JP2001019796A - Removal and recycle of vinylidene chloride-based resin - Google Patents

Removal and recycle of vinylidene chloride-based resin

Info

Publication number
JP2001019796A
JP2001019796A JP19527899A JP19527899A JP2001019796A JP 2001019796 A JP2001019796 A JP 2001019796A JP 19527899 A JP19527899 A JP 19527899A JP 19527899 A JP19527899 A JP 19527899A JP 2001019796 A JP2001019796 A JP 2001019796A
Authority
JP
Japan
Prior art keywords
based resin
vinylidene chloride
olefin
resin
substrate
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
JP19527899A
Other languages
Japanese (ja)
Inventor
Koichi Ogawa
好一 小川
Masaki Kataoka
正樹 片岡
Kenji Kataoka
憲二 片岡
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP19527899A priority Critical patent/JP2001019796A/en
Publication of JP2001019796A publication Critical patent/JP2001019796A/en
Pending legal-status Critical Current

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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
    • 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

  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for dissolving/extracting a polyvinylidene chloride resin-coated layer from an olefin-based resin substrate and for advantageously recycling the olefin-based resin substrate and dissolved/extracted matter at a low cost so as to be simultaneously and industrially returnable (repeatedly utilizable). SOLUTION: This method is to cut out an olefin resin-based substrate down to adequate size which is made of e.g. biaxial oriented polypropylene film and is coated with a polyvinylidene chloride-based resin, to mix the substrate pieces with an industrial solvent selected from the group consisting of a fraction from crude petroleum oil, volatile oil, lamp oil and light oil by stirring at 65-85 deg.C and to dissolve polyvinylidene chloride on the surface of the substrate film to be extracted/removed.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は塩化ビニリデン系樹
脂塗布層を有するオレフィン系樹脂基体から塩化ビニリ
デン系樹脂を除去し、しかも該オレフィン系樹脂基体と
除去した塩化ビニリデン系樹脂塗布層とをそれらのオレ
フィン系樹脂と塩化ビニリデン系樹脂との二種類の物性
を夫々劣化させることなく、それらをリターナブル(繰
り返し利用)でき得ることを特徴とした低温処理による
除去再利用方法に関するものである。
The present invention relates to a method for removing a vinylidene chloride resin from an olefin resin substrate having a vinylidene chloride resin coating layer, and combining the olefin resin substrate and the removed vinylidene chloride resin coating layer with each other. The present invention relates to a method for removing and reusing by low-temperature treatment, characterized in that two kinds of physical properties of an olefin resin and a vinylidene chloride resin can be returned (repeatedly used) without deteriorating the respective properties.

【0002】[0002]

【従来の技術】塩化ビニリデン系樹脂は、酸素及び水蒸
気バリアー性に優れており、そのため他の樹脂(ポリオ
レフィン、PET等)に塩化ビニリデン系樹脂を積層し
たものが、包装用フィルム、シート、成形容器等に多く
用いられている。これらの成形品の製造過程で生ずるト
リミングロスや不良品、使用済みの成形品は通常、焼却
あるいは埋立処分されていた。これでは空気や地下水の
汚染となり、問題となる。特にこの塩化ビニリデン系樹
脂は加熱溶融、燃焼により塩素系ガスが発生するため、
環境浄化、省資源対策の観点から、発生抑制、再使用の
促進、繰り返し利用が、今後の環境経済システムを構築
する上で不可欠になり、又これら再生樹脂の諸物性を考
慮すると予め積層成形品から塩化ビニリデン系樹脂を分
離してオレフィン系樹脂と塩化ビニリデン系樹脂とを分
取して別々に処理されたものが工業原料として活用され
ることが望まれる。
2. Description of the Related Art Vinylidene chloride resins are excellent in oxygen and water vapor barrier properties. Therefore, those obtained by laminating vinylidene chloride resins on other resins (polyolefin, PET, etc.) are used for packaging films, sheets and molded containers. It is often used for such purposes. Trimming loss, defective products, and used molded products generated during the production process of these molded products are usually incinerated or landfilled. This causes air and groundwater contamination, which is a problem. In particular, this vinylidene chloride-based resin generates chlorine-based gas by heating and melting and burning,
From the viewpoint of environmental purification and resource saving measures, suppression of generation, promotion of reuse, and repeated use will be indispensable in constructing an environmental and economic system in the future. It is desired that the vinylidene chloride-based resin be separated from the oil, the olefin-based resin and the vinylidene chloride-based resin are separated and treated separately to be used as an industrial raw material.

【0003】各層樹脂フィルムを一旦製造して接着剤等
で貼り合わせた積層フィルムや共押出しラミネーション
によって得られて積層フィルムから各樹脂成分を回収す
る方法としては例えば次のような方法が提案されてい
る。 (1) 積層シートを加熱ロール等で加熱することによっ
て、フィルムの状態で各層に分離し、回収する方法。
(特開平2−131907号) (2) 塩化ビニリデン樹脂積層成形物を粗粉砕、熱水処
理、微粉砕し、該粉砕物を界面活性剤を含む水媒体中で
ゆっくり攪拌処理して塩化ビニリデン樹脂を沈降、分離
する方法。(特開平5−261735号) (3) 塩化ビニリデン系樹脂塗布層を有するオレフィン
系樹脂基体を、界面活性剤0.1wt%以上の水溶液中で、1
00℃以上樹脂基体が溶融する温度より低い温度で攪拌処
理することを特徴とする樹脂基体表の塩化ビニリデン系
樹脂の除去方法。(特開平9−279066号)
As a method of recovering each resin component from a laminated film or a laminated film obtained by co-extrusion lamination, in which a resin film for each layer is once manufactured and bonded with an adhesive or the like, for example, the following method has been proposed. I have. (1) A method in which a laminated sheet is heated by a heating roll or the like to separate and collect each layer in a film state.
(JP-A-2-131907) (2) The vinylidene chloride resin laminate molded product is roughly pulverized, treated with hot water, and finely pulverized, and the pulverized product is slowly stirred in an aqueous medium containing a surfactant to obtain a vinylidene chloride resin. To settle and separate. (3) An olefin resin substrate having a vinylidene chloride-based resin coating layer was treated with an aqueous solution containing 0.1 wt% or more of a surfactant in an aqueous solution of 0.1 wt% or more.
A method for removing a vinylidene chloride-based resin from a surface of a resin substrate, wherein the stirring is performed at a temperature of 00 ° C. or higher and lower than a temperature at which the resin substrate melts. (JP-A-9-279066)

【0004】しかし、(1)の方法は粉砕物等のように、
フィルム状に剥離困難なものについては適用できない。
(2)の方法は、粉砕物から塩化ビニリデン系樹脂を回収
し得る有効な手段ではあるが、成形品を1mm以下にまで
微粉砕する必要がある。また、近年は積層成形品の性能
面から各層間の接着強度が強められる方向で技術が開発
されており、その結果従来の方法では塩化ビニリデン系
樹脂の分離が充分でない場合もある。特に、二軸延伸ポ
リプロピレンフィルム等の基材に塩化ビニリデン系樹脂
を主体とする液を塗布、乾燥して得られたフィルムは、
一般に塩化ビニリデン系樹脂の層が非常に薄く、しかも
基材に強固に密着しているが、これを基材から分離する
ための簡便で有効な手段は提案されていなかった。
[0004] However, the method of (1) is similar to pulverized material, etc.
It cannot be applied to a film that is difficult to peel off.
The method (2) is an effective means for recovering the vinylidene chloride resin from the pulverized product, but it is necessary to pulverize the molded product to 1 mm or less. In recent years, technology has been developed in the direction of increasing the adhesive strength between the layers from the viewpoint of the performance of the laminated molded product, and as a result, the separation of the vinylidene chloride resin may not be sufficient in the conventional method. In particular, a film obtained by applying a liquid mainly composed of vinylidene chloride-based resin to a substrate such as a biaxially stretched polypropylene film, and drying,
Generally, the vinylidene chloride-based resin layer is very thin and firmly adhered to the substrate, but no simple and effective means for separating the layer from the substrate has been proposed.

【0005】(3)は解決手段としてポリ塩化ビリニデン
が塗布された二軸延伸ポリプロピレンフィルムを適当の
大きさに裁断し、界面活性剤濃度0.1wt%以上の水溶液
中で100℃以上の温度で攪拌処理しフィルム表面のポリ
塩化ビニリデンを脆化剥離させて除去する方法であり、
(2)と(3)は両方ともに活面活性剤を使用しており汚水処
理が困難な問題である。100℃以上の温度を加えるため
オレフィン系樹脂の劣化を生じ、また塩化ビニリデン系
樹脂は分解着色し再利用できない物質に変化してしまう
ので、工業的に有利な方法ではない。しかも排水処理や
作業工程が簡便ではなく、コスト面でも高く経済性に欠
ける。
[0005] (3) As a solution, a biaxially stretched polypropylene film coated with polyvinylidene chloride is cut into an appropriate size and stirred at a temperature of 100 ° C or more in an aqueous solution having a surfactant concentration of 0.1% by weight or more. It is a method of treating and removing the polyvinylidene chloride on the film surface by embrittlement peeling,
Both (2) and (3) use a surfactant and are difficult to treat sewage. The application of a temperature of 100 ° C. or more causes deterioration of the olefin resin, and the vinylidene chloride resin is decomposed and colored to change into a substance that cannot be reused, so that this is not an industrially advantageous method. In addition, wastewater treatment and work processes are not simple, and cost is high and lacks economic efficiency.

【0006】[0006]

【発明が解決しようとする課題】本発明は上記のような
実状に鑑みてなされたものであり、オレフィン系樹脂基
体に塗布された塩化ビニリデン系樹脂層を基材表面より
効率よく分離除去してオレフィン系樹脂と塩化ビニリデ
ン系樹脂とを夫々分取し、これら二つの物質が劣化され
ずに回収され、直ちに繰り返し利用できるようにしたも
のである。また、処理に於ける溶剤等は回収され繰り返
し使用されるので、安価なコストで一切の廃棄物がでず
非常に経済性に富んだ方法を提供することを目的とす
る。
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above situation, and is intended to efficiently separate and remove a vinylidene chloride resin layer applied to an olefin resin substrate from the surface of the substrate. An olefin-based resin and a vinylidene chloride-based resin are separately collected, and these two substances are recovered without deterioration and can be used immediately and repeatedly. Another object of the present invention is to provide a method which is very economical because solvents and the like in the treatment are recovered and used repeatedly, so that no waste is generated at low cost.

【0007】[0007]

【課題を解決するための手段】すなわち、本発明は塩化
ビニリデン系樹脂塗布層を有するオレフィン系樹脂基体
を石油系溶剤中で100℃以下好ましくは40〜70℃という
低い温度で攪拌処理してオレフィン系樹脂基体表面の塩
化ビニリデン系樹脂塗布層を除去する方法を提供する。
さらに具体的には、上記方法において、攪拌装置を備え
かつ石油系溶剤を充した攪拌容器と、この攪拌容器の上
下部位に夫々接続されかつ攪拌装置を備えたパイプとか
らなり裁断された塩化ビニリデン系塗布層を有するオレ
フィン系樹脂基体の裁断片が該容器とパイプ内を循環さ
れるようになっており、更に容器の側面に石油系溶剤中
に溶解された塩化ビニリデン系樹脂を回収し、濃縮機よ
り生じる新しい溶剤が攪拌容器内に注入されることが繰
り返されるので、短時間で効率よく塩化ビニリデン系樹
脂の溶解、抽出が行なわれ、分取、処理されたものが良
質のオレフィン系樹脂と塩化ビニリデン系樹脂を与える
画期的な方法を提供する。
That is, the present invention relates to an olefin-based resin substrate having a vinylidene chloride-based resin coating layer in a petroleum-based solvent by stirring at a temperature of 100 ° C. or lower, preferably 40 to 70 ° C. A method for removing a vinylidene chloride-based resin coating layer on the surface of a resin-based substrate.
More specifically, in the above method, the cut vinylidene chloride comprising a stirring vessel provided with a stirring device and filled with a petroleum solvent, and pipes respectively connected to upper and lower portions of the stirring vessel and provided with a stirring device. A piece of an olefin-based resin substrate having a system-based coating layer is circulated in the container and the pipe, and further collects and concentrates vinylidene chloride-based resin dissolved in a petroleum-based solvent on the side of the container. Since the new solvent generated by the machine is repeatedly injected into the stirring vessel, the vinylidene chloride-based resin is efficiently dissolved and extracted in a short time, and the fractionated and treated product is combined with a high-quality olefin-based resin. An innovative method for providing a vinylidene chloride resin is provided.

【0008】[0008]

【発明の実施の形態】以下に本発明を詳細に説明する。
本発明が適用される塩化ビニリデン系樹脂塗布層を有す
るオレフィン系樹脂基体における塩化ビニリデン系樹脂
塗布層は、塩化ビニリデン系樹脂を有機溶媒に溶解した
もの、あるいは水性媒体に乳化剤等を用いて分散させた
ものをロールコート、グラビアコート、キスコート、エ
アーナイフコート等の方法でオレフィン系樹脂基体に塗
布、乾燥することにより形成されている。しかし塗布し
た塩化ビニリデン系樹脂は一旦乾燥したものは剥離し難
く、しかもあらゆる溶剤類に溶け難い被膜を形成する優
れたものである。塩化ビニリデン系樹脂としてはポリ塩
化ビニリデンの他、塩化ビニル、(メタ)アクリル酸エ
ステル、アクリロニトリルα、β−エチレン性不飽和カ
ルボン酸類等のモノマーと塩化ビニリデンとの共重合体
を挙げることができる。オレフィン系樹脂としては、エ
チレン単独重合体、エチレンα−オレフィン共重合体、
プロピレン単独重合体、プロピレンα−オレフィン共重
合体、ポリブテン−1、ポリ−4−メチルペンテン−1
等を挙げることができる。但し最近では積層成形品の性
能面から各層の接着強度が強められる方向で技術が開発
されると共に、柔軟剤や安定剤、抗菌剤等、各社が得意
とする添加剤を用いており、これに対応するには効率の
悪い場合も生じるので、灯油(ケロシン)の使用が推奨
される。勿論灯油以外の溶剤も挙げられ使用可能ではあ
るが、本発明を総合的に判断すれば工業的経済性を重視
せざるを得ないので、まずコスト面、入手利便性、保管
安全性、処理工程操作性などの点を考慮する必要上か
ら、灯油が本発明において優れている。しかし灯油のみ
に限定されるものではない。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail.
The vinylidene chloride-based resin coating layer in the olefin-based resin substrate having the vinylidene chloride-based resin coating layer to which the present invention is applied is obtained by dissolving a vinylidene chloride-based resin in an organic solvent or dispersing an aqueous medium using an emulsifier or the like. It is formed by applying and drying the olefin-based resin substrate by a method such as roll coating, gravure coating, kiss coating, and air knife coating. However, the applied vinylidene chloride-based resin is excellent in that once dried, it is difficult to peel off and forms a film that is hardly soluble in any solvent. Examples of the vinylidene chloride-based resin include, in addition to polyvinylidene chloride, copolymers of vinylidene chloride with monomers such as vinyl chloride, (meth) acrylate, acrylonitrile α, and β-ethylenically unsaturated carboxylic acids. As the olefin resin, ethylene homopolymer, ethylene α-olefin copolymer,
Propylene homopolymer, propylene α-olefin copolymer, polybutene-1, poly-4-methylpentene-1
And the like. However, in recent years, technologies have been developed in the direction of increasing the adhesive strength of each layer from the viewpoint of the performance of laminated molded products, and additives that each company is good at, such as softeners, stabilizers, antibacterial agents, etc., are used. Use of kerosene (kerosene) is recommended, as it may be inefficient to deal with it. Of course, solvents other than kerosene can be used as well, but if the present invention is comprehensively judged, industrial economics must be emphasized. First, cost, availability, storage safety, and processing Kerosene is excellent in the present invention because it is necessary to consider operability and the like. However, it is not limited only to kerosene.

【0009】本発明においては一連工業溶剤として、原
油からの直接留分として揮発油(石油エーテル・石油ベ
ンジン・リグロイン・ミネラルスピリット)・灯油・軽
油等が挙げられる。これらは先述のように添加剤に対応
する時に上記の中から選ばれた単一溶剤のみで処理後に
洗浄剤として使用し目的をはたす場合も生じる。オレフ
ィン系基体はフィルム、シート、成形容器、チューブ等
のようないずれの形状のものでもよく、また無延伸、一
軸延伸、ニ軸延伸等の処理を施したものでもよい。また
紙繊維、金属等の他の素材が付着ないし積層されていて
もよい。
In the present invention, a series of industrial solvents include volatile oils (petroleum ether, petroleum benzine, ligroin, mineral spirits), kerosene, light oil, etc. as a direct fraction from crude oil. As mentioned above, when corresponding to additives, they may be used as a cleaning agent after being treated with only a single solvent selected from the above, and this may serve the purpose. The olefin-based substrate may have any shape such as a film, a sheet, a molded container, a tube and the like, and may have been subjected to treatment such as non-stretching, uniaxial stretching and biaxial stretching. Further, other materials such as paper fiber and metal may be attached or laminated.

【0010】本発明における溶剤処理工程では、塩化ビ
ニリデン系樹脂塗布層を有するオレフィン系樹脂基体
は、例えば5mm角程度以下の不定形な大きさに裁断され
ていることが好ましく、これにより攪拌容器およびパイ
プ内の攪拌翼との接触面積が大きく循環時のパイプ内の
通過が良好となる。ただし、被処理物が積層されたり、
袋綴じ熱圧着部分が多くある場合には被処理物を更に微
粉砕することが望まれる。
In the solvent treatment step of the present invention, the olefin resin substrate having the vinylidene chloride resin coating layer is preferably cut into an irregular size of, for example, about 5 mm square or less. The contact area with the stirring blade in the pipe is large, and the passage through the pipe during circulation is good. However, when the objects to be processed are stacked,
In the case where there are many bag binding thermocompression bonding parts, it is desired to further finely pulverize the workpiece.

【0011】処理温度は100℃以下であれば充分であ
り、処理時間は特に制限されるものではない。通常15分
〜60分程度が好ましい。処理物の物性を考え温度はなる
べく低い位置に設定し時間も短く設定する。あらかじめ
処理物の小試作実験を通じて行うことが良い。
It is sufficient that the processing temperature is 100 ° C. or less, and the processing time is not particularly limited. Usually, about 15 to 60 minutes is preferable. Considering the physical properties of the processed material, the temperature is set as low as possible and the time is set short. It is better to carry out through small trial production experiments of the processed material in advance.

【0012】[0012]

【実施例】実施例1 厚さ5μmの塩化ビニリデン系樹脂が片面にコーティン
グされた厚さ30μmの二軸延伸ポリプロピレンフィルム
を約5mm角以下の不定形に裁断されたものを試料とし
て、この試料10gおよび灯油(市販品)280mlを内該攪拌
機の下部に濾板を取付けた容器に仕込み、攪拌しながら
85℃で15分間加熱した後に加熱を止め常温に戻してから
濾過処理し濾液からは直ちに濃縮機により塩化ビニリデ
ン系樹脂を回収し、溶剤は元の攪拌機付き容器中に戻し
更に上記と同じ操作を行う。
EXAMPLE 1 A 30 μm thick biaxially oriented polypropylene film coated on one side with a vinylidene chloride resin having a thickness of 5 μm was cut into an irregular shape of about 5 mm square or less. And 280 ml of kerosene (commercially available) are charged into a container having a filter plate attached to the lower portion of the stirrer and stirred.
After heating at 85 ° C for 15 minutes, the heating was stopped and the temperature was returned to room temperature, followed by filtration, and the vinylidene chloride resin was immediately recovered from the filtrate by a concentrator, and the solvent was returned to the original container with a stirrer, and the same operation as above was performed. Do.

【0013】この2回の操作を合計30分行い、濾液も前
と同じく回収し2回の回収物を合体させて乾燥して仕上
げる。得られたポリプロピレンの色調、ポリ塩化ビニリ
デン系樹脂除去率、残留塩素量を表1に示す。なおポリ
塩化ビニリデン系樹脂除去率はスパテル上に少量の試料
を乗せ加熱する時の臭いと溶融時の色調で目視判定で簡
単に評価し、残量塩素量はイオンクロマト分析法により
測定した。
These two operations are performed for a total of 30 minutes, and the filtrate is recovered as before, and the two recovered materials are combined and dried to finish. Table 1 shows the color tone, the polyvinylidene chloride resin removal rate, and the residual chlorine amount of the obtained polypropylene. The removal rate of the polyvinylidene chloride-based resin was easily evaluated by visual judgment based on the smell when a small amount of the sample was put on a spatula and heating and the color tone at the time of melting, and the residual chlorine amount was measured by ion chromatography.

【0014】実施例2 加熱温度を65℃と低く保ち、加熱時間を20分で2回と
し、他は実施例1と同様に行なったが、不充分な処理で
あったので、同じ方法を更に1回繰り返し行なうことで
実施例1と同様の物を得ることができた。温度が低温の
場合は処理、時間が長くかかるが、比較評価したところ
同等の物性結果を得た。
Example 2 The heating temperature was kept low at 65 ° C., and the heating time was set to twice in 20 minutes. The other steps were the same as in Example 1, but the processing was insufficient. By repeating the process once, the same product as in Example 1 could be obtained. When the temperature is low, it takes a long time to process, but when compared and evaluated, the same physical property results were obtained.

【表1】 [Table 1]

【0015】[0015]

【発明の効果】本発明の方法によれば、ポリ塩化ビニリ
デン系樹脂のみのフィルムを始めとし、塩化ビニリデン
系樹脂が塗布されたオレフィン系樹脂基体から効率よく
塩化ビニリデン系樹脂塗布層を除去することができ、し
かもこの基体と除去された塩化ビニリデン系樹脂共にリ
ターナブル(繰り返し利用)できる。現今環境と資源保
護の観点より、環境型経済システムを構築することに不
可欠なことから、本発明はこの視点にかなうかたちの従
来に見い出されない特徴のある発明である。
According to the method of the present invention, it is possible to efficiently remove a vinylidene chloride-based resin coating layer from an olefin-based resin substrate coated with a vinylidene chloride-based resin, including a film made of only polyvinylidene chloride-based resin. In addition, both the substrate and the removed vinylidene chloride resin can be returned (used repeatedly). Since it is indispensable to construct an environmental economic system from the viewpoint of protecting the environment and resources at present, the present invention is an invention with features not found in the past that meets this viewpoint.

【0016】又、本発明は低温に於いて処理されるた
め、その基体及び塗布層を含めた被処理物、溶剤などす
べてが劣化されることがないので工業的に優れて処理法
であり、処理されたすべてのものが市販品と同等の物性
を維持しており、オレフィン系樹脂基体についても降伏
点応力、破断点杭張力、破断点伸び衝撃強度等の試験結
果はまったく異なることなく品質が保たれている。また
廃液も一切生じない画期的な方法である。
Further, since the present invention is processed at a low temperature, the object to be processed including the substrate and the coating layer, the solvent and the like are not degraded, so that it is an industrially excellent processing method. All the treated products maintain the same physical properties as the commercial products, and the quality of the olefin-based resin base is not different from the test results such as stress at yield, pile tension at break, and elongation at break. Is kept. This is a revolutionary method that does not generate any waste liquid.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 塩化ビニリデン系樹脂塗布層を有するオ
レフィン系樹脂基体を石油系溶剤中で、100℃以下の低
い温度で攪拌溶解処理し、該樹脂基体表面の塩化ビニリ
デン系樹脂塗布層を溶解除去することによりオレフィン
系樹脂基体と油化ビニリデン系樹脂の溶解抽出物とを分
取し、二つの再生された物質が同時に再利用できること
を特徴とする方法。
An olefin resin substrate having a vinylidene chloride-based resin coating layer is stirred and dissolved in a petroleum-based solvent at a low temperature of 100 ° C. or less to dissolve and remove the vinylidene chloride-based resin coating layer on the surface of the resin substrate. A method of separating an olefin-based resin substrate and a dissolved extract of vinylidene oil-based resin, whereby two regenerated substances can be reused at the same time.
【請求項2】 前記攪拌溶解処理が、攪拌と抽出を兼ね
備えた装置において連続的に作業される請求項1に記載
の方法。
2. The method according to claim 1, wherein the stirring and dissolving process is continuously operated in an apparatus having both stirring and extraction.
【請求項3】 前記オレフィン系樹脂がポリプロピレン
である請求項1または2に記載の方法。
3. The method according to claim 1, wherein the olefin resin is polypropylene.
【請求項4】 攪拌溶解処理の1部または全部における
処理温度が120℃以上樹脂基体が溶融する温度以下であ
る請求項1〜3のいずれか1項に記載の方法。
4. The method according to claim 1, wherein the processing temperature in part or all of the stirring and dissolving processing is 120 ° C. or higher and the temperature at which the resin substrate melts.
JP19527899A 1999-07-09 1999-07-09 Removal and recycle of vinylidene chloride-based resin Pending JP2001019796A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19527899A JP2001019796A (en) 1999-07-09 1999-07-09 Removal and recycle of vinylidene chloride-based resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19527899A JP2001019796A (en) 1999-07-09 1999-07-09 Removal and recycle of vinylidene chloride-based resin

Publications (1)

Publication Number Publication Date
JP2001019796A true JP2001019796A (en) 2001-01-23

Family

ID=16338510

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2001019796A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018187808A (en) * 2017-04-28 2018-11-29 地方独立行政法人山口県産業技術センター Method for sorting and collecting composite material and sorting and collecting apparatus used for the same
JP7460069B2 (en) 2020-03-23 2024-04-02 株式会社ユニチカテクノス Method and device for recovering thermoplastic resin film from polyvinylidene chloride coating film

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018187808A (en) * 2017-04-28 2018-11-29 地方独立行政法人山口県産業技術センター Method for sorting and collecting composite material and sorting and collecting apparatus used for the same
JP7460069B2 (en) 2020-03-23 2024-04-02 株式会社ユニチカテクノス Method and device for recovering thermoplastic resin film from polyvinylidene chloride coating film

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