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JP2649419B2 - Separation and recovery method of composite waste - Google Patents

Separation and recovery method of composite waste

Info

Publication number
JP2649419B2
JP2649419B2 JP15851489A JP15851489A JP2649419B2 JP 2649419 B2 JP2649419 B2 JP 2649419B2 JP 15851489 A JP15851489 A JP 15851489A JP 15851489 A JP15851489 A JP 15851489A JP 2649419 B2 JP2649419 B2 JP 2649419B2
Authority
JP
Japan
Prior art keywords
waste
pvc
urethane
materials
composite
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 - Fee Related
Application number
JP15851489A
Other languages
Japanese (ja)
Other versions
JPH0323909A (en
Inventor
元博 近藤
寛治 大山
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.)
Toyota Motor Corp
Howa Co Ltd
Original Assignee
Howa Textile Industry Co Ltd
Toyota Motor 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 Howa Textile Industry Co Ltd, Toyota Motor Corp filed Critical Howa Textile Industry Co Ltd
Priority to JP15851489A priority Critical patent/JP2649419B2/en
Publication of JPH0323909A publication Critical patent/JPH0323909A/en
Application granted granted Critical
Publication of JP2649419B2 publication Critical patent/JP2649419B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B9/00General arrangement of separating plant, e.g. flow sheets
    • B03B9/06General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
    • B03B9/061General arrangement of separating plant, e.g. flow sheets specially adapted for refuse the refuse being industrial
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/52Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、複数の材料が接着した複合材の廃棄物(ス
クラップ、不良品等)から、1種又はそれ以上の材料を
分離回収する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a method for separating and recovering one or more materials from a composite waste (scrap, defective product, etc.) to which a plurality of materials are adhered. About.

〈従来の技術〉 最近では資源の有限性、原材料価格の高騰又は公害防
止の観点から、廃棄物の再生利用が一段と強く要請され
るようになってきている。単一の材料からなる廃棄物で
あればその再生利用は容易である。しかし複数の材料が
接着した複合材については、それを構成する各材料を採
算性よく分離回収することが不可能であることが多く、
再生利用が殆どの場合行なわれていない。
<Conventional Technology> In recent years, from the viewpoint of resource finiteness, soaring raw material prices or preventing pollution, there is an increasing demand for recycling of waste. Recycling of waste consisting of a single material is easy. However, for a composite material to which a plurality of materials are bonded, it is often impossible to recover and collect each of the constituent materials with good profitability.
Recycling is not done in most cases.

そのような複合材の廃棄物の一例として、ポリウレタ
ンとPVC(ポリ塩化ビニル)が積層した廃棄物(以下、
ウレタン付着PVC廃棄物という)がある。これは自動車
内装部品等の製造工場で多量に発生するものであるが、
通常焼却又は埋立処分されている。しかしウレタン付着
PVC廃棄物を焼却処分すると、PVC中に含まれている塩素
が塩化水素となり、それが焼却炉やその付帯設備を腐食
させるので設備の寿命が短くなるうえに公害問題を引き
起こし易い。
As an example of such composite material waste, polyurethane and PVC (polyvinyl chloride) laminated waste (hereinafter, referred to as waste)
Urethane-adhered PVC waste). This occurs in large quantities in manufacturing plants for automobile interior parts, etc.
Usually incinerated or landfilled. But urethane adhesion
When PVC waste is incinerated, chlorine contained in the PVC becomes hydrogen chloride, which corrodes the incinerator and its ancillary equipment, shortening the life of the equipment and causing pollution problems.

そのため一部でウレタン付着PVC廃棄物の分離回収が
試みられている。その方法はウレタン付着PVC廃棄物を
カッターミル等で破砕することによりPVCからウレタン
を剥離させ、その破砕集合物を多段の分級装置で分級す
ることによりPVCとウレタンを分離回収する方法であ
る。
For this reason, some attempts have been made to separate and collect urethane-bound PVC waste. In this method, urethane adhered to PVC is crushed by a cutter mill or the like to separate urethane from PVC, and the crushed aggregate is classified by a multi-stage classifier to separate and collect PVC and urethane.

〈発明が解決しようとする課題〉 上記のウレタン付着PVC廃棄物の分離回収方法には次
のような問題点がある: カッターミルによる粉砕はマクロ的にはPVCからウレ
タンを剥離することであるが、ミクロ的にはカッターに
よりウレタン付着PVC廃棄物を純ウレタン片、幾らかの
ウレタンが付着したPVC片、及び純PVC片の3種に切断す
ることであり、PVC層の薄い廃棄物では前2片の生成が
主であるから、回収されたPVCにはその物性低下の主因
となるウレタンの混入が避けられない; カッターミルによる粉砕ではウレタンとPVCがほぼ同
等の大きさで粉砕されるため、フルイによる分級が行な
えず、比重差による分級が必要となるが、その場合、気
流中での飛散距離の差を利用する簡便な乾式分級方法で
は各粉砕片がどの方向を向くかで受ける風力が左右され
るのでウレタンとPVCを十分に分級できず、湿式分級方
法では操作が非常に面倒となる。
<Problems to be Solved by the Invention> The above-mentioned method of separating and recovering urethane-adhered PVC waste has the following problems: Milling by a cutter mill is to peel urethane from PVC macroscopically. Microscopically, a cutter cuts urethane-adhered PVC waste into three types: pure urethane pieces, PVC pieces to which some urethane is attached, and pure PVC pieces. Urethane, which is the main cause of the deterioration of physical properties, is unavoidable in the recovered PVC because it mainly generates pieces. Since the urethane and PVC are crushed by the cutter mill in almost the same size, Classification by sieving cannot be performed and classification by specific gravity difference is required.In this case, a simple dry classification method that uses the difference in scattering distance in the air stream will cause Left and right It can not be sufficiently classified urethane and PVC because the operation is very troublesome in wet classification method.

以上のように、複数の異なる材料が接着した複合材か
ら分離回収された材料は、一般的に不純物を含むために
新品の材料に比較して物性的に劣るという問題があり、
一方高純度に分離回収しようとすれば極めて低収率で企
業の採算ベースに乗りにくいという問題がある。これら
の問題が複合材廃棄物の分離回収・再生利用を困難にし
ている。
As described above, a material separated and recovered from a composite material to which a plurality of different materials are bonded generally has a problem that physical properties are inferior to a new material due to containing impurities.
On the other hand, there is a problem that it is difficult to separate and recover with high purity at a very low yield and to be profitable for a company. These problems make separation, recovery and recycling of composite waste difficult.

本発明は上記諸問題を解決する目的でなされたもので
あり、その解決しようとする課題は、複数の材料が接着
した複合材の廃棄物から、その構成材料を簡便なる手段
を以って高純度且つ高収率に分離回収する方法を提供す
ることである。
The present invention has been made for the purpose of solving the above-mentioned problems, and the problem to be solved is to improve the constituent material from a composite material to which a plurality of materials are adhered by using a simple means. It is an object of the present invention to provide a method of separating and recovering the compound in a high purity and a high yield.

〈課題を解決するための手段〉 上記課題を解決できる本発明の複合材廃棄物の分離回
収方法は、硬さの異なる複数の材料が接着した複合材の
廃棄物を粗粉砕し、次いでそれを高速攪拌機で攪拌する
ことにより各材料毎に異なる平均粒度に粉砕した後、分
級することを特徴とする。
<Means for Solving the Problems> The method for separating and recovering composite material waste according to the present invention, which can solve the above-described problems, roughly crushes composite material waste to which a plurality of materials having different hardnesses are adhered, and then crushes it. The material is pulverized to a different average particle size for each material by stirring with a high-speed stirrer, and then classified.

本発明方法において、廃棄物はその各材料の硬さが互
いに異なる必要があり、ウレタン付着PVCのように硬さ
の差が大きいほど良好に分離回収できるが、通常複合材
の廃棄物は互いに硬さの異なる材料でできているから、
本発明方法は殆どの廃棄物に対して適用できる。なお
“複数の材料が接着した複合材”というのは、その各材
料が相互に溶融したり、均一に分散したりしていない材
料、例えば各材料が積層した又は組み合わさった材料を
意味する。複合材の構成材料としては熱可塑性樹脂、熱
硬化性樹脂、軟質及び軟質ゴム等が挙げられる。
In the method of the present invention, the hardness of each waste material must be different from each other, and the greater the difference in hardness, such as urethane-attached PVC, the better the separation and recovery can be achieved. Made of different materials,
The method of the present invention is applicable to most wastes. The “composite material in which a plurality of materials are bonded” means a material in which the materials are not mutually melted or uniformly dispersed, for example, a material in which the materials are stacked or combined. Examples of the constituent material of the composite material include a thermoplastic resin, a thermosetting resin, soft and soft rubber, and the like.

本発明方法はいわば、廃棄物を粗粉砕する第1工程、
高速攪拌機で粉砕する第2工程及び粉砕集合物を分級す
る第3工程からなっている。以下各工程ごとに説明す
る。
The method of the present invention is, so to speak, a first step of coarsely pulverizing waste,
It comprises a second step of pulverizing with a high-speed stirrer and a third step of classifying the pulverized aggregate. Hereinafter, each step will be described.

第1工程での粗粉砕は、工場等から発生する廃棄物が
トリミング屑のように細長いものであるから、第2工程
での作業性を向上させるために行なうものである。よっ
て粗粉砕といえどもなるべく細かくした方がよいが、細
かくするほど粉砕コストがアップし、再生利用のメリッ
トが無くなる。一方、大きく粗粉砕するほど次工程での
作業性が悪化する。そのため第1工程の粗粉砕工程では
適当な破砕機もしくは切断機等を用いて、外寸約20mm〜
50mm程度の塊状物に粗粉砕するのが好ましい。
The coarse grinding in the first step is performed in order to improve the workability in the second step, because the waste generated from the factory or the like is elongated like trimming waste. Therefore, it is better to make the coarse grinding as fine as possible, but the finer the grinding, the higher the grinding cost and the advantage of recycling is lost. On the other hand, the larger the coarse pulverization, the worse the workability in the next step. Therefore, in the first coarse crushing step, an external size of about 20 mm to
It is preferable to roughly pulverize into a lump of about 50 mm.

第2工程はいわば高速攪拌機による廃棄物の粉砕工程
である。従来のカッターミルによる粉砕は複合材の各材
料とも同程度に粉砕しているのに対して、本発明におい
ては材料毎に異なる平均粒度に即ち各材料が互いに離れ
た粒度分布を持つこととなるように粉砕する。
The second step is, so to speak, a step of pulverizing waste with a high-speed stirrer. Whereas conventional pulverization with a cutter mill pulverizes each material of the composite material to the same degree, in the present invention, each material has a different average particle size, that is, each material has a particle size distribution separated from each other. And crush.

従来、攪拌機は2種以上の材料を均一に混合するのに
利用されていたのに対して、本発明では2種以上の材料
を分離するのに利用するため、従来とは全く正反対の作
用を働かせることになる。またその効果として上記の選
択的粉砕が可能となる。
Conventionally, a stirrer has been used to uniformly mix two or more types of materials, whereas in the present invention, since it is used to separate two or more types of materials, the stirrer has a completely opposite effect. Will work. As an effect thereof, the above-mentioned selective pulverization becomes possible.

高速攪拌機の回転数、回転羽根形状、攪拌時間、温度
等の条件は処理する複合材廃棄物の各材料が異なる粒度
で粉砕されるように選択すればよい。
The conditions such as the number of revolutions of the high-speed stirrer, the shape of the rotating blades, the stirring time, and the temperature may be selected so that each material of the composite waste to be treated is pulverized with different particle sizes.

第3工程では、第2工程で得られた粉砕集合体を適当
に分級するが、粒度差を利用してフルイ分けするのが簡
便であり、傾斜式、振動式、回転式等のフルイ分け機で
十分である。もし各材料にかなりの比重差がある場合に
は従来通り比重を利用して分離することもできる。
In the third step, the pulverized aggregate obtained in the second step is appropriately classified, but it is easy to sift using a difference in particle size, and a sieving machine such as an inclined type, a vibrating type, and a rotary type is used. Is enough. If there is a considerable difference in specific gravity between the materials, separation can be performed by using the specific gravity as in the past.

〈作用〉 硬さの異なる材料が接着した複合材の廃棄物を高速攪
拌機で攪拌すると、廃棄物は高速で回転する攪拌羽根か
ら剪断力を受ける。それに対する応力は硬さの異なる材
料毎に異なることから、一材料のみが粉砕されるか又は
各材料が離れた粒度分布を持つように粉砕される。粉砕
集合体を粒度の揃ったいくつかの級別に分けると各材料
の単離されたものが得られる。
<Operation> When a composite waste to which materials having different hardnesses are bonded is stirred by a high-speed stirrer, the waste receives shearing force from a high-speed rotating stirring blade. Since the stress on it differs for different hardness materials, only one material is ground or each material is ground to have a discrete particle size distribution. Separating the milled aggregate into several grades of uniform particle size provides an isolated version of each material.

〈実施例〉 自動車用インストルメントパネルパッド(内層材:軟
質ウレタンフォーム、表皮材:PVC)の製造工程で生じる
トリミング屑(約140×50cmの枠形、周囲肉部の幅10〜1
5cm、同厚さ10〜15mm)を入手し、外寸30mm程度の大き
さに粗粉砕した。この粉砕は通常の一軸式のカッターミ
ルを利用し、φ30のカッタースクリーンを通過した粗粉
砕物を集め、それを次ぎのように高速攪拌処理した。
<Example> Trimming debris (approximately 140 x 50 cm frame shape, width of surrounding meat part 10 to 1) generated in the manufacturing process of automotive instrument panel pads (inner layer material: soft urethane foam, skin material: PVC)
5 cm, the same thickness 10-15 mm) was obtained and coarsely pulverized to a size of about 30 mm in outer size. For this pulverization, a general uniaxial cutter mill was used to collect the coarse pulverized materials that passed through a φ30 cutter screen, and the resulting mixture was subjected to a high-speed stirring treatment as follows.

ここで使用する高速攪拌機は、三井三池化工機(株)
製の三井ヘンシェルミキサーFM150Jであり、図に示すよ
うな構造をしている。混合槽1の容量は150であり、
温度調節できるジャケット2を備えている。排出弁3の
開閉はエアシリンダ4で行なわれる。上羽根5及び下羽
根6は三相誘導電動機7により回転する。図中の8はベ
ルトが掛け渡された各Vプーリを表わしている。
The high-speed stirrer used here is Mitsui Miike Kakoki Co., Ltd.
Mitsui Henschel Mixer FM150J, which has the structure shown in the figure. The capacity of the mixing tank 1 is 150,
A jacket 2 capable of controlling the temperature is provided. The opening and closing of the discharge valve 3 is performed by an air cylinder 4. The upper blade 5 and the lower blade 6 are rotated by a three-phase induction motor 7. Reference numeral 8 in the figure denotes each V pulley around which the belt is stretched.

エアー抜き9及びデフレクタ10が取り付けられている
蓋11を開け、ウレタン付着PVC廃棄物の粗粉砕物を投入
し蓋11を閉めてから高速攪拌機を作動させると、混合槽
1内の処理物は下羽根6によって上方向の回転力を与え
られ流動し、上羽根5によって強力な剪断力を受ける。
この剪断力によって極めて短時間でウレタンがPVCから
剥脱されると共に微粉砕される。PVCはほぼ粗粉砕時の
寸法のままである。
When the lid 11 to which the air vent 9 and the deflector 10 are attached is opened, a coarsely crushed urethane-adhered PVC waste is put in, the lid 11 is closed, and then the high-speed stirrer is operated. The blade 6 is given an upward rotational force to flow, and receives a strong shearing force by the upper blade 5.
Due to this shearing force, urethane is exfoliated from PVC and pulverized in a very short time. PVC is almost the same size as when coarsely crushed.

この処理では室温常圧下、上記高速攪拌機を7000rpm
で5分間回転させた。取り出した処理物を次いで8メッ
シュのフルイによって粒径1〜2mmの粉末状ウレタンと
外寸30mm程度のシート片状PVCを分離した。こうして回
収されたPVCは理論回収率の約95%であった。
In this process, the above high-speed stirrer is operated at 7000 rpm under room temperature and normal pressure.
For 5 minutes. The treated product was then separated with an 8-mesh sieve into powder urethane having a particle size of 1 to 2 mm and sheet-like PVC having an outer dimension of about 30 mm. The PVC thus recovered was about 95% of the theoretical recovery.

上記の様に分離回収されたPVCを2本ロール機にて15
分間練ることによって試験片を作り、比重、硬さ、引張
強さ、伸び、及び引裂強さについて調べた。なお比重は
JIS−K−7112試験法6.2水中置換法によって測定し、硬
さはJIS−K−6031試験法:スプリング硬度(20℃)法
で測定した。また引張強さ、伸び及び引裂強さはいづれ
もJIS−K−6301試験法に基づいて測定した。
The PVC separated and recovered as described above is rolled into a 15
Specimens were made by kneading for minutes and examined for specific gravity, hardness, tensile strength, elongation, and tear strength. The specific gravity is
JIS-K-7112 test method 6.2 Measured by the underwater displacement method, and the hardness was measured by the JIS-K-6031 test method: spring hardness (20 ° C) method. The tensile strength, elongation and tear strength were all measured based on the JIS-K-6301 test method.

得られた試験結果を下記表に示す。対照試験として従
来方法により分離回収されたPVC、新品のPVC及び未処理
の廃棄物について行なわれた試験の結果も示す。
The test results obtained are shown in the table below. As a control test, the results of tests performed on PVC separated and recovered by the conventional method, new PVC, and untreated waste are also shown.

この結果から従来方法よりも本発明方法で分離回収さ
れたPVCの方が再生利用に適する物性を備えていること
が分かる。
From this result, it can be seen that the PVC separated and recovered by the method of the present invention has physical properties more suitable for recycling than the conventional method.

上記のように回収されたPVCは単体でPVCシートとして
利用したり、炭酸カルシウム等を加えて防振シート等と
して利用できる。また回収されたウレタンは微粉化して
いるため高付加価値製品として幅広く利用できる。その
利用先としては、サンバイザー基材、クッション材等が
ある。
The PVC recovered as described above can be used alone as a PVC sheet, or can be used as a vibration-proof sheet or the like by adding calcium carbonate or the like. The recovered urethane is finely divided and can be widely used as a high value-added product. As a use destination, there are a sun visor base material and a cushion material.

この実施例では2層構造の廃棄物を用いたが、3層以
上の廃棄物でも本実施例と同様にあるいは高速攪拌とフ
ルイ分けを繰り返して材料の分離回収を行なえることは
今までの説明から容易に理解されよう。
In this embodiment, waste having a two-layer structure is used. However, it is possible to separate and collect materials in the same manner as in the present embodiment or by repeating high-speed stirring and sieving for waste having three or more layers. Will be easily understood from.

〈発明の効果〉 本発明の複合材廃棄物の分離回収方法は以下のような
効果を奏する。
<Effects of the Invention> The method for separating and recovering composite waste of the present invention has the following effects.

まず高速攪拌機の回転羽根により複合材廃棄物に剪断
力を与えて各材料をほぼ完全に分離できるので回収率が
一段の向上し、省資源に寄与できる。
First, the shearing force is applied to the composite material waste by the rotating blades of the high-speed stirrer, so that each material can be separated almost completely, so that the recovery rate is further improved and can contribute to resource saving.

また上記のほぼ完全な分離によって、回収された材料
の純度が高まる。このことは物性的に新品材料に尚更近
いものが得られることを意味しており、再利用範囲の拡
大を図ることができる。
The almost complete separation also increases the purity of the recovered material. This means that a material that is even closer to a new material in physical properties can be obtained, and the range of reuse can be expanded.

そのうえ各材料を互いに粒度の異なる粉砕物として回
収できるため、分級方法が容易であり、フルイでも十分
分級できる。したがって分離回収費の低コスト化を実現
できる。
In addition, since each material can be collected as pulverized materials having different particle sizes, the classification method is easy, and even a sieve can be sufficiently classified. Therefore, the cost of separation and collection can be reduced.

【図面の簡単な説明】[Brief description of the drawings]

図は本発明方法の一実施例で使用された高速攪拌機を示
す概要図である。
FIG. 1 is a schematic diagram showing a high-speed stirrer used in one embodiment of the method of the present invention.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】硬さの異なる複数の材料が接着した複合材
の廃棄物を粗粉砕し、次いでそれを高速攪拌機で攪拌す
ることにより各材料毎に異なる平均粒度に粉砕した後、
分級することを特徴とする複合材廃棄物の分離回収方
法。
The method comprises the steps of: coarsely pulverizing a composite waste to which a plurality of materials having different hardnesses are adhered, and then pulverizing the composite waste to a different average particle size for each material by stirring it with a high-speed stirrer;
A method for separating and recovering composite material waste, characterized by classifying.
JP15851489A 1989-06-21 1989-06-21 Separation and recovery method of composite waste Expired - Fee Related JP2649419B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15851489A JP2649419B2 (en) 1989-06-21 1989-06-21 Separation and recovery method of composite waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15851489A JP2649419B2 (en) 1989-06-21 1989-06-21 Separation and recovery method of composite waste

Publications (2)

Publication Number Publication Date
JPH0323909A JPH0323909A (en) 1991-01-31
JP2649419B2 true JP2649419B2 (en) 1997-09-03

Family

ID=15673402

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15851489A Expired - Fee Related JP2649419B2 (en) 1989-06-21 1989-06-21 Separation and recovery method of composite waste

Country Status (1)

Country Link
JP (1) JP2649419B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4216638C1 (en) * 1992-05-20 1993-09-16 Daimler-Benz Aktiengesellschaft, 70567 Stuttgart, De
JP5604085B2 (en) * 2009-11-24 2014-10-08 カルソニックカンセイ株式会社 Laminated resin crushing and separating device

Also Published As

Publication number Publication date
JPH0323909A (en) 1991-01-31

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