JPS6354769B2 - - Google Patents
Info
- Publication number
- JPS6354769B2 JPS6354769B2 JP55120083A JP12008380A JPS6354769B2 JP S6354769 B2 JPS6354769 B2 JP S6354769B2 JP 55120083 A JP55120083 A JP 55120083A JP 12008380 A JP12008380 A JP 12008380A JP S6354769 B2 JPS6354769 B2 JP S6354769B2
- Authority
- JP
- Japan
- Prior art keywords
- pyrolysis gas
- melting furnace
- resin
- furnace
- burner
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
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
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/82—Recycling of waste of electrical or electronic equipment [WEEE]
Landscapes
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、ラミネートアルミ箔、アルミサツ
シ材、アルミ箔、被覆電線のような樹脂被覆金属
製品から、金属を回収する装置に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to an apparatus for recovering metal from resin-coated metal products such as laminated aluminum foil, aluminum sash material, aluminum foil, and coated electric wire.
なお、樹脂被覆とは、上記の様に表面に樹脂が
被覆せられたものはもとより、アルミサツシ等の
材型の溝にシール材等の樹脂を挾持したものも含
むものとする。 Note that the resin coating includes not only those whose surfaces are coated with resin as described above, but also those in which a resin such as a sealing material is sandwiched in the grooves of a material such as an aluminum sash.
従来技術とその問題点
樹脂被覆金属製品から金属を回収する場合、従
来は大気中における焼却法により行なわれてし
た。ところが、この方法では金属自身も酸化し、
回収効率が悪くなるという欠点があつた。そこ
で、溶解炉内をArガス、N2ガス等の不活性ガス
で充満させるか、あるいは炉内を真空減圧状態に
することにより、炉内を非酸化性雰囲気としてこ
の雰囲気を保持しつつ樹脂被覆金属製品を溶融す
る方法が考えられる。しかしながら、この方法で
は金属の回収効率は良くなるが、炉内を非酸化性
雰囲気に保持するためのランニングコストが高く
なるという欠点があつた。また、金属を溶融せし
めるさいに生じる樹脂の熱分解ガス中に、分解タ
ール状物質が多量に発生するためにこれを処理す
る設備が必要となり、コストが高くなるという問
題があつた。さらに、金属を溶融させるための熱
エネルギーをかなり必要とするので、この点にお
いても経済性に問題があつた。Prior art and its problems When recovering metal from resin-coated metal products, conventional incineration in the atmosphere was used. However, with this method, the metal itself also oxidizes,
The drawback was that the collection efficiency deteriorated. Therefore, by filling the melting furnace with an inert gas such as Ar gas or N2 gas, or by reducing the pressure inside the furnace to a vacuum state, the resin coating can be performed while maintaining a non-oxidizing atmosphere inside the furnace. One possible method is to melt the metal product. However, although this method improves metal recovery efficiency, it has the disadvantage that running costs for maintaining the inside of the furnace in a non-oxidizing atmosphere become high. In addition, since a large amount of decomposed tar-like substances are generated in the thermal decomposition gas of the resin that is generated when the metal is melted, equipment for processing this is required, resulting in an increase in cost. Furthermore, since a considerable amount of thermal energy is required to melt the metal, there is also an economical problem in this respect.
この発明は上記実情に鑑みてなされたものであ
つて、あらゆる点で経済性に優れた樹脂被覆金属
製品からの金属回収装置を提供することを目的と
する。 This invention has been made in view of the above circumstances, and it is an object of the present invention to provide a metal recovery device from resin-coated metal products that is economical in all respects.
問題点を解決するための手段
この発明による樹脂被覆金属製品からの金属回
収装置は、樹脂被覆金属製品溶解炉と、この溶解
炉の外部にこれを近接して配置されかつ炎孔が溶
解炉に向けられた溶解炉加熱バーナおよび熱分解
ガス燃焼バーナと、溶解炉内上端部と熱分解ガス
燃焼バーナとを連通させる熱分解ガス供給路と、
熱分解ガス燃焼バーナに酸素を供給する酸素供給
路とからなるものである。Means for Solving the Problems The apparatus for recovering metal from resin-coated metal products according to the present invention includes a resin-coated metal product melting furnace, and a flame hole disposed outside the melting furnace in close proximity to the melting furnace. a pyrolysis gas supply path that communicates a melting furnace heating burner and a pyrolysis gas combustion burner, and an upper end of the melting furnace and the pyrolysis gas combustion burner;
It consists of an oxygen supply path that supplies oxygen to the pyrolysis gas combustion burner.
実施例
以下、この発明を、実施例を示す図面に基いて
説明する。Embodiments Hereinafter, the present invention will be explained based on drawings showing embodiments.
樹脂被覆金属製品からの金属回収装置は、上端
が開口した樹脂被覆金属溶解炉1と、溶解炉1の
外部にこれを近接して配置されかつ炎孔が溶解炉
1に向けられた炉1を加熱するための溶解炉加熱
バーナ2と、同じく溶解炉1の下端部の外部にこ
れを近接して配置されかつ炎孔が溶解炉1の下端
部に向けられた熱分解ガス燃焼バーナ3と、溶解
炉1内の上端部と熱分解ガス燃焼バーナ3との間
に配されて、炉1内とバーナ3とを連通させる熱
分解ガス供給路4と、熱分解ガス燃焼バーナ3に
酸素を供給する酸素供給路5とからなる。 The apparatus for recovering metal from resin-coated metal products includes a resin-coated metal melting furnace 1 whose upper end is open, and a furnace 1 which is placed close to the outside of the melting furnace 1 and whose flame holes are directed toward the melting furnace 1. A melting furnace heating burner 2 for heating; a pyrolysis gas combustion burner 3 which is also disposed outside and close to the lower end of the melting furnace 1 and whose flame hole is directed toward the lower end of the melting furnace 1; A pyrolysis gas supply passage 4 is disposed between the upper end of the melting furnace 1 and the pyrolysis gas combustion burner 3 and communicates the interior of the furnace 1 with the burner 3, and supplies oxygen to the pyrolysis gas combustion burner 3. and an oxygen supply path 5.
溶解炉1、熱分解ガス燃焼バーナ3および熱分
解ガス供給部4は耐火物でつくられた加熱室6内
に収納されている。 The melting furnace 1, the pyrolysis gas combustion burner 3, and the pyrolysis gas supply section 4 are housed in a heating chamber 6 made of refractory material.
溶解炉1の下端部には加熱室6の底壁を貫通し
て外方に延びる溶湯取出路7が設けられている。 A molten metal outlet passage 7 is provided at the lower end of the melting furnace 1 and extends outward through the bottom wall of the heating chamber 6.
加熱バーナ2は、加熱室6の周壁に複数個取付
けられており、それぞれ周壁を外側から貫通して
炎孔が内方を向くようになされている。 A plurality of heating burners 2 are attached to the peripheral wall of the heating chamber 6, and each penetrates the peripheral wall from the outside so that the flame hole faces inward.
加熱室6の頂壁には樹脂被覆金属製品投入口8
が設けられている。この投入口8は、図面に示す
ように蓋9で閉じておいてもよいし、あるいは常
に開口しておいてもよい。なぜならば、樹脂の熱
分解ガスが重いために、炉1内に充満した熱分解
ガスは、液体が容器からあふれるように、炉1か
らあふれて供給路4を経てバーナ3に至り、投入
口8から逃げることがないからである。また、加
熱室6の頂壁には熱分解ガスを燃焼させた後の排
気ガスを排出するための排気口10が設けられて
いる。 There is a resin-coated metal product inlet 8 on the top wall of the heating chamber 6.
is provided. This inlet 8 may be closed with a lid 9 as shown in the drawings, or may be kept open at all times. This is because the pyrolysis gas of the resin is heavy, so the pyrolysis gas filling the furnace 1 overflows from the furnace 1 through the supply path 4 to the burner 3, just like liquid overflowing from a container, and reaches the burner 3 through the supply port 8. This is because there is no escape from it. Furthermore, an exhaust port 10 is provided on the top wall of the heating chamber 6 for discharging exhaust gas after combusting the pyrolysis gas.
このような装置において、投入口8からポリエ
チレンおよび酢酸ビニルで被覆された樹脂被覆ア
ルミニウム箔11(樹脂被覆金属製品)を、溶解
炉1内に投入する。ついで、溶解炉加熱バーナ2
で炉1を加熱すると、炉1内の温度が所定の温度
に達し、箔11を被覆している樹脂(ポリエチレ
ンおよび酢酸ビニル)は熱分解されてガス化す
る。そして、この熱分解ガスが炉1内に充満し
て、炉1内は非酸化性雰囲気となる。熱分解ガス
は、炉1内に充満した後も発生し、余剰のガスは
第1図に矢印で示すように、ガス自身の重さで熱
分解ガス供給路4を通つて熱分解ガス燃焼バーナ
3に至る。ここで、熱分解ガスと酸素とが適当な
混合比となるように、酸素供給路5からバーナ3
に酸素を供給し、バーナ3で熱分解ガスを燃焼さ
せる。このときに、熱分解ガスに含まれている熱
分解タール状物質も完全に燃焼する。こうして、
溶解炉1内の温度が300℃を越えると溶解炉加熱
バーナ2を消して、熱分解ガス燃焼バーナ3だけ
で溶解炉1を加熱する。なぜならば、炉1内の温
度が300℃を越えると熱分解ガスの発生量が急激
に増加するために、この熱分解ガスを燃焼させる
ことにより得られるエネルギーによつて溶解炉1
を充分に加熱することができるからである。その
後、炉1内の温度がアルミニウムの融点を越える
とアルミニウム箔1は溶融し、その溶湯が溶湯取
出路7から取出される。一方、熱分解ガスを燃焼
させることにより発生した排気ガスは排気口10
から外部に排出されるが、この排気ガス中からは
CO2とH2Oのみが検出される。 In such an apparatus, a resin-coated aluminum foil 11 (resin-coated metal product) coated with polyethylene and vinyl acetate is charged into the melting furnace 1 from an input port 8 . Next, melting furnace heating burner 2
When the furnace 1 is heated, the temperature inside the furnace 1 reaches a predetermined temperature, and the resin (polyethylene and vinyl acetate) covering the foil 11 is thermally decomposed and gasified. This pyrolysis gas then fills the furnace 1, creating a non-oxidizing atmosphere inside the furnace 1. Pyrolysis gas is generated even after the furnace 1 is filled, and the excess gas is passed through the pyrolysis gas supply path 4 by the weight of the gas itself to the pyrolysis gas combustion burner, as shown by the arrow in Fig. 1. 3. Here, the oxygen supply path 5 is connected to the burner 3 so that the pyrolysis gas and oxygen have an appropriate mixing ratio.
The pyrolysis gas is combusted by the burner 3. At this time, the pyrolysis tar-like substances contained in the pyrolysis gas are also completely combusted. thus,
When the temperature inside the melting furnace 1 exceeds 300°C, the melting furnace heating burner 2 is turned off and the melting furnace 1 is heated only by the pyrolysis gas combustion burner 3. This is because when the temperature inside the furnace 1 exceeds 300°C, the amount of pyrolysis gas generated increases rapidly.
This is because it can be heated sufficiently. Thereafter, when the temperature inside the furnace 1 exceeds the melting point of aluminum, the aluminum foil 1 is melted, and the molten metal is taken out from the molten metal removal path 7. On the other hand, the exhaust gas generated by burning the pyrolysis gas is discharged from the exhaust port 10.
However, from this exhaust gas,
Only CO 2 and H 2 O are detected.
上記実施例においては、炉1内の温度が300℃
を越えると、溶解炉加熱バーナ2を消して熱分解
ガス燃焼バーナ3だけで溶解炉1を加熱している
ので、加熱バーナ2用の燃料を大幅に節約するこ
とができるが、金属製品が溶融するまで加熱バー
ナ2を使用してもよい。その場合にも加熱バーナ
2だけで加熱する場合よりは加熱バーナ2用の燃
料を大幅に節約することができる。また、熱分解
ガスの発生量が不十分で、熱分解ガスを燃焼させ
て得られるエネルギーだけでは、金属製品の融点
以上に加熱することができない場合には、当然の
ことながら加熱バーナ2を併用しなければならな
いが、この場合にも、もちろん加熱バーナ2用の
燃料を節約することができる。 In the above example, the temperature inside the furnace 1 is 300°C.
If the melting furnace heating burner 2 exceeds The heating burner 2 may be used until the In this case as well, the fuel for the heating burner 2 can be significantly saved compared to the case where the heating burner 2 alone is used for heating. In addition, if the amount of pyrolysis gas generated is insufficient and it is not possible to heat the metal product above its melting point using only the energy obtained by burning the pyrolysis gas, heating burner 2 is of course used in combination. However, in this case as well, the fuel for the heating burner 2 can of course be saved.
発明の効果
この発明の装置によれば、上述のようにして、
金属製品を被覆している樹脂の熱分解ガスが溶解
炉内に充満した後、熱分解ガスが熱分解ガス供給
路を通つて熱分解ガス燃焼バーナに至つてここで
燃焼されるので、溶解炉内を、熱分解ガスで非酸
化性雰囲気に保つた状態で、溶解炉の外側から樹
脂被覆金属製品を加熱することができる。したが
つて、金属を溶融させるさいに金属が酸化消耗す
るのを完全に防止でき、金属の回収効率が向上す
る。Effects of the Invention According to the device of this invention, as described above,
After the pyrolysis gas from the resin coating the metal product fills the melting furnace, the pyrolysis gas passes through the pyrolysis gas supply path to the pyrolysis gas combustion burner, where it is burned. The resin-coated metal product can be heated from outside the melting furnace while maintaining a non-oxidizing atmosphere inside with pyrolysis gas. Therefore, it is possible to completely prevent the metal from being consumed by oxidation when melting the metal, and the metal recovery efficiency is improved.
また、金属製品を被覆している樹脂の熱分解ガ
スで非酸化性雰囲気をつくるので、別途に不活性
ガスを用いたり、真空減圧したりする必要もな
く、非酸化性雰囲気をつくるためのランニングコ
ストは不要になる。また、金属を溶融するための
熱エネルギとして金属製品を被覆していた樹脂の
熱分解ガスを燃焼させて、このさいに生じる熱を
用いるので、従来の方法に比べて、金属を溶融さ
せるための燃料使用量を大幅に減少させることが
できる、さらに、熱分解ガスを燃焼させるさい
に、このガスに含まれているタール状物質も燃焼
するので、別個にこのタール状物質を処理する設
備が不要となり、その費用も省略することができ
る。したがつてこの発明の装置を使用した方法は
あらゆる点で経済的に優れている。 In addition, since a non-oxidizing atmosphere is created using the thermal decomposition gas of the resin that coats the metal product, there is no need to use a separate inert gas or to reduce the pressure in a vacuum. The cost becomes unnecessary. In addition, the heat generated during this process is used by burning the thermal decomposition gas of the resin that coats the metal product as thermal energy for melting the metal. The amount of fuel used can be significantly reduced.Furthermore, when the pyrolysis gas is combusted, the tar-like substances contained in this gas are also combusted, so there is no need for separate equipment to process this tar-like substance. Therefore, that cost can also be omitted. Therefore, the method using the device of this invention is economically superior in all respects.
図面はこの発明による製品の実施例を示し、第
1図は垂直縦断面図、第2図は第1図の―線
にそう断面図である。
1……溶解炉、2……溶解炉加熱バーナ、3…
…熱分解ガス燃焼バーナ、4……熱分解ガス供給
路、5……酸素供給路。
The drawings show an embodiment of the product according to the invention, in which FIG. 1 is a vertical sectional view, and FIG. 2 is a sectional view taken along the line --- in FIG. 1... Melting furnace, 2... Melting furnace heating burner, 3...
...Pyrolysis gas combustion burner, 4...Pyrolysis gas supply path, 5...Oxygen supply path.
Claims (1)
の外部にこれに近接して配置されかつ炎孔が溶解
炉1に向けられた溶解炉加熱バーナ2および熱分
解ガス燃焼バーナ3と、溶解炉1内上端部と熱分
解ガス燃焼バーナ3とを連通させる熱分解ガス供
給路4と、熱分解ガス燃焼バーナ3に酸素を供給
する酸素供給路5とからなる、樹脂被覆金属製品
からの金属回収装置。1 Resin coated metal product melting furnace 1 and this melting furnace 1
A melting furnace heating burner 2 and a pyrolysis gas combustion burner 3 are arranged outside and close to the melting furnace 1 and have flame holes directed toward the melting furnace 1, and an upper end inside the melting furnace 1 and the pyrolysis gas combustion burner 3. An apparatus for recovering metals from resin-coated metal products, comprising a pyrolysis gas supply path 4 that communicates with the pyrolysis gas supply path 4 and an oxygen supply path 5 that supplies oxygen to the pyrolysis gas combustion burner 3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12008380A JPS5743941A (en) | 1980-08-29 | 1980-08-29 | Method and apparatus for recovering metal from resin coated metal product |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12008380A JPS5743941A (en) | 1980-08-29 | 1980-08-29 | Method and apparatus for recovering metal from resin coated metal product |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5743941A JPS5743941A (en) | 1982-03-12 |
| JPS6354769B2 true JPS6354769B2 (en) | 1988-10-31 |
Family
ID=14777476
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12008380A Granted JPS5743941A (en) | 1980-08-29 | 1980-08-29 | Method and apparatus for recovering metal from resin coated metal product |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5743941A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5335882A (en) * | 1976-09-14 | 1978-04-03 | Mitsubishi Electric Corp | Conveyance means operation interval display device |
-
1980
- 1980-08-29 JP JP12008380A patent/JPS5743941A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5743941A (en) | 1982-03-12 |
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