JPS6137934A - Regenerating method of al from waste al can - Google Patents

Regenerating method of al from waste al can

Info

Publication number
JPS6137934A
JPS6137934A JP59157307A JP15730784A JPS6137934A JP S6137934 A JPS6137934 A JP S6137934A JP 59157307 A JP59157307 A JP 59157307A JP 15730784 A JP15730784 A JP 15730784A JP S6137934 A JPS6137934 A JP S6137934A
Authority
JP
Japan
Prior art keywords
pieces
waste
supplied
conveyer
melting
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
JP59157307A
Other languages
Japanese (ja)
Inventor
Kizo Nara
奈良 喜蔵
Keitaro Okawa
大川 桂太郎
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.)
OOTE KINZOKU KK
Mitsubishi Metal Corp
Original Assignee
OOTE KINZOKU KK
Mitsubishi Metal Corp
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 OOTE KINZOKU KK, Mitsubishi Metal Corp filed Critical OOTE KINZOKU KK
Priority to JP59157307A priority Critical patent/JPS6137934A/en
Publication of JPS6137934A publication Critical patent/JPS6137934A/en
Pending 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

Abstract

PURPOSE:To suppress Al oxidation and to improve regenerating yield, by cutting a waste Al can, decomposing and removing the coated film of organic compound by dry distillation, press forming said material and melting them by conventional method. CONSTITUTION:The waste Al can is dropped on a conveyer 2 from a hopper 1, and crushed by a crusher 4 after removing iron material therein by a primary magnetic separator 3. Crushed pieces are washed on a conveyer 5, then supplied to the first preheating hopper 8 and preheated after iron piece therein is removed on a conveyer 9 by the second magnetic separator 7. Next, said pieces are supplied to a dry distillation kiln 12 at a prescribed temp. by rotary valves 11 to heat them to about 400-500 deg.C by a combustion chamber 13, the organic coating material coated on the surface is decomposed thermally, most of them are converted to gas, and a part thereof is carbonized and removed from Al pieces. Next, said pieces are supplied to a quantitative supplying apparatus 17 in order by rotary valves 11, press formed by a pressing machine, and said material is supplied to a melting furnace through the second preheating hopper 19.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は飲食物缶詰容器などに使われるアルミニウム(
以下Alと略記する)製の缶の使用済みのものあるいは
生産工程の不良品など(gAl缶)からMを再生する方
法に関する。
[Detailed Description of the Invention] Industrial Field of Application The present invention is applied to aluminum (
The present invention relates to a method for recycling M from used cans made of (hereinafter abbreviated as Al) or defective products in the production process (gAl cans).

従来の技術 従来廃Al缶からのAlの再生は、集収された廃缶から
磁力選別などにより鉄缶を除去し9分別されたAl缶を
切断して小片とし、これを洗浄して異物を除いた後再度
磁力選別して鉄系金属片を除去し2分別されたM切断片
を燃焼炉に入れ表面に形成されている保護塗膜や印刷塗
膜などを直接燃焼して除去してから溶解するつぼ中で溶
解するか又は保護塗膜や印刷塗膜をつけたまま溶解し。
Conventional technology Conventionally, aluminum can be recycled from waste aluminum cans by removing iron cans from the collected waste cans by magnetic sorting, cutting the separated aluminum cans into small pieces, and cleaning them to remove foreign matter. After that, they are magnetically sorted again to remove ferrous metal pieces, and the two separated M cut pieces are placed in a combustion furnace where protective coatings and printed coatings formed on the surface are directly burned to remove them, and then melted. Melt in a crucible or with a protective coating or printed coating still on.

インゴットに鋳造する方法が一般的である。A common method is to cast it into an ingot.

発明が解決しようとする問題点 従来の脱ラッカーの方法はキルン等で廃アルミ缶を焙焼
するが、この時発生するガスを処理する為に多額の費用
を要していた特に臭気をなくす為にアフターバーニング
方式で行うが空気が入っている為ガス量も多く、その技
術的対応も容易でなく公害問題にもなシかねない状態で
あった。また燃焼工程において大量のAlが同時に酸化
されて回収不能となる不利があり、また燃焼後にAl片
を溶解るつぼに投入するとAl片が軽いために溶湯表面
に浮いてさらに酸化が進むという問題もあった。本発明
はこのようなAdの酸化による損失のないAl再生法を
提供することを目的とする。
Problems that the invention aims to solve The conventional method of delacquering involves roasting waste aluminum cans in a kiln, etc., but a large amount of money is required to treat the gas generated at this time.Especially in order to eliminate odor. This is done using the afterburning method, but since it contains air, there is a large amount of gas, and it is not easy to deal with it technically, which could lead to pollution problems. In addition, there is the disadvantage that a large amount of Al is oxidized at the same time during the combustion process and cannot be recovered, and there is also the problem that when the Al pieces are put into the melting crucible after combustion, the Al pieces are light and float on the surface of the molten metal, causing further oxidation. Ta. An object of the present invention is to provide a method for regenerating Al without such loss due to oxidation of Ad.

問題点を解決するための手段 前記の問題点に錯みAl切断片の直接燃焼をやめ、空気
を断って乾留を試みたところ表面の塗膜は熱分解して気
化し2表面から大部分除去され。
Means to solve the problem: Confusing the above problem, we stopped the direct combustion of the Al cut pieces and attempted carbonization while cutting off the air, but the coating film on the surface was thermally decomposed and vaporized, and most of it was removed from the surface. It is.

Al はまったく酸化を受けないことを見い出した。It was discovered that Al does not undergo oxidation at all.

また気化した熱分解物は乾留炉の低温帯域で可燃性の油
状物として回収され液化されない成分も可燃性のガスで
あった。
In addition, the vaporized thermal decomposition products were recovered as flammable oils in the low-temperature zone of the carbonization furnace, and the components that were not liquefied were also flammable gases.

次にAl溶解るつぼにAl片を投入する際、  Al厚
を表プレスにより塊状に成形して投入すると。
Next, when introducing the Al pieces into the Al melting crucible, the thickness of the Al is formed into a lump using a surface press.

みかけ密度が大きい程AiIの酸化による損失が減るこ
とを見い出し本発明に到達した。
The present invention was achieved by discovering that the larger the apparent density, the lower the loss due to oxidation of AiI.

発明の構成 本発明により廃Al缶を切断した後2選別された切断片
を溶解し、鋳造してAlインゴットを得る廃Al缶から
のAlの再生方法において、溶解に先立ち乾留工程を設
けてAl缶表面に形成されている有機化合物の塗膜を分
解除去し、得られたAn片をプレスにより圧縮成形して
プレス塊とした後常法により溶解することを%、徴とす
る廃Aキ缶からのAlの再生法が提供される。
Structure of the Invention According to the present invention, in a method for recycling Al from a waste Al can, in which an Al ingot is obtained by cutting a waste Al can, and then melting and casting the two sorted cut pieces, a carbonization step is provided prior to melting. Waste A cans characterized by decomposing and removing the coating film of organic compounds formed on the can surface, compressing the obtained Ann pieces using a press to make a pressed mass, and then dissolving it by a conventional method. A method for regenerating Al from is provided.

また本発明によれば、上記の方法であって、乾留工程に
おいて発生する気体生成物を乾留のだめの燃料の一部と
して使用することを特徴とする方法が提供される。
According to the present invention, there is also provided the above-mentioned method, characterized in that the gaseous products generated during the carbonization step are used as part of the fuel in the carbonization reservoir.

本発明方法における乾留温度は高温相短時間で乾留でき
るが400〜500℃程度で十分Al缶の有機物塗膜を
熱分解することができる。乾留釦よる熱分解物の回収は
廃プラスチックや廃タイヤの乾留装置に使われているも
のと同タイプのもの(例えば、特開昭54−15447
7号、特開昭56−133432号)がそのまま使用で
き2回収した熱分解物を乾留炉の燃料として循環利用す
ることにより煙、悪臭、粉塵の問題を解決できる。
Although the carbonization temperature in the method of the present invention can be carbonized in a short time during the high temperature phase, a carbonization temperature of about 400 to 500 DEG C. is sufficient to thermally decompose the organic coating film on the Al can. The recovery of pyrolysis products using a carbonization button is the same type as that used in carbonization equipment for waste plastics and tires (for example, Japanese Patent Application Laid-Open No. 15447-1983).
7, JP-A No. 56-133432) can be used as is, and the problem of smoke, bad odor, and dust can be solved by recycling the recovered thermal decomposition product as fuel for the carbonization furnace.

また乾留後のAl片の溶解には投入試料ができるだけA
l溶湯の表面に浮かび出ないように少しでもみかけ密度
の大きい塊状にしておくことが必要で、80係以上の回
収率を達成するにはみかけ密度が1.0以上であること
を要する。
In addition, when dissolving the Al piece after carbonization, the input sample should be as much as possible.
It is necessary to form lumps with as high an apparent density as possible so as not to float on the surface of the molten metal, and in order to achieve a recovery rate of 80 or more, the apparent density must be 1.0 or more.

発明の効果 本発明の方法は、乾留によ多発生したガスを最小限にし
、少々くとも完全燃焼により、ガスの臭気が系外に出る
ことは全くなくこれにかかる費用も従来の方法と比べる
と全く問題にならない位安価なものとなった。またAl
の酸化が著るしく抑制され、  Alの回収率が向上し
た。熱分解物の循環利用によジ煙、悪臭、粉塵の問題が
なくなっただけでなく、エネルギーコストも低減できた
Effects of the Invention The method of the present invention minimizes the amount of gas generated during carbonization, and at least completely burns the gas, so that no gas odor is released from the system, and the cost involved is also lower than that of conventional methods. It has become so cheap that it is not a problem at all. Also, Al
The oxidation of Al was significantly suppressed, and the recovery rate of Al was improved. The recycling of pyrolysis products not only eliminated the problems of smoke, odor, and dust, but also reduced energy costs.

実施態様 添付第1図は本発明の方法を実施するための装置の系統
を示す図である。
Embodiment FIG. 1 shows a system of apparatus for carrying out the method of the invention.

廃Al缶は原料ホッパー1から原料コンベアー2の上に
落され、−次磁選機3によって鉄製品(ブリキ缶など)
を除去され、破砕機、好ましくはハンマークラッシャー
で、好ましくは5cTt角程度の片に破砕され、破砕片
コンベヤー5上に落とされ、ここで洗浄スプレーで洗浄
され、洗浄片コンベアー9上に落され、二次磁選機7に
よって鉄片が除去され、第1予熱ホツパー8に落される
。第1予熱ホツパーの排出管にはロータリーバルブ11
が設けられ、それによって定められた速度で乾留釜12
に供給される。
The waste Al cans are dropped from the raw material hopper 1 onto the raw material conveyor 2, and then processed into iron products (such as tin cans) by the magnetic separator 3.
is removed, crushed into pieces, preferably about 5 cTt square, by a crusher, preferably a hammer crusher, and dropped onto a crushed piece conveyor 5, where it is washed with a cleaning spray and dropped onto a washed piece conveyor 9, The iron pieces are removed by a secondary magnetic separator 7 and dropped into a first preheating hopper 8. A rotary valve 11 is installed in the discharge pipe of the first preheating hopper.
is provided, and the carbonization vessel 12 is heated at a speed determined by the
supplied to

外に外套管13を有し、これが燃焼室をなしている。そ
の排出ガスは一部は導管30,31によって第1加温ホ
ツパー8のジャケットに導かれ、他は導管30,32に
よって後に詳しく述べる第2加温ホツパー19のジャケ
ットにも送られる。その調節のために弁lOが設けられ
ている。
It has a jacket tube 13 on the outside, which forms a combustion chamber. A part of the exhaust gas is led to the jacket of the first heating hopper 8 by conduits 30, 31, and the other part is also sent to the jacket of the second heating hopper 19, which will be described in detail later, by conduits 30, 32. A valve lO is provided for its adjustment.

燃焼室13にはオイルバーナー15およびガスバーナー
16が設けられている。燃焼釜12には振動を加えて被
処理Al破砕片が移動しやすくしてもよい。いずれにし
ても彼処31 Al破砕片はここで加熱されつつ下降し
出口に設けられたロータリーパルプ11′によって順次
排出されて、定量供給装置」7に落される。
The combustion chamber 13 is provided with an oil burner 15 and a gas burner 16. Vibrations may be applied to the combustion pot 12 to facilitate movement of the Al crushed pieces to be treated. In any case, the Al crushed pieces 31 descend while being heated here, and are sequentially discharged by a rotary pulp 11' provided at the outlet, and are dropped into a quantitative supply device 7.

燃焼室における被処理Al破砕片の加熱温度は400〜
500℃で、550°Cが限度である。Al破砕片がこ
のように酸素の不存在下に加熱されるとその表面に塗布
されていた有機物質の塗装材料は熱分解し、大部分が気
体となり一部は炭化してAl片よシ除去される。
The heating temperature of the Al crushed pieces to be treated in the combustion chamber is 400~
At 500°C, the limit is 550°C. When the crushed Al pieces are heated in the absence of oxygen, the organic coating material applied to the surface is thermally decomposed, most of it turns into gas, some of it carbonizes, and the Al pieces are removed. be done.

定量供給装置は、爪のついたベルトコンベアーのような
ものでAl片を定速度で掻き出してプレス機18に供給
する。プビス機は好ましくは「バイオキューブプレス」
の名称で市販されている機械であって、 Al片はこれ
によって3m 立方の立方体に形成され、キューブコン
ベヤー33によって第2予熱ホツパー19に送られ、そ
れよシ溶解炉に供給される。
The quantitative supply device is a belt conveyor with claws that scrapes out the Al pieces at a constant speed and supplies them to the press 18. Pubis machine is preferably "Biocube Press"
With this machine, the aluminum pieces are formed into 3 m cubes and sent by a cube conveyor 33 to a second preheating hopper 19, which in turn feeds the melting furnace.

有機塗料物質の分解によって生成したガスは主として炭
化水素系モノマーであるが常温で油状の物質とポリ塩化
ビニルのような塩素含有物質から生じた塩酸や水なども
含む。この乾留ガスは導管14を経て凝縮塔(油水分離
装置)23に送られる。凝縮塔23はジャケット構造に
力っていて冷却水の入口20と出口21が設けられてい
る。乾留ガスはここで冷却されて高沸点の低分ゴ量ガス
と比較的低沸点の油状物および水性物に分離され。
The gas generated by the decomposition of organic paint materials is mainly hydrocarbon monomers, but also contains oily substances at room temperature and hydrochloric acid and water generated from chlorine-containing substances such as polyvinyl chloride. This carbonized gas is sent to a condensation tower (oil/water separator) 23 via a conduit 14. The condensing tower 23 has a jacket structure and is provided with an inlet 20 and an outlet 21 for cooling water. The carbonized gas is cooled here and separated into high boiling point, low fractionation gas and relatively low boiling point oily and aqueous substances.

塩化氷菓ガスなどを含むガスは導管22によりガス清浄
装置26に送られ、ここで苛性ソーダ水溶液の噴霧を受
けて清浄化されてからミストセパレーター29で水性部
分を完全に除去されてから前記ガスバーナー16に送ら
れて燃焼される。
Gas containing chlorinated ice cream gas etc. is sent to a gas purifier 26 through a conduit 22, where it is purified by being sprayed with an aqueous solution of caustic soda, and the aqueous portion is completely removed by a mist separator 29 before being sent to the gas burner 16. is sent to be burned.

一方凝縮塔23で分離された油状物と水性物は油水分離
器34に送られ、水性部分は廃棄され。
On the other hand, the oily matter and aqueous matter separated in the condensing column 23 are sent to an oil-water separator 34, and the aqueous part is discarded.

油状物は第2オイルタンクに移され、ここで第1オイル
タンク28より供給される新規な燃料油と混合されてオ
イルバーナー15によって燃焼される。
The oil is transferred to the second oil tank where it is mixed with fresh fuel oil supplied from the first oil tank 28 and burned by the oil burner 15.

このように本発明の方法によれば廃Al缶は連続的に処
理され、生成する乾留ガスを燃料の一部として再循環燃
焼するので極めて効率的経済的である。
As described above, according to the method of the present invention, waste Al cans are continuously treated and the carbonized gas produced is recirculated and burned as part of the fuel, so it is extremely efficient and economical.

Al1!の溶解に際してAlの回収率はAl破砕片のプ
レス塊のカサ比重に関係する。実験によって求められた
この関係を第2図に示す。これによればカサ比重と回収
率は殆んど直線的な関係にある。
Al1! The recovery rate of Al during melting is related to the bulk specific gravity of the pressed mass of crushed Al pieces. This relationship determined through experiments is shown in FIG. According to this, there is an almost linear relationship between bulk specific gravity and recovery rate.

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

第1図は本発明の方法を実施するだめの装置系統の概念
図である。 第2図はAl破砕片のプレス塊のカサ比重と溶解回収率
の関係を示す。 第1図において
FIG. 1 is a conceptual diagram of an apparatus system for carrying out the method of the present invention. FIG. 2 shows the relationship between the bulk specific gravity of a pressed mass of crushed Al pieces and the dissolution recovery rate. In Figure 1

Claims (1)

【特許請求の範囲】 1、廃Al缶を切断した後、選別された切断片を溶解し
、鋳造してAlインゴットを得る廃Al缶からのAlの
再生方法において、溶解に先立ち乾留工程を設けてAl
缶表面に形成されている有機化合物の塗膜を分解除去し
、得られたAl片をプレスにより圧縮成形してプレス塊
とした後常法により溶解することを特徴とする廃Al缶
からのAlの再生法。 2、廃Al缶を切断した後、選別された切断片を溶解し
、鋳造してAlインゴットを得る廃Al缶からのAlの
再生方法において、溶解に先立ち乾留工程を設けてAl
缶表面に形成されている有機化合物の塗膜を分解除去し
、得られたAl片をプレスにより圧縮成形してプレス塊
とした後常法により溶解し、乾留工程で得られる分解生
成物を乾留工程の燃料として使用することを特徴とする
方法。
[Claims] 1. In a method for recycling Al from a waste Al can, in which after cutting a waste Al can, the sorted cut pieces are melted and cast to obtain an Al ingot, a carbonization step is provided prior to melting. Al
Al from waste Al cans, which is characterized by decomposing and removing the organic compound coating formed on the can surface, compressing the obtained Al pieces using a press to form a pressed mass, and then dissolving it by a conventional method. regeneration method. 2. After cutting a waste Al can, the selected cut pieces are melted and cast to obtain an Al ingot. In a method for recycling Al from a waste Al can, a carbonization step is provided prior to melting to remove Al.
The organic compound coating formed on the can surface is decomposed and removed, the resulting Al pieces are compression-molded using a press to form a pressed mass, and then melted using a conventional method, and the decomposition products obtained in the carbonization process are carbonized. A method characterized in that it is used as a fuel in a process.
JP59157307A 1984-07-30 1984-07-30 Regenerating method of al from waste al can Pending JPS6137934A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59157307A JPS6137934A (en) 1984-07-30 1984-07-30 Regenerating method of al from waste al can

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59157307A JPS6137934A (en) 1984-07-30 1984-07-30 Regenerating method of al from waste al can

Publications (1)

Publication Number Publication Date
JPS6137934A true JPS6137934A (en) 1986-02-22

Family

ID=15646804

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59157307A Pending JPS6137934A (en) 1984-07-30 1984-07-30 Regenerating method of al from waste al can

Country Status (1)

Country Link
JP (1) JPS6137934A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01188637A (en) * 1988-01-21 1989-07-27 Shintouyou Kinzoku Kogyo Kk Treatment of aluminum can scrap
JPH07118765A (en) * 1993-10-22 1995-05-09 Kawashima:Kk Production of aluminum deoxidized briquette lump
JPH07197139A (en) * 1993-07-16 1995-08-01 Kawashima:Kk Flux-containing aluminum deoxidizing briquette
WO1996001332A1 (en) * 1994-07-05 1996-01-18 Nippon Chuzo Kabushiki Kaisha Method and apparatus for used aluminum can recycling
JP2007224391A (en) * 2006-02-24 2007-09-06 Fujifilm Corp Method for regenerating used planographic printing plate
KR100792001B1 (en) 2007-06-07 2008-01-04 주식회사 디에스 Forged aluminium, and method and apparatus for manufacturing the same
KR100910630B1 (en) 2008-10-30 2009-08-05 (주)그룹오상 Method for recycling aluminium in package
JP2010138478A (en) * 2008-12-15 2010-06-24 Harufusa Iwasaki Method for recycling waste aluminum product
CN109092843A (en) * 2018-06-20 2018-12-28 西昌宏鑫实业有限公司 A kind of metal smelt system and method for recycling waste

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5819731A (en) * 1981-07-27 1983-02-04 Nec Corp Magnetic recording material

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5819731A (en) * 1981-07-27 1983-02-04 Nec Corp Magnetic recording material

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01188637A (en) * 1988-01-21 1989-07-27 Shintouyou Kinzoku Kogyo Kk Treatment of aluminum can scrap
JPH0567687B2 (en) * 1988-01-21 1993-09-27 Shintoyo Kinzoku Kogyo Kk
JPH07197139A (en) * 1993-07-16 1995-08-01 Kawashima:Kk Flux-containing aluminum deoxidizing briquette
JPH07118765A (en) * 1993-10-22 1995-05-09 Kawashima:Kk Production of aluminum deoxidized briquette lump
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WO1996001332A1 (en) * 1994-07-05 1996-01-18 Nippon Chuzo Kabushiki Kaisha Method and apparatus for used aluminum can recycling
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JP2007224391A (en) * 2006-02-24 2007-09-06 Fujifilm Corp Method for regenerating used planographic printing plate
KR100792001B1 (en) 2007-06-07 2008-01-04 주식회사 디에스 Forged aluminium, and method and apparatus for manufacturing the same
KR100910630B1 (en) 2008-10-30 2009-08-05 (주)그룹오상 Method for recycling aluminium in package
WO2010050672A1 (en) * 2008-10-30 2010-05-06 (주)그룹오상 Method for recovering aluminum from packing materials by plasma pyrolysis/gasification
JP2010138478A (en) * 2008-12-15 2010-06-24 Harufusa Iwasaki Method for recycling waste aluminum product
CN109092843A (en) * 2018-06-20 2018-12-28 西昌宏鑫实业有限公司 A kind of metal smelt system and method for recycling waste

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