JPS6357731A - Treatment of aluminum swarf or the like - Google Patents
Treatment of aluminum swarf or the likeInfo
- Publication number
- JPS6357731A JPS6357731A JP61198119A JP19811986A JPS6357731A JP S6357731 A JPS6357731 A JP S6357731A JP 61198119 A JP61198119 A JP 61198119A JP 19811986 A JP19811986 A JP 19811986A JP S6357731 A JPS6357731 A JP S6357731A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- turnings
- temp
- aluminum
- supplied
- 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
Links
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims description 28
- 229910052782 aluminium Inorganic materials 0.000 title claims description 27
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 11
- 238000010438 heat treatment Methods 0.000 claims abstract description 11
- 239000001301 oxygen Substances 0.000 claims abstract description 11
- 238000003763 carbonization Methods 0.000 claims description 15
- 238000003756 stirring Methods 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 10
- 238000005520 cutting process Methods 0.000 claims description 7
- 239000002699 waste material Substances 0.000 claims description 7
- 238000012545 processing Methods 0.000 claims description 6
- 239000007789 gas Substances 0.000 abstract description 20
- 239000003921 oil Substances 0.000 abstract description 11
- 238000002844 melting Methods 0.000 abstract description 10
- 230000008018 melting Effects 0.000 abstract description 10
- 239000000446 fuel Substances 0.000 abstract description 9
- 238000007796 conventional method Methods 0.000 abstract description 7
- 239000002994 raw material Substances 0.000 abstract description 6
- 238000002485 combustion reaction Methods 0.000 abstract description 4
- 238000000197 pyrolysis Methods 0.000 abstract description 4
- 238000007514 turning Methods 0.000 abstract 7
- 239000003570 air Substances 0.000 abstract 1
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 235000003642 hunger Nutrition 0.000 abstract 1
- 238000007789 sealing Methods 0.000 abstract 1
- 230000037351 starvation Effects 0.000 abstract 1
- 239000000843 powder Substances 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 235000013312 flour Nutrition 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 230000002265 prevention Effects 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000011888 foil Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000012994 industrial processing Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はアルミニウム切削屑等の処理方法に関するもの
であって、アルミニウム資源の回収に寄与するものであ
り、アルミニ業界において重用されるだけでなく、廃棄
アルミ箔の有効利用、環境の美化、公害発生の防止にも
非常な貢献をなすものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a method for processing aluminum cutting waste, etc., and contributes to the recovery of aluminum resources, and is not only used extensively in the aluminum industry. It also makes a significant contribution to the effective use of waste aluminum foil, beautification of the environment, and prevention of pollution.
アルミニウムないしはアルミニウム製品の製造工程にお
いて発生するダライ粉と呼ばれるアルミニウム切削屑又
は回収アルミ屑としてシュレッダ−屑、アルミ箔屑等が
溶解再生されている。Shredder scraps, aluminum foil scraps, and the like are melted and recycled as aluminum cutting scraps or recovered aluminum scraps called die powder generated in the manufacturing process of aluminum or aluminum products.
しかしながら、ダライ粉には水分、油分その他の不純物
が付着ないし混在しているため、ダライ粉を、何らの処
理も施すことなく、直接溶解炉に送って溶解すれば溶解
歩留りが低く、かつ溶湯投入時の爆発的な燃焼による作
業環境の悪化等のために通常なされていない。However, water, oil, and other impurities are attached to or mixed with the powder, so if the powder is directly sent to the melting furnace and melted without any treatment, the melting yield will be low, and the molten metal will not be charged. This is not normally done due to the deterioration of the working environment due to explosive combustion.
そこで、溶解炉での溶解処理に先立ち、これらの不純物
を除去するために、ロータリーキルン内でダライ粉をバ
ーナー炎で直接加熱し600〜800℃程度の高温で加
熱処理する方法が従来行われているのが現状であって、
本発明のように完全にシールした連続処理乾留炉を使用
したり、嫌気条件下で供給酸素濃度を制御して部分燃焼
による最適温度維持によって加熱乾溜処理したり、また
、炉全体を回転するのではなく炉内の攪拌装置により処
理アルミ切削屑等を攪拌したりするシステムは従来知ら
れておらず、全く未知のものである。Therefore, in order to remove these impurities prior to melting in a melting furnace, the conventional method is to heat the powder directly with a burner flame in a rotary kiln at a high temperature of about 600 to 800 degrees Celsius. is the current situation,
It is possible to use a completely sealed continuous process carbonization furnace as in the present invention, to control the supplied oxygen concentration under anaerobic conditions, and to maintain the optimum temperature through partial combustion to carry out the heating carbonization process, or by rotating the entire furnace. A system in which treated aluminum cuttings and the like are stirred using a stirring device inside the furnace has not been known in the past, and is completely unknown.
上記したように、従来から行われているロータリーキル
ンを用いる高熱処理法では、処理中の層表面の酸化膜が
厚くなり、溶解した後の回収アルミ地金の歩留りが悪い
ばかりでなく、ロータリーキルンが開放型のため排ガス
量が多く再燃処理に多量の燃費がかかり、かつ排ガス処
理も大規模になる、換言すれば非常に多くのエネルギー
を要するという、工業的見地からすれば致命的ともいう
べき大きな欠点は避けられない。As mentioned above, in the conventional high heat treatment method using a rotary kiln, the oxide film on the surface of the layer during treatment becomes thick, which not only results in a poor yield of recovered aluminum metal after melting, but also causes the rotary kiln to become open. Because of the type, the amount of exhaust gas is large, and the reburning process requires a large amount of fuel, and the exhaust gas treatment is also large-scale.In other words, it requires a very large amount of energy, which is a major drawback that can be called fatal from an industrial perspective. is unavoidable.
本発明は、このような技術の現状に鑑みてなされたもの
であって、アルミニウムの回収にすぐれた。省エネルギ
ー型の工業的処理方法を新規に開発する目的でなされた
ものである。The present invention was made in view of the current state of technology, and is excellent in recovering aluminum. This was done for the purpose of developing a new energy-saving industrial treatment method.
本発明は上記目的達成のためになされたものであって、
ダライ粉からのアルミニウム回収のメカニズムを徹底的
に研究し、排出ガスの有効利用、各エレメントの有機的
結合について化学工業的な面からも研究を加えた結果、
従来既知の方法では所期の目的が達成し得ないとの知見
を得1発想の転換の必要のあることを知った。The present invention has been made to achieve the above object,
As a result of thorough research on the mechanism of aluminum recovery from Dalai powder, as well as research on the effective use of exhaust gas and the organic bonding of each element, from a chemical industry perspective,
I learned that I could not achieve my desired goal using conventionally known methods, and realized that I needed to change my way of thinking.
そこで徹底的に研究した結果、アルミニウム回収の歩留
り低下の原因は、開放下、ロータリーキルン内で好気条
件でダライ粉を高温処理することにより、アルミニウム
が酸化されてしまうからであるとの知見を得た。この知
見に基き嫌気条件下における工業的加熱処理について各
方面から検討した結果、乾留炉の使用に着目するに到っ
た。そして更に実験をくり返した結果、乾留炉を使用す
れば、従来のロータリーキルンを使用する場合よりも非
常に低い温度で加熱処理することが可能であり、そのう
え歩留りも大巾に上昇することが判明した。As a result of thorough research, we found that the reason for the decrease in aluminum recovery yield was that the aluminum was oxidized due to the high temperature treatment of the powder in an open rotary kiln under aerobic conditions. Ta. Based on this knowledge, we investigated various aspects of industrial heat treatment under anaerobic conditions, and as a result, we focused on the use of a carbonization furnace. After repeated experiments, it was discovered that using a carbonization furnace allows heat treatment to be performed at much lower temperatures than when using a conventional rotary kiln, and also significantly increases the yield. .
そして乾留炉を更に有効に稼動させるために、各種の工
夫を試みて、炉内を攪拌装置によって攪拌したところ、
従来法では92%程度の溶解歩留りしかなかったのに対
して、95%以上の溶歩留りを呈するという工業的大成
果が得られ、しかも従来法においては800℃以上もの
高温加熱処理が必要であるのに対して、約400℃とい
う従来法の約半分の低温で、上記のような高い歩留りが
得られるという予期せざる著効が奏されるという新規な
有用知見を確認した。その結果、燃費も大巾に節約でき
ることも併せて確認し1本発明を完成するに到ったので
ある。In order to make the carbonization furnace work even more effectively, we tried various methods to agitate the inside of the furnace using a stirring device.
While the conventional method had a melting yield of only about 92%, this was a great industrial achievement in that it achieved a melting yield of over 95%, and the conventional method required high-temperature heat treatment of over 800°C. On the other hand, we have confirmed a new and useful finding that the above-mentioned high yield can be obtained at a low temperature of about 400° C., which is about half that of the conventional method. As a result, it was also confirmed that fuel consumption could be greatly reduced, and the present invention was completed.
本発明において処理する原料は、アルミニウム切削屑等
であるが、これには、アルミニウム製品の製造時に発生
するアルミニウム屑、切削屑、シュレッダ−屑のほか、
使用済のアルミ缶等アルミ製品の使用済層といったアル
ミニウム含有物がすべて包含される。The raw material to be processed in the present invention is aluminum cutting waste, etc., which includes aluminum waste, cutting waste, shredder waste, etc. generated during the manufacturing of aluminum products, and
All aluminum-containing materials are included, such as the used layer of aluminum products such as used aluminum cans.
以下、本発明を実施するための装置を参照しながら、本
発明を添付図面について詳細に説明する。The invention will now be described in detail with reference to the accompanying drawings and with reference to an apparatus for carrying out the invention.
予め粉砕した油分及び水分が付着した原料ダライ粉をホ
ッパー1に供給し、スクリューフィーダ2からシールさ
れた原料供給口を通して乾留炉3内に供給する。乾留炉
3内には、攪拌装置を設けるが、本実施例では回転軸4
を乾留炉本体の中に貫通せしめ、回転軸4には複数個の
攪拌羽根5をとりつけ、軸の回転とともにダライ粉を攪
拌して加熱が均一に行われるようにする1回転軸4は、
伝導袋@6を介して可変速モータMによって回転せしめ
る。回転数は、処理原料であるダライ粉の種類1粒度、
汚染度によっても相違するが、約8rpm程度とするの
がよい。本実施例においては攪拌翼を回転せしめている
が、スクリュ一方式による攪拌装置等既知の攪拌装置が
適宜使用される。Pre-pulverized raw material dry powder adhering to oil and moisture is supplied to a hopper 1, and is supplied from a screw feeder 2 into a carbonization furnace 3 through a sealed raw material supply port. A stirring device is provided in the carbonization furnace 3, but in this embodiment, a rotating shaft 4 is provided.
is passed through the carbonization furnace main body, and a plurality of stirring blades 5 are attached to the rotating shaft 4, which stirs the flour as the shaft rotates to ensure uniform heating.
It is rotated by a variable speed motor M via a conduction bag @6. The rotation speed depends on the type and particle size of the powder used as processing raw material,
Although it varies depending on the degree of contamination, it is preferable to set the speed to about 8 rpm. Although the stirring blades are rotated in this embodiment, a known stirring device such as a one-screw type stirring device may be used as appropriate.
乾留炉3内は完全にシールして密閉しておき、炉内は嫌
気状態つまり酸素欠乏雰囲気にしておく。The inside of the carbonization furnace 3 is completely sealed and kept in an anaerobic state, that is, an oxygen-deficient atmosphere.
したがって、開口部、軸の貫通部等は気密保持バルブ、
気密開閉カバー、気密シール等で密封シールしておく。Therefore, openings, shaft penetrations, etc. should be filled with airtight valves,
Seal tightly with an airtight opening/closing cover, airtight seal, etc.
炉3内は、供給ロアからパイプ8.9を介して重油その
他の燃料及び空気(又は酸素)を最初のみ供給して燃焼
させ、炉内温度を300〜500℃程度に維持コントロ
ールする。その後は燃料を供給することなく、酸素濃度
を制御することにより蒸発可燃物が燃焼し、温度を維持
する。Inside the furnace 3, heavy oil, other fuel, and air (or oxygen) are supplied from the supply lower through the pipe 8.9 only at the beginning to cause combustion, and the temperature inside the furnace is maintained and controlled at about 300 to 500°C. After that, the evaporated combustibles are combusted by controlling the oxygen concentration without supplying fuel, and the temperature is maintained.
炉内のダライ粉は、攪拌羽根によって攪拌されつつ移動
しながら付着した油分、水分はガス化する。上記炉内温
度を維持するように、空気をコントロールしながら供給
ロアから加え、上記発生ガスの一部は、部分燃焼させる
。嫌気加熱によって、ダライ粉に付着している少量の油
分、水分はもとより、アルミ缶に印刷されている塗料等
大量の油分も充分に且つ効率よくガス化して、ダライ粉
は清浄化される。The flour in the furnace is moved while being stirred by stirring blades, and the oil and moisture attached to it are gasified. In order to maintain the temperature inside the furnace, air is added from the supply lower while being controlled, and a part of the generated gas is partially combusted. By anaerobic heating, not only small amounts of oil and water adhering to the flour but also large amounts of oil such as paint printed on aluminum cans are sufficiently and efficiently gasified and the flour is cleaned.
このようにして発生したガスの大部分は、ガス排出口1
0から炉外へ排出される。これは可燃ガスなので、エネ
ルギーの有効利用、ガス成分の有効利用及び大気汚染公
害の防止といった観点から、本実施例ではパイプ11を
介して再燃炉12で処理する構成とした。Most of the gas generated in this way is at the gas outlet 1.
0 and is discharged from the furnace. Since this is a combustible gas, this embodiment has a configuration in which it is treated in a reburning furnace 12 via a pipe 11 from the viewpoints of effective use of energy, effective use of gas components, and prevention of air pollution.
再燃炉12内では、ガス供給口13から上記発生ガスを
炉内に導入供給し、一方、供給口14からはパイプ8.
9から燃料及び空気を充分に供給し、800〜1000
℃程度の温度で発生ガスを完全燃焼させて油分はCO□
とH,O等に酸化させ、完全に処理し、併せて脱臭も行
う。この段階で、ダライ粉に由来する油分、水分は完全
に分解、脱臭されて無害なものとなるので、このまま大
気中に放出することも可能であるが、更に次の処理に付
してもよい。In the reburning furnace 12, the generated gas is introduced and supplied into the furnace through a gas supply port 13, while a pipe 8.
Supply sufficient fuel and air from 9 to 800 to 1000
The generated gas is completely combusted at a temperature of about ℃, and the oil becomes CO□
It is oxidized to H, O, etc., completely treated, and deodorized at the same time. At this stage, the oil and water derived from the dalai powder are completely decomposed and deodorized and become harmless, so it can be released into the atmosphere as is, but it can also be subjected to further processing. .
すなわち、再燃炉で発生したガスは、酸素プアガスであ
り、これを排出口15から取り出してパイプ16を介し
て冷却器17に導く。冷却器17にはパイプ18から水
、空気その他の流体を供給しておいて、上記した高温の
酸素プアガスと接触させて熱交換を行い、酸素プアガス
は300〜500℃程度に冷却する一方、水等の流体は
加温して温水又は蒸気等にする。That is, the gas generated in the reburning furnace is oxygen-poor gas, which is taken out from the exhaust port 15 and guided to the cooler 17 via the pipe 16. Water, air, and other fluids are supplied to the cooler 17 from a pipe 18, and are brought into contact with the above-mentioned high-temperature oxygen poor gas for heat exchange. Such fluids are heated to turn them into hot water, steam, etc.
上記により冷却したガスは、パイプ19、排気ファン2
0を介してそのまま大気中に放出するが、−部は、パイ
プ21.循環ファン22及びパイプ27を介して、ダラ
イ粉取出管23へと導入して炉3内に戻してやる。該冷
却ガスは、窒素及び炭酸ガスに富み、酸素は極めて少な
いガスであり、なお且つ充分な熱量を保持しているので
、これを炉内に吹き込んでやることによって、排出ダラ
イ粉の飽和状態における付着油分等を洗滌して清浄化し
たダライ粉とするが、併せて、炉内への熱源の供給も行
うものであり、このようにして燃費の節約もはかること
ができる。The gas cooled by the above is passed through the pipe 19 and the exhaust fan 2.
0 into the atmosphere as it is, but the - part is discharged directly into the atmosphere through pipe 21. It is introduced into the dry powder take-out pipe 23 via the circulation fan 22 and pipe 27 and returned into the furnace 3. The cooling gas is rich in nitrogen and carbon dioxide gas and contains very little oxygen, and it retains a sufficient amount of heat, so by blowing it into the furnace, the exhaust powder is saturated. The dry powder is cleaned by washing away adhering oil and the like, but it also supplies a heat source to the inside of the furnace, and in this way it is possible to save on fuel consumption.
このようにして乾留炉3内で処理されたダライ粉は、油
分、水分等の不純物が除去されるだけでなく、従来法に
比して酸化膜が少なく、その結果アルミ製品の歩留りが
大巾にアップする。このようにして得た酸化物の少ない
高品質の清浄化ダライ粉は、ダライ粉取出管23からス
クリューフィーダ24を介して溶解炉25へと送られ、
常法によってこれを溶解処理して良質の製品26を得る
のである。The dry powder treated in this way in the carbonization furnace 3 not only has impurities such as oil and moisture removed, but also has less oxide film compared to conventional methods, and as a result, the yield of aluminum products is greatly improved. Upload to. The high-quality cleaned powder with less oxides thus obtained is sent from the powder extraction pipe 23 to the melting furnace 25 via the screw feeder 24.
A high quality product 26 is obtained by dissolving this in a conventional manner.
上記した装置を用いて、原料ダライ粉1tを次のような
条件で処理した。乾留炉内温度450℃、攪拌翼回転数
8 rpm、再燃炉内温度900℃、冷却器からの酸素
プアガス温度450℃。そして溶解炉で常法によって処
理して、良質の製品を97%の歩留りで得た。Using the above-mentioned apparatus, 1 ton of raw material powder was treated under the following conditions. The temperature inside the carbonization furnace was 450°C, the stirring blade rotation speed was 8 rpm, the temperature inside the reburning furnace was 900°C, and the temperature of the oxygen poor gas from the cooler was 450°C. It was then treated in a melting furnace in a conventional manner to obtain a good quality product with a yield of 97%.
本発明は、上記したように乾留炉を用いて嫌気条件下で
ダライ粉を加熱乾溜処理する新規な構成を採用したので
、加熱温度が従来法に比し、極端に低く出来るのでアル
ミニウムをアルミナ等に酸化させることなく油分や水分
を効率よく除去することができ、その結果製品アルミニ
ウムの歩留りが大巾に向上するという著効が得られる。As described above, the present invention employs a new configuration in which dry distillation treatment is performed by heating dry powder under anaerobic conditions using a carbonization furnace.As a result, the heating temperature can be extremely lower than that of conventional methods, allowing aluminum to be heated and dry-distilled under anaerobic conditions. It is possible to efficiently remove oil and moisture without causing oxidation, resulting in a significant improvement in the yield of product aluminum.
そのうえ、排出ガスは、乾留炉から直接外部へ放出する
のではなくて、再燃処理及び冷却処理とを有機的に結合
して全体をシステム化することによって、無害のものと
した後外部に放出し、またその一部は乾留炉に戻してや
ってその熱と嫌気性とを再利用するので、更に燃費が安
くなると同時に大気汚染を防止するという効果も更に併
せ得られ机
しかも、本実施例においてはバッチ処理について述べた
が、必要なバルブ操作を行うことによって連続処理も自
由に行うことができる。Moreover, rather than releasing the exhaust gas directly from the carbonization furnace to the outside, the system organically combines the reburning process and the cooling process to make the exhaust gas harmless and then release it to the outside. In addition, since a part of it is returned to the carbonization furnace and its heat and anaerobic properties are reused, fuel consumption is further reduced and at the same time an effect of preventing air pollution is obtained. Although batch processing has been described, continuous processing can also be carried out freely by performing necessary valve operations.
このように本発明によれば、従来技術に比してはるかに
低いエネルギーでしかも非常に高い歩留りを得ることが
でき、本発明が特に大規模な工業的処理に特に適してい
ることがわかる。また、公害防止技術としても本発明が
非常に卓越していることも容易に理解することができる
。Thus, according to the present invention, a very high yield can be obtained with much lower energy than in the prior art, and it can be seen that the present invention is particularly suitable for large-scale industrial processing. Furthermore, it can be easily understood that the present invention is extremely superior as a pollution prevention technology.
図面は、本発明を実施するための装置の1例を図示した
ものである。The drawings illustrate one example of an apparatus for carrying out the invention.
Claims (1)
留炉内に供給し、攪拌しながら、酸素濃度を制御して部
分燃焼させ、温度を維持し、かつ嫌気条件下で加熱乾溜
処理することを特徴とするアルミニウム切削屑等の処理
方法。Aluminum cuttings, etc. are fed into a closed carbonization furnace equipped with a stirring device, and while stirring, the oxygen concentration is controlled and partially combusted, the temperature is maintained, and the heating process is carried out under anaerobic conditions. Characteristic method for processing aluminum cutting waste, etc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19811986A JPH0617520B2 (en) | 1986-08-26 | 1986-08-26 | Treatment method for aluminum cutting chips |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19811986A JPH0617520B2 (en) | 1986-08-26 | 1986-08-26 | Treatment method for aluminum cutting chips |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6357731A true JPS6357731A (en) | 1988-03-12 |
| JPH0617520B2 JPH0617520B2 (en) | 1994-03-09 |
Family
ID=16385774
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19811986A Expired - Lifetime JPH0617520B2 (en) | 1986-08-26 | 1986-08-26 | Treatment method for aluminum cutting chips |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0617520B2 (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0238538A (en) * | 1988-07-27 | 1990-02-07 | Asahi Tec Corp | Method and apparatus for remelting aluminum alloy turning |
| JPH04158976A (en) * | 1990-10-23 | 1992-06-02 | Hitachi Metals Ltd | Chip treating equipment and casting equipment |
| JPH06160288A (en) * | 1992-07-28 | 1994-06-07 | G D Spa | Detector, especially apparatus for surface inspection of cigarette |
| WO1995023239A1 (en) * | 1994-02-23 | 1995-08-31 | Han Spoel | Method and apparatus for recovery of non-ferrous metals from scrap and dross |
| JP2003089826A (en) * | 2001-09-19 | 2003-03-28 | Asahi Tec Corp | Compound dissolution method |
| JP2009144994A (en) * | 2007-12-14 | 2009-07-02 | Nichikon Seisakusho:Kk | Exhaust gas circulating type drying method and its device, and recycle method and its system for metal chip |
| JP2019183275A (en) * | 2018-03-30 | 2019-10-24 | 株式会社広築 | Melting method and melting unit of aluminum chip |
-
1986
- 1986-08-26 JP JP19811986A patent/JPH0617520B2/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0238538A (en) * | 1988-07-27 | 1990-02-07 | Asahi Tec Corp | Method and apparatus for remelting aluminum alloy turning |
| JPH04158976A (en) * | 1990-10-23 | 1992-06-02 | Hitachi Metals Ltd | Chip treating equipment and casting equipment |
| JPH06160288A (en) * | 1992-07-28 | 1994-06-07 | G D Spa | Detector, especially apparatus for surface inspection of cigarette |
| US5688470A (en) * | 1994-02-02 | 1997-11-18 | Spoel; Han | Apparatus for recovery of non-ferrous metals from scrap and dross |
| WO1995023239A1 (en) * | 1994-02-23 | 1995-08-31 | Han Spoel | Method and apparatus for recovery of non-ferrous metals from scrap and dross |
| US5540752A (en) * | 1994-02-23 | 1996-07-30 | Spoel; Han | Method for recovery of non-ferrous metals from scrap and dross |
| JP2003089826A (en) * | 2001-09-19 | 2003-03-28 | Asahi Tec Corp | Compound dissolution method |
| JP2009144994A (en) * | 2007-12-14 | 2009-07-02 | Nichikon Seisakusho:Kk | Exhaust gas circulating type drying method and its device, and recycle method and its system for metal chip |
| JP2019183275A (en) * | 2018-03-30 | 2019-10-24 | 株式会社広築 | Melting method and melting unit of aluminum chip |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0617520B2 (en) | 1994-03-09 |
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