JP2000273555A - Method for regenerating coated magnesium scrap - Google Patents

Method for regenerating coated magnesium scrap

Info

Publication number
JP2000273555A
JP2000273555A JP8006999A JP8006999A JP2000273555A JP 2000273555 A JP2000273555 A JP 2000273555A JP 8006999 A JP8006999 A JP 8006999A JP 8006999 A JP8006999 A JP 8006999A JP 2000273555 A JP2000273555 A JP 2000273555A
Authority
JP
Japan
Prior art keywords
molten metal
atmosphere
gas
waste material
coated magnesium
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.)
Granted
Application number
JP8006999A
Other languages
Japanese (ja)
Other versions
JP4136170B2 (en
Inventor
Kohei Kubota
耕平 久保田
Yoichi Nosaka
洋一 野坂
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 Mining and Smelting Co Ltd
Original Assignee
Mitsui Mining and Smelting 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 Mining and Smelting Co Ltd filed Critical Mitsui Mining and Smelting Co Ltd
Priority to JP08006999A priority Critical patent/JP4136170B2/en
Publication of JP2000273555A publication Critical patent/JP2000273555A/en
Application granted granted Critical
Publication of JP4136170B2 publication Critical patent/JP4136170B2/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
    • Y02P10/10Reduction of greenhouse gas [GHG] emissions
    • Y02P10/146Perfluorocarbons [PFC]; Hydrofluorocarbons [HFC]; Sulfur hexafluoride [SF6]
    • 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

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a regenerating method excellent in environmental properties in which the scrap of parts and products made of coated magnesium material is decomposed without using flux and also without generating harmful organic gas caused by the oxidation of a coating material, the coating material is decomposed, the decomposed products are removed, and it is regenerated. SOLUTION: Coated magnesium scrap is dissolved under the ordinary temp. or reduced pressure in a gaseous atmosphere of Ar, He, Ne, SF6, CO2, SO2 or N2, the molten metal is held under the pressure in the atmosphere, the coating material is decomposed into an inorganic matter, and the molten metal is then held under the reduced pressure in the atmosphere, by which the decomposed products in the coating material are removed.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は塗装されたマグネシ
ウム及びマグネシウム合金(本明細書においてはこれら
を総称してマグネシウム系又はマグネシウム系材料とい
う)廃材の再生方法に関し、より詳しくは、塗装された
マグネシウム系材料製の部品・製品のスクラップをフラ
ックスを用いることなく且つ塗料の酸化に伴う有害な有
機系ガスを発生させることなしで溶解させ、塗料を分解
させ、分解生成物を除去し、更に、溶湯中にマグネシウ
ム系材料の特性に悪影響を及ぼす量の酸化物等の異物が
存在する場合にはそれらの異物を浮上させ、分離して再
生する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for reclaiming painted magnesium and magnesium alloy (herein collectively referred to as magnesium-based or magnesium-based materials) waste, and more particularly to a method for refining painted magnesium and magnesium alloy. Dissolves scraps of parts and products made of system materials without using flux and without generating harmful organic gases due to oxidation of paint, decomposes paint, removes decomposition products, and further melts The present invention relates to a method for floating and separating and regenerating foreign substances such as oxides in an amount that adversely affects the properties of a magnesium-based material.

【0002】[0002]

【従来の技術】近年、軽量材料のニーズが高まり、樹脂
材料や軽量金属材料が用いられてきている。しかし、樹
脂材料は一般的にリサイクルが困難であるため環境性に
問題があるのに対して、金属材料は一般的にリサイクル
が容易であるため、マグネシウム系材料、アルミニウム
系材料等の実用軽量金属中最も密度の小さい軽量マグネ
シウム系材料が注目され、特に、自動車あるいは携帯用
家電製品用材料として注目される流れとなっている。
2. Description of the Related Art In recent years, the need for lightweight materials has increased, and resin materials and lightweight metal materials have been used. However, resin materials are generally difficult to recycle, and therefore have environmental problems. On the other hand, metal materials are generally easy to recycle, and practical lightweight metals such as magnesium-based materials and aluminum-based materials are used. Of these, lightweight magnesium-based materials having the smallest density have attracted attention, and in particular, have been attracting attention as materials for automobiles or portable home electric appliances.

【0003】マグネシウム系材料製の部品・製品は、ク
ロメート等の化成処理(酸化処理)を施した後、塗装を
施して使用されることが多い。このような塗装されたマ
グネシウム系材料製の部品・製品は、リサイクルに際
し、そのままで大気中、700℃近傍で溶解され、その
高温により塗料を燃焼させているのが現状である。塗料
の燃焼で発生するガス中には有機系のC4 9 4 N、
9 13N、C8 9 ON、C9 9 N、C5 152
N、C7 7 ON等が含まれ、多くの場合にダイオキシ
ンも発生する。リサイクル温度が高温であればあるほど
有機系ガス成分の単素数(炭素重合度)は小さくなり、
有害性は低下するが、マグネシウムの発火の危険性から
従来以上の高温での溶解処理は困難である。また、塗装
されたマグネシウム系廃材に限らずマグネシウムのリサ
イクルでは大量のフラックスが使用されるため環境への
影響も懸念される。
[0003] Parts and products made of a magnesium-based material are often used after being subjected to a chemical conversion treatment (oxidation treatment) such as chromate and then coated. At present, such painted parts and products made of a magnesium-based material are melted in the air at around 700 ° C. as they are, and the paint is burned by the high temperature. Organic C 4 H 9 O 4 N,
C 9 H 13 N, C 8 H 9 ON, C 9 H 9 N, C 5 H 15 O 2
N, C 7 H 7 ON and the like, and in many cases, dioxin is also generated. The higher the recycling temperature, the lower the unit number (carbon polymerization degree) of the organic gas component,
Although the toxicity is reduced, it is difficult to dissolve at a higher temperature than before because of the danger of magnesium ignition. Also, recycling of magnesium, not limited to painted magnesium waste, involves a large amount of flux, so there is a concern about environmental impact.

【0004】[0004]

【発明が解決しようとする課題】前記したように、マグ
ネシウム系材料が樹脂材料に比較して環境性・リサイク
ル性の点で優位性を有することが、特に最近のマグネシ
ウムの用途拡大の大きな駆動力になっていることから
も、またマグネシウムの需要が世界的に急拡大している
ので、今後、塗装されたマグネシウム系材料製の部品・
製品のスクラップが大量に発生すると予想されることか
らも、塗装されたマグネシウム系材料製の部品・製品の
リサイクル技術の確立が求められている。
As described above, the fact that a magnesium-based material has an advantage in terms of environmental friendliness and recyclability as compared with a resin material is a great driving force particularly in recent applications of magnesium. And the demand for magnesium is rapidly expanding worldwide, so parts and parts made of painted magnesium-based materials will be used in the future.
Since it is expected that a large amount of product scrap will be generated, it is required to establish a recycling technology for painted magnesium-based parts and products.

【0005】従って、本発明は、塗装されたマグネシウ
ム系材料製の部品・製品のスクラップをフラックスを用
いることなく且つ塗料の酸化に伴う有害な有機系ガスを
発生させることなしで溶解させ、塗料を分解させ、分解
生成物を除去して再生する、環境性に優れた再生方法を
提供することを課題としている。更に、マグネシウム系
材料の特性に悪影響を及ぼす量の酸化物等の異物が溶湯
中に存在する場合には、それらの異物を浮上させ、分離
して再生する方法に関する。
Accordingly, the present invention provides a method for dissolving scraps of painted parts and products made of a magnesium-based material without using a flux and without generating harmful organic gases accompanying the oxidation of the paint. It is an object of the present invention to provide an environmentally-friendly regeneration method for decomposing and removing decomposition products for regeneration. Further, the present invention relates to a method of floating, separating, and regenerating foreign substances such as oxides in a molten metal in an amount that adversely affects the properties of the magnesium-based material.

【0006】[0006]

【課題を解決するための手段】本発明者等は、上記課題
を達成するために鋭意検討した結果、塗装されたマグネ
シウム系材料製の部品・製品のスクラップを、酸素分圧
が極めて低く、溶湯に悪影響を与えない雰囲気中で溶解
させ、その溶湯をその雰囲気中に保持することにより塗
料を酸化させずに無機物に分解でき、また減圧下に保持
することによりその分解生成物が除去できることを見出
し、本発明に到達した。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies in order to achieve the above object, and as a result, it has been found that scraps of painted magnesium-based materials and parts have extremely low oxygen partial pressure, It has been found that it is possible to dissolve the coating in an atmosphere that does not have an adverse effect on the coating and to decompose the coating material into inorganic substances without oxidizing the coating by holding the molten metal in the atmosphere, and to remove the decomposition products by holding the coating under reduced pressure. Reached the present invention.

【0007】更に、上記のようにして塗料成分の分解、
除去された溶湯中に特定のガスを吹込んで該溶湯中に含
まれる酸化物、スラッジ、塗料の分解残留物等の異物を
浮上させ、分離することにより該溶湯を一層充分に清浄
化、再生できることを見いだし、本発明に到達した。
[0007] Further, as described above,
Injection of a specific gas into the removed molten metal to float foreign matters such as oxides, sludge, and decomposition residues of paint contained in the molten metal, and to separate and separate the molten metal more sufficiently to clean and regenerate the molten metal. And arrived at the present invention.

【0008】即ち、本発明の塗装されたマグネシウム系
廃材の再生方法は、塗装されたマグネシウム系廃材をA
r、He、Ne、SF6 、CO2 、SO2 又はN2 ガス
雰囲気中、常圧下又は減圧下で溶解させ、その溶湯を該
雰囲気中、該圧力下に保持して塗料を無機物に分解さ
せ、次いで該溶湯を該雰囲気中、減圧下に保持すること
により塗料の分解生成物を除去することを特徴とする。
That is, in the method for regenerating a coated magnesium waste material according to the present invention, the coated magnesium waste material is treated as A
r, He, Ne, SF 6 , CO 2 , SO 2, or N 2 gas atmosphere is dissolved under normal pressure or reduced pressure, and the molten metal is held in the atmosphere under the pressure to decompose the coating material into inorganic substances. Then, the decomposition product of the paint is removed by maintaining the molten metal under reduced pressure in the atmosphere.

【0009】また、本発明の塗装されたマグネシウム系
廃材の再生方法は、上記の方法によって塗料を無機物に
分解して除去し、引き続いてその溶湯中に清浄化ガスと
してAr、He、Ne、SF6 、CO2 、SO2 又はN
2 ガス、あるいはこれらのガスと乾燥空気との混合ガス
を細かく泡立てながら吹込むことによって該溶湯中の酸
化物等の異物を浮上させ、分離することを特徴とする。
Further, in the method for regenerating the coated magnesium waste material of the present invention, the coating material is decomposed into inorganic substances and removed by the above-mentioned method, and subsequently, Ar, He, Ne, SF and SF are contained in the molten metal as a cleaning gas. 6 , CO 2 , SO 2 or N
The method is characterized in that foreign substances such as oxides in the molten metal are floated and separated by blowing the two gases or a mixed gas of these gases and dry air while finely bubbling them.

【0010】[0010]

【発明の実施の形態】本発明の再生方法で再生の対象と
している塗装されたマグネシウム系廃材は、マグネシウ
ム又はマグネシウム合金(例えば、ダイカスト用のマグ
ネシウム合金であるAZ91、AM60、AM50、A
S41)製の鋳造品、ダイカスト品、加工品(板材、線
材)等でその表面に塗料による塗装が施されている部品
・製品の使用済みの回収品や、製造過程で生じる不良品
を包含する。
BEST MODE FOR CARRYING OUT THE INVENTION A coated magnesium waste material to be regenerated by the regenerating method of the present invention is magnesium or a magnesium alloy (for example, AZ91, AM60, AM50, A50, which is a magnesium alloy for die casting).
S41) Includes used and collected products, such as cast products, die-cast products, processed products (plates, wires), etc., whose surfaces are coated with paint, and defective products generated in the manufacturing process. .

【0011】本発明においては、塗料はマグネシウム系
材料製の部品・製品の塗装に一般的に用いられている全
ての塗料を包含し、例えば、フェノール樹脂系塗料、尿
素樹脂系塗料、メラミン樹脂系塗料、ビニル樹脂系塗
料、エポキシ樹脂系塗料、ポリエステル樹脂系塗料、ケ
イ素樹脂系塗料、フラン樹脂系塗料、セルロース系塗
料、クリアーラッカー等を含む。
In the present invention, the paint includes all paints generally used for painting parts and products made of magnesium-based materials, such as phenolic resin-based paints, urea resin-based paints, and melamine resin-based paints. Paints, vinyl resin paints, epoxy resin paints, polyester resin paints, silicon resin paints, furan resin paints, cellulose paints, clear lacquers and the like.

【0012】それらの塗装されたマグネシウム系廃材を
再生処理する場合に懸念されることとしては、塗装され
たマグネシウム系廃材を溶解する際に塗料が燃焼して有
害な有機系ガスが発生することがある。また、塗料中の
顔料として金属酸化物が用いられている場合にはそれら
が溶湯中に混入するという問題がある。更に、塗料が用
いられていないマグネシウム系廃材の再生でも問題とな
る酸化物や離型剤等の異物の混入も同様に問題となる。
One of the concerns when regenerating the coated magnesium waste material is that when the coated magnesium waste material is dissolved, the paint burns to generate harmful organic gases. is there. Further, when metal oxides are used as pigments in paints, there is a problem that they are mixed in the molten metal. In addition, contamination of foreign matters such as oxides and release agents, which is a problem even in the case of recycling magnesium-based waste materials in which no paint is used, also poses a problem.

【0013】本発明の再生方法においては、塗装された
マグネシウム系廃材をAr、He、Ne、SF6 、CO
2 、SO2 又はN2 ガス雰囲気中で、即ち酸素分圧が極
めて低く、溶湯に悪影響を与えない雰囲気中で、常圧下
又は減圧下で溶解させ、その溶湯を該雰囲気中に保持す
るので、塗料を酸化させずに無機物に分解でき、また減
圧下に保持することによりその分解生成物を除去するこ
とができる。
In the regenerating method of the present invention, the coated magnesium waste material is treated with Ar, He, Ne, SF 6 , CO
2 , in an SO 2 or N 2 gas atmosphere, that is, in an atmosphere in which the oxygen partial pressure is extremely low and does not adversely affect the molten metal, at normal pressure or reduced pressure, and the molten metal is held in the atmosphere. The paint can be decomposed into inorganic substances without being oxidized, and the decomposition products can be removed by keeping the paint under reduced pressure.

【0014】上記のような雰囲気については、塗装され
たマグネシウム系廃材を装入したチャンバー内を50T
orr以下に減圧し、チャンバー内の雰囲気をAr、H
e、Ne、SF6 、CO2 、SO2 又はN2 ガスで置換
することにより形成することが好ましい。このようにす
る理由はチャンバー内の酸素を排除することにあるの
で、減圧度が高い(減圧後の圧力が低い)ほど良好な結
果が得られ、減圧後の圧力が50Torrよりも高い場
合には酸素分圧がある程度残存するため塗料は一部酸化
されることになる。しかしながら、減圧後の圧力が50
Torrよりも高くても、この雰囲気置換を2〜3回繰
返すことにより適正な雰囲気を得ることができる。
As for the atmosphere as described above, the inside of the chamber in which the painted magnesium waste material is charged is 50 T
orr or less, and the atmosphere in the chamber is Ar, H
e, Ne, SF 6 , CO 2 , SO 2, or N 2 gas is preferable to be formed by replacing the gas. Since the reason for this is to exclude oxygen in the chamber, better results are obtained as the degree of decompression is higher (the pressure after depressurization is lower). When the pressure after depressurization is higher than 50 Torr, Since the oxygen partial pressure remains to some extent, the paint is partially oxidized. However, the pressure after decompression is 50
Even if it is higher than Torr, an appropriate atmosphere can be obtained by repeating this atmosphere replacement two or three times.

【0015】塗装されたマグネシウム系廃材を溶解させ
る際の上記の雰囲気の圧力については特には制限されな
いが、加圧する必要は全くない。塗料の分解だけを考慮
すれば常圧でもよいが、分解後の除去を速くするために
は、即ち再生効率を高める為には減圧になっていること
が好ましい。このような条件下で溶解して得た溶湯を上
記の雰囲気中に、塗料が完全に無機物に分解するまで保
持する。保持する時間は塗料の種類、マグネシウム系材
料に対する塗料の相対量に依存して変化する。塗料の分
解の終了は、分解ガスの発生の停止に起因するチャンバ
ー内の圧力の変化によって確認できる。
The pressure of the above atmosphere when dissolving the coated magnesium waste material is not particularly limited, but there is no need to pressurize at all. Normal pressure may be used if only the decomposition of the paint is considered, but it is preferable to reduce the pressure in order to speed up the removal after the decomposition, that is, to increase the regeneration efficiency. The molten metal obtained by melting under such conditions is held in the above atmosphere until the paint is completely decomposed into inorganic substances. The holding time varies depending on the type of the paint and the relative amount of the paint to the magnesium-based material. Completion of the decomposition of the paint can be confirmed by a change in the pressure in the chamber caused by stopping the generation of the decomposition gas.

【0016】塗装されたマグネシウム系廃材を溶解させ
る温度、及びその溶湯を保持する温度については通常の
鋳造の際の溶湯温度と同一でよく、600から700℃
までの間にあることが望ましい。塗料の主成分は有機物
であり、必要に応じて金属酸化物などの顔料を含有する
ので、溶湯温度が600〜700℃で、酸素が排除され
ている条件下では、有機物は完全に分解して主として炭
素として溶湯中に残留する。溶湯温度が600℃未満の
場合には有機物の分解速度が遅かったり、分解が不十分
であったりする傾向があり、また、溶湯温度が700℃
を超える場合には大気中にに戻す際に燃焼しやすいとい
う問題がある。従って、安全性の点から溶湯温度が60
0から650℃までの間にあることが一層望ましい。
The temperature at which the coated magnesium waste material is melted and the temperature at which the molten metal is held may be the same as the temperature of the molten metal at the time of ordinary casting, and is from 600 to 700 ° C.
It is desirable to be between. The main component of the paint is an organic substance, and if necessary, a pigment such as a metal oxide is contained. Therefore, under conditions where the temperature of the molten metal is 600 to 700 ° C. and oxygen is excluded, the organic substance is completely decomposed. Mainly remains in the molten metal as carbon. When the temperature of the molten metal is lower than 600 ° C., the decomposition rate of the organic matter tends to be slow or insufficiently decomposed.
When the temperature exceeds the limit, there is a problem that the fuel is easily burned when returning to the atmosphere. Therefore, from the viewpoint of safety, the molten metal temperature is 60
More preferably, it is between 0 and 650 ° C.

【0017】また、必要に応じて塗料に添加される金属
酸化物も溶湯中に残存する。更に、マグネシウム系材料
製の部品・製品は、下地処理としてクロメート等の化成
処理(酸化処理)を施した後、塗装を施すのが一般的で
あるので、これに伴う酸化物も溶湯中に残存する。
Further, metal oxides which are added to the paint as required also remain in the molten metal. Furthermore, since parts and products made of a magnesium-based material are generally subjected to a chemical conversion treatment (oxidation treatment) such as chromate as a base treatment, and then a coating is applied, oxides accompanying this also remain in the molten metal. I do.

【0018】なお、マグネシウム系材料の鋳造において
は、繰返し溶解し、再生利用を行うと、金属成分の変動
は認められないのに溶湯の流動性も鋳物の耐食性も劣化
することが知られている。これは酸化物、離型剤等の異
物の混入に起因するものである。このような異物が溶湯
中に残存している場合には、これらの異物を除去するこ
とが望ましく、また、場合によっては除去することが必
須となる。
In the casting of a magnesium-based material, it is known that if the material is repeatedly melted and recycled, the fluidity of the molten metal and the corrosion resistance of the casting deteriorate even though the metal component is not changed. . This is due to the inclusion of foreign substances such as oxides and release agents. If such foreign matter remains in the molten metal, it is desirable to remove such foreign matter, and in some cases, it is essential to remove it.

【0019】そこで、塗料を分解し、除去した後に、引
き続いて、溶湯に悪影響を与えないガスを溶湯中に吹込
んで、そのガスが気泡として溶湯中を浮上する過程で該
溶湯中に浮遊している酸化物や離型剤等の異物を気泡に
付着させて一緒に浮上させ、分離させた。
Then, after the paint is decomposed and removed, a gas which does not adversely affect the molten metal is continuously blown into the molten metal, and the gas floats in the molten metal in a process of floating as bubbles in the molten metal. Foreign substances such as oxides and mold release agents are attached to the bubbles, floated together, and separated.

【0020】溶湯中にガスを吹込む際の溶湯温度につい
ては通常の鋳造の際の溶湯温度と同一でよいが、溶湯温
度が600℃以下の場合にはガス吹込みに伴う溶湯温度
の低下が溶湯の鋳造性に悪影響を及ぼし、また、溶湯温
度が700℃以上の場合には保護ガスとしてSF6 やS
2 を含むガスを用いても不十分であった。従って、溶
湯温度は600から700℃までの間にあることが望ま
しく、600から650℃までの間にあることが一層望
ましい。
The temperature of the molten metal at the time of blowing gas into the molten metal may be the same as the temperature of the molten metal at the time of ordinary casting. However, when the temperature of the molten metal is 600 ° C. or less, the temperature of the molten metal decreases due to gas injection. This has an adverse effect on the castability of the molten metal, and when the temperature of the molten metal is 700 ° C. or higher, SF 6 or S
The use of a gas containing O 2 was insufficient. Therefore, the temperature of the molten metal is preferably between 600 and 700 ° C., more preferably between 600 and 650 ° C.

【0021】溶湯中に吹込むガスとして種々のガスを用
いて上記の溶湯温度条件下で試験を繰り返した。溶湯中
に吹込んだガスが溶湯中を浮上する過程で、該溶湯中に
浮遊している酸化物や離型剤等の異物が気泡に付着して
一緒に浮上する必要があり、しかも溶湯中に吹込んだガ
スは溶湯にあまり悪影響を与えない(例えば、溶湯とあ
まり反応しない)ことが必要である。これらの条件を満
足し、所望の効果が達成される清浄化ガスの種類として
Ar、He、Ne、SF6 、CO2 、SO2 又はN2
ス、あるいはこれらのガスと乾燥空気(湿分を含まない
空気)との混合ガスが見い出された。なお、上記のガス
と乾燥空気との混合ガスや、SF6 及びN2 ガスを用い
る場合には、Mg溶湯との反応生成物がわずかに生成す
る。従って、溶湯中に吹込むガスとしては、Ar、H
e、Ne、SF6 、CO2 が望ましく、SO2 又はN2
ガス、あるいは上記のガスと乾燥空気との混合ガスも使
用できる。
The test was repeated under the above-mentioned molten metal temperature conditions using various gases as the gas blown into the molten metal. In the process in which the gas blown into the molten metal floats in the molten metal, foreign substances such as oxides and release agents floating in the molten metal need to adhere to the air bubbles and float together. It is necessary that the gas blown into the melt does not adversely affect the molten metal (for example, does not significantly react with the molten metal). Ar, He, Ne, SF 6 , CO 2 , SO 2 or N 2 gas, or these gases and dry air (moisture Gas containing no air) was found. When a mixed gas of the above-mentioned gas and dry air, or SF 6 and N 2 gas is used, a reaction product with the molten Mg is slightly generated. Therefore, the gas blown into the molten metal is Ar, H
e, Ne, SF 6 and CO 2 are preferable, and SO 2 or N 2
Gas or a mixture of the above gases and dry air can also be used.

【0022】本発明においては、清浄化ガスと溶湯との
接触を効率的にするために、清浄化ガスを溶湯中に細か
く泡立てながら吹込む。また、この際に、溶湯中に吹込
む清浄化ガスにより溶湯に対流を生じさせて全ての溶湯
と清浄化ガスとの有効な接触を生じさせるのに充分な流
量で且つ溶湯を有効に清浄化するのに充分な時間、清浄
化ガスを溶湯中に吹込むことが望ましい。
In the present invention, the cleaning gas is blown into the melt while finely bubbling in order to make the contact between the cleaning gas and the melt more efficient. At this time, the molten gas is effectively cleaned at a flow rate sufficient to cause convection in the molten metal by the cleaning gas blown into the molten metal and to cause effective contact between all the molten metal and the cleaning gas. It is desirable to blow the cleaning gas into the melt for a sufficient time to do so.

【0023】清浄化ガスを細かく泡立てながら吹込むこ
とによって溶湯中の酸化物等の異物の少なくとも一部が
浮上するので、この浮上した異物、及び溶湯中に残存し
ている異物を金属製又はセラミックス製のフィルターで
有効に分離、除去することができる。このフィルターに
よる分離、除去技術は塗料の分解生成物を除去した直後
の溶湯にも適用できる。このように処理することによ
り、一般的に溶湯の流動性が向上すると共に、溶湯中の
吸蔵ガスが減少し、その結果として吸蔵ガスに起因する
鋳造欠陥が減少するという効果も達成される。
At least a part of foreign matters such as oxides in the molten metal floats by blowing the cleaning gas while finely bubbling the bubbles. Separation and removal can be performed effectively using a filter made of aluminum. This separation and removal technique using a filter can also be applied to the molten metal immediately after removing the decomposition products of the paint. By performing such treatment, the fluidity of the molten metal is generally improved, and the occluded gas in the molten metal is reduced, and as a result, the casting defects caused by the occluded gas are also reduced.

【0024】本発明の清浄化方法は、塗装されたマグネ
シウム系廃材のみを溶解して得た溶湯に適用できるだけ
でなく、勿論、新地金とマグネシウム廃材とを併用する
場合にも適用できる。このように併用する場合には、マ
グネシウム系廃材の割合を0〜100%の範囲内で適当
に設定できるが、一般的には50%以下にすることが望
ましい。このように新地金と併用する場合には溶湯表面
に浮上するドロス量は少量となる。
The cleaning method of the present invention can be applied not only to a molten metal obtained by dissolving only a painted magnesium waste material, but also to a case where a new ingot and a magnesium waste material are used in combination. When such a combination is used, the ratio of the magnesium-based waste material can be appropriately set within a range of 0 to 100%, but is generally desirably set to 50% or less. Thus, when used together with new metal, the amount of dross floating on the surface of the molten metal is small.

【0025】実施例1 塗装されたマグネシウム系廃材として、AZ91合金
(Mg−9%Al−0.7%Zn−0.2%Mn)製鋳
造品の表面をDOW1法によって化成処理し、中塗り塗
料としてサイクロン999(東京ペイント株式会社製)
を用い、上塗り塗料としてMGR−481ゴールド(東
京ペイント株式会社製)を用いて塗装した製品の使用済
みの回収品を用いた。
Example 1 As a coated magnesium waste material, the surface of a cast product made of an AZ91 alloy (Mg-9% Al-0.7% Zn-0.2% Mn) is subjected to a chemical conversion treatment by the DOW1 method, followed by intermediate coating. Cyclone 999 as a paint (Tokyo Paint Co., Ltd.)
And a used recovered product of a product coated using MGR-481 Gold (manufactured by Tokyo Paint Co., Ltd.) as a top coat.

【0026】図1に概略図で示す溶解炉1内にこの回収
品の破砕物2を装入し、真空吸引管3を介して溶解炉内
を50Torrに減圧し、その後清浄化ガス導入管4を
介してArを封入して1気圧とした(即ち、溶解炉内を
実質的にArで置換した)。その内容物を加熱して溶解
させた。その溶湯を650℃に10分間保持した。
The crushed material 2 of the recovered product is charged into a melting furnace 1 shown schematically in FIG. 1, and the pressure in the melting furnace is reduced to 50 Torr via a vacuum suction pipe 3. Ar was sealed to 1 atm (ie, the inside of the melting furnace was substantially replaced with Ar). The contents were heated to dissolve. The melt was kept at 650 ° C. for 10 minutes.

【0027】処理した後、溶解炉内のガスを分析したと
ころ、大部分がArであり、その他にH2 O、N2 、O
2 、CO2 が検出され、それ以外の分子量のガスは極め
て微弱であった。また、得られた溶湯中にはC及びA
l,Fe,Pb,Ba,Cr等の酸化物が検出された。
After the treatment, the gas in the melting furnace was analyzed, and it was found that most of the gas was Ar, and that H 2 O, N 2 , O
2. CO 2 was detected, and gases of other molecular weights were extremely weak. C and A are contained in the obtained molten metal.
Oxides such as l, Fe, Pb, Ba, and Cr were detected.

【0028】実施例2〜3 図2に概略図で示す溶解炉、即ち溶湯量が18kg(1
0リットル)、溶湯表面積が約500cm2 で溶湯表面
から15cm下の位置に、清浄化ガスを溶湯中に細かく
泡立てる吹込み装置を設置した溶解炉を用い、実施例1
で用いた回収品を用い、溶解炉1内にこの回収品の破砕
物2を装入し、真空吸引管3を介して溶解炉内を50T
orrに減圧し、その後清浄化ガス導入管4、清浄化ガ
スを溶湯中に細かく泡立てる吹込み装置5を介してAr
を封入して1気圧とした(即ち、溶解炉内を実質的にA
rで置換した)。その内容物を加熱して溶解させた。そ
の溶湯を650℃に10分間保持した。
Embodiments 2 to 3 The melting furnace shown schematically in FIG.
0 liter), a molten metal having a surface area of about 500 cm 2 and 15 cm below the surface of the molten metal, and a melting furnace equipped with a blowing device for finely bubbling a cleaning gas into the molten metal was used.
Using the recovered product used in the above, the crushed product 2 of this recovered product is charged into the melting furnace 1, and the inside of the melting furnace is evacuated through the vacuum suction pipe 3 to 50T.
orr, and then through a purifying gas introducing pipe 4 and a blowing device 5 for finely bubbling the purifying gas into the molten metal.
To 1 atm (that is, substantially A
r). The contents were heated to dissolve. The melt was kept at 650 ° C. for 10 minutes.

【0029】その後、ガス導入管4、清浄化ガスを溶湯
中に細かく泡立てる吹込み装置5を介してArを毎分
0.1リットルの流量で20分(実施例2)又は40分
(実施例3)吹き込んだ。処理後の溶湯の清浄度を評価
するためにピンホール試験と塩水噴霧試験を実施した。
Thereafter, Ar is supplied at a flow rate of 0.1 liter per minute for 20 minutes (Example 2) or 40 minutes (Example 2) through the gas introducing pipe 4 and the blowing device 5 for finely bubbling the cleaning gas into the molten metal. 3) I blew it. A pinhole test and a salt spray test were performed to evaluate the cleanliness of the molten metal after the treatment.

【0030】<ピンホール試験>溶湯約50ccをデシ
ケーター中のるつぼに注湯し、デシケーターを真空吸引
しながら凝固させた。得られた鋳物材の比重からピンホ
ール量を測定した。その結果を第1表に示す。溶湯中に
酸化物が存在する場合には凝固時に発生するガスが酸化
物にトラップされてピンホールが生成することは周知で
あるから、本試験により溶湯中の酸化物の除去状況を推
測することができる。
<Pinhole Test> About 50 cc of the molten metal was poured into a crucible in a desiccator, and the desiccator was solidified while being suctioned under vacuum. The pinhole amount was measured from the specific gravity of the obtained casting material. Table 1 shows the results. It is well known that if oxides are present in the molten metal, the gas generated during solidification is trapped by the oxides and pinholes are generated. Can be.

【0031】<塩水噴霧試験>JIS Z 2371に
従って塩水噴霧試験を実施した。5%食塩水を用い、2
0時間保持後の白錆の発生の有無を目視で観察した。そ
の結果を、白錆の発生が認められなかった場合には○、
白錆の発生が僅かに認められた場合には△、白錆の発生
が明白に認められた場合には×として第1表中に示す。
<Salt Spray Test> A salt spray test was conducted according to JIS Z2371. Using 5% saline, 2
The occurrence of white rust after holding for 0 hour was visually observed. When no white rust was found, the results were evaluated as ○,
The results are shown in Table 1 as Δ when slight generation of white rust was observed, and as × when white rust was clearly observed.

【0032】比較例1 実施例2〜3で用いた回収品の代わりに、鋳造工場で発
生したAZ91合金(Mg−9%Al−0.7%Zn−
0.2%Mn)の無塗装スクラップを用い、清浄化ガス
であるArを毎分0.1リットルの流量で10分間吹き
込んだ以外を、実施例2〜3と同様に処理した。処理後
の溶湯の清浄度は第1表に示す通りであった。
Comparative Example 1 An AZ91 alloy (Mg-9% Al-0.7% Zn-) generated in a foundry was used instead of the recovered product used in Examples 2-3.
Processing was performed in the same manner as in Examples 2 to 3, except that Ar as a cleaning gas was blown at a flow rate of 0.1 liter per minute for 10 minutes using 0.2% Mn) unpainted scrap. The cleanliness of the molten metal after the treatment was as shown in Table 1.

【0033】 [0033]

【0034】[0034]

【発明の効果】以上に説明したように、本発明の再生方
法は、塗装されたマグネシウム系材料製の部品・製品の
スクラップを簡易な装置で、フラックスを用いることな
く且つ塗料の酸化に伴う有害な有機系ガスを発生させる
ことなしで溶解させ、塗料を分解させ、分解生成物を除
去して再生する、環境性に優れた再生方法を提供するこ
とができる。
As described above, the recycling method of the present invention is capable of scrapping painted parts and products made of a magnesium-based material with a simple apparatus without using flux and harmful to the oxidation of paint. It is possible to provide an environmentally friendly recycling method of dissolving without generating any organic gas, decomposing the coating material, and removing and regenerating the decomposition products.

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

【図1】 本発明の再生方法の実施に用いることのでき
る装置の概略図である。
FIG. 1 is a schematic diagram of an apparatus that can be used for carrying out a reproduction method of the present invention.

【図2】 本発明の再生方法の実施に用いることのでき
るその他の装置の概略図である。
FIG. 2 is a schematic view of another apparatus that can be used for performing the reproducing method of the present invention.

【符号の説明】[Explanation of symbols]

1 溶解炉 2 破砕物 3 真空吸引管 4 清浄化ガス導入管 5 細かく泡立てる吹込み装置 DESCRIPTION OF SYMBOLS 1 Melting furnace 2 Crushed material 3 Vacuum suction pipe 4 Purification gas introduction pipe 5 Blowing device for fine bubbling

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】塗装されたマグネシウム系廃材をAr、H
e、Ne、SF6 、CO2 、SO2又はN2 ガス雰囲気
中、常圧下又は減圧下で溶解させ、その溶湯を該雰囲気
中、該圧力下に保持して塗料を無機物に分解させ、次い
で該溶湯を該雰囲気中、減圧下に保持することにより塗
料の分解生成物を除去することを特徴とする塗装された
マグネシウム系廃材の再生方法。
1. The coated magnesium waste material is Ar, H
e, Ne, SF 6 , CO 2 , SO 2 or N 2 gas atmosphere is dissolved under normal pressure or reduced pressure, the molten metal is kept under the pressure in the atmosphere to decompose the coating material into inorganic substances, A method for regenerating a coated magnesium waste material, comprising removing decomposition products of a paint by maintaining the molten metal under reduced pressure in the atmosphere.
【請求項2】塗装されたマグネシウム系廃材を装入した
チャンバー内を50Torr以下に減圧し、チャンバー
内の雰囲気をAr、He、Ne、SF6 、CO2 、SO
2 又はN2 ガスで置換し、該雰囲気中、常圧下又は減圧
下で該廃材を溶解させ、その溶湯を該雰囲気中、該圧力
下に600〜700℃に保持して塗料を無機物に分解さ
せ、次いで該溶湯を該雰囲気中、減圧下に保持すること
により塗料の分解生成物を除去することを特徴とする請
求項1記載の再生方法。
2. The pressure in the chamber containing the coated magnesium waste material is reduced to 50 Torr or less, and the atmosphere in the chamber is Ar, He, Ne, SF 6 , CO 2 , SO 2 .
2 or N 2 gas, the waste material is dissolved in the atmosphere under normal pressure or reduced pressure, and the molten metal is maintained at 600 to 700 ° C. in the atmosphere under the pressure to decompose the coating material into inorganic substances. 2. A method according to claim 1, wherein the decomposition product of the paint is removed by maintaining the molten metal under reduced pressure in the atmosphere.
【請求項3】請求項1又は2記載の方法によって塗料を
無機物に分解して除去し、引き続いてその溶湯中に清浄
化ガスとしてAr、He、Ne、SF6 、CO2 、SO
2 又はN2 ガス、あるいはこれらのガスと乾燥空気との
混合ガスを細かく泡立てながら吹込むことによって該溶
湯中の酸化物等の異物を浮上させ、分離することを特徴
とする塗装されたマグネシウム系廃材の再生方法。
3. The method according to claim 1 or 2, wherein the paint is decomposed into inorganic substances and removed, and subsequently, Ar, He, Ne, SF 6 , CO 2 , SO 2 are added as a cleaning gas in the molten metal.
2 or N 2 gas, or a mixed gas of these gases and dry air, is blown while finely bubbling, so that foreign substances such as oxides in the molten metal are floated and separated. How to recycle waste materials.
【請求項4】50重量%以上の新地金と50重量%以下
の塗装されたマグネシウム系廃材とを併用することを特
徴とする請求項1、2又は3記載の再生方法。
4. The recycling method according to claim 1, wherein 50% by weight or more of the new metal and 50% by weight or less of the coated magnesium waste material are used in combination.
【請求項5】塗装されたマグネシウム系廃材を請求項1
〜4の何れかに記載の方法によって再生し、引き続いて
その溶湯を金属製又はセラミック製のフィルターで濾過
することを特徴とする塗装されたマグネシウム系廃材の
再生方法。
5. The coated magnesium waste material according to claim 1.
5. A method for regenerating a coated magnesium waste material, comprising regenerating by the method described in any one of (4) to (4), and subsequently filtering the molten metal through a metal or ceramic filter.
JP08006999A 1999-03-24 1999-03-24 How to recycle painted magnesium-based waste Expired - Fee Related JP4136170B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003035917A3 (en) * 2001-10-24 2003-07-17 Gabor Vallo Method for processing magnesium containing scrap by melting in a vacuum furnace
JP2007126720A (en) * 2005-11-04 2007-05-24 Japan Atomic Energy Agency Equipment and method for refining molten metal
JP2008170414A (en) * 2007-06-27 2008-07-24 Nippon Kinzoku Kagaku Kk Molten aluminum container for pinhole test

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003035917A3 (en) * 2001-10-24 2003-07-17 Gabor Vallo Method for processing magnesium containing scrap by melting in a vacuum furnace
JP2007126720A (en) * 2005-11-04 2007-05-24 Japan Atomic Energy Agency Equipment and method for refining molten metal
JP2008170414A (en) * 2007-06-27 2008-07-24 Nippon Kinzoku Kagaku Kk Molten aluminum container for pinhole test

Also Published As

Publication number Publication date
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