embodiment of the device of the present invention.

【符号の説明】[Explanation of symbols]

1 初晶粒子生成器具 2 溶湯保持容器 3 耐熱鋼製殻 4 離型材 5 初晶粒子押圧体 6 加圧スタンプ 7 油圧シリンダ 8 残部溶湯排出器具 9 油圧クレーン 10 油圧クレーンのフック 11 溶湯保持容器の把手 12 初晶粒子回収器具 13 支持棒 14 移送体 15 初晶粒子 16 残部溶湯 17,27 走間炉 18 溶湯 19 溶解炉 20 樋 21 残部溶湯貯留槽 22 初晶粒子回収箱 23 交換用加圧スタンプ 24 レール 31〜37 溶湯保持容器 DESCRIPTION OF SYMBOLS 1 Primary crystal particle generator 2 Melt holding container 3 Heat resistant steel shell 4 Mold release material 5 Primary crystal particle pressing body 6 Press stamp 7 Hydraulic cylinder 8 Remaining molten metal discharge device 9 Hydraulic crane 10 Hydraulic crane hook 11 Handle for molten metal holding container 12 Primary crystal particle collection equipment 13 Support rod 14 Transfer body 15 Primary crystal particles 16 Remaining molten metal 17,27 Running furnace 18 Molten metal 19 Melting furnace 20 Gutter 21 Remaining molten metal storage tank 22 Primary crystal particle collection box 23 Press stamp for replacement 24 Rail 31-37 Molten holding container

───────────────────────────────────────────────────── フロントページの続き (72)発明者 尾原 弘一 東京都千代田区丸の内2丁目6番1号 古河電気工業株式会社内 審査官 諸岡 健一 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Koichi Ohara 2-6-1 Marunouchi, Chiyoda-ku, Tokyo Examiner, Furukawa Electric Co., Ltd. Kenichi Morooka

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 溶湯保持容器内に保持されたアルミスク
ラップ溶湯を、この溶湯の液相線以下、固相線以上の温
度範囲内で保持して生成させた前記溶湯中の初晶粒子
を、前記溶湯保持容器底部に高圧力で押圧する初晶粒子
押圧器具、初晶粒子押圧体上方の残部溶湯を前記容器内
から排出する残部溶湯排出器具、初晶粒子押圧体を容器
から回収する初晶粒子回収器具からなるアルミスクラッ
プの精製装置において、前記の初晶粒子押圧器具、残部
溶湯排出器具、初晶粒子回収器具が順次所定間隔を開け
て設置され、初晶粒子回収器具と初晶粒子押圧器具との
間に、溶湯が供給される前の段階で、溶湯保持容器を予
熱する為の走間炉が配置されており、前記各々の器具
は、前記容器を移送する為のコンベヤの所定位置に順次
配置されていることを特徴とするアルミスクラップの精
製装置。
1. The primary crystal particles in the aluminum scrap produced by holding the aluminum scrap molten metal held in the molten metal holding vessel in a temperature range below the liquidus line and above the solidus line of the molten metal, A primary crystal pressing device for pressing the bottom of the molten metal container with high pressure, a residual molten metal discharging device for discharging the remaining molten metal above the primary crystal particle pressing body from the container, and a primary crystal for recovering the primary crystal pressing body from the container. In the apparatus for purifying aluminum scrap comprising a particle recovery device, the primary crystal particle pressing device, the remaining molten metal discharge device, and the primary crystal particle recovery device are sequentially installed at predetermined intervals, and the primary crystal particle recovery device and the primary crystal particle pressing device are installed. With instruments
In the meantime, before the molten metal is supplied,
A running furnace for heating is arranged, and each of the above appliances is
Are sequentially disposed at predetermined positions on a conveyor for transferring said containers .
【請求項2】 溶湯保持容器内に保持されたアルミスク
ラップ溶湯を、この溶湯の液相線以下、固相線以上の温
度範囲内で所定速度で冷却して初晶粒子を生成させる初
晶粒子生成器具、溶湯中に生成した初晶粒子を前記溶湯
保持容器底部に高圧力で押圧する初晶粒子押圧器具、初
晶粒子押圧体上方の残部溶湯を前記容器内から排出する
残部溶湯排出器具、初晶粒子押圧体を容器から回収する
初晶粒子回収器具からなるアルミスクラップの精製装置
において、前記の初晶粒子生成器具、初晶粒子押圧器
具、残部溶湯排出器具、初晶粒子回収器具が順次所定間
隔を開けて設置され、初晶粒子回収器具と初晶粒子生成
器具との間に、溶湯が供給される前の段階で、溶湯保持
容器を予熱する為の走間炉が配置されており、前記各々
の器具は、前記容器を移送する為のコンベヤの所定位置
に順次配置されていることを特徴とするアルミスクラッ
プの精製装置。
2. Primary crystal particles for producing primary crystal particles by cooling an aluminum scrap molten metal held in a molten metal holding container at a predetermined speed in a temperature range below the liquidus line and above the solidus line of the molten metal. A generating device, a primary crystal particle pressing device for pressing the primary crystal particles generated in the molten metal to the bottom of the molten metal holding container at a high pressure, a residual molten metal discharging device for discharging the remaining molten metal above the primary crystal particle pressing body from the container, In an aluminum scrap refining apparatus comprising a primary crystal particle recovery device for recovering a primary crystal particle pressing body from a container, the primary crystal particle generation device, the primary crystal particle pressing device, the remaining molten metal discharge device, and the primary crystal particle recovery device are sequentially arranged. Installed at predetermined intervals, primary crystal particle collection equipment and primary crystal particle generation
Before the molten metal is supplied to the equipment, the molten metal is held
A running furnace for preheating the vessel is arranged,
Equipment is located at a predetermined position on the conveyor for transferring the containers.
An aluminum scrap refining device, which is sequentially arranged in a unit.
JP35045793A 1993-12-28 1993-12-28 Aluminum scrap refining equipment Expired - Fee Related JP2662178B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35045793A JP2662178B2 (en) 1993-12-28 1993-12-28 Aluminum scrap refining equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35045793A JP2662178B2 (en) 1993-12-28 1993-12-28 Aluminum scrap refining equipment

Publications (2)

Publication Number Publication Date
JPH07197140A JPH07197140A (en) 1995-08-01
JP2662178B2 true JP2662178B2 (en) 1997-10-08

Family

ID=18410631

Family Applications (1)

Application Number Title Priority Date Filing Date
JP35045793A Expired - Fee Related JP2662178B2 (en) 1993-12-28 1993-12-28 Aluminum scrap refining equipment

Country Status (1)

Country Link
JP (1) JP2662178B2 (en)

Also Published As

Publication number Publication date
JPH07197140A (en) 1995-08-01

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