JPH04333531A - Method for recovering metal from mixed waste of metal and plastic - Google Patents
Method for recovering metal from mixed waste of metal and plasticInfo
- Publication number
- JPH04333531A JPH04333531A JP3131616A JP13161691A JPH04333531A JP H04333531 A JPH04333531 A JP H04333531A JP 3131616 A JP3131616 A JP 3131616A JP 13161691 A JP13161691 A JP 13161691A JP H04333531 A JPH04333531 A JP H04333531A
- Authority
- JP
- Japan
- Prior art keywords
- plastic
- metal
- pieces
- piece
- metallic
- 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
Links
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 53
- 239000002184 metal Substances 0.000 title claims abstract description 53
- 239000004033 plastic Substances 0.000 title claims abstract description 53
- 229920003023 plastic Polymers 0.000 title claims abstract description 53
- 239000010812 mixed waste Substances 0.000 title claims abstract description 12
- 238000000034 method Methods 0.000 title claims description 7
- 150000002739 metals Chemical class 0.000 claims abstract description 8
- 239000000203 mixture Substances 0.000 claims abstract description 4
- 150000001247 metal acetylides Chemical class 0.000 claims description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 9
- 239000010949 copper Substances 0.000 abstract description 6
- 229910052782 aluminium Inorganic materials 0.000 abstract description 4
- 229910052802 copper Inorganic materials 0.000 abstract description 4
- 229910052742 iron Inorganic materials 0.000 abstract description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 abstract description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 abstract description 3
- 230000005484 gravity Effects 0.000 abstract description 3
- 239000006148 magnetic separator Substances 0.000 abstract description 2
- 239000005539 carbonized material Substances 0.000 abstract 2
- 238000002485 combustion reaction Methods 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 239000002440 industrial waste Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- -1 aluminum (Al) Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000013502 plastic waste Substances 0.000 description 1
- 239000002699 waste material Substances 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)
- Gasification And Melting Of Waste (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】この発明は金属とプラスチックと
の混合廃棄物を燃焼させてプラスチックを炭化物にして
金属を回収する方法に係るものである。BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to a method of burning mixed waste of metal and plastic to convert the plastic into carbide and recover the metal.
【0002】0002
【従来の技術】従来の金属とプラスチックとの混合廃棄
物は焼却炉でそのまま焼却されたり、または家庭からの
ゴミと同様に埋め立てられたりなどの処理方法がある。BACKGROUND OF THE INVENTION Conventional methods for treating mixed metal and plastic waste include incinerating it in an incinerator, or burying it in a landfill in the same way as household waste.
【0003】0003
【発明が解決しようとする課題】これらの従来の金属と
プラスチックとの混合廃棄物の処理方法のうち前者では
、プラスチックが焼却炉で焼却される際に発生する高温
のために焼却炉がすぐに損傷したり、混合廃棄物中の金
属が高温のため溶解して焼却炉の内壁に付着したりなど
するという問題点があった。更に焼却炉内で溶解した金
属(Fe、Al、Cuなど)は利用価値がほとんどない
合金となってしまうという問題点があった。また従来の
処理方法の後者では、金属とプラスチックとの混合廃棄
物をそのまま埋め立てられるので嵩張るとともに腐蝕し
ないという問題点があるとともに金属を回収せずに有効
利用してないという問題点があった。[Problem to be Solved by the Invention] In the former method of treating mixed waste of metal and plastic, the incinerator quickly burns due to the high temperature generated when the plastic is incinerated in the incinerator. There were problems such as damage and the metals in the mixed waste melting due to the high temperature and adhering to the inner walls of the incinerator. Furthermore, there is a problem in that the metals (Fe, Al, Cu, etc.) melted in the incinerator become alloys with little utility value. In addition, in the latter conventional treatment method, the mixed waste of metal and plastic is directly landfilled, which is bulky and does not corrode, and there is also the problem that the metal is not recovered and is not used effectively.
【0004】この発明は従来の金属とプラスチックとの
混合廃棄物の処理方法が有するこれらの問題点を解消し
、金属を酸化や溶解させずに限られた資源を有効に回収
することや焼却炉を損傷させないこと、そしてプラスチ
ックを完全に燃焼させて炭化物にして嵩の小さい炭化物
(灰)を産業廃棄場、例えば埋立地に埋め立てたりなど
することを目的としたものである。[0004] This invention solves these problems that conventional methods of treating mixed waste of metal and plastic have, and makes it possible to effectively recover limited resources without oxidizing or dissolving the metal, and to use an incinerator. The purpose is to completely burn the plastic and turn it into char, and the small char (ash) can be disposed of in an industrial waste site, such as a landfill.
【0005】[0005]
【課題を解決するための手段】この発明は所定の大きさ
以下に粉砕した金属細片とプラスチック細片とを重量比
4対1位の割合に混合した物をロータリーキルンで所定
の温度で燃焼させてから、炭化物を除去して金属を回収
させた方法である。[Means for Solving the Problems] This invention involves burning a mixture of metal pieces crushed to a predetermined size or less and plastic pieces at a weight ratio of about 4:1 in a rotary kiln at a predetermined temperature. After that, the carbide is removed and the metal is recovered.
【0006】[0006]
【作用】所定の大きさ以下に粉砕した金属細片とプラス
チック細片とをロータリーキルンで所定の温度で燃焼さ
せることによりプラスチック細片は良く燃焼されて嵩が
小さい炭化物となるとともに金属細片は酸化がほとんど
行われないし、かつ溶解されないで、炭化物を除去して
良質な金属細片だけが回収される。[Operation] By burning metal pieces and plastic pieces that have been crushed to below a predetermined size in a rotary kiln at a predetermined temperature, the plastic pieces are well burned and become carbide with small bulk, and the metal pieces are oxidized. Very little is done and no melting is done, carbide is removed and only high quality metal pieces are recovered.
【0007】[0007]
【実施例】次にこの発明の金属とプラスチックとの混合
廃棄物より金属の回収方法を1実施例について説明する
。アルミニウム(Al)、鉄(Fe)、銅(Cu)の金
属とプラスチックとの混合廃棄物を粉砕機により粉砕し
、粉砕機の孔が直径50mmのスクリーンにより50m
m以下の形ちが不定形の金属細片とプラスチック細片だ
けを通過させる。[Embodiment] Next, one embodiment of the method of recovering metal from mixed waste of metal and plastic according to the present invention will be described. A mixed waste of metals such as aluminum (Al), iron (Fe), and copper (Cu) and plastics is crushed by a crusher, and the holes of the crusher are 50 m long by a screen with a diameter of 50 mm.
Only irregularly shaped metal and plastic pieces with a size of less than m are allowed to pass through.
【0008】スクリーンを通過した金属細片とプラスチ
ック細片はベルトコンベアーで比重選別機に運ばれて、
比重選別機により金属細片とプラスチック細片とに分離
される。分離された金属細片はコンベアーで金属細片の
貯蔵タンクに貯蔵される。また分離されたプラスチック
細片は空送されたサイクロンで空気が分級されてプラス
チック細片はプラスチック細片の貯蔵タンクに貯蔵され
る。[0008] The metal pieces and plastic pieces that have passed through the screen are conveyed to a specific gravity sorter by a belt conveyor.
A specific gravity separator separates metal pieces and plastic pieces. The separated metal pieces are stored on a conveyor in a metal piece storage tank. Further, the separated plastic pieces are classified by air-fed cyclone, and the plastic pieces are stored in a plastic piece storage tank.
【0009】金属細片の貯蔵タンクとプラスチック細片
の貯蔵タンクからそれぞれのスクリューコンベアにより
金属細片とプラスチック細片とを重量比4対1位の割合
でロータリーキルンに供給する。ロータリーキルンの中
は最初、バーナーによりプラスチック細片の引火点まで
昇温させるが、プラスチック細片が自己燃焼する温度は
プラスチック細片の種類によって異なるが、通常約30
0℃から約500℃である。ロータリーキルンで自己燃
焼したプラスチック細片はサラサラの燃えつきた炭化物
となり、この炭化物と金属細片はロータリーキルンの排
出口から排出させる。ロータリーキルンから排出された
金属細片と炭化物はスクリューコンベアーにより篩い機
に運ばれて、篩い機で炭化物は篩い分けられ、金属細片
を回収する。回収した金属細片は鉄が磁選機により分け
られ、他の金属の細片は人間などにより選別される。[0009] From the storage tank for metal pieces and the storage tank for plastic pieces, metal pieces and plastic pieces are supplied to the rotary kiln at a weight ratio of about 4:1 by respective screw conveyors. Inside the rotary kiln, the burner first raises the temperature of the plastic pieces to the flash point, but the temperature at which the plastic pieces self-combust varies depending on the type of plastic pieces, but is usually around 30°C.
The temperature range is from 0°C to about 500°C. The plastic debris that self-combusts in the rotary kiln becomes a smooth burnt-out char, and this char and metal debris are discharged from the outlet of the rotary kiln. The metal chips and carbide discharged from the rotary kiln are conveyed by a screw conveyor to a sieve machine, where the carbide is sieved and the metal chips are recovered. The recovered metal pieces are separated into iron by a magnetic separator, and other metal pieces are sorted out by humans.
【0010】自己燃焼したプラスチック細片は予め大き
なプラスチックの容器、フィルムから直径50mm位の
スクリーンを通過する大きさに粉砕してあるとともに回
転しているロータリーキルンの中で金属細片がプラスチ
ック細片を掻上げ羽根(ルーバー)の役割を果すのでプ
ラチック細片の集合体をバラバラにして酸素を円滑に供
給してプラスチック細片を良く自己燃焼させるためにプ
ラスチック細片はベタベタした未燃カーボン(炭化物)
にはならずに、サラサラした炭化物(灰)となる。同時
に金属細片は約300℃から約500℃に加熱されるだ
けで酸素はプラスチック細片の自己燃焼に消費されるた
めに酸化され金属細片は酸化されないし、また溶解され
ないでアルミニウム(Al)、鉄(Fe)、銅(Cu)
としてそれぞれ単体としてロータリーキルンの排出口よ
り排出される。このようにロータリーキルンより約30
0℃から約500℃に加熱された金属細片と炭化物が排
出されるのでロータリーキルンの内部温度はほぼ一定化
される。[0010] The self-combusted plastic pieces are pulverized in advance from a large plastic container and film to a size that can pass through a screen with a diameter of about 50 mm, and the metal pieces are crushed into plastic pieces in a rotating rotary kiln. Since it plays the role of a raking blade (louver), it breaks up the aggregate of plastic pieces and supplies oxygen smoothly.In order to make the plastic pieces self-combust well, the plastic pieces are made of sticky unburned carbon (carbide).
It does not turn into charcoal, but instead becomes a smooth carbide (ash). At the same time, the metal strips are only heated from about 300°C to about 500°C, and the oxygen is oxidized because it is consumed by self-combustion of the plastic pieces, so the metal pieces are not oxidized or melted, and the aluminum (Al) , iron (Fe), copper (Cu)
Each product is discharged from the rotary kiln outlet as a single unit. In this way, about 30
The internal temperature of the rotary kiln is kept almost constant since the metal pieces and carbide heated from 0°C to about 500°C are discharged.
【0011】なお、良好な自己燃焼と雰囲気温度を保つ
ためにプラスチックの種類(または金属細片の種類)に
よりプラスチック細片、金属細片のロータリーキルンへ
の投入量を調整した方がよいし、更にロータリーキルン
の回転数と傾斜度を調整した方が更によい。また金属細
片とプラスチック細片の大きさは金属細片とプラスチッ
ク細片とが混合しやすいためとともにプラスチック細片
が自己燃焼しやすいためにそれぞれの細片は直径約30
mmから約50mmのスクリーンを通過できる大きさが
よい。[0011] In order to maintain good self-combustion and atmospheric temperature, it is better to adjust the amount of plastic pieces and metal pieces fed into the rotary kiln depending on the type of plastic (or type of metal pieces). It is even better to adjust the rotation speed and inclination of the rotary kiln. In addition, the size of the metal and plastic pieces is such that each piece has a diameter of about 30 mm, because the metal and plastic pieces are easy to mix together, and the plastic pieces tend to self-combust.
A size that allows it to pass through a screen of about 50 mm to about 50 mm is preferable.
【0012】0012
【発明の効果】この発明は金属とプラスチックとの混合
廃棄物を所定の大きさ以下に粉砕し、分離した後に、こ
の金属細片とプラスチック細片とを所定の重量比の割合
に混合してロータリーキルンで所定の温度で燃焼させて
炭化物を除去して金属を回収する方法であるから、金属
は酸化されないとともに溶解されないで良好な状態で回
収することができるし、また限られた資源を有効に再利
用することができる。そしてプラスチック細片が自己燃
焼して発生した熱は金属細片に吸収されて所定の温度(
約300℃から約500℃)以上にならないために燃焼
炉であるロータリーキルンを損傷しないという効果があ
る。更にロータリーキルンの中で金属細片がプラスチッ
ク細片を掻き上げ羽根の役割を果すためにプラスチック
細片をバラバラにして酸素を円滑に供給してプラスチッ
ク細片を完全に自己燃焼して完全な炭化物(灰)にする
ことができるし、このように嵩の小さい完全な炭化物を
産業廃棄場、例えば埋立地に埋め立てることにより埋立
地を長期間にわたって有効に利用することができる。[Effects of the Invention] This invention crushes mixed waste of metal and plastic to a predetermined size or less, separates the waste, and then mixes the metal pieces and plastic pieces in a predetermined weight ratio. Since this method recovers metals by burning them at a predetermined temperature in a rotary kiln and removing carbides, the metals can be recovered in good condition without being oxidized or melted, and it is also an effective way to use limited resources. Can be reused. The heat generated by the self-combustion of the plastic strips is absorbed by the metal strips and reaches a predetermined temperature (
Since the temperature does not exceed 300° C. to 500° C., the rotary kiln, which is a combustion furnace, is not damaged. Furthermore, in the rotary kiln, the metal pieces scrape up the plastic pieces and act as blades, breaking the plastic pieces apart and supplying oxygen smoothly, allowing the plastic pieces to completely self-combust and turn into complete carbide ( By burying such a small-volume, complete charred material in an industrial waste site, such as a landfill, the landfill can be used effectively over a long period of time.
Claims (1)
、直径約30mmから50mmのスクリーンを通過する
大きさに、粉砕してから、金属細片とプラスチック細片
とを分離し、金属細片とプラスチック細片とを重量比4
対1位の割合に混合した混合物をロータリーキルンで約
300℃から約500℃で燃焼させ、金属細片から炭化
物を除去することを特徴とする金属とプラスチックとの
混合廃棄物より金属の回収方法。Claim 1: Mixed waste of metal and plastic is crushed to a size that can pass through a screen with a diameter of about 30 mm to 50 mm, and then metal pieces and plastic pieces are separated, and metal pieces and plastic pieces are separated. Weight ratio of plastic strips to 4
A method for recovering metals from a mixed waste of metals and plastics, which comprises burning a mixture in a ratio of 1 to 1 in a rotary kiln at about 300°C to about 500°C to remove carbides from metal pieces.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3131616A JPH04333531A (en) | 1991-05-08 | 1991-05-08 | Method for recovering metal from mixed waste of metal and plastic |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3131616A JPH04333531A (en) | 1991-05-08 | 1991-05-08 | Method for recovering metal from mixed waste of metal and plastic |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04333531A true JPH04333531A (en) | 1992-11-20 |
Family
ID=15062231
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3131616A Pending JPH04333531A (en) | 1991-05-08 | 1991-05-08 | Method for recovering metal from mixed waste of metal and plastic |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04333531A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104480311A (en) * | 2014-11-21 | 2015-04-01 | 邱江波 | Method for separating metal and organic matters |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0253494A (en) * | 1988-08-18 | 1990-02-22 | Kyowa Hakko Kogyo Co Ltd | Production of d-glutamic acid |
-
1991
- 1991-05-08 JP JP3131616A patent/JPH04333531A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0253494A (en) * | 1988-08-18 | 1990-02-22 | Kyowa Hakko Kogyo Co Ltd | Production of d-glutamic acid |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104480311A (en) * | 2014-11-21 | 2015-04-01 | 邱江波 | Method for separating metal and organic matters |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR880002400B1 (en) | Method for melting and treating waste | |
| EP0467929B1 (en) | Method and apparatus for waste treatment | |
| FR2498957A1 (en) | METHOD AND APPARATUS FOR REGENERATING USEFUL SAND SAND | |
| CN113843264A (en) | Method and system for treating waste salt through microwave thermal desorption and oxidation | |
| JP4672896B2 (en) | Regeneration method of incineration ash | |
| JPH1180761A (en) | Fuel production from waste | |
| KR102061159B1 (en) | Method and apparatus for mixed thermal treatment of organic sludge and contaminated soil | |
| JP3278384B2 (en) | Pollution-free regeneration treatment plant for waste | |
| JPH04333531A (en) | Method for recovering metal from mixed waste of metal and plastic | |
| JPH08245966A (en) | Treatment of waste by carbonization | |
| JPH0348624B2 (en) | ||
| JPH11190510A (en) | Incinerating method of waste in incinerator and treating method of slag generated by waste incineration | |
| CN216881002U (en) | System for through rotary kiln microwave thermal desorption and oxidation treatment waste salt | |
| JP4004252B2 (en) | Waste melting treatment method | |
| JP2001021125A (en) | Apparatus for recovering valuable resources and method for recovering valuable resources in dry distillation pyrolysis melting combustion equipment for waste | |
| JP2001280614A (en) | Waste treatment equipment | |
| JP2010216763A (en) | Waste disposal method, and method of recovering metal from waste | |
| JPH0952079A (en) | Shredder-A device for processing and recycling dust | |
| JP4660260B2 (en) | Recycling equipment for construction residue | |
| JP7100602B2 (en) | Incinerator ash treatment method and treatment equipment | |
| JP4737731B2 (en) | Method of firing construction soil | |
| JP2706634B2 (en) | Recycling method of main ash of stalker type incinerator | |
| CN113877937B (en) | Method and system for thermal desorption and oxidation treatment of waste salt through rotary kiln microwaves | |
| JP2014088457A (en) | Method for carbonization treatment of waste and carbonizing device | |
| JP3917775B2 (en) | Recycling method of incineration ash |