[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JP2013147523A - Dry distillation apparatus and method for recovering metallic resources using the same - Google Patents

Dry distillation apparatus and method for recovering metallic resources using the same Download PDF

Info

Publication number
JP2013147523A
JP2013147523A JP2012006757A JP2012006757A JP2013147523A JP 2013147523 A JP2013147523 A JP 2013147523A JP 2012006757 A JP2012006757 A JP 2012006757A JP 2012006757 A JP2012006757 A JP 2012006757A JP 2013147523 A JP2013147523 A JP 2013147523A
Authority
JP
Japan
Prior art keywords
dry distillation
metal
cylindrical body
aluminum
distillation apparatus
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
JP2012006757A
Other languages
Japanese (ja)
Inventor
Nobuaki Mizuki
伸明 水木
Naoki Takasaka
直樹 高坂
Kazuhiro Take
一広 竹
Kunihiro Tejima
邦弘 手嶋
Natsuko Kobayashi
夏子 小林
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.)
TONAMI TRANSPORTATION CO Ltd
Diamond Engineering Co Ltd
Original Assignee
TONAMI TRANSPORTATION CO Ltd
Diamond Engineering 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 TONAMI TRANSPORTATION CO Ltd, Diamond Engineering Co Ltd filed Critical TONAMI TRANSPORTATION CO Ltd
Priority to JP2012006757A priority Critical patent/JP2013147523A/en
Publication of JP2013147523A publication Critical patent/JP2013147523A/en
Pending legal-status Critical Current

Links

Images

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

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Coke Industry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a dry distillation apparatus in which the recovery of metallic resources from a metal and organic substance composite raw material can be performed by one rotary kiln.SOLUTION: A dry distillation apparatus includes a cylinder that includes: a feed section of a material to be processed in one end thereof; and a carrying out part of a processed material in the other end thereof, wherein the cylinder is rotatably supported. The cylinder is slightly inclined or horizontal so that the carrying out part side is located downward of the feed section, thereby the material to be processed gradually moves to the carrying out part side by the rotation of the cylinder, the cylinder is partitioned in two or more processing chambers by partition walls that open partially to pass the material to be processed, and the amount of air or supporting gas of the processing chamber that is nearer the carrying-out part is relatively more increased than that of the processing chamber near the feed section among the two or more processing chambers.

Description

本発明は金属と有機物とが複合又は混合状態にある原料から乾留により金属資源を回収するのに効果的な乾留装置に関する。   The present invention relates to a dry distillation apparatus effective for recovering metal resources by dry distillation from a raw material in which a metal and an organic substance are in a composite or mixed state.

紙又はプラスチック材あるいはそれらの積層材に、アルミ箔を積層したものや蒸着した複合材がある。
この種のアルミ複合材は各種飲料の容器、各種液体食品の容器、食品及び菓子類の包装材、医薬品の包装材等多くの分野にて使用され、使用後は廃棄物として処理されている。
しかし、アルミ層の厚みが薄く通常の廃棄物の焼却ではこのアルミ層が酸化されてしまい、金属アルミとしての回収が困難であった。
そこで本発明者らは、アルミが加熱により融けない温度でこれらのアルミ系廃棄物を乾留処理することで金属アルミを回収できないか検討した。
There are paper or plastic materials, or laminates of these materials in which aluminum foil is laminated or a vapor-deposited composite material.
This kind of aluminum composite material is used in many fields such as containers for various beverages, containers for various liquid foods, packaging materials for foods and confectionery, and packaging materials for pharmaceuticals.
However, the thickness of the aluminum layer is thin, and the incineration of ordinary waste oxidizes the aluminum layer, making it difficult to recover it as metallic aluminum.
Therefore, the present inventors have examined whether or not metal aluminum can be recovered by subjecting these aluminum wastes to dry distillation at a temperature at which aluminum does not melt by heating.

アルミ箔を積層した、あるいはアルミを蒸着したプラスチック材又は紙材あるいはその複合材は乾留初期の加熱温度300〜450℃の段階では可燃性ガスが多く発生するために乾留室を低酸素状態にしなければ発火し、800℃以上の燃焼状態になる。
それでは融点が約600℃前後の金属アルミを回収することができない。
また、複合材から揮発成分が留出した後はアルミの表面に炭化物が付着したままの状態になり、純度の高いアルミを回収することができなかった。
そこでロータリーキルンの試験機を用いて相対的に空気の供給量を少なく抑えつつ、第1回目の乾留処理を行い、次に第1回目よりも相対的に空気の供給量を多くして第2回目の乾留処理をした。
その結果、表面が銀白色の純度の高い金属アルミ箔が得られた。
しかしながら、2回処理となると1台のロータリーキルンでは連続処理ができず、2台のロータリーキルンをつなぐことは設備が大型になるだけでなく、エネルギー消費も多くなる問題があった。
Plastic materials, paper materials, or composite materials with aluminum foil laminated or aluminum deposited on it must generate low-oxygen conditions in the dry distillation chamber because a lot of flammable gas is generated at the heating temperature of 300 to 450 ° C at the initial stage of dry distillation. If it fires, it becomes a combustion state of 800 ° C. or higher.
Then, metal aluminum having a melting point of about 600 ° C. cannot be recovered.
Moreover, after the volatile component was distilled from the composite material, the carbide remained attached to the surface of the aluminum, and high purity aluminum could not be recovered.
Therefore, using the rotary kiln tester, the first dry distillation treatment was performed while keeping the air supply amount relatively low, and then the air supply amount was increased more than the first time, and the second time. The dry distillation treatment was performed.
As a result, a highly pure metal aluminum foil having a silver-white surface was obtained.
However, when two treatments are performed, continuous treatment cannot be performed with one rotary kiln, and connecting two rotary kilns has a problem that not only the equipment becomes large, but also energy consumption increases.

特許文献1に多段式ロータリーキルンを開示するが、これも複数のロータリーキルンをつないだものである。   Patent Document 1 discloses a multistage rotary kiln, which also connects a plurality of rotary kilns.

特開2001−31412号公報JP 2001-31412 A

本発明は1台のロータリーキルンで金属・有機物複合原料から金属資源の回収ができる乾留装置の提供を目的とする。   An object of the present invention is to provide a dry distillation apparatus capable of recovering metal resources from a metal / organic composite raw material with a single rotary kiln.

1つの回転支持された円筒体中を被処理物が徐々に搬出部側に向けて移動する際に、従来のロータリーキルンでは、炉内の被処理物の供給部側と搬出部側とで空気又は助燃ガス量に差を設けることが難しかった。
本発明に係る乾留処理装置は、各被処理物に適した段階的な乾留ができ、特に複合原料からの金属の回収に適し、一端に被処理物の供給部を有し、他端に処理物の搬出部を有する回転支持された円筒体を備えた乾留装置であって、前記円筒体は、搬出部側が供給部よりも下方に位置するように僅かに傾斜又は水平になっていることで当該円筒体の回転により、被処理物が徐々に搬出部側に移動し、当該被処理物を通過させるための部分的に開口した仕切壁にて複数の処理室に仕切ってあり、前記複数の処理室のうち、供給部に近い処理室よりも搬出部に近い処理室の空気又は助燃ガス量を相対的に多くしたことを特徴とする。
ここで複数の処理室に仕切るとは、1つの円筒体の内側を回転軸方向に沿って、この円筒体の回転により被処理物が徐々に搬出部側に向けて移動する際に、被処理物が通過できるように部分的に開口した仕切壁で仕切ることで各処理室における空気又は助燃ガスの量に差を設けることが可能にしたことをいう。
また、2つ以上に区分けするものであれば処理室の数に制限がなく、対象となる被処理物(原料)の水分率、有機物と金属の配合割合に応じて多段階に乾留処理する趣旨である。
従って、本発明に係る乾留装置の前に予備的な乾燥装置等を有してもよい。
円筒体を複数の処理室に区分したことにより、乾留ガスが最も発生する処理室から効率よくこの乾留ガスを回収することができるので、複数の処理室のうち少なくとも1つの処理室は発生した可燃性液体又は/及び可燃性ガスの回収手段を有するのが好ましい。
回収した可燃性液体又は/及び可燃性ガスは燃料として再利用するのが好ましい。
In the conventional rotary kiln, when the object to be processed moves gradually toward the unloading part in one rotation-supported cylindrical body, air or air is supplied between the supply part side and the unloading part side of the object to be processed in the furnace. It was difficult to make a difference in the amount of auxiliary combustion gas.
The carbonization treatment apparatus according to the present invention is capable of gradual carbonization suitable for each material to be treated, particularly suitable for recovering metals from composite raw materials, having a material supply part at one end, and processing at the other end. A carbonization device comprising a rotation-supported cylindrical body having an object carry-out section, wherein the cylinder body is slightly inclined or horizontal so that the carry-out section side is positioned below the supply section. Due to the rotation of the cylindrical body, the object to be processed is gradually moved toward the unloading part, and is partitioned into a plurality of processing chambers by partially opened partition walls for allowing the object to be processed to pass therethrough. Among the processing chambers, the amount of air or auxiliary combustion gas in the processing chamber close to the unloading unit is relatively larger than that in the processing chamber close to the supply unit.
Here, partitioning into a plurality of processing chambers means that the object to be processed is moved when the inner side of one cylindrical body is gradually moved toward the unloading portion by the rotation of the cylindrical body. It means that it is possible to provide a difference in the amount of air or auxiliary combustion gas in each processing chamber by partitioning with a partition wall partially opened so that an object can pass through.
In addition, the number of treatment chambers is not limited as long as it can be divided into two or more, and the purpose of the dry distillation treatment is multi-stage depending on the moisture content of the object to be treated (raw material) and the blending ratio of organic matter and metal. It is.
Therefore, you may have a preliminary drying apparatus etc. in front of the carbonization apparatus which concerns on this invention.
By dividing the cylindrical body into a plurality of processing chambers, it is possible to efficiently recover the dry distillation gas from the processing chamber in which the dry distillation gas is most generated. Therefore, at least one of the plurality of processing chambers has generated combustible gas. It is preferable to have a means for recovering the combustible liquid and / or combustible gas.
The recovered flammable liquid and / or flammable gas is preferably reused as fuel.

このように1つの円筒体の内側を複数の処理室に区分けしたので、被処理物を段階的に乾留するのに適し、特に被処理物として金属・有機物複合原料を供給し、供給部側に近い処理室にて可燃性液体及びガス成分を留出させ、搬出部側に近い処理室で脱炭処理することで、炭化物や有機不純物の少ない金属資源を回収することができる。
ここで、金属・有機物複合材料とは金属成分と、紙、プラスチック、木質材料等の有機物とが複合化されているものをいい、複合形態は積層,混合,マトリックス中の分散等、その状態の種類を問わない。
その中でも特にアルミニウム及びその合金、マグネシウム及びその合金等の低融点金属やチタニウム及びその合金のように酸化されやすい金属の回収に有効である。
さらにはアルミ箔を積層又はアルミ蒸着した紙又は/及びプラスチック等の包装材のアルミ系複合廃棄物からアルミニウム及びその合金を回収するのに有効である。
これらの金属は、酸素との親和性が高く、金属が箔のように薄い場合に紙やプラスチックが燃焼することなく炭化させる工程と、金属に炭化物として付着している不純物を脱炭処理する工程とを一つのキルンで実現した点に本発明の特徴がある。
As described above, since the inside of one cylindrical body is divided into a plurality of processing chambers, it is suitable for dry distillation of the object to be processed in stages. In particular, the metal / organic composite raw material is supplied as the object to be processed, and is supplied to the supply unit side. A combustible liquid and a gas component are distilled off in a nearby processing chamber and decarburized in a processing chamber close to the carrying-out side, thereby recovering metal resources with less carbides and organic impurities.
Here, a metal / organic composite material is a composite of a metal component and an organic material such as paper, plastic, wood, etc., and the composite form is such as lamination, mixing, dispersion in a matrix, etc. Any type.
Among them, it is particularly effective for recovering low-melting metals such as aluminum and its alloys, magnesium and its alloys, and metals that are easily oxidized such as titanium and its alloys.
Furthermore, it is effective for recovering aluminum and its alloys from aluminum-based composite waste of packaging materials such as paper and / or plastic laminated with aluminum foil or deposited with aluminum.
These metals have a high affinity with oxygen, and when the metal is thin like a foil, a process of carbonizing paper and plastic without burning, and a process of decarburizing impurities adhering to the metal as carbides The feature of the present invention is that the above is realized by one kiln.

本発明は外熱または内熱方式による還元性雰囲気加熱システムを採用するロータリーキルンなどの回転体において、1つの円筒体の内側を回転軸方向に沿って複数の処理室に区分けしたので、従来の多段式ロータリーキルンを用いることなく、被処理物の処理状態に応じて段階的な乾留条件及び脱炭条件を設定することができるので、円筒体の回転駆動装置、加熱装置等の共通化が可能であり、コンパクトで省エネルギー化を図った乾留装置となる。   In the rotary body such as a rotary kiln adopting a reducing atmosphere heating system using an external heat or internal heat system, the present invention divides the inside of one cylindrical body into a plurality of processing chambers along the rotation axis direction. Without using a rotary kiln, stepwise carbonization conditions and decarburization conditions can be set according to the processing state of the workpiece, so that it is possible to share a cylindrical rotation drive device, heating device, etc. It is a dry distillation device that is compact and saves energy.

また、このような乾留装置を用いることで、例えば包装材に用いられた後に廃棄されたアルミ系複合廃棄物を処理すると、プラスチック等の有機成分が多量に発生する乾留初期には供給する空気又は助燃ガスを少なくするか、あるいは空気等の供給を止めた状態で加熱することで発火することを防止でき、アルミ箔等が酸化消失するのを抑えることができる。
この状態ではアルミ箔等の表面に茶褐色のカーボン類の不純物が残っているが、その後の処理室で空気や助燃ガスの供給量を相対的に多くしてもカーボン類の不純物が発火することなく脱炭するので、不純物の少ない純度の高いアルミニウム及びその合金からなるアルミ箔等が得られる。
In addition, by using such a carbonization device, for example, when aluminum composite waste discarded after being used for packaging materials is processed, air supplied in the initial stage of carbonization where a large amount of organic components such as plastic is generated or It is possible to prevent ignition by reducing the amount of the auxiliary combustion gas or by heating in a state where supply of air or the like is stopped, and it is possible to suppress the oxidation loss of the aluminum foil or the like.
In this state, brown carbon impurities remain on the surface of the aluminum foil or the like, but even if the supply amount of air or auxiliary combustion gas is relatively increased in the subsequent processing chamber, the carbon impurities do not ignite. Since decarburization is performed, high-purity aluminum with few impurities and an aluminum foil made of an alloy thereof can be obtained.

本発明に係る乾留装置の構造例を模式的に示す。The structural example of the carbonization apparatus which concerns on this invention is shown typically.

本発明に係る乾留装置10は図1に模式的に示すように、被処理物(原材料)を供給する供給部11bと、処理を終えた処理物を搬出する搬出部11cとを有する円筒体11を、前後2つのリング体15a,15bを介してローラー支持部16a,16bで回転支持している。
円筒体11は供給部11bと搬出部11cとが水平か又は供給部11bよりも搬出部11cの方が下になるように0.1〜2°傾斜した状態で支持されていて、図示を省略したスプロケット駆動やギヤ駆動等の回転駆動装置により回転制御されている。
円筒体11の内側は回転軸方向に沿って仕切壁12にて複数の処理室に仕切られている。
本実施例では円筒体11を供給部側の前室13と搬出部側の後室14の2つの処理室に仕切壁12にて仕切った例になっているが、処理室の数に制限はない。
また、本実施例では被処理物が撹拌しながら搬出部11c側に移動するように円筒体11の内側の回転方向に沿って所定の間隔を設けながらパドル11aを取り付けた例になっている。
円筒体11の外周側は熱風式の加熱部30を有する外熱型ロータリーキルンとなっている。
As schematically shown in FIG. 1, a dry distillation apparatus 10 according to the present invention has a cylindrical body 11 having a supply part 11b for supplying an object to be processed (raw material) and an unloading part 11c for unloading the processed object. Is rotatably supported by the roller support portions 16a and 16b via the two front and rear ring bodies 15a and 15b.
The cylindrical body 11 is supported in a state where the supply portion 11b and the carry-out portion 11c are horizontal or inclined by 0.1 to 2 ° so that the carry-out portion 11c is lower than the supply portion 11b. The rotation is controlled by a rotary drive device such as a sprocket drive or a gear drive.
The inside of the cylindrical body 11 is partitioned into a plurality of processing chambers by a partition wall 12 along the rotation axis direction.
In this embodiment, the cylindrical body 11 is divided into two processing chambers, a front chamber 13 on the supply unit side and a rear chamber 14 on the unloading unit side, by the partition wall 12, but the number of processing chambers is limited. Absent.
Further, in this embodiment, the paddle 11a is attached while providing a predetermined interval along the rotation direction inside the cylindrical body 11 so that the object to be processed moves toward the carry-out portion 11c while stirring.
The outer peripheral side of the cylindrical body 11 is an external heating type rotary kiln having a hot air heating unit 30.

仕切壁12は円筒体11と一緒に回転するように円筒体11の内側に取り付けられ、被処理物は通過するが、空気や発生ガスの移動を抑えるように外周側を部分的に開口した通過開口部12aと、中央部に配管を通すための配管挿通孔12bとを有する。
中央部の配管挿通孔12bも前室13と後室14との間で空気や排ガスの移動が少なくなるように小さな開口部となっている。
通過開口部12aと配管挿通孔12bの合せた開口部の面積は、円筒体の内側断面積に対して5〜15%の範囲が好ましい。
The partition wall 12 is attached to the inside of the cylindrical body 11 so as to rotate together with the cylindrical body 11, and the object to be processed passes through it, but the outer peripheral side is partially opened so as to suppress the movement of air and generated gas. It has the opening part 12a and the piping insertion hole 12b for letting piping pass in the center part.
The central pipe insertion hole 12b is also a small opening so that movement of air and exhaust gas between the front chamber 13 and the rear chamber 14 is reduced.
The area of the combined opening of the passage opening 12a and the pipe insertion hole 12b is preferably in the range of 5 to 15% with respect to the inner cross-sectional area of the cylindrical body.

前室13は前室空気供給管18aと前室排ガス管17aが備えられていて、空気の供給量と排ガス量が制御されている。
この前室排ガス管17aで回収した可燃ガスは燃料として回収できる。
後室14は後室空気供給管18bと後室排ガス管17bが備えられていて、空気の供給量と排ガス量が制御されている。
なお、各処理室で空気や助燃ガスの量が制御できれば、それぞれの処理室にこの空気供給管及び排ガス管の両方を設ける必要はない。
The front chamber 13 is provided with a front chamber air supply pipe 18a and a front chamber exhaust gas pipe 17a, and the supply amount of air and the amount of exhaust gas are controlled.
The combustible gas recovered by the front chamber exhaust pipe 17a can be recovered as fuel.
The rear chamber 14 is provided with a rear chamber air supply pipe 18b and a rear chamber exhaust pipe 17b, and the supply amount of air and the amount of exhaust gas are controlled.
If the amount of air or auxiliary combustion gas can be controlled in each processing chamber, it is not necessary to provide both the air supply pipe and the exhaust gas pipe in each processing chamber.

円筒体11の供給部11b側には外部から空気が浸入するのを抑えながら接続した供給装置20を有する。
本実施例はスクリュー21を内蔵した例になっていて、このスクリュー21の回転により被処理部材Mが搬送供給されるようになっている。
円筒体11の搬出部11c側には外部から空気が浸入するのを防止しながら接続した資源回収部19を有し、ここに処理が終わった金属資源Mが回収される。
The cylindrical body 11 has a supply device 20 connected to the supply unit 11b side while suppressing air from entering from the outside.
This embodiment they become an example with a built-in screw 21, the member to be processed M 1 is adapted to be conveyed supplied by the rotation of the screw 21.
The discharge portion 11c side of the cylindrical body 11 has a resource collection unit 19 connected while preventing the air from the outside entering, metal resources M 2 the process is completed here is recovered.

上記のような乾留装置10を用いて、アルミ系廃棄物から金属アルミを回収する実験を行った。
実験は円筒体11の内径約600mm、加熱部全長約1700mm、この軸方向中央部に仕切壁12を取り付けたものを用いた。
従って、前室13及び後室14の加熱面積はそれぞれ約1.6mである。
プラスチックが積層したアルミ系廃棄物の場合に前室の空気供給量は、0.5〜6Nm/プラスチック−kgの範囲が好ましく、後室の空気供給量は、10〜30Nm/Al−kgが好ましい。
Using the carbonization apparatus 10 as described above, an experiment was conducted to recover metallic aluminum from aluminum-based waste.
In the experiment, a cylindrical body 11 having an inner diameter of about 600 mm, a heating part with an overall length of about 1700 mm, and a partition wall 12 attached to the central part in the axial direction was used.
Accordingly, the heating areas of the front chamber 13 and the rear chamber 14 are each about 1.6 m 2 .
In the case of plastic waste laminated aluminum, the air supply amount in the front chamber is preferably in the range of 0.5-6 Nm 3 / plastic-kg, and the air supply amount in the rear chamber is 10-30 Nm 3 / Al-kg. Is preferred.

前室13及び後室14の処理室の温度が580〜620℃になるように円筒体11を外部から熱風加熱し、PET:80%,アルミ:20%とからなる包装材の廃棄物を5kg/h投入した。
前室13に被処理材1kg当たり5Nmになるように空気を供給し、後室14に被処理材に含まれるアルミ1kg当たり30Nmになるように空気を供給した状態で乾留及び脱炭処理した結果、不純物1%以下の金属アルミを回収できた。
The cylindrical body 11 is heated with hot air from the outside so that the temperatures of the processing chambers of the front chamber 13 and the rear chamber 14 are 580 to 620 ° C., and 5 kg of packaging waste consisting of PET: 80% and aluminum: 20% / H input.
Carbonization and decarburization treatment in a state of supplying air to be treated material 1kg per 5 Nm 3, air was supplied so that the aluminum 1kg per 30 Nm 3 contained in the treated material in the rear chamber 14 into the front chamber 13 As a result, metallic aluminum having impurities of 1% or less could be recovered.

実施例1と同じ加熱条件で、実施例1に用いた同じ被処理材を25kg/h投入し、前室13の空気供給量を1Nm/被処理物1kg,後室14の空気供給量を10Nm/アルミ分1kgとした。
これにより、不純物5%以下の金属アルミを回収できた。
In the same heating conditions as in Example 1, Example The same workpiece is 25 kg / h introduced using the 1, prechamber 13 1 Nm 3 / treatment object 1kg an air supply, the air supply amount of the rear chamber 14 10 Nm 3 / aluminum content 1 kg.
As a result, metal aluminum having an impurity content of 5% or less was recovered.

(比較例1)
円筒体11の仕切壁12を取り外した状態で、加熱温度580〜620℃、空気供給量1Nm/被処理物1kgの条件で、被処理材25kg/h投入、一室による乾留処理を行ったところ、アルミの表面が茶褐色であり、不純物の量が23%もあった。
(Comparative Example 1)
With the partition wall 12 of the cylindrical body 11 removed, the material to be treated was charged at 25 kg / h and the dry distillation treatment was performed in one chamber under the conditions of a heating temperature of 580 to 620 ° C., an air supply amount of 1 Nm 3 / a material to be treated of 1 kg. However, the surface of aluminum was brown and the amount of impurities was 23%.

上記、実施例2と比較例1との結果から、本発明に係る乾留装置を用いるとアルミ系廃棄物から純度の高い金属アルミを回収することができることが明らかになった。   From the results of Example 2 and Comparative Example 1 described above, it was revealed that high-purity metallic aluminum can be recovered from aluminum-based waste when the dry distillation apparatus according to the present invention is used.

10 乾留装置
11 円筒体
11a パドル
11b 供給部
11c 搬出部
12 仕切壁
12a 通過開口部
13 前室
14 後室
15a リング体
15b リング体
16a ローラー支持部
16b ローラー支持部
17a 前室排ガス管
17b 後室排ガス管
18a 前室空気供給管
18b 後室空気供給管
19 資源回収部
30 加熱部
DESCRIPTION OF SYMBOLS 10 Carbonization apparatus 11 Cylindrical body 11a Paddle 11b Supply part 11c Unloading part 12 Partition wall 12a Passing opening part 13 Front chamber 14 Rear chamber 15a Ring body 15b Ring body 16a Roller support part 16b Roller support part 17a Front chamber exhaust pipe 17b Rear chamber exhaust gas Tube 18a Front chamber air supply tube 18b Rear chamber air supply tube 19 Resource recovery unit 30 Heating unit

Claims (4)

一端に被処理物の供給部を有し、他端に処理物の搬出部を有する回転支持された円筒体を備えた乾留装置であって、
前記円筒体は、搬出部側が供給部よりも下方に位置するように僅かに傾斜又は水平になっていることで当該円筒体の回転により、被処理物が徐々に搬出部側に移動し、当該被処理物を通過させるための部分的に開口した仕切壁にて複数の処理室に仕切ってあり、
前記複数の処理室のうち、供給部に近い処理室よりも搬出部に近い処理室の空気又は助燃ガス量を相対的に多くしたことを特徴とする乾留装置。
It is a dry distillation apparatus comprising a rotation-supported cylindrical body having a workpiece supply part at one end and a delivery part for the treatment object at the other end,
The cylindrical body is slightly inclined or horizontal so that the unloading part side is located below the supply part, so that the workpiece is gradually moved to the unloading part side by the rotation of the cylindrical body. It is partitioned into a plurality of processing chambers by a partially opened partition wall for passing the object to be processed,
A dry distillation apparatus characterized in that, among the plurality of processing chambers, the amount of air or auxiliary combustion gas in the processing chamber close to the carry-out portion is relatively larger than the processing chamber close to the supply portion.
前記複数の処理室のうち少なくとも1つの処理室は発生した可燃性液体又は/及び可燃性ガスの回収手段を有することを特徴とする請求項1記載の乾留装置。   2. The dry distillation apparatus according to claim 1, wherein at least one of the plurality of processing chambers has a means for recovering the generated combustible liquid and / or combustible gas. 請求項1又は2記載の乾留装置を用いて、被処理物として金属・有機物複合原料を供給し、
供給部側に近い処理室にて可燃性液体及びガス成分を留出させ、搬出部側に近い処理室にて脱炭処理することで金属資源を回収することを特徴とする金属資源の回収方法。
Using the carbonization apparatus according to claim 1 or 2, supplying a metal / organic composite raw material as an object to be treated,
A method for recovering a metal resource, characterized in that a combustible liquid and a gas component are distilled off in a processing chamber close to the supply unit, and the metal resource is recovered by decarburizing in the processing chamber close to the unloading unit. .
前記金属・有機物複合原料がアルミ系複合廃棄物であり、回収金属がアルミニウム及びその合金であることを特徴とする請求項3記載の金属資源の回収方法。   4. The method for recovering a metal resource according to claim 3, wherein the metal / organic composite material is aluminum composite waste, and the recovered metal is aluminum and its alloy.
JP2012006757A 2012-01-17 2012-01-17 Dry distillation apparatus and method for recovering metallic resources using the same Pending JP2013147523A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2012006757A JP2013147523A (en) 2012-01-17 2012-01-17 Dry distillation apparatus and method for recovering metallic resources using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2012006757A JP2013147523A (en) 2012-01-17 2012-01-17 Dry distillation apparatus and method for recovering metallic resources using the same

Publications (1)

Publication Number Publication Date
JP2013147523A true JP2013147523A (en) 2013-08-01

Family

ID=49045369

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2012006757A Pending JP2013147523A (en) 2012-01-17 2012-01-17 Dry distillation apparatus and method for recovering metallic resources using the same

Country Status (1)

Country Link
JP (1) JP2013147523A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104449773A (en) * 2014-10-20 2015-03-25 辽宁科技大学 Method and device for upgrading low-rank pulverized coal
WO2016155236A1 (en) * 2015-04-03 2016-10-06 石家庄新华能源环保科技股份有限公司 Dividing-wall rotary kiln device

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02272294A (en) * 1989-04-12 1990-11-07 Takasago Ind Co Ltd Rotary kiln
JPH0849826A (en) * 1994-08-05 1996-02-20 Takasago Ind Co Ltd Externally heating rotary kiln
JPH1099815A (en) * 1996-09-30 1998-04-21 Toshiba Corp Method and apparatus for treatment
JP2000080386A (en) * 1998-09-04 2000-03-21 Tokyo Yogyo Co Ltd Preparation of fuel from sludge
JP2000513764A (en) * 1997-05-30 2000-10-17 アルコア・ネーデルランド・ベー・ブイ Method for treating a material comprising aluminum and plastic
JP2001240918A (en) * 1999-12-24 2001-09-04 Mettsu Corporation:Kk Method for recovering aluminum from used beverage can

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02272294A (en) * 1989-04-12 1990-11-07 Takasago Ind Co Ltd Rotary kiln
JPH0849826A (en) * 1994-08-05 1996-02-20 Takasago Ind Co Ltd Externally heating rotary kiln
JPH1099815A (en) * 1996-09-30 1998-04-21 Toshiba Corp Method and apparatus for treatment
JP2000513764A (en) * 1997-05-30 2000-10-17 アルコア・ネーデルランド・ベー・ブイ Method for treating a material comprising aluminum and plastic
JP2000080386A (en) * 1998-09-04 2000-03-21 Tokyo Yogyo Co Ltd Preparation of fuel from sludge
JP2001240918A (en) * 1999-12-24 2001-09-04 Mettsu Corporation:Kk Method for recovering aluminum from used beverage can

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104449773A (en) * 2014-10-20 2015-03-25 辽宁科技大学 Method and device for upgrading low-rank pulverized coal
WO2016155236A1 (en) * 2015-04-03 2016-10-06 石家庄新华能源环保科技股份有限公司 Dividing-wall rotary kiln device

Similar Documents

Publication Publication Date Title
CN103380218A (en) Valuable metal recovery method
JP2013147523A (en) Dry distillation apparatus and method for recovering metallic resources using the same
US10527280B2 (en) High organic concurrent decoating kiln
JP2010012409A (en) Heat treatment device/method
JP5019347B2 (en) Magnesium alloy cutting waste processing method
WO2011142001A1 (en) Method and device for producing pelm kernel shell charcoal
JP6289167B2 (en) Method for producing activated carbon
US7828548B2 (en) Reduction kiln
JP2009161845A (en) Method for pretreatment of scrap
RU2336125C1 (en) Method of continuous production of peat-mineral hydrophobic oil sorbent
JP2015190651A (en) Waste treatment method
JP4908914B2 (en) Processing equipment such as aluminum chips
CN110592369B (en) Hot sodium loading and modification process for vanadium removal tailings in organic matter refining
TW202231882A (en) Zinc collection method
CN205909285U (en) Preliminary treatment type sludge incineration processing system
CN206018645U (en) A kind of Disposal System of Mud Burning
JP3519622B2 (en) Multi-stage treatment of charge
CN104017962A (en) Protective atmosphere generating device
CN205909284U (en) High -efficient sludge incineration processing system
JP2016141832A (en) Method for treating oil-impregnated dust sludge, and method for producing iron making raw material
US707638A (en) Process of producing steel direct from oxid-of-iron ore.
JP5356699B2 (en) Pyrolysis treatment system and pyrolysis treatment method
JP2017190923A (en) Rotary kiln
JP4301410B2 (en) Method for producing dry distillation graphite from waste tires
Elanskij Processing the steel scrap: experience of German specialists.

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20140711

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20150605

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20150610

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20150729

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20150817