JPS60212434A - Separation and recovery of composite material - Google Patents

Separation and recovery of composite material

Info

Publication number
JPS60212434A
JPS60212434A JP59068635A JP6863584A JPS60212434A JP S60212434 A JPS60212434 A JP S60212434A JP 59068635 A JP59068635 A JP 59068635A JP 6863584 A JP6863584 A JP 6863584A JP S60212434 A JPS60212434 A JP S60212434A
Authority
JP
Japan
Prior art keywords
solvent
resin
adhesive
composite
aluminum foil
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
JP59068635A
Other languages
Japanese (ja)
Inventor
Yoshihiro Shirai
白井 義弘
Yasuo Saito
齋藤 保夫
Takao Hioki
日置 高夫
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.)
Takeda Pharmaceutical Co Ltd
Original Assignee
Takeda Chemical Industries 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 Takeda Chemical Industries Ltd filed Critical Takeda Chemical Industries Ltd
Priority to JP59068635A priority Critical patent/JPS60212434A/en
Publication of JPS60212434A publication Critical patent/JPS60212434A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • B29B2017/0213Specific separating techniques
    • B29B2017/0293Dissolving the materials in gases or liquids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/0097Glues or adhesives, e.g. hot melts or thermofusible adhesives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2705/00Use of metals, their alloys or their compounds, for preformed parts, e.g. for inserts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2705/00Use of metals, their alloys or their compounds, for preformed parts, e.g. for inserts
    • B29K2705/02Aluminium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2009/00Layered products
    • B29L2009/003Layered products comprising a metal layer
    • 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

Abstract

PURPOSE:A composite of a thermoplastic resin and aluminum foil is dipped in a specific solvent to dissolve off the adhesive, then rinsed with water to separate into the resin and the foil, thus enabling their recovery in pure forms free from the other components. CONSTITUTION:A composite which has been made by adhering aluminum foil to thermoplastic resin with an adhesive is dipped in a solvent which can penetrate the resin and dissolves the adhesive to dissolve off the adhesive or lower its adhesion. Then, the composite is taken out of the solvent, then rinsed with water to peel off the aluminum foil from the resin. The solvent used contains 15vol% of a solvent selected from alkyl esters of lower fatty acids, lower aliphatic ketones, 6-10C hydrocarbon, 1-8C halogenated hydrocarbons and ethers.

Description

【発明の詳細な説明】 本発明は熱可塑性樹脂とアルミニウム箔の複合体から熱
可塑性樹脂とアルミニウム箔を分離して、それらを別個
に回収する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for separating a thermoplastic resin and aluminum foil from a composite of thermoplastic resin and aluminum foil and recovering them separately.

熱可塑性合成樹脂とアルミニウム箔とを接着剤で接着し
てなる複合体は医薬品2食品などの包装材として繁用さ
れており、医薬品9食品などの製造工場においては前記
複合体の貫き滓が多量に副生する。従来これらの複合体
廃棄物の回収法として、■破砕し、樹脂の熱変形温度以
上に加熱し収縮せしめて樹脂とアルミニウム箔とを剥離
分別する方法(特開昭48−68678)、■樹脂とア
ルミニウムの複合体廃棄物を粉砕した後、比重がアルミ
ニウムの比重より小さくかつ樹脂の比重より大きい有機
溶媒中で攪拌し、樹脂含有層およびアルミニウム含有層
を分取しこれらの各層から溶剤を除去することにより樹
脂およびアルミニウムを別々に回収する方法(特開昭5
4−127988)が知られている。しかし、上記■の
方法では樹脂とアルミニウム箔とが完全に剥離せず、■
の方法においても樹脂層に少量のアルミニウムが混入し
たり、アルミニウム層に少量の樹脂が混入し、いずれの
方法においても両者を完全に分離することができない。
Composites made by bonding thermoplastic synthetic resin and aluminum foil with adhesive are frequently used as packaging materials for pharmaceutical products, food products, etc., and manufacturing plants for pharmaceutical products, food products, etc. have a large amount of sludge from the composite materials. as a by-product. Conventionally, methods for recovering these composite wastes include: (1) crushing, heating above the thermal deformation temperature of the resin to shrink it, and peeling and separating the resin and aluminum foil (Japanese Unexamined Patent Publication No. 48-68678); (1) separating the resin from the aluminum foil; After pulverizing the aluminum composite waste, it is stirred in an organic solvent whose specific gravity is lower than that of aluminum and higher than that of resin, and the resin-containing layer and the aluminum-containing layer are separated and the solvent is removed from each of these layers. A method of separately recovering resin and aluminum by
4-127988) is known. However, in the above method (■), the resin and aluminum foil are not completely separated, and
Even in the above method, a small amount of aluminum is mixed into the resin layer, or a small amount of resin is mixed into the aluminum layer, and it is not possible to completely separate the two in either method.

このように従来公知の方法はいずれも充分に満足できる
ものではない。
As described above, none of the conventionally known methods is fully satisfactory.

本発明者らはこのような事情に鑑み、種々検討した結果
、熱可塑性樹脂とアルミニウムとを容易に分離してそれ
ぞれを回収する方法を見いだし本発明を完成した。
In view of these circumstances, the present inventors conducted various studies, and as a result found a method for easily separating thermoplastic resin and aluminum and recovering each, and completed the present invention.

すなわち本発明は、熱可塑性樹脂とアルミニウム箔を接
着剤で接着してなる複合体を、該熱可塑性樹脂を透過し
、かつ該接着剤を理解しうる溶媒に浸漬して、該接着剤
を溶解するかまたはその接着力を低下せしめた後、該複
合体と溶媒層とを分離し、該複合体を水洗し、ついで該
複合体の樹脂とアルミニウム箔とを引き離すことを特徴
とする熱可塑性樹脂とアルミニウム箔とを個々に回収す
る方法である。
That is, in the present invention, a composite formed by bonding a thermoplastic resin and aluminum foil with an adhesive is immersed in a solvent that can penetrate the thermoplastic resin and understand the adhesive to dissolve the adhesive. or reduce the adhesive force thereof, the composite and the solvent layer are separated, the composite is washed with water, and then the resin of the composite and the aluminum foil are separated. This method collects aluminum foil and aluminum foil individually.

前記熱可塑性樹脂としてはたとえば、ポリオレフィン系
樹脂(ポリエチレン、ポリプロピレン)。
Examples of the thermoplastic resin include polyolefin resins (polyethylene, polypropylene).

ポリ塩化ビニル、ポリ塩ビニリデン、ポリエステル(ポ
リエステルテレクタレートなど)などがあげられる。
Examples include polyvinyl chloride, polyvinylidene chloride, and polyester (polyester terreclate, etc.).

本発明において用いられる溶媒は熱可塑性樹脂を透過し
、かつ接着剤を溶解し・うるものであればいかなるもの
でもよく、その具体例としてはたとえば、酢酸メチル、
酢酸エチル、酢酸ブチル、プロピオン酸メチル、プロピ
オン酸エチル、酪酸メチル、酪酸エチルなど炭素数8〜
6の低級脂肪酸の低級アルキルエステル類、たとえばア
セトン。
The solvent used in the present invention may be any solvent as long as it can penetrate the thermoplastic resin and dissolve the adhesive. Specific examples thereof include methyl acetate,
Ethyl acetate, butyl acetate, methyl propionate, ethyl propionate, methyl butyrate, ethyl butyrate, etc. with 8 or more carbon atoms
6 lower alkyl esters of lower fatty acids, such as acetone.

メチルエチルケトン、メチルイソブチルケトン。Methyl ethyl ketone, methyl isobutyl ketone.

ジエチルケトン、シクロヘキザノン、メチルシクロヘキ
サノンなど炭素類8〜7の低級脂族ケトン類、たとえば
ヘキ勺ン、オクタン、ノナン、デカン、ベンゼン、トル
エン、キシレンな、!”炭素数6〜10の炭化水素類、
たとえば四塩化炭素、ジクロルエタン、トリクロルエタ
ン、ジクロルエチレン、トリクロルエチレン、テトラク
ロルエチレンなど炭素数1〜8のハロゲン化炭化水素、
たとえばジメチルエーテル、ジエチルエーテル、メチル
エチルエーテル、テトラヒドロフランなどのエーテル類
およびこれらのうちの2種以上の混合物があげられる。
Lower aliphatic ketones with 8 to 7 carbon atoms such as diethyl ketone, cyclohexanone, methylcyclohexanone, etc., such as hexane, octane, nonane, decane, benzene, toluene, xylene, etc. ``Hydrocarbons having 6 to 10 carbon atoms,
For example, halogenated hydrocarbons having 1 to 8 carbon atoms, such as carbon tetrachloride, dichloroethane, trichloroethane, dichloroethylene, trichlorethylene, and tetrachlorethylene;
Examples include ethers such as dimethyl ether, diethyl ether, methyl ethyl ether, and tetrahydrofuran, and mixtures of two or more of these.

これらの溶媒は他の溶媒との混合物であってもよく、こ
の揚台本発明で規定する溶媒が少なくとも15容量%、
好ましくは20容凰%含まれているものが用いられる。
These solvents may be a mixture with other solvents, and this lifting table contains at least 15% by volume of the solvent defined in the present invention.
Preferably, one containing 20% by volume is used.

本発明において使用可能な混合溶媒の具体例としてはた
とえば、ガソリン、ソルベントナフサなどがあげられる
Specific examples of the mixed solvent that can be used in the present invention include gasoline, solvent naphtha, and the like.

通常熱可塑性樹脂とアルミ箔との接着はエチレン酢ピコ
−ポリマー系、エチレン系ポリマーのホットメルト接着
剤が用いられており、このような接着剤で接着されてい
る複合体であれば本発明を適用できる。
Normally, hot melt adhesives such as ethylene acetate pico-polymer and ethylene polymer are used to bond thermoplastic resin and aluminum foil, and the present invention can be applied to composites bonded with such adhesives. Applicable.

本発明の方法において用いられる複合体は帯状。The composite used in the method of the invention is strip-shaped.

シート状などいかなる形状のものでもよいが、長さが1
m以上の帯状のものが好ましい。また帯状の複合体はロ
ール状に巻きとられた形態のものが好適である。
It can be of any shape, such as a sheet, but the length is 1
It is preferable to use a band-like material having a length of m or more. Further, it is preferable that the band-shaped composite is wound into a roll.

本発明を実施するにあたっては、まず複合体ヲ溶媒中に
浸漬する。具体的手段としては槽内に溶媒を満たし、こ
の中に複合体を投入してもよモ)シ、また槽内にまず複
合体を収容し、ついでここに溶媒を満たしてもよい。こ
れにより複合体の樹脂表面から溶媒が樹脂中に浸透し、
樹脂を透過して接着剤の層に達する。この浸漬は接着剤
が溶解するかまたは接着剤の接着力が樹脂の引張り強さ
およびアルミ箔の引張り強さのいずれよりも弱まるまで
行なわれる。浸漬時間は樹脂の種類、厚さ、溶媒の種類
、温度により異るが、通常2分〜8時間程度である。用
いる溶媒の引火点が比較的高い場合には加熱してもよく
、加熱により、接着剤の溶解またはその接着力の低下速
度を早めることができる。加熱は溶媒の引火点より低い
温度で行なわれる。樹脂がポリ塩化ビニル、ポリ塩化ビ
ニリデンである場合には、溶媒として、低級脂肪酸の低
級アルキルエステル類、低級脂肪族ケトン類、炭素数1
〜8のハロゲン化炭化水素類およびエーテル類からなる
群から選ばれた溶媒の一種以上を少なくとも16容量%
含有する溶媒を用いるのがよい。この場合樹脂の厚さが
0.16〜0.85mmで溶媒の温度が室温附近であれ
ば浸漬時間は2分〜8時間程度が適当である。樹脂がポ
リオレフィンである場合には溶媒として低級脂肪酸の低
級アルキルエステル類、低級脂肪族ケトン類、炭素数1
〜8のハロゲン化炭化水素類および炭素数6〜8の炭化
水素類からなる群から選ばれた溶媒の一種以上を少なく
とも15容量%含有する溶媒を用いるのがよく、この場
合樹脂の厚さが0.15〜0.25で、溶媒の温度が室
温附近であれば浸漬時間は80分〜8時間程度が適当で
ある。樹脂がポリエステルである場合には溶媒として低
級脂肪酸の低級アルキルエステル類および炭素数6〜8
の炭化水素類からなる群から選ばれた溶媒の一種以上を
少なくとも15容量%含有する溶媒を用いるのがよく、
この場合樹脂の厚さが0.15〜0.8間で、溶媒の温
度が室温附近であれば浸漬時間は1〜6時間程度が適当
である。浸漬時間があまり短かすぎると接着剤の接着力
の低下がおこらず、逆に長すぎると樹脂の膨潤が進み樹
脂の引張り強度が弱くなるために好ましくない。
In carrying out the present invention, the composite is first immersed in a solvent. As a specific means, the tank may be filled with a solvent and the complex may be introduced into the tank, or the complex may be first stored in the tank and then the solvent may be filled in the tank. As a result, the solvent penetrates into the resin from the resin surface of the composite,
It passes through the resin and reaches the adhesive layer. This dipping is continued until the adhesive dissolves or the adhesive strength of the adhesive becomes weaker than both the tensile strength of the resin and the aluminum foil. The immersion time varies depending on the type and thickness of the resin, the type of solvent, and the temperature, but is usually about 2 minutes to 8 hours. If the flash point of the solvent used is relatively high, heating may be used, and heating can accelerate the dissolution of the adhesive or the rate at which its adhesive strength decreases. Heating is carried out at a temperature below the flash point of the solvent. When the resin is polyvinyl chloride or polyvinylidene chloride, the solvent may be lower alkyl esters of lower fatty acids, lower aliphatic ketones, or carbon atoms having 1
at least 16% by volume of one or more solvents selected from the group consisting of ~8 halogenated hydrocarbons and ethers;
It is better to use a solvent that contains In this case, if the thickness of the resin is 0.16 to 0.85 mm and the temperature of the solvent is around room temperature, the appropriate immersion time is about 2 minutes to 8 hours. When the resin is a polyolefin, lower alkyl esters of lower fatty acids, lower aliphatic ketones, and carbon atoms of 1 are used as solvents.
It is preferable to use a solvent containing at least 15% by volume of one or more solvents selected from the group consisting of halogenated hydrocarbons having a carbon number of ~8 and hydrocarbons having a carbon number of 6 to 8; in this case, the thickness of the resin is 0.15 to 0.25, and if the temperature of the solvent is around room temperature, the appropriate immersion time is about 80 minutes to 8 hours. When the resin is polyester, a lower alkyl ester of a lower fatty acid and a carbon number of 6 to 8 are used as a solvent.
It is preferable to use a solvent containing at least 15% by volume of one or more solvents selected from the group consisting of hydrocarbons,
In this case, if the thickness of the resin is between 0.15 and 0.8 and the temperature of the solvent is around room temperature, the appropriate immersion time is about 1 to 6 hours. If the immersion time is too short, the adhesive force of the adhesive will not decrease, and if the immersion time is too long, the resin will swell and the tensile strength of the resin will become weaker, which is not preferable.

本発明の方法においては、ついで複合体と溶媒層を分離
する。この具体的手段としては、槽内の溶媒を切っても
よく複合体を槽内から取り出してもよい。
In the method of the invention, the complex and solvent layers are then separated. As a specific means for this, the solvent in the tank may be turned off, or the complex may be taken out from the tank.

溶媒層と分離された複合体はついで水洗される。The composite separated from the solvent layer is then washed with water.

この具体的手段としては、複合体に水をかけて溶媒を洗
い流してもよく、複合体を槽に入れ、これに水を満たし
て複合体に付着している溶媒を水で置換したのち複合体
を槽から取り出してもよい。
As a specific means for this, the solvent may be washed away by pouring water onto the complex, or the complex may be placed in a tank and filled with water to replace the solvent adhering to the complex with water. may be removed from the tank.

複合体の水洗は溶媒層と分離したのち直ちに行なうのが
よい。複合体を溶媒層と分離したのち長時間放置してお
くと、複合体に付着している溶媒が樹脂中に浸透し樹脂
をさらに膨潤せしめ樹脂の引張り強度を一層弱めるし、
また空気中に溶媒が揮敗するので好ましくない。
It is preferable to wash the composite with water immediately after separating it from the solvent layer. If the composite is left for a long time after being separated from the solvent layer, the solvent adhering to the composite will penetrate into the resin and further swell the resin, further weakening the tensile strength of the resin.
Further, the solvent evaporates in the air, which is not preferable.

水洗された複合体はついで樹脂とアルミニウム箔とに引
き離される。この具体的な手段としては樹脂とアルミニ
ウム箔を物理的な手段で別方向に引っばることにより行
なわれる。接着剤が溶媒により溶かされたものはこの操
作により簡単に分離できるし、また接着剤が完全に溶か
されていなくてもその接着力が低下していれば上記操作
により両者は容易に引き離される。複合体が帯状でロー
ル状の形態である場合にはロールをときながら樹脂とア
ルミニウム箔を引き離し、それぞれを別々にロール状に
巻きとってもよい。また樹脂、アルミニウム箔のそれぞ
れは分離しまたは引き離した後順次截断してもよい。
The washed composite is then separated into resin and aluminum foil. A specific method for this is to physically pull the resin and aluminum foil in different directions. If the adhesive has been dissolved by the solvent, it can be easily separated by this operation, and even if the adhesive is not completely dissolved, if its adhesive strength has decreased, the two can be easily separated by the above operation. When the composite is in the form of a strip or roll, the resin and aluminum foil may be separated by rolling the roll, and each may be wound into a roll separately. Further, the resin and aluminum foil may be separated or separated and then cut one after another.

このようにして熱可塑性樹脂とアルミニウム箔の複合体
廃棄物から樹脂とアルミニウム箔とを別々に回収するこ
とができ、これらはそれぞれの用途に再使用される。
In this way, the resin and aluminum foil can be recovered separately from the composite waste of thermoplastic resin and aluminum foil, and these can be reused for their respective uses.

本発明の方法によれば樹脂およびアルミニウムの双方を
回収でき、しかも回収されたアルミニウムおよび樹脂は
ともに他方の混入が全くなく、両者はそれぞれ純粋なも
のとして単離される。
According to the method of the present invention, both resin and aluminum can be recovered, and both the recovered aluminum and resin are completely free from contamination with the other, and both are isolated as pure substances.

以下に実施例を記載して本発明をより具体的に説明する
EXAMPLES The present invention will be described in more detail with reference to Examples below.

実施例1 ポリ塩化ビニル樹脂(厚さ0.151g)とアルミ箔と
をエチレン−酢酸ビニル系コーポリマーのホットメルト
接着剤で接着した複合体(rl12101N。
Example 1 A composite (rl12101N) in which polyvinyl chloride resin (thickness: 0.151 g) and aluminum foil are adhered with a hot melt adhesive of ethylene-vinyl acetate copolymer.

長さ4m)をロール状に巻いたもの(ロールの直径:約
60順)を内径約(3QMIN、高さ約260顛の円筒
状容器に入れこれにラッカーシンナー(酢酸エチル50
V%、イソプロパツール20V%。
4m in length) wound into a roll (roll diameter: approx. 60 mm) is placed in a cylindrical container with an inner diameter of approx.
V%, isopropanol 20V%.

アセトン15V%、トルエン15V%)を入れて室温下
80分間浸漬した。ついで溶媒を取り出し、水を満たし
て水洗した。水洗を2回繰返したのち複合体を円筒状容
器から取り出した。樹脂゛とアルミ箔は完全に剥離して
おり、両者は殆んど抵抗なく分離できる。端部を手動で
樹脂フィルムとアルミ箔に分離してそれぞれの端部を巻
取りロール2基を備えた分離装置の各示合−ルに取り付
け、約0.6〜xm/秒の速度でそれぞれを巻取り分離
して、樹脂フィルムとアルミ箔を個々に回収した。
Acetone 15V%, toluene 15V%) were added thereto and immersed at room temperature for 80 minutes. Then, the solvent was taken out, the container was filled with water, and the container was washed with water. After repeating water washing twice, the composite was taken out from the cylindrical container. The resin and aluminum foil were completely peeled off, and the two could be separated with almost no resistance. The ends were manually separated into resin film and aluminum foil, and each end was attached to each roll of a separating device equipped with two take-up rolls, and each end was separated at a speed of about 0.6 to x m/sec. was rolled up and separated, and the resin film and aluminum foil were collected individually.

実施例2〜21 実施例1で用いた複合体を実施例1と同様にして下記の
条件で処理し、樹脂フィルムとアルミ箔を個々に回収し
た。
Examples 2 to 21 The composite used in Example 1 was treated in the same manner as in Example 1 under the following conditions, and the resin film and aluminum foil were individually collected.

注)1)浸漬終了後樹脂とアルミ箔は完全に剥離してお
り、両者は殆んど抵抗なく分離できる。
Note) 1) After the immersion, the resin and aluminum foil are completely peeled off, and the two can be separated with almost no resistance.

2)水洗後樹脂フィルムが白色になった。2) The resin film turned white after washing with water.

8)浸漬終了後樹脂とアルミ箔は剥離してしないが、接
着力は弱く、物理的な力を加えて樹脂とアルミ箔を別方
向に引き離すことにより両者は容易に分離できる。
8) After immersion, the resin and aluminum foil do not separate, but the adhesive strength is weak, and they can be easily separated by applying physical force and pulling the resin and aluminum foil apart in different directions.

実施例22 ポリプロピレン(厚さ0.211av)とアルミ箔とを
ポリエチレン系のホットメルト接着剤で接着した複合体
(巾210MM、長さ約450mをロール状に巻いたも
の(ロールの直径:約380ffll)を内径約400
mN、高さ約250朋の上蓋付円筒状容器に入れ、これ
にトリクロロエチレンを入れて室温下1時間浸漬した。
Example 22 Composite made of polypropylene (thickness 0.211 av) and aluminum foil adhered with polyethylene hot melt adhesive (width 210 mm, length approximately 450 m rolled into a roll (roll diameter: approximately 380 ffll) ) with an inner diameter of approximately 400
The mixture was placed in a cylindrical container with a lid of about 250 mN and height, and trichlorethylene was added thereto and immersed at room temperature for 1 hour.

ついで溶媒を抜き去り、実施例1と同様な操作で水洗し
た。(樹脂フィルムとアルミ箔は完全に剥離しており、
両者は殆んど抵抗なく剥離する。)以下、実施例1と同
様に処理して樹脂フィルムとアルミ箔を個々に回収した
Then, the solvent was removed and the sample was washed with water in the same manner as in Example 1. (The resin film and aluminum foil have completely peeled off,
Both peel off with almost no resistance. ) Thereafter, the resin film and aluminum foil were individually collected by processing in the same manner as in Example 1.

実施例28〜36 実施例22で用いた複合体(ただし、長さは4m)をロ
ール状に巻いたもの(ロールの直径:約601’l)を
用いて実施例1と同様の操作により下記の条件で処理し
、樹脂とアルミ箔を個々に回収した。
Examples 28 to 36 The following was carried out in the same manner as in Example 1 using the composite used in Example 22 (length: 4 m) wound into a roll (roll diameter: approximately 601'l). The resin and aluminum foil were collected separately.

注、備考欄の1)、 2)、 8)は実施例2〜21の
表中の意味と同じである。
Notes and notes 1), 2), and 8) have the same meanings as in the tables of Examples 2 to 21.

実施例87〜50 下記5種の複合体を下記の条件で実施例1と同様に処理
して樹脂フィルムとアルミ箔とを個々に回収した。
Examples 87-50 The following five types of composites were treated in the same manner as in Example 1 under the following conditions, and the resin film and aluminum foil were individually collected.

複合体 ■ ポリエチレン樹脂フィルム(厚さ0.2511ff
)とアルミ箔とをポリエチレン−酢酸ビニルコーポリマ
ー系ホットメルト接着剤で接着した複合体(巾210g
m、長さ約4m)をロール状に巻いたもの(ロールの直
径:約60M) ■ ポリ塩化ビニリデン樹脂フィルム(厚さ0゜2 m
m )とアルミ箔とをエチレン−酢酸ビニルコーポリマ
ー系ホットメルト接着剤で接着した複合体(+1J2t
o*鴎長さ約4 m )をロール状に巻いたもの(ロー
ルの直径:約60im)■ ポリエステル樹脂フィルム
(厚さ0.8 記)とアルミ;6とをポリエチレン系ホ
ットメルト接着剤で接漬した複合体(rl、] 210
 ytyt、長さ約4m)をロール状に巻いたもの(ロ
ールの直径:約60mm) ■ ポリ塩化ビニール(150μ)、ポリ[、A化ビニ
リデン(18μ)、ポリエチレン(15μ)ポリ塩化ビ
ニリデン(18μ)、ポリ塩化ビニール(150/()
をこの順序でラミネートした樹脂フィルムとアルミ箔と
をエチレン−酢酸ビニル系コーポリマーのホットメルト
接着剤で接着した複合体(rl」2to鰭、長さ約4m
)をロール状に巻いたもの(ロールの直径:約6on+
)注、備考4iYtlの1)、 2)、 8)は実施例
2〜21の表中の意味と同じである。
Composite ■ Polyethylene resin film (thickness 0.2511ff
) and aluminum foil adhered using a polyethylene-vinyl acetate copolymer hot melt adhesive (width 210g)
m, length approximately 4 m) wound into a roll (roll diameter: approximately 60 m) ■ Polyvinylidene chloride resin film (thickness 0゜2 m)
m) and aluminum foil adhered using ethylene-vinyl acetate copolymer hot melt adhesive (+1J2t
4 m long) wound into a roll (diameter of roll: approximately 60 im) ■ Polyester resin film (thickness: 0.8 mm) and aluminum; 6 are bonded using polyethylene hot melt adhesive. Soaked complex (rl,] 210
ytyt, length approx. 4m) rolled into a roll (roll diameter: approx. 60mm) ■ Polyvinyl chloride (150μ), polyvinylidene A (18μ), polyethylene (15μ), polyvinylidene chloride (18μ) , polyvinyl chloride (150/()
A composite (RL) 2to fin, approximately 4m in length, is made by laminating a resin film and aluminum foil in this order and bonding them with an ethylene-vinyl acetate copolymer hot melt adhesive.
) rolled into a roll (roll diameter: approx. 6 on+
) Notes and Notes 4iYtl 1), 2), and 8) have the same meanings as in the tables of Examples 2 to 21.

手 続 補 正 書(自発) 昭和59年5 月70日 2、発明の名称 複合材料の分離回収法 3、補正をする者 事件との関係 特許出願人 住 所 大阪市東区道修町2丁目27番地名 称(29
3)武田薬品工業株式会社代表者 倉 林 育 四 部 4、代理人 住 所 大阪市淀川区十三本町2丁目17番85号武田
薬品工業株式会社大阪工場内 6、補正の対象 明細書の発明の詳細な説明の欄 7、補正の内容 (1)明細書第4頁第14行の「理解」を「溶解、Jに
訂正する。
Procedure Amendment (voluntary) May 70, 1980 2 Name of the invention Composite material separation and recovery method 3 Relationship to the case of the person making the amendment Patent applicant address 2-27 Doshomachi, Higashi-ku, Osaka Name (29
3) Takeda Pharmaceutical Co., Ltd. Representative: Iku Kurabayashi Department 4, Agent address: Takeda Pharmaceutical Co., Ltd. Osaka Factory, 2-17-85 Jusanhonmachi, Yodogawa-ku, Osaka City 6, Invention of the specification subject to amendment Detailed explanation column 7, contents of amendment (1) "Understanding" in page 4, line 14 of the specification is corrected to "dissolution, J.

(2) 同書第5頁第3行の「ポリ塩ビニリデン」を「
ポリ塩化ビニリデン」に訂正する。
(2) “Polyvinylidene chloride” on page 5, line 3 of the same book is “
Corrected to "Polyvinylidene Chloride."

(3)同書第5頁第4行の「ポリエステルテレクタレー
ト」ヲ「ポリエチレンテレフタレート」に訂正する。
(3) "Polyester terephthalate" on page 5, line 4 of the same book has been corrected to "polyethylene terephthalate."

(4)同書第6頁第12行の「エチレン糸ポリマ刊を「
ポリエチレン系」に訂正する。
(4) “Published by Ethylene Thread Polymer” on page 6, line 12 of the same book.
Corrected to "polyethylene-based".

(5)同書第8頁第10行のro、15〜0.25Jの
後にrffJを挿入する。
(5) Insert rffJ after ro, 15 to 0.25J on page 8, line 10 of the same book.

(6)回書第12頁に記載の表中、実施例6の使用溶媒
をつぎのとおり訂正する。
(6) In the table on page 12 of the circular, the solvent used in Example 6 is corrected as follows.

[ラッカーシンナー(トルエン42V%、キシレン14
V%、酢エチ15V%、酢ブチ1v%、酢酸イソグチル
エヌテ)v i V N +メタノール4v%メチルイ
ソブチ〜ケトン2v%、エタノ−/L/3v%、イソグ
ロバノー/L’4V96+n−ブタノ−/1/3v96
.イソブタノール2v%、アセトン5V%。
[Lacquer thinner (toluene 42V%, xylene 14%)
V%, ethyl acetate 15V%, butyl acetate 1v%, isobutyl acetate) vi V N + methanol 4v% methyl isobutylene ~ ketone 2v%, ethano/L/3v%, isoglobanol/L'4V96+n-butano/1/3v96
.. Isobutanol 2v%, acetone 5V%.

メチルエチルケトン4v%」 以上Methyl ethyl ketone 4v%” that's all

Claims (1)

【特許請求の範囲】 1、熱T′iJ塑性41′j1脂とアルミニウム箔を接
着剤で接着してなる複合体を、該熱可塑性樹脂を透過し
かつ該接着剤を溶解しうる溶媒に浸漬して、該接着剤を
溶解するかまたはその接着力を低下せしめた後、該複合
体と溶媒層とを分離し、該複合体を水洗し、ついで該ト
見合体の樹脂とアルミニウム箔とを引き離すことを特徴
とする熱用方 塑性樹脂とアルミニウム箔を個々に回収す添。 2、溶媒が(V低級脂肪酸の低級アルキルエステル類、
■低級脂肪族ケトン類、(3)炭素a6〜10の炭化水
素類、■炭素数1〜8のハロゲン化炭化水素類および(
■エーテル類からなる群から選ばれた溶媒の一種以上を
少なくとも15容量%含有する溶媒である特許請求の範
囲第1項記載の方法。 8 接着剤がエチレン−酢酸ビニルコーポリマー系また
はポリエチレン系のホットメルト接着剤である特許請求
の範囲第1項記載の方法。 4、熱可塑性樹脂がポリ塩化ビニルまたはポリ塩化ビニ
リデンであり、溶媒が低級脂肪酸の低級アルキルエステ
ル類、低級脂肪族ケトン類。 炭素数1〜8のハロゲン化炭化水素類およびエーテ類か
らなる群から選ばれた溶媒の一種以上を少なくとも15
容量%含有する溶媒である特許請求の範囲第1項記載の
方法。 5、熱可塑性樹脂がポリオレフィンであり、溶媒が低級
脂肪酸の低級アルキルエステル類、低級脂肪族ケトン類
、炭素数1〜8のハロゲン化炭化水素類および炭素数6
〜10の炭化水素類からなる群から選ばれた溶媒の一種
以上を少なくとも15容量%含有する溶媒である特許請
求の範囲第1項記載の方法。 6、熱可塑性樹脂がポリエステルであり、溶媒が低級脂
肪酸の低級アルキルエステル類および炭素数2〜6のハ
ロゲン化炭化水素類からなる群から選ばれた溶媒の一種
以上を少なくとも15容量%含有する溶媒である特許請
求の範囲第4項記載の方法。
[Claims] 1. A composite formed by bonding thermal T'iJ plasticity 41'j1 resin and aluminum foil with an adhesive is immersed in a solvent that can permeate the thermoplastic resin and dissolve the adhesive. After dissolving the adhesive or reducing its adhesive strength, the composite and the solvent layer are separated, the composite is washed with water, and then the composite resin and aluminum foil are separated. An additive that collects thermoplastic resin and aluminum foil individually by separating them. 2. The solvent is (V lower alkyl esters of lower fatty acids,
■Lower aliphatic ketones, (3) hydrocarbons with a6 to 10 carbon atoms, ■halogenated hydrocarbons with 1 to 8 carbon atoms, and (
(2) The method according to claim 1, wherein the solvent contains at least 15% by volume of one or more solvents selected from the group consisting of ethers. 8. The method according to claim 1, wherein the adhesive is an ethylene-vinyl acetate copolymer-based or polyethylene-based hot melt adhesive. 4. The thermoplastic resin is polyvinyl chloride or polyvinylidene chloride, and the solvent is lower alkyl esters of lower fatty acids or lower aliphatic ketones. At least 15 solvents selected from the group consisting of halogenated hydrocarbons having 1 to 8 carbon atoms and ethers.
% by volume of the solvent. 5. The thermoplastic resin is a polyolefin, and the solvent is lower alkyl esters of lower fatty acids, lower aliphatic ketones, halogenated hydrocarbons having 1 to 8 carbon atoms, and 6 carbon atoms.
The method according to claim 1, wherein the solvent contains at least 15% by volume of one or more solvents selected from the group consisting of -10 hydrocarbons. 6. The thermoplastic resin is polyester, and the solvent contains at least 15% by volume of one or more solvents selected from the group consisting of lower alkyl esters of lower fatty acids and halogenated hydrocarbons having 2 to 6 carbon atoms. The method according to claim 4.
JP59068635A 1984-04-05 1984-04-05 Separation and recovery of composite material Pending JPS60212434A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59068635A JPS60212434A (en) 1984-04-05 1984-04-05 Separation and recovery of composite material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59068635A JPS60212434A (en) 1984-04-05 1984-04-05 Separation and recovery of composite material

Publications (1)

Publication Number Publication Date
JPS60212434A true JPS60212434A (en) 1985-10-24

Family

ID=13379388

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59068635A Pending JPS60212434A (en) 1984-04-05 1984-04-05 Separation and recovery of composite material

Country Status (1)

Country Link
JP (1) JPS60212434A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1993008229A1 (en) * 1991-10-23 1993-04-29 Nordenia Verpackungswerke Ag Process for transforming in particular polyethylene composite foils into re-usable raw materials
US5290505A (en) * 1990-11-26 1994-03-01 Wnc-Nitrochemie Gmbh Method of recycling adhesive-coated plastic sheet material
US5390860A (en) * 1992-05-15 1995-02-21 Tetra Laval Holdings & Finance Sa Method and apparatus for separating paper fiber and plastics from mixed waste materials and products obtained thereby
US5421526A (en) * 1991-05-29 1995-06-06 Tetra Laval Holdings & Finance Sa Method of recovering individual component parts from packaging material waste
ES2087013A1 (en) * 1993-10-25 1996-07-01 Univ Valencia Process for recovering polyethylene and aluminium from polyethylene-coated aluminium sheets from container wastes of the "pack" type
JP2002264130A (en) * 2001-03-07 2002-09-18 Kanegafuchi Chem Ind Co Ltd Method of recycling interior material of automobile
WO2003104315A1 (en) * 2002-06-07 2003-12-18 Anderson Crovador Massura Process for separation of multilayered films used for packagings
TWI384079B (en) * 2008-05-22 2013-02-01 Shufen Liao Method of treating simultaneously recycled copper sulfate solution and aluminum foil bag
JP2014105253A (en) * 2012-11-27 2014-06-09 Yokohama Yushi Kogyo Kk Release agent of ethylene-vinyl acetate copolymer
EP4144786A1 (en) * 2014-05-05 2023-03-08 Saperatec GmbH Method and apparatus for recycling packaging material
JP2023065309A (en) * 2021-10-27 2023-05-12 株式会社ダイトク Separate recovery system and separate recovery method of composite material

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5290505A (en) * 1990-11-26 1994-03-01 Wnc-Nitrochemie Gmbh Method of recycling adhesive-coated plastic sheet material
US5421526A (en) * 1991-05-29 1995-06-06 Tetra Laval Holdings & Finance Sa Method of recovering individual component parts from packaging material waste
WO1993008229A1 (en) * 1991-10-23 1993-04-29 Nordenia Verpackungswerke Ag Process for transforming in particular polyethylene composite foils into re-usable raw materials
US5390860A (en) * 1992-05-15 1995-02-21 Tetra Laval Holdings & Finance Sa Method and apparatus for separating paper fiber and plastics from mixed waste materials and products obtained thereby
ES2087013A1 (en) * 1993-10-25 1996-07-01 Univ Valencia Process for recovering polyethylene and aluminium from polyethylene-coated aluminium sheets from container wastes of the "pack" type
JP2002264130A (en) * 2001-03-07 2002-09-18 Kanegafuchi Chem Ind Co Ltd Method of recycling interior material of automobile
WO2003104315A1 (en) * 2002-06-07 2003-12-18 Anderson Crovador Massura Process for separation of multilayered films used for packagings
TWI384079B (en) * 2008-05-22 2013-02-01 Shufen Liao Method of treating simultaneously recycled copper sulfate solution and aluminum foil bag
JP2014105253A (en) * 2012-11-27 2014-06-09 Yokohama Yushi Kogyo Kk Release agent of ethylene-vinyl acetate copolymer
EP4144786A1 (en) * 2014-05-05 2023-03-08 Saperatec GmbH Method and apparatus for recycling packaging material
JP2023065309A (en) * 2021-10-27 2023-05-12 株式会社ダイトク Separate recovery system and separate recovery method of composite material

Similar Documents

Publication Publication Date Title
JP6514208B2 (en) Shrinkable packaging label coating that facilitates recycling
JPS60212434A (en) Separation and recovery of composite material
JP4909266B2 (en) Battery exterior label
DE3442998A1 (en) CONTAINER WITH PLASTIC LABEL AND METHOD FOR APPLYING THE LABEL
WO2000062273A1 (en) Easily removable label for reusable containers
EP0951004B1 (en) Easily removable label for reusable container
JP6949322B2 (en) Separate recovery method for composite materials and separate recovery equipment used for this method
SE454069B (en) PROCEDURE FOR MANUFACTURING LAMINATE CONTAINING METAL AND THERMOPLASTIC LAYERS, AND CONTAINERS THEREOF
JPS6317706B2 (en)
JP2020515655A (en) Method and apparatus for recycling packaging material
EP3774250B1 (en) Method for the sustainable and energy-saving production of a recyclable plastic container provided with a label
WO2018187203A1 (en) Shrink wrap label coating to facilitate recycling
DE102015205935A1 (en) Easily removable label without release liner especially for reusable containers
JP4865938B2 (en) Insulated container
DE2239652C3 (en) Sticky notes or tape for packaging purposes
JP4748934B2 (en) Battery exterior label
JP4445714B2 (en) Labeled container
JPH08260067A (en) Method for recovering aluminum from laminated foil
JP3250749B2 (en) Saponified ethylene-vinyl acetate copolymer solution and use thereof
JPH1185035A (en) Vapor deposited label
JP3173740B2 (en) Saponified ethylene-vinyl acetate copolymer solution and use thereof
GB1245923A (en) Improvements relating to the fabricating of web material
JPS6211640A (en) Sheet-shaped material having perfume resistance
JP4334782B2 (en) Powder storage member and toner storage container using the same
JPH07179831A (en) Surface protection film