JP3452332B2 - Method for removing coating on resin substrate surface - Google Patents
Method for removing coating on resin substrate surfaceInfo
- Publication number
- JP3452332B2 JP3452332B2 JP05776294A JP5776294A JP3452332B2 JP 3452332 B2 JP3452332 B2 JP 3452332B2 JP 05776294 A JP05776294 A JP 05776294A JP 5776294 A JP5776294 A JP 5776294A JP 3452332 B2 JP3452332 B2 JP 3452332B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- substrate
- aqueous solution
- resin substrate
- alkali
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/582—Recycling of unreacted starting or intermediate materials
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing Of Solid Wastes (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、塗膜の除去方法に関
し、特に、塗膜を特定の条件下でアルカリ処理によって
易剥離化しさらに特定の研磨処理をすることにより被膜
を表面に有している基体の被膜を除去し、基体を再度同
一用途を含む工業的用途にリサイクル使用できる経時着
色のない樹脂材料とするための被膜の除去法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for removing a coating film, and more particularly, to a coating film on the surface of which the coating film is easily peeled by an alkali treatment under a specific condition and further subjected to a specific polishing treatment. The present invention relates to a method for removing a coating film on a substrate, so that the substrate can be reused as a resin material which is not colored over time and can be reused for industrial applications including the same applications.
【0002】[0002]
【従来の技術】一般に、樹脂成形品は、金属製品、ガラ
ス製品などに比較し、軽量で耐衝撃性に優れているばか
りでなく、安価で成形加工が容易であるなどの利点を有
しており、自動車、家庭電化製品、日用雑貨品、その他
の多くの分野で使用されている。特に自動車業界におい
ては車体重量の軽量化を図るため、年々車体に占める樹
脂製部品の点数が増加の傾向にある。これら樹脂製品の
多くは、耐傷つき・耐候性能の向上、製品美観向上の手
段として塗装が施される。この塗装に用いられる塗料に
は、樹脂成形品との接着性、塗膜自身の性能の面から三
次元架橋構造を形成する材料が多く用いられる。しか
し、この優れた塗膜性能が故に、なんらかの理由で塗装
により形成された硬化された被膜(硬化塗膜)を剥離さ
せる必要が生じた場合、強固な架橋構造を持つ硬化され
た被膜は容易には剥離されない。2. Description of the Related Art Generally, resin molded products have advantages such as light weight and excellent impact resistance as compared with metal products and glass products, as well as low cost and easy molding process. It is used in automobiles, home appliances, household goods, and many other fields. Particularly in the automobile industry, the number of resin parts occupying the vehicle body tends to increase year by year in order to reduce the weight of the vehicle body. Many of these resin products are coated as a means for improving scratch resistance, weather resistance, and improving product aesthetics. As the coating material used for this coating, a material that forms a three-dimensional crosslinked structure is often used in terms of the adhesiveness to the resin molded product and the performance of the coating film itself. However, due to this excellent coating performance, if for some reason it becomes necessary to peel off the cured coating formed by coating (cured coating), a cured coating with a strong crosslinked structure can be easily prepared. Is not peeled off.
【0003】一方、被膜の剥離は、塗装工程に不良が発
生した場合や、性能の劣化した旧塗膜を新塗膜に置き換
える場合、被塗装樹脂成形品の樹脂基材のみを再利用す
る場合など多くの場面で必要とされ、産業上重要な技術
である。従来行われてきた被膜の剥離、除去方法は、物
理的剥離、化学的剥離に大別される。この内、物理的剥
離はサンドペーパーなどで被膜を削る方法である。化学
的剥離は大略次に揚げる3つに分けられる。
1)塩素系溶剤を主成分とする剥離剤による除去(特公
昭51−34238号公報、同57−76065号公
報、同59−117567号公報)。
2)有機物質を主成分とする剥離剤による除去(特開昭
50−109925号公報、特開平1−289878号
公報、同2−274775号公報)。
3)無機物質を主成分とする剥離剤による除去(特開昭
50−109925号公報、同59−131674号公
報、同61−162568号公報)。
また、その他、上記3種の剥離剤の主成分を任意に混合
してなる剥離剤、また、これらに他の成分を任意に混合
してなる剥離剤を使用する除去方法もある。On the other hand, peeling of the coating film is carried out when a defect occurs in the coating process, when the old coating film having deteriorated performance is replaced by a new coating film, or when only the resin base material of the resin molding product to be reused is reused. It is an important industrial technology that is required in many situations. Conventional peeling and removing methods of the coating film are roughly classified into physical peeling and chemical peeling. Of these, physical peeling is a method of scraping the coating with sandpaper or the like. The chemical peeling is roughly divided into the following three frying. 1) Removal by a release agent containing a chlorine-based solvent as a main component (JP-B-51-34238, JP-A-57-76065 and JP-A-59-117567). 2) Removal by a release agent containing an organic substance as a main component (JP-A-50-109925, JP-A-1-289878, JP-A-2-274775). 3) Removal by a release agent containing an inorganic substance as a main component (JP-A-50-109925, JP-A-59-131674, JP-A-61-2162568). In addition, there is also a removal method using a release agent obtained by arbitrarily mixing the main components of the above-mentioned three types of release agents, or a release agent obtained by arbitrarily mixing these with other components.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、このよ
うな従来の被膜の除去法にあっては、除去しようとする
被膜の種類、厚み等により被膜の除去が不完全になるこ
とがある。被膜を除去した樹脂製品を再度同一用途にリ
サイクル使用する場合、被膜の除去が不完全であると製
品の物性等が低下してしまう。これを解決するため、ア
ルカリ処理と研磨処理とを組合わせた方法を本願出願人
は特願平4−256457号で提案した。これにより被
膜の除去が完全になったが、基体の着色の問題が生じる
場合があった。すなわち、得られた再生基体を用いて再
生樹脂製品とし、塗装等を行なった後、経時により塗装
後の着色が起こるといった問題があった。However, in such a conventional method for removing a coating film, the removal of the coating film may be incomplete depending on the type and thickness of the coating film to be removed. When the resin product from which the film has been removed is reused for the same purpose again, if the film is not completely removed, the physical properties of the product will deteriorate. In order to solve this, the applicant of the present application has proposed a method combining an alkali treatment and a polishing treatment in Japanese Patent Application No. 4-256457. This completed the removal of the coating, but sometimes caused substrate coloring problems. That is, there has been a problem that a colored resin after coating occurs over time after a coating or the like is performed using the obtained recycled substrate as a recycled resin product.
【0005】本発明の目的は、このような従来技術の問
題点を解決し、樹脂製品等の基体表面に形成された被膜
を十分に除去して樹脂物性の低下を防ぎ、かつ、基体の
塗装後の着色の経時変化がなく、リサイクル使用可能な
再生樹脂とすることができる被膜の除去方法を提供する
ことにある。The object of the present invention is to solve the above-mentioned problems of the prior art, to sufficiently remove the coating film formed on the surface of a substrate such as a resin product to prevent deterioration of the physical properties of the resin, and to coat the substrate. It is an object of the present invention to provide a method for removing a coating that can be used as a recycled resin that can be recycled without causing a change in coloration with time.
【0006】[0006]
【課題を解決するための手段】すなわち本発明は、表面
に被膜を有する樹脂基体を、アルカリ濃度が0.1wt
%以上で酸素濃度が5ppm以下のアルカリ水溶液中
で、温度110℃以上で該基体が溶融する温度より低い
温度で加熱処理し、さらに該基体を研磨することを特徴
とする樹脂基体表面の被膜の除去方法を提供する。That is, according to the present invention, a resin substrate having a film on its surface has an alkali concentration of 0.1 wt.
% In an alkaline aqueous solution having an oxygen concentration of 5 ppm or less at a temperature of 110 ° C. or more and a temperature lower than the melting temperature of the substrate, and further polishing the substrate. Provide a removal method.
【0007】ここで、表面に被膜を有する樹脂基体を、
アルカリ濃度が0.2〜4wt%で酸素濃度が3ppm
以下のアルカリ水溶液中で、温度140℃以上で該基体
が溶融する温度より低い温度で加熱処理し、さらに該基
体を研磨するのが好ましい。Here, the resin substrate having a coating on its surface is
Alkali concentration is 0.2-4wt% and oxygen concentration is 3ppm
It is preferable to heat-treat at a temperature of 140 ° C. or higher at a temperature lower than the melting temperature of the substrate, and further polish the substrate in the following alkaline aqueous solution.
【0008】また、前記アルカリ水溶液に不活性気体を
供給して、水溶液中の酸素濃度を減少させ、さらに不活
性気体を気相部に供給して加圧、脱圧を行い気相中の酸
素濃度を減少させてアルカリ処理するのが好ましい。Further, an inert gas is supplied to the alkaline aqueous solution to reduce the oxygen concentration in the aqueous solution, and further an inert gas is supplied to the gas phase part to pressurize and depressurize the oxygen in the gas phase. It is preferable to carry out alkali treatment with a reduced concentration.
【0009】ここで、水に不活性気体を供給して、水中
の酸素濃度を減少させた後、アルカリを加えて前記アル
カリ水溶液を調製し、さらに不活性気体を気相部に供給
して加圧、脱圧を行い気相中の酸素濃度を減少させてア
ルカリ処理するのが好ましい。Here, after supplying an inert gas to water to reduce the oxygen concentration in the water, an alkali is added to prepare the alkaline aqueous solution, and then an inert gas is supplied to the gas phase part to add the gas. It is preferable to perform pressure and depressurization to reduce the oxygen concentration in the gas phase and perform the alkali treatment.
【0010】前記アルカリ水溶液を80〜100℃に加
熱し、水溶液中の酸素濃度を減少させ、さらに不活性気
体を気相部に供給して加圧、脱圧を行い気相中の酸素濃
度を減少させてアルカリ処理するのが好ましい。The alkaline aqueous solution is heated to 80 to 100 ° C. to reduce the oxygen concentration in the aqueous solution, and an inert gas is supplied to the gas phase part to pressurize and depressurize the oxygen concentration in the gas phase. It is preferable to reduce the amount and perform the alkali treatment.
【0011】水を80〜100℃に加熱し、水中の酸素
濃度を減少させた後、アルカリを加えて前記アルカリ水
溶液を調製し、さらに不活性気体を気相部に供給して加
圧、脱圧を行い気相中の酸素濃度を減少させてアルカリ
処理するのが好ましい。After heating the water to 80 to 100 ° C. to reduce the oxygen concentration in the water, an alkali is added to prepare the alkaline aqueous solution, and an inert gas is further supplied to the gas phase portion to pressurize and depressurize. The alkali treatment is preferably performed by applying pressure to reduce the oxygen concentration in the gas phase.
【0012】アルカリ水溶液に酸素吸収剤を添加して水
溶液中の酸素濃度を減少させ、さらに不活性気体を気相
部に供給して加圧、脱圧を行い気相中の酸素濃度を減少
させてアルカリ処理するのが好ましい。An oxygen absorber is added to the alkaline aqueous solution to reduce the oxygen concentration in the aqueous solution, and an inert gas is supplied to the gas phase portion to pressurize and depressurize the oxygen phase to reduce the oxygen concentration in the gas phase. It is preferable to treat with alkali.
【0013】水に酸素吸収剤を添加して水中の酸素濃度
を減少させた後、アルカリを加えて前記アルカリ水溶液
を調製し、さらに不活性気体を気相部に供給して加圧、
脱圧を行い気相中の酸素濃度を減少させてアルカリ処理
するのが好ましい。After adding an oxygen absorbent to water to reduce the oxygen concentration in the water, an alkali is added to prepare the aqueous alkali solution, and an inert gas is further supplied to the gas phase section to pressurize the solution.
It is preferable to carry out alkali treatment by depressurizing to reduce the oxygen concentration in the gas phase.
【0014】表面に被膜を有する樹脂基体を、アルカリ
濃度が0.1wt%以上で酸素濃度が5ppm以下のア
ルカリ水溶液中で、温度110℃以上で該基体が溶融す
る温度より低い温度で加熱処理し、さらに該基体をスク
リューフィーダー型研磨装置中で、基体の溶融温度より
30〜110℃低い温度で研磨するのが好ましい。[0014] The resin substrate having a coating on the surface, the alkali concentration of oxygen concentration 0.1 wt% or more in the following alkaline aqueous solution 5 ppm, heat treatment at a temperature lower than the temperature at which said substrate is melted at temperature of 110 ° C. or higher Furthermore, it is preferable to polish the substrate in a screw feeder type polishing apparatus at a temperature lower by 30 to 110 ° C. than the melting temperature of the substrate.
【0015】表面に被膜を有する樹脂基体を、アルカリ
濃度が0.2〜4wt%で酸素濃度が3ppm以下のア
ルカリ水溶液中で、温度140℃以上で該基体が溶融す
る温度より低い温度で加熱処理し、さらに該基体をスク
リューフィーダー型研磨装置中で、基体の溶融温度より
30〜110℃低い温度で研磨するのが好ましい。A resin substrate having a coating on its surface is heat-treated in an alkaline aqueous solution having an alkali concentration of 0.2 to 4 wt% and an oxygen concentration of 3 ppm or less at a temperature of 140 ° C. or higher and a temperature lower than the melting temperature of the substrate. Furthermore, it is preferable to polish the substrate in a screw feeder type polishing apparatus at a temperature lower by 30 to 110 ° C. than the melting temperature of the substrate.
【0016】表面に被膜を有する樹脂基体を、アルカリ
濃度が0.1wt%以上で酸素濃度が5ppm以下のア
ルカリ水溶液中で、温度110℃以上で該基体が溶融す
る温度より低い温度で加熱処理し、さらに該基体を高速
槽型攪拌器タイプの研磨装置中で、温度70〜120℃
で、研磨剤と水と共に攪拌混合し、研磨するのが好まし
い。A resin substrate having a coating on its surface is heat-treated in an alkaline aqueous solution having an alkali concentration of 0.1 wt% or more and an oxygen concentration of 5 ppm or less at a temperature of 110 ° C. or higher and a temperature lower than the melting temperature of the substrate. The substrate is further heated at a temperature of 70 to 120 ° C. in a high speed tank type agitator type polishing apparatus.
Then, it is preferable to stir and mix with an abrasive and water, and to polish.
【0017】表面に被膜を有する樹脂基体を、アルカリ
濃度が0.2〜4wt%で酸素濃度が3ppm以下のア
ルカリ水溶液中で、温度140℃以上で該基体が溶融す
る温度より低い温度で加熱処理し、さらに該基体を高速
槽型攪拌器タイプの研磨装置中で、温度70〜120℃
で、研磨剤と水と共に攪拌混合し、研磨するのが好まし
い。[0017] The resin substrate having a coating on the surface, the alkali concentration in an oxygen concentration in the following alkaline aqueous solution 3ppm in 0.2~4Wt%, temperature 1 4 0 ° C. at a temperature lower than the temperature at which said substrate is melted at least After heat treatment, the substrate is heated in a high-speed tank-type stirrer-type polishing apparatus at a temperature of 70 to 120 ° C.
Then, it is preferable to stir and mix with an abrasive and water, and to polish.
【0018】表面に被膜を有する樹脂基体を、アルカリ
濃度が0.1wt%以上で酸素濃度が5ppm以下のア
ルカリ水溶液中で、温度110℃以上で該基体が溶融す
る温度より低い温度で加熱処理し、さらに該基体を、砥
粒を水に分散した研磨液を用いて液体ホーニング処理
し、研磨するのが好ましい。A resin substrate having a coating on its surface is heat-treated in an alkaline aqueous solution having an alkali concentration of 0.1 wt% or more and an oxygen concentration of 5 ppm or less at a temperature of 110 ° C. or higher and a temperature lower than the melting temperature of the substrate. Further, it is preferable to polish the substrate by liquid honing using a polishing liquid in which abrasive grains are dispersed in water.
【0019】表面に被膜を有する樹脂基体を、アルカリ
濃度が0.2〜4wt%で酸素濃度が3ppm以下のア
ルカリ水溶液中で、温度140℃以上で該基体が溶融す
る温度より低い温度で加熱処理し、さらに該基体を、砥
粒を水に分散した研磨液を用いて液体ホーニング処理
し、研磨するのが好ましい。[0019] The resin substrate having a coating on the surface, the alkali concentration in an oxygen concentration in the following alkaline aqueous solution 3ppm in 0.2~4Wt%, temperature 1 4 0 ° C. at a temperature lower than the temperature at which said substrate is melted at least It is preferable that the substrate is heat-treated, and then the substrate is subjected to a liquid honing treatment using a polishing liquid in which abrasive grains are dispersed in water to polish the substrate.
【0020】以下、本発明の被膜の除去方法(以下、
「本発明の方法」と省略することがある。)について詳
細に説明する。The method for removing the coating film of the present invention (hereinafter, referred to as
It may be abbreviated as “the method of the present invention”. ) Will be described in detail.
【0021】本発明の方法は、樹脂基体の表面に形成さ
れた被膜を除去する方法である。被膜を除去される樹脂
基体は、特に制限されず、いずれの材質であってもよ
い。またガラス繊維やカーボン繊維、無機粉体により充
填補強された樹脂基体も含まれる。特に、本発明の方法
は、ポリオレフィンからなる基体の表面の被膜を除去す
る際に有効である。ポリオレフィンからなる基体の中で
も、特にポリプロピレンは、ポリオレフィンの中でも融
点が高く、より高温で有効なアルカリ処理が可能なた
め、本発明の方法は有効である。The method of the present invention is a method of removing the coating film formed on the surface of the resin substrate. The resin substrate from which the coating film is removed is not particularly limited and may be any material. Further, a resin substrate filled and reinforced with glass fiber, carbon fiber, or inorganic powder is also included. In particular, the method of the present invention is effective in removing the coating film on the surface of the substrate made of polyolefin. Among the substrates made of polyolefin, polypropylene, in particular, has a high melting point among polyolefins and can be effectively treated with alkali at a higher temperature, so that the method of the present invention is effective.
【0022】本発明方法を適用する際の基体の形状は、
特に制限されない。アルカリ水溶液での水性剥離工程に
ついていえば、剥離液と被膜との接触面積が増大するの
で粉砕体、粒状体等であるのが好ましい。その大きさ
は、およそ粒径0.5〜20mmであるのが好ましい。The shape of the substrate when the method of the present invention is applied is
There is no particular limitation. In the case of the aqueous stripping step using an alkaline aqueous solution, the contact area between the stripping solution and the coating film is increased, so that it is preferably a pulverized body or a granular body. The size is preferably about 0.5 to 20 mm in particle size.
【0023】本発明の方法は、樹脂基体の表面に形成さ
れた被膜、特に硬化塗膜を除去する方法として有効であ
る。本発明の方法によって剥離される硬化塗膜は、フェ
ノール系塗料、ポリエステル系塗料、アルキッド系塗
料、アクリル系塗料、ポリウレタン系塗料、エポキシ系
塗料などの塗料を塗布し、硬化して形成された被膜が挙
げられる。特に、自動車の塗装に用いられるポリエステ
ルウレタン、ポリエステルメラミン、アクリルウレタ
ン、アクリルメラミンなどからなる硬化塗膜を剥離する
のに、本発明の方法は好適である。The method of the present invention is effective as a method for removing a coating film formed on the surface of a resin substrate, particularly a cured coating film. The cured coating film peeled by the method of the present invention is a coating film formed by coating a coating material such as a phenolic coating material, a polyester coating material, an alkyd coating material, an acrylic coating material, a polyurethane coating material, an epoxy coating material, and curing the coating material. Is mentioned. In particular, the method of the present invention is suitable for peeling off a cured coating film made of polyester urethane, polyester melamine, acrylic urethane, acrylic melamine or the like used for coating automobiles.
【0024】さらに、この硬化塗膜は、樹脂基体の表面
に直接形成されているものでもよいし、プライマー層を
介して樹脂基体の表面に形成されているものでもよい。
このプライマーは特に限定されず、この種の樹脂基体の
表面に硬化塗膜を形成するために用いられる、いずれの
プライマーでもよい。また、樹脂基体表面は硬化塗膜と
の密着性改良のため、プラズマ処理、フレーム処理、ウ
ォーターブラストなどの表面処理がなされていてもよ
い。Further, this cured coating film may be directly formed on the surface of the resin substrate, or may be formed on the surface of the resin substrate via a primer layer.
This primer is not particularly limited, and any primer used for forming a cured coating film on the surface of this type of resin substrate may be used. Further, the surface of the resin substrate may be subjected to surface treatment such as plasma treatment, flame treatment, water blasting or the like in order to improve adhesion with the cured coating film.
【0025】本発明の方法は、種々の塗料により形成さ
れた多層被膜の除去に有効である。除去される被膜の厚
みは、特に限定されるものではないが、硬化塗膜として
200μm厚以下が好ましく、10〜100μm、さら
に30〜40μmがより好ましい。The method of the present invention is effective in removing multilayer coatings formed by various paints. The thickness of the coating film to be removed is not particularly limited, but the thickness of the cured coating film is preferably 200 μm or less, more preferably 10 to 100 μm, and further preferably 30 to 40 μm.
【0026】本発明の方法で用いられるアルカリ性物質
を含む水溶液は水性剥離液である。このアルカリ物質と
しては、特に限定されないが、例えば、LiOH、Na
OH、KOH、Mg(OH)2 、Ca(OH)2 などの
無機アルカリ性物質などが挙げられる。これらは1種単
独でも2種以上を組み合わせてもよい。好ましくは、N
aOH、KOH、より好ましくはNaOHが用いられ
る。The aqueous solution containing an alkaline substance used in the method of the present invention is an aqueous stripping solution. The alkaline substance is not particularly limited, but examples thereof include LiOH and Na.
Examples thereof include inorganic alkaline substances such as OH, KOH, Mg (OH) 2 and Ca (OH) 2 . These may be used alone or in combination of two or more. Preferably N
aOH, KOH, and more preferably NaOH is used.
【0027】アルカリ性物質の濃度は、0.1wt%以
上であり、好ましくは0.1〜5wt%、さらに0.2
〜4wt%であるのがより好ましい。この濃度とするの
は、被膜が充分に剥離され、一方低アルカリ濃度なので
取り扱い時の危険が少なく、廃水の処理が容易であるか
らである。The concentration of the alkaline substance is 0.1 wt% or more, preferably 0.1 to 5 wt%, and 0.2
More preferably, it is ˜4 wt%. The reason for this concentration is that the coating film is sufficiently peeled off, and on the other hand, since the alkali concentration is low, there is little danger in handling and waste water is easily treated.
【0028】また、このアルカリ水溶液は、前記アルカ
リ性物質以外に、必要に応じて、他の配合剤を含んでい
ても良い。例えば、界面活性剤、アンモニア、アミン
類、有機溶媒などを処理促進剤として、少量、特に50
wt%以下含んでいてもよい。界面活性剤としては、例
えば、アルキルベンゼンスルホン酸塩、ジアルキルスル
ホコハク酸塩、ポリオキシエチレンアルキルエーテルな
どがあげられ、アミン類としては、例えば、トリエチル
アミンなどのアミン、モノエタノールアミンなどのアル
カノールアミンなどが挙げられる。また、有機溶媒とし
ては、例えば、メチルアルコール、1−プロピルアルコ
ール、2−プロピルアルコール、t−ブチルアルコール
など水との相溶性が良好であるものが挙げられる。In addition to the alkaline substance, the alkaline aqueous solution may contain other compounding agents, if necessary. For example, surfactants, ammonia, amines, organic solvents, etc. are used as treatment accelerators in small amounts, especially 50
It may be contained by wt% or less. Examples of the surfactant include alkylbenzene sulfonate, dialkylsulfosuccinate, polyoxyethylene alkyl ether, and the like, and examples of amines include amines such as triethylamine and alkanolamines such as monoethanolamine. To be Examples of the organic solvent include those having good compatibility with water such as methyl alcohol, 1-propyl alcohol, 2-propyl alcohol and t-butyl alcohol.
【0029】本発明の方法において、上述のアルカリ水
溶液によって樹脂基体をアルカリ処理する方法は、特に
限定されず、基体をアルカリ水溶液を満たした槽中に浸
漬する方法、オートクレーブ中で加圧下にアルカリ水溶
液中に基体を浸漬する方法、基体をアルカリ水溶液に連
続的に接触する方法など、いかなる処理方法でもよい。
特に高温で基体を処理する場合には、加圧状態となるた
め、オートクレーブ中でアルカリ水溶液中に浸漬する方
法がよい。加圧状態で処理する場合、圧力は、温度16
0℃で5kg/cm2程度である。In the method of the present invention, the method of alkali-treating the resin substrate with the above-mentioned alkaline aqueous solution is not particularly limited, and the substrate is immersed in a tank filled with the alkaline aqueous solution, or the alkaline aqueous solution is under pressure in an autoclave. Any treatment method such as a method of immersing the substrate therein or a method of continuously contacting the substrate with an alkaline aqueous solution may be used.
Particularly when the substrate is treated at a high temperature, it is in a pressurized state, so that it is preferable to immerse the substrate in an alkaline aqueous solution in an autoclave. When processing under pressure, the pressure is 16
It is about 5 kg / cm 2 at 0 ° C.
【0030】本発明の方法において、上述のアルカリ水
溶液で硬化塗膜を表面に有する基体を処理する際の温度
は、110℃以上、好ましくは140℃以上で基体が溶
融する温度よりも低い温度であり、例えば、ポリオレフ
ィンからなる基体を処理する温度は、110〜170℃
であり、150〜170℃、より好ましくは150〜1
60℃である。さらに、処理時間は、硬化塗膜の種類、
膜厚、基体の形状、寸法、あるいは処理温度などに応じ
て適宜選択すればよく、通常、5分〜1時間程度、好ま
しくは10分〜40分程度である。In the method of the present invention, the temperature for treating the substrate having the cured coating film on its surface with the above-mentioned alkaline aqueous solution is 110 ° C. or higher, preferably 140 ° C. or higher, and lower than the temperature at which the substrate melts. Yes, for example, the temperature for treating a substrate made of polyolefin is 110 to 170 ° C.
And 150 to 170 ° C., more preferably 150 to 1
It is 60 ° C. Furthermore, the processing time depends on the type of cured coating film,
It may be appropriately selected depending on the film thickness, the shape and size of the substrate, the processing temperature, etc., and is usually about 5 minutes to 1 hour, preferably about 10 minutes to 40 minutes.
【0031】アルカリ水溶液処理は、酸素濃度5ppm
以下で行なう必要があり、予め脱酸素を行なうのが好ま
しい。ここで、酸素濃度を5ppm以下とする方法とし
て、上記アルカリ水溶液を仕込んだ槽中またはオートク
レーブ中に窒素などの不活性気体をバブリングし該アル
カリ水溶液中の溶存酸素を除去する方法がある。この場
合、不活性気体として窒素、炭酸ガス、水蒸気などを使
用することが好ましい。また、バブリングする時間はア
ルカリ水溶液の量、ガスの吹き込み量、処理槽の形状な
どによって異なるが、一般に5分以上のバブリングを行
なうことが望ましい。またアルカリ水溶液を調製するた
めに使用する水を仕込んだ槽中またはオートクレーブ中
に不活性気体をバブリングして溶存酸素を除去した後、
アルカリを加えてアルカリ水溶液を調製しても良い。Oxygen concentration 5 ppm
It is necessary to perform the following, and it is preferable to perform deoxidation in advance. Here, as a method of adjusting the oxygen concentration to 5 ppm or less, there is a method of bubbling an inert gas such as nitrogen into a tank or an autoclave charged with the alkaline aqueous solution to remove dissolved oxygen in the alkaline aqueous solution. In this case, it is preferable to use nitrogen, carbon dioxide gas, steam or the like as the inert gas. The bubbling time varies depending on the amount of the alkaline aqueous solution, the amount of gas blown, the shape of the processing tank, etc., but it is generally desirable to perform bubbling for 5 minutes or more. In addition, after removing the dissolved oxygen by bubbling an inert gas in a tank or an autoclave charged with water used for preparing an alkaline aqueous solution,
An alkaline aqueous solution may be prepared by adding an alkali.
【0032】上記方法以外にも、酸素濃度を5ppm以
下とする方法として、上記アルカリ水溶液を70℃以上
の温度に常圧下で加熱し、溶存酸素を除去する方法があ
る。加熱温度は70℃以上でより高温の方が溶存酸素除
去効果は大きく、80〜100℃程度が好ましい。ま
た、加熱時間は加熱温度、アルカリ水溶液の量、処理槽
の形状によって異なるが、3分以上が好ましい。またア
ルカリ水溶液を調製するために使用する水を70℃以上
の温度に常圧下で加熱して溶存酸素を除去した後、アル
カリを加えてアルカリ水溶液を調製しても良い。In addition to the above method, there is a method of removing the dissolved oxygen by heating the alkaline aqueous solution to a temperature of 70 ° C. or more under normal pressure as a method of adjusting the oxygen concentration to 5 ppm or less. When the heating temperature is 70 ° C. or higher, the higher the temperature, the greater the effect of removing dissolved oxygen, and it is preferably about 80 to 100 ° C. The heating time varies depending on the heating temperature, the amount of the alkaline aqueous solution, and the shape of the treatment tank, but is preferably 3 minutes or more. Further, water used for preparing the alkaline aqueous solution may be heated to a temperature of 70 ° C. or higher under normal pressure to remove dissolved oxygen, and then an alkali may be added to prepare the alkaline aqueous solution.
【0033】酸素濃度を5ppm以下にする方法とし
て、上記アルカリ水溶液中に亜硫酸ソーダなどの酸素吸
収剤を少量、好ましくは0.3〜5g/lを添加する方
法がある。酸素吸収剤としては、亜硫酸ソーダ、亜硫酸
カリ、亜硫酸カルシウム等の亜硫酸塩、亜燐酸塩、次亜
燐酸ソーダ、次亜燐酸カリ等の次亜燐酸塩等の無機還元
性物質、およびカテコール、ブレンツカテキンなどの有
機還元性化合物があるが、酸素吸収効果、廃水処理の観
点より、亜硫酸塩、亜燐酸塩の使用が好ましい。また、
酸素吸収効果を高めるために、40℃以上の温度に処理
液を加熱すると良い。処理時間はアルカリ水溶液の量、
酸素吸収剤の使用量、処理槽の形状などによって異なる
が40℃以上に加熱して5分以上、好ましくは、10〜
30分である。また、アルカリ水溶液を調製するために
使用する水に、酸素吸収剤を添加して溶存酸素を除去し
た後、アルカリを加えてアルカリ水溶液を調製しても良
い。As a method of reducing the oxygen concentration to 5 ppm or less, there is a method of adding a small amount of an oxygen absorbent such as sodium sulfite, preferably 0.3 to 5 g / l to the above alkaline aqueous solution. Examples of the oxygen absorbent include sodium sulfite, potassium sulfite, calcium sulfite, and other sulfites, phosphites, sodium hypophosphite, potassium hypophosphite, and other inorganic reducing substances, and catechol and blends. Although there are organic reducing compounds such as catechin, it is preferable to use sulfite or phosphite from the viewpoint of oxygen absorption effect and wastewater treatment. Also,
In order to enhance the oxygen absorption effect, the treatment liquid may be heated to a temperature of 40 ° C. or higher. The treatment time depends on the amount of alkaline aqueous solution,
It depends on the amount of the oxygen absorbent used, the shape of the treatment tank, etc., but is heated to 40 ° C. or higher for 5 minutes or longer, preferably 10 to
30 minutes. Further, an oxygen absorbent may be added to water used for preparing an alkaline aqueous solution to remove dissolved oxygen, and then an alkali may be added to prepare an alkaline aqueous solution.
【0034】一方、アルカリ水溶液を仕込んだ槽の気相
部の酸素を除去する方法として、窒素等の不活性気体で
加圧し、その後常圧に脱圧する操作を繰り返す方法があ
る。繰り返し回数は好ましくは5〜3回である。この場
合、不活性気体として窒素、炭素ガス、水蒸気などを使
用することが好ましい。また、加圧する時間は不活性気
体の吹き込み量、処理槽の形状などによって異なるが、
一般に2分以上行なうことが望ましい。その他、気相部
に窒素等の不活性気体を流す方法もある。この場合、不
活性気体として窒素、炭酸ガス、水蒸気などを使用する
ことが好ましい。また、不活性気体を流す時間はガスの
吹き込み量、処理槽の形状などによって異なるが、一般
に5分以上行なうことが望ましい。On the other hand, as a method of removing oxygen in the gas phase portion of a tank charged with an alkaline aqueous solution, there is a method of repeating pressurization with an inert gas such as nitrogen and then depressurizing to normal pressure. The number of repetitions is preferably 5 to 3 times. In this case, it is preferable to use nitrogen, carbon gas, steam or the like as the inert gas. Also, the time for pressurization varies depending on the amount of inert gas blown, the shape of the processing tank, etc.
Generally, it is desirable to carry out for 2 minutes or more. In addition, there is also a method of flowing an inert gas such as nitrogen into the gas phase part. In this case, it is preferable to use nitrogen, carbon dioxide gas, steam or the like as the inert gas. The time for flowing the inert gas varies depending on the amount of gas blown, the shape of the processing tank, and the like, but it is generally desirable that the time is 5 minutes or more.
【0035】なお、同一の処理槽内の液相部と気相部の
いずれか一方で酸素を除去すると他方に含有される酸素
と平衡状態になってしまい酸素の除去が充分行えないこ
とがある。例えば、液相部を加熱処理すると気相部の空
気中に含まれる酸素と液相部の酸素とが平衡になり脱酸
素できないことになる。このため同一の処理槽内の液相
部の脱酸素処理と気相部の脱酸素処理とを、処理条件に
応じて逐次行ったり別々に行ったりするのが好ましい。Incidentally, if oxygen is removed from either the liquid phase part or the gas phase part in the same processing tank, it may be in equilibrium with the oxygen contained in the other part, so that the oxygen may not be sufficiently removed. . For example, if the liquid phase part is heat-treated, oxygen contained in the air of the gas phase part and oxygen of the liquid phase part will be in equilibrium and deoxidation cannot be performed. For this reason, it is preferable to perform the deoxidation treatment of the liquid phase portion and the deoxygenation treatment of the gas phase portion in the same treatment tank sequentially or separately depending on the treatment conditions.
【0036】第1の研磨方法では、基体をアルカリ水溶
液で処理した後、アルカリ水溶液から基体を分離し、あ
るいは分離せずにそのまま、基体表面同志を接触させて
研磨する。基体表面同志を接触させて研磨する方法は、
研磨機中に粒状の樹脂基体を入れ、樹脂基体同志、樹脂
基体と研磨機に設けられた機械的研磨手段、樹脂基体と
研磨機のバレル(外壁)との間に剪断力を発生させて基
体表面を研磨する。なお研磨する基体を水、アルコール
等により濡らし、研磨処理を行っても良い。In the first polishing method, after the substrate is treated with the alkaline aqueous solution, the substrate is separated from the alkaline aqueous solution, or the substrate surfaces are brought into contact with each other and polished without being separated. The method of polishing by bringing the substrate surfaces into contact with each other is
Put a granular resin substrate into the polishing machine, and generate a shearing force between the resin substrate, the mechanical polishing means provided on the resin substrate and the polishing machine, and the barrel (outer wall) of the polishing machine. Polish the surface. The substrate to be polished may be wetted with water, alcohol or the like to carry out the polishing treatment.
【0037】本発明の方法において、基体表面同志の研
磨を行う研磨機は、精米機に類似した構造をとることが
でき、きねつき式、臼らせん式、円筒摩擦式、自動循環
式、研削式等がある。特に樹脂を溶融押し出しする場合
に用いられるスクリューフィーダー型押出機と類似の構
造をもつスクリューフィーダー型研磨機が好ましく、こ
の構造では、内部に組み込まれたスクリューの回転力で
樹脂基体同志、樹脂基体とスクリューおよびバレル(外
壁)との間に剪断力を発生させ基体表面同志を研磨する
ことができる。剪断力を効果的に発生させるスクリュー
構造と、バレルの表面構造をとることが好ましい。研磨
時の剪断エネルギーは、0.2KW/kg基体樹脂以上
の条件で研磨するのが好ましい。In the method of the present invention, the polishing machine for polishing the surfaces of the substrates can have a structure similar to that of a rice polishing machine, such as a knurling type, a die spiral type, a cylindrical friction type, an automatic circulation type and a grinding type. Etc. Particularly, a screw feeder type polishing machine having a structure similar to that of a screw feeder type extruder used when melt-extruding a resin is preferable, and in this structure, the resin substrate is mixed with the resin substrate by the rotational force of the screw incorporated inside, and the resin substrate. A shearing force can be generated between the screw and the barrel (outer wall) to polish the substrate surfaces. It is preferable to have a screw structure that effectively generates shearing force and a barrel surface structure. The shearing energy during polishing is preferably 0.2 KW / kg or more as the base resin.
【0038】本発明の方法において、スクリューフィー
ダー型研磨機の操作条件は研磨効果を顧慮した場合、樹
脂基体の溶融温度より30〜110℃低い温度、好まし
くは50〜100℃低い温度が好ましい。ポリオレフィ
ンからなる基体を処理する場合、好ましくは60〜11
0℃で行うことができる。In the method of the present invention, the operating condition of the screw feeder type polishing machine is preferably 30 to 110 ° C. lower than the melting temperature of the resin substrate, more preferably 50 to 100 ° C. lower than the melting temperature of the resin substrate in consideration of the polishing effect. When treating a substrate made of polyolefin, preferably 60 to 11
It can be carried out at 0 ° C.
【0039】第2の研磨方法では、基体をアルカリ水溶
液で処理した後、アルカリ水溶液から基体を分離し、あ
るいは分離せずにそのまま、基体表面を研磨材で研磨す
る。基体表面を研磨材で研磨する方法は、板状の基体表
面に研磨材をブラスト処理する等いかなる方法でもよい
が、特に高速槽型攪拌器タイプの研磨装置中で、研磨材
と基体とを高速攪拌する方法が好ましい。In the second polishing method, after the substrate is treated with the alkaline aqueous solution, the substrate is separated from the alkaline aqueous solution, or the surface of the substrate is polished with an abrasive as it is without being separated. The method of polishing the surface of the substrate with the abrasive may be any method such as blasting the surface of the substrate in the form of a plate, but especially in a high-speed tank-type agitator type polishing apparatus, the abrasive and the substrate can be treated at high speed. A stirring method is preferred.
【0040】本発明の方法において、基体表面の研磨を
行う高速槽型攪拌機は一般に粉体や粒状物の攪拌に使用
されている槽型攪拌機例えばヘンシェルミキサー類似の
構造を持った装置で攪拌中に研磨効果が上がるように攪
拌羽、邪魔板の構造を設計したものである。高速とは、
攪拌羽の回転数が約1000回/1分間以上程度のもの
をいう。In the method of the present invention, the high-speed tank-type stirrer for polishing the surface of the substrate is generally a tank-type stirrer which is used for stirring powders or granules, for example, an apparatus having a structure similar to a Henschel mixer. The structure of the stirring blade and baffle plate is designed to improve the polishing effect. High speed means
The number of rotations of the stirring blade is about 1000 times / minute or more.
【0041】本発明の方法において、研磨材および研磨
材を含む研磨液組成は研磨効果に影響を与え、研磨材の
粒径が60μmより小さいと衝突時の力が小さく研磨効
果がない、また、150μmより大きいと衝突時の力が
大きくなり、柔らかい樹脂基体の場合は研磨材が基体中
にめり込むことがある。このため、研磨材の粒径は80
〜120μmが好ましい。本発明の方法において、基体
と研磨材の割合は、重量比で、1:0.1〜0.5が研
磨効果の面より望ましい。研磨材は、アルミナ粉体、ピ
ーチパウダー、珪砂等が用いられ、珪砂が好ましい。In the method of the present invention, the polishing agent and the composition of the polishing liquid containing the polishing agent affect the polishing effect. If the particle size of the polishing agent is less than 60 μm, the force at the time of collision is small and the polishing effect is not exerted. If it is larger than 150 μm, the force at the time of collision becomes large, and in the case of a soft resin substrate, the abrasive may get caught in the substrate. Therefore, the particle size of the abrasive is 80
˜120 μm is preferable. In the method of the present invention, the weight ratio of the substrate to the abrasive is preferably 1: 0.1 to 0.5 from the viewpoint of the polishing effect. As the abrasive, alumina powder, peach powder, silica sand, etc. are used, and silica sand is preferable.
【0042】研磨材は研磨液とともに用いるのが好まし
く、研磨液の具体例は、アルコール、水等が挙げられ
る。研磨液中の研磨材と研磨液との割合は研磨材:研磨
液=2:3〜6が望ましい。本発明の方法において、研
磨処理時の温度は樹脂基体の溶融温度より50〜110
℃低い温度が研磨効果の面より望ましい。ポリオレフィ
ンからなる基体を処理する温度は、好ましくは70〜1
20℃、より好ましくは80〜100℃で行うことがで
きる。好ましい組み合せとして、基体1kgに対し珪砂
0.1〜0.5kg、水0.4〜0.8kgを用いて温
度70〜120℃で表面研磨を行うことがある。The polishing material is preferably used together with a polishing liquid, and specific examples of the polishing liquid include alcohol and water. The ratio of the polishing material to the polishing liquid in the polishing liquid is preferably polishing material: polishing liquid = 2: 3 to 6. In the method of the present invention, the temperature during the polishing treatment is 50 to 110, which is higher than the melting temperature of the resin substrate.
A temperature lower by ℃ is desirable from the viewpoint of polishing effect. The temperature for treating the substrate made of polyolefin is preferably 70 to 1
It can be performed at 20 ° C, more preferably 80 to 100 ° C. As a preferable combination, surface polishing is performed at a temperature of 70 to 120 ° C. using 0.1 to 0.5 kg of silica sand and 0.4 to 0.8 kg of water per 1 kg of the substrate.
【0043】第3の研磨方法では、基体をアルカリ水溶
液で処理した後、アルカリ水溶液から基体を分離し、あ
るいは分離せずにそのまま、基体表面を液体ホーニング
処理する。In the third polishing method, after treating the substrate with the alkaline aqueous solution, the substrate is separated from the alkaline aqueous solution, or the substrate surface is subjected to liquid honing treatment without being separated.
【0044】液体ホーニング処理は、微細な砥粒を水に
混ぜ研磨液として高速で加工面に吹きつける表面仕上法
である。研磨液に使用するものは、珪砂、ピーチパウダ
ー等が挙げられるが、特に80から200メッシュのア
ルミナ粉体を、該粉体に対して2〜5倍量、好ましくは
3〜5倍量の水に分散した研磨液を用いるのが好まし
い。The liquid honing treatment is a surface finishing method in which fine abrasive grains are mixed with water and sprayed as a polishing liquid at a high speed on a processed surface. Examples of the polishing liquid used include silica sand and peach powder. Particularly, 80 to 200 mesh alumina powder is used in an amount of 2 to 5 times, preferably 3 to 5 times the amount of water. It is preferable to use a polishing liquid dispersed in.
【0045】アルミナの粒径が200メッシュより小さ
いと液体ホーニング処理時のアルミナ粒子の樹脂基材へ
の衝突エネルギーが小さく十分な研磨効果が得られな
い。一方、アルミナの粒径が80メッシュより大きいと
衝突エネルギーが大きくなり、樹脂基材の中にアルミナ
粒子がめり込むことがある。このため、使用するアルミ
ナの粒径は80〜200メッシュが望ましい。If the particle size of alumina is smaller than 200 mesh, the energy of collision of the alumina particles with the resin base material during the liquid honing process is small and a sufficient polishing effect cannot be obtained. On the other hand, when the particle size of alumina is larger than 80 mesh, the collision energy becomes large, and the alumina particles may be embedded in the resin base material. Therefore, the particle size of alumina used is preferably 80 to 200 mesh.
【0046】液体ホーニング処理の噴出圧力は、好まし
くは、2〜3kg/cm2で行う。液体ホーニング時の噴出圧
力が2kg/cm2以下の場合ほとんど研磨効果が認められ
ず、3kg/cm2を超えると基体内部まで削り取られてしま
う。このため、噴出圧力は2〜3kg/cm2の範囲が望まし
い。The jetting pressure of the liquid honing treatment is preferably 2 to 3 kg / cm 2 . When the jetting pressure during liquid honing is 2 kg / cm 2 or less, almost no polishing effect is observed, and when it exceeds 3 kg / cm 2 , the inside of the substrate is scraped off. Therefore, it is desirable that the ejection pressure be in the range of 2 to 3 kg / cm 2 .
【0047】[0047]
【実施例】以下、本発明の実施例及び比較例によって本
発明を具体的に説明するが、本発明は、これらの実施例
になんら限定されるものではない。The present invention will be specifically described below with reference to Examples of the present invention and Comparative Examples, but the present invention is not limited to these Examples.
【0048】「塗装試料の準備」各例において、カーボ
ンブラックを0.5wt%含有するポリプロピレン(三
井石油化学工業(株)製、商品名:ハイポール X44
0,以下、PPと略称する)を射出成形に供して、厚さ
3mmの角板を作製した。この角板を1,1,1−トリ
クロルエタン蒸気に30秒曝して処理した後、室温下、
30分間放置して乾燥した。次に、角板の1,1,1−
トリクロルエタンで処理された表面に、プライマー(三
井石油化学(株)製、ユニストールP−801)を、エ
アースプレーガンを用いて、乾燥後のプライマー膜厚が
約10μm程度になる様に塗布した後、常温で10分間
セッティングを行った。その後、角板のプライマー膜の
上に熱硬化性塗料である一液型アクリルメラミン塗料
(関西ペイント(株)製、ソフレックス#1200)
を、エアースプレーガン(吐出圧1kg/cm2)を用いて、
硬化性塗膜の膜厚が30〜40μmになるように塗布
し、10分間セッティングを行った。次いで、120
℃、30分間で塗膜を硬化させ、PP製の角板の表面に
プライマーを介して硬化塗膜を形成した塗装試料を得
た。[Preparation of coating sample] In each example, polypropylene containing 0.5 wt% of carbon black (manufactured by Mitsui Petrochemical Industry Co., Ltd., trade name: HYPOL X44)
0, hereinafter abbreviated as PP) was subjected to injection molding to produce a square plate having a thickness of 3 mm. After this square plate was exposed to 1,1,1-trichloroethane vapor for 30 seconds and treated, at room temperature,
It was left to dry for 30 minutes. Next, the square plate 1,1,1-
A primer (UNISTOL P-801 manufactured by Mitsui Petrochemical Co., Ltd.) was applied to the surface treated with trichloroethane using an air spray gun so that the primer film thickness after drying would be about 10 μm. After that, setting was performed at room temperature for 10 minutes. After that, a one-pack type acrylic melamine paint (Soflex # 1200, manufactured by Kansai Paint Co., Ltd.), which is a thermosetting paint, is applied on the primer film of the square plate
Using an air spray gun (discharge pressure 1 kg / cm 2 )
The curable coating film was applied so as to have a film thickness of 30 to 40 μm and set for 10 minutes. Then 120
The coating film was cured at 30 ° C. for 30 minutes to obtain a coated sample in which a cured coating film was formed on the surface of a square plate made of PP via a primer.
【0049】「塗装試料の塗膜除去」得られた試験片を
約3mm角のチップに粉砕し、得られたチップを窒素ガ
スをバブリングさせ溶液中の酸素濃度を表1〜3に示す
濃度とし、アルカリ濃度を表1〜3に示す濃度としたア
ルカリ水溶液中に投入した。別に、得られたチップを亜
硫酸ソーダ等の酸素吸収剤を添加、加熱し、溶存酸素の
濃度を表1〜3に示す濃度とし、アルカリ濃度を表1に
示す濃度としたアルカリ水溶液中に投入した。また別
に、80〜100℃に加熱し、溶存酸素およびアルカリ
濃度を表1〜3に示す濃度としたアルカリ水溶液中に得
られたチップを投入した。(この時、気相部の酸素濃度
を低減するために窒素圧で5気圧に加圧−常圧まで減圧
の操作を3回繰り返した。気相中の酸素濃度は5ppm
であった。)その後、表1〜3に示す温度、時間で、浸
漬し、アルカリ処理した後、室温まで冷却し、実施例1
〜12、比較例1〜5とした。浸漬し、アルカリ処理し
た後のチップは、スクリューフィーダー型研磨機(東洋
精米機(株)製、精米機を使用)中に投入し、表1に示
す条件で研磨処理を行った。別に、浸漬処理後の試料チ
ップを槽型高速攪拌機(ヘンシェルミキサーを使用)中
に投入し、試料チップ、研磨材、水を表2に示す条件に
従い添加し、表2に示す条件で研磨処理を行った。な
お、攪拌速度は、3000回/分であった。また別に、
浸漬処理後の試料チップを液体ホーニング装置(不二精
機(株)製)中に投入し、表3に示す条件で研磨処理を
行った。"Removal of coating film of coated sample" The obtained test piece was crushed into chips of about 3 mm square, and the obtained chips were bubbled with nitrogen gas to adjust the oxygen concentration in the solution to the concentration shown in Tables 1 to 3. , And was placed in an alkaline aqueous solution having an alkali concentration shown in Tables 1 to 3. Separately, an oxygen absorbent such as sodium sulfite was added to the obtained chips and heated, and the chips were put into an alkaline aqueous solution having dissolved oxygen concentrations shown in Tables 1 to 3 and alkali concentrations shown in Table 1. . Separately, the obtained chip was put into an alkaline aqueous solution which was heated to 80 to 100 ° C. and had dissolved oxygen and alkali concentrations shown in Tables 1 to 3. (At this time, in order to reduce the oxygen concentration in the gas phase part, the operation of pressurizing to 5 atm with nitrogen pressure-depressurizing to normal pressure was repeated 3 times.
Met. ) Then, after immersion in the temperature and time shown in Tables 1 to 3, alkali treatment, and then cooling to room temperature, Example 1
-12 and Comparative Examples 1-5. The chips after immersion and alkali treatment were placed in a screw feeder type polishing machine (using a rice polishing machine manufactured by Toyo Rice Milling Machine Co., Ltd.) and subjected to polishing treatment under the conditions shown in Table 1. Separately, the sample chip after the dipping treatment was put into a tank type high-speed stirrer (using a Henschel mixer), the sample chip, the abrasive, and water were added according to the conditions shown in Table 2, and the polishing treatment was performed under the conditions shown in Table 2. went. The stirring speed was 3000 times / minute. In addition,
The sample chip after the dipping treatment was put into a liquid honing device (manufactured by Fuji Seiki Co., Ltd.), and the polishing treatment was performed under the conditions shown in Table 3.
【0050】「塗膜除去効果の評価」本発明を用いて上
記のように被膜を除去し、その処理後の試料チップを自
動車用バンパに使用することを想定して下記の各種試験
を実施した。結果を表1〜3に示す。
(試験片の作製)上記処理後の試料チップを成形温度2
00℃で射出成形に供して1.6mm厚板および円板な
ど必要な試験片を作製した。
(1)引張試験(引張降伏強度、引張破断伸度)
JIS K7113に準拠し、23℃において測定し
た。
(2)高速面衝撃強度
射出成形により1.6mm厚×100mm直径の円板を
成形する。この円板を下穴直径60mmを有する台上に
設置した後、この円板を2.5m/秒の速度で25mm
(1インチ)直径の落錘にて打ち抜き、破壊エネルギー
(J,ジュール)を求める。試験機としてオリエンテッ
ク(株)製高速衝撃試験機を用いた。衝撃強度が不足す
ると、軽衝突時にバンパが破損し、車体を損傷させたり
飛散した樹脂片で二次災害を引き起こすのでこれを防止
するためには破壊エネルギーが15(J)ジュール以
上、破壊状態が延性であることが必要である。なお、破
壊状態は表中で以下の符号で示した。
5D :試験片5枚中5枚が延性破壊
4D1B:試験片5枚中4枚が延性破壊、1枚が脆性破
壊
5B :試験片5枚中5枚が脆性破壊
(自動車用バンパの作製)上記処理後の試料チップを用
いて2000トン射出成形機により樹脂温度250℃に
て図1に斜視図で示す形状のバンパを成形した。
(3)バンパ成形品の外観評価
成形したバンパの外観を目視にて観察した。また塗装後
のバンパーの経時変色性を測定した。
評価判定基準
○ バンパ表面で残存塗料などによる粗ブツの他、凹
凸、ウネリ、変形、ソリ、ひけ、艶ムラ、シルバーマー
クなど外観不良が目立たず、光沢も良好である。
× バンパ表面で外観不良が目立ったり、光沢がない。"Evaluation of effect of removing coating film" The following various tests were carried out on the assumption that the coating film was removed as described above using the present invention and the sample chip after the treatment was used for a bumper for automobiles. . The results are shown in Tables 1 to 3. (Preparation of test piece) The sample chip after the above treatment is molded at a molding temperature of 2
It was subjected to injection molding at 00 ° C. to prepare required test pieces such as a 1.6 mm thick plate and a circular plate. (1) Tensile test (tensile yield strength, tensile elongation at break) Measured at 23 ° C. in accordance with JIS K7113. (2) A high-speed surface impact strength injection molding is used to mold a disk having a thickness of 1.6 mm and a diameter of 100 mm. After placing this disc on a table having a prepared hole diameter of 60 mm, the disc was moved to 25 mm at a speed of 2.5 m / sec.
It is punched out with a falling weight having a diameter of (1 inch), and the breaking energy (J, joule) is obtained. A high-speed impact tester manufactured by Orientec Co., Ltd. was used as a tester. If the impact strength is insufficient, the bumper will be damaged at the time of a light collision, causing damage to the car body or causing a secondary disaster with scattered resin pieces. To prevent this, the breaking energy is 15 (J) joules or more, and the breaking state is It must be ductile. The broken state is shown by the following symbols in the table. 5D: 5 out of 5 test pieces were ductile fracture 4D 1B: 4 out of 5 test pieces were ductile fracture, 1 was brittle fracture 5B: 5 out of 5 test pieces were brittle fracture (manufacture of automobile bumpers) Above A bumper having the shape shown in the perspective view of FIG. 1 was molded at a resin temperature of 250 ° C. by a 2000-ton injection molding machine using the processed sample chip. (3) Appearance Evaluation of Bumper Molded Product The appearance of the molded bumper was visually observed. In addition, the discoloration property of the bumper after coating was measured. Evaluation Criteria ○ In addition to rough spots due to residual paint on the bumper surface, unevenness, swelling, deformation, warping, sink marks, uneven gloss, silver marks, etc. are not noticeable and the gloss is good. × The appearance of the bumper surface is not noticeable, and there is no gloss.
【0051】(塗装品の経時変色性の評価)上記のよう
に作製したバンパーを1,1,1−トリクロルエタン蒸
気に30秒曝して処理した後、室温下、30分間放置し
て乾燥した。次に、バンパーの1,1,1−トリクロル
エタンで処理された表面に、プライマー(#WKOホワ
イトパール;日本ペイント製)を、エアースプレーガン
を用いて、乾燥後のプライマー膜厚が約10μm程度に
なるように塗布した後、常温で10分間セッティングを
行なった。その後、バンパーのプライマー膜の上に熱硬
化性樹脂塗料である二液ウレタン塗料(NAX PPプ
ライマー 一液型;日本ペイント製)を、エアースプレ
ーガン(吐出圧1kg/cm2 )を用いて、硬化性塗膜
の膜厚が30〜40μmになるように塗布し、10分間
セッティングを行なった。次いで、180℃、30分間
で塗膜を硬化させ、PP製のパンパーの表面にプライマ
ーを介して硬化塗膜を形成した塗装試料を得た。この塗
装試料の色相をJIS Z8729−1980に準拠し
測定後、90℃のエアーオーブン中に240時間加熱処
理した後、再度色相をJIS Z8729−1980に
準拠した方法で測定した。上記測定結果より、塗装の加
熱変色性を示す△b値(加熱処理後のb値−加熱処理前
のb値)を求め、塗装の経時変色性を評価した。
(4)バンパ成形品の衝突実験
(試験方法)台車あるいは実車にバンパを取り付け、常
温および−30℃の雰囲気中で、振り子型の衝撃物(車
重相当)でバンパを打撃する。
(評価方法)
常温バンパ変形量:衝撃物によるへこみ量として60m
m未満を○、60mm以上を×とする。
−30℃耐衝撃性:破壊しないものを○、破壊するもの
を×とする。また、塗装の加熱変色性を示す△b値が
2.0以上のものを×(不可)とした。
(5)バンパ成形品の総合評価
外観評価または衝撃試験において、×が1コ以上のもの
を×(不可)とした。(Evaluation of discoloration property of coated article with time) The bumper prepared as described above was exposed to 1,1,1-trichloroethane vapor for 30 seconds, treated, and then left at room temperature for 30 minutes to dry. Next, a primer (#WKO White Pearl; made by Nippon Paint Co., Ltd.) was applied to the surface of the bumper treated with 1,1,1-trichloroethane with an air spray gun so that the primer film thickness after drying was about 10 μm. After coating, the coating was applied at room temperature for 10 minutes. After that, a two-component urethane paint (NAX PP primer one-component type; made by Nippon Paint), which is a thermosetting resin paint, is cured on the primer film of the bumper using an air spray gun (discharge pressure 1 kg / cm 2 ). The coating film was applied so that the film thickness of the functional coating film was 30 to 40 μm, and the setting was performed for 10 minutes. Then, the coating film was cured at 180 ° C. for 30 minutes to obtain a coated sample in which a cured coating film was formed on the surface of PP bumper via a primer. The hue of this coated sample was measured according to JIS Z8729-1980, and then heat-treated in an air oven at 90 ° C. for 240 hours, and then the hue was measured again by the method according to JIS Z8729-1980. From the above measurement results, the Δb value (b value after heat treatment-b value before heat treatment) showing the heat discoloration of the coating was obtained, and the color discoloration of the coating over time was evaluated. (4) Bumper molded article collision test (test method) A bumper is attached to a truck or an actual vehicle, and the bumper is hit with a pendulum type impact object (equivalent to vehicle weight) in an atmosphere of normal temperature and -30 ° C. (Evaluation method) Room temperature bumper deformation amount: 60m as the amount of dents due to impact objects
Less than m is ◯, and 60 mm or more is x. −30 ° C. impact resistance: The one that does not break is ◯, and the one that breaks is x. In addition, those having a Δb value of 2.0 or more, which indicates the heat discoloration of the coating, were rated as x (impossible). (5) Comprehensive Evaluation of Bumper Molded Product In the appearance evaluation or the impact test, a product having x of 1 or more was evaluated as x (impossible).
【0052】[0052]
【表1】 [Table 1]
【0053】[0053]
【表2】 [Table 2]
【0054】[0054]
【表3】 [Table 3]
【0055】[0055]
【発明の効果】本発明の方法によれば、取り扱い時の危
険が少なく廃水の処理が容易である低濃度アルカリ水溶
液を用いて、被膜を、剥離または剥離し易くし、さらに
基体表面を特定の方法で研磨処理することにより、樹脂
基体の被膜が充分に剥離され、しかもこの基体を着色変
化の心配なく再度工業的用途にリサイクル使用すること
ができる。According to the method of the present invention, by using a low-concentration alkaline aqueous solution which is easy to treat wastewater with less danger of handling, the coating can be peeled or easily peeled off, and the surface of the substrate can be specified. By carrying out the polishing treatment by the method, the coating film of the resin substrate is sufficiently peeled off, and the substrate can be recycled and reused for industrial use again without fear of color change.
【図1】 本発明の評価に用いたバンパの斜視図であ
る。FIG. 1 is a perspective view of a bumper used for evaluation of the present invention.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 構 宏 介 神奈川県横浜市神奈川区宝町2番地 日 産自動車株式会社内 (72)発明者 寺 田 昌 浩 神奈川県横浜市神奈川区宝町2番地 日 産自動車株式会社内 (56)参考文献 特開 平7−108532(JP,A) 特開 平7−112436(JP,A) 特開 平6−23747(JP,A) 特開 平5−228937(JP,A) (58)調査した分野(Int.Cl.7,DB名) B29B 17/00 - 17/02 C08J 11/00 - 11/28 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Kosuke 2 Takara-cho, Kanagawa-ku, Yokohama-shi, Kanagawa Nissan Motor Co., Ltd. (72) Masahiro Terada 2 Takara-cho, Kanagawa-ku, Yokohama, Kanagawa Nissan Within the automobile corporation (56) Reference JP-A-7-108532 (JP, A) JP-A-7-112436 (JP, A) JP-A-6-23747 (JP, A) JP-A-5-228937 (JP , A) (58) Fields surveyed (Int.Cl. 7 , DB name) B29B 17/00-17/02 C08J 11/00-11/28
Claims (14)
濃度が0.1wt%以上で酸素濃度が5ppm以下のア
ルカリ水溶液中で、温度110℃以上で該基体が溶融す
る温度より低い温度で加熱処理し、さらに該基体を研磨
することを特徴とする樹脂基体表面の被膜の除去方法。1. A resin substrate having a coating on its surface is heated in an alkaline aqueous solution having an alkali concentration of 0.1 wt% or more and an oxygen concentration of 5 ppm or less at a temperature of 110 ° C. or more and a temperature lower than the melting temperature of the substrate. A method for removing a coating film on a surface of a resin substrate, which comprises treating and further polishing the substrate.
濃度が0.2〜4wt%で酸素濃度が3ppm以下のア
ルカリ水溶液中で、温度140℃以上で該基体が溶融す
る温度より低い温度で加熱処理し、さらに該基体を研磨
することを特徴とする樹脂基体表面の被膜の除去方法。2. A resin substrate having a coating on its surface is heated in an alkaline aqueous solution having an alkali concentration of 0.2 to 4 wt% and an oxygen concentration of 3 ppm or less at a temperature of 140 ° C. or higher and lower than the melting temperature of the substrate. A method for removing a coating film on a surface of a resin substrate, which comprises heat treatment and polishing the substrate.
て、水溶液中の酸素濃度を減少させ、さらに不活性気体
を気相部に供給して加圧、脱圧を行い気相中の酸素濃度
を減少させてアルカリ処理する請求項1または2に記載
の樹脂基体表面の被膜の除去方法。3. An inert gas is supplied to the alkaline aqueous solution to reduce the oxygen concentration in the aqueous solution, and an inert gas is further supplied to the gas phase portion to pressurize and depressurize the oxygen in the gas phase. The method for removing a coating film on the surface of a resin substrate according to claim 1, wherein the treatment is performed with an alkali with a reduced concentration.
度を減少させた後、アルカリを加えて前記アルカリ水溶
液を調製し、さらに不活性気体を気相部に供給して加
圧、脱圧を行い気相中の酸素濃度を減少させてアルカリ
処理する請求項1または2に記載の樹脂基体表面の被膜
の除去方法。4. An inert gas is supplied to water to reduce the oxygen concentration in the water, and then an alkali is added to prepare the alkaline aqueous solution. Further, an inert gas is supplied to the gas phase part to pressurize. The method for removing a coating film on the surface of a resin substrate according to claim 1 or 2, wherein depressurization is performed to reduce the oxygen concentration in the gas phase, and the alkali treatment is performed.
熱し、水溶液中の酸素濃度を減少させ、さらに不活性気
体を気相部に供給して加圧、脱圧を行い気相中の酸素濃
度を減少させてアルカリ処理する請求項1または2に記
載の樹脂基体表面の被膜の除去方法。5. The alkaline aqueous solution is heated to 80 to 100 ° C. to reduce the oxygen concentration in the aqueous solution, and an inert gas is supplied to the vapor phase portion to pressurize and depressurize the oxygen in the vapor phase. The method for removing a coating film on the surface of a resin substrate according to claim 1, wherein the treatment is performed with an alkali with a reduced concentration.
濃度を減少させた後、アルカリを加えて前記アルカリ水
溶液を調製し、さらに不活性気体を気相部に供給して加
圧、脱圧を行い気相中の酸素濃度を減少させてアルカリ
処理する請求項1または2に記載の樹脂基体表面の被膜
の除去方法。6. The water is heated to 80 to 100 ° C. to reduce the oxygen concentration in the water, and then an alkali is added to prepare the alkaline aqueous solution. Further, an inert gas is supplied to the gas phase part to pressurize. The method for removing a coating film on the surface of a resin substrate according to claim 1 or 2, wherein depressurization is performed to reduce the oxygen concentration in the gas phase, and the alkali treatment is performed.
溶液中の酸素濃度を減少させ、さらに不活性気体を気相
部に供給して加圧、脱圧を行い気相中の酸素濃度を減少
させてアルカリ処理する請求項1または2に記載の樹脂
基体表面の被膜の除去方法。7. An oxygen absorbent is added to an alkaline aqueous solution to reduce the oxygen concentration in the aqueous solution, and an inert gas is supplied to the gas phase portion to pressurize and depressurize the oxygen concentration in the gas phase. The method for removing a coating film on the surface of a resin substrate according to claim 1 or 2, wherein the treatment is carried out by reducing the alkali.
を減少させた後、アルカリを加えて前記アルカリ水溶液
を調製し、さらに不活性気体を気相部に供給して加圧、
脱圧を行い気相中の酸素濃度を減少させてアルカリ処理
する請求項1または2に記載の樹脂基体表面の被膜の除
去方法。8. An oxygen absorbent is added to water to reduce the oxygen concentration in the water, and then an alkali is added to prepare the alkaline aqueous solution. Further, an inert gas is supplied to the gas phase part to pressurize,
The method for removing a coating film on the surface of a resin substrate according to claim 1 or 2, wherein depressurization is performed to reduce the oxygen concentration in the gas phase and alkali treatment is performed.
濃度が0.1wt%以上で酸素濃度が5ppm以下のア
ルカリ水溶液中で、温度110℃以上で該基体が溶融す
る温度より低い温度で加熱処理し、さらに該基体をスク
リューフィーダー型研磨装置中で、基体の溶融温度より
30〜110℃低い温度で研磨する請求項1または3〜
8のいずれかに記載の樹脂基体表面の被膜の除去方法。9. A resin substrate having a coating on the surface, the alkali concentration of oxygen concentration 0.1 wt% or more in the following alkaline aqueous solution 5 ppm, at a temperature lower than the temperature at which said substrate is melted at temperature of 110 ° C. or higher A heat treatment, and further polishing the substrate in a screw feeder type polishing apparatus at a temperature 30 to 110 ° C. lower than the melting temperature of the substrate.
9. The method for removing a coating film on the surface of a resin substrate according to any of 8.
リ濃度が0.2〜4wt%で酸素濃度が3ppm以下の
アルカリ水溶液中で、温度140℃以上で該基体が溶融
する温度より低い温度で加熱処理し、さらに該基体をス
クリューフィーダー型研磨装置中で、基体の溶融温度よ
り30〜110℃低い温度で研磨する請求項2〜8のい
ずれかに記載の樹脂基体表面の被膜の除去方法。10. A resin substrate having a coating on its surface is heated in an alkaline aqueous solution having an alkali concentration of 0.2 to 4 wt% and an oxygen concentration of 3 ppm or less at a temperature of 140 ° C. or higher and a temperature lower than the melting temperature of the substrate. The method for removing a coating film on the surface of a resin substrate according to any one of claims 2 to 8, wherein the substrate is heat-treated and further polished in a screw feeder type polishing apparatus at a temperature lower than the melting temperature of the substrate by 30 to 110 ° C.
リ濃度が0.1wt%以上で酸素濃度が5ppm以下の
アルカリ水溶液中で、温度110℃以上で該基体が溶融
する温度より低い温度で加熱処理し、さらに該基体を高
速槽型攪拌器タイプの研磨装置中で、温度70〜120
℃で、研磨剤と水と共に攪拌混合し、研磨することを特
徴とする請求項1または3〜8のいずれかに記載の樹脂
基体表面の被膜の除去方法。11. A resin substrate having a coating on its surface is heated in an alkaline aqueous solution having an alkali concentration of 0.1 wt% or more and an oxygen concentration of 5 ppm or less at a temperature of 110 ° C. or more and a temperature lower than the melting temperature of the substrate. And further treating the substrate in a high-speed tank-type stirrer-type polishing apparatus at a temperature of 70-120.
The method for removing a coating film on the surface of a resin substrate according to any one of claims 1 or 3 to 8, wherein the method is carried out by stirring and mixing together with an abrasive and water at ℃.
リ濃度が0.2〜4wt%で酸素濃度が3ppm以下の
アルカリ水溶液中で、温度140℃以上で該基体が溶融
する温度より低い温度で加熱処理し、さらに該基体を高
速槽型攪拌器タイプの研磨装置中で、温度70〜120
℃で、研磨剤と水と共に攪拌混合し、研磨することを特
徴とする請求項2〜8のいずれかに記載の樹脂基体表面
の被膜の除去方法。The resin substrate having a coating 12. The surface, an alkali concentration of oxygen concentration in the following alkaline aqueous solution 3ppm in 0.2~4Wt%, lower than the temperature at which said substrate melts at a temperature 1 4 0 ° C. or higher The substrate is heated at a temperature of 70 to 120 in a high-speed tank-type agitator type polishing apparatus.
The method for removing a coating film on a surface of a resin substrate according to any one of claims 2 to 8, wherein the method is carried out by stirring and mixing together with an abrasive and water at ℃.
リ濃度が0.1wt%以上で酸素濃度が5ppm以下の
アルカリ水溶液中で、温度110℃以上で該基体が溶融
する温度より低い温度で加熱処理し、さらに該基体を、
砥粒を水に分散した研磨液を用いて液体ホーニング処理
し、研磨することを特徴とする請求項1または3〜8の
いずれかに記載の樹脂基体表面の被膜の除去方法。13. A resin substrate having a coating on its surface is heated in an alkaline aqueous solution having an alkali concentration of 0.1 wt% or more and an oxygen concentration of 5 ppm or less at a temperature of 110 ° C. or more and a temperature lower than the melting temperature of the substrate. And further treating the substrate,
9. The method for removing a coating film on the surface of a resin substrate according to claim 1 or 3, wherein liquid honing treatment is performed using a polishing liquid in which abrasive grains are dispersed in water, and polishing is performed.
リ濃度が0.2〜4wt%で酸素濃度が3ppm以下の
アルカリ水溶液中で、温度140℃以上で該基体が溶融
する温度より低い温度で加熱処理し、さらに該基体を、
砥粒を水に分散した研磨液を用いて液体ホーニング処理
し、研磨することを特徴とする請求項2〜8のいずれか
に記載の樹脂基体表面の被膜の除去方法。The resin substrate having a coating 14. The surface, an alkali concentration of oxygen concentration in the following alkaline aqueous solution 3ppm in 0.2~4Wt%, lower than the temperature at which said substrate melts at a temperature 1 4 0 ° C. or higher Heat treatment at a temperature, and further, the substrate is
9. The method for removing a coating film on the surface of a resin substrate according to claim 2, wherein liquid honing treatment is performed using a polishing liquid in which abrasive grains are dispersed in water, and polishing is performed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP05776294A JP3452332B2 (en) | 1994-03-28 | 1994-03-28 | Method for removing coating on resin substrate surface |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP05776294A JP3452332B2 (en) | 1994-03-28 | 1994-03-28 | Method for removing coating on resin substrate surface |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07266337A JPH07266337A (en) | 1995-10-17 |
JP3452332B2 true JP3452332B2 (en) | 2003-09-29 |
Family
ID=13064898
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Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP05776294A Expired - Fee Related JP3452332B2 (en) | 1994-03-28 | 1994-03-28 | Method for removing coating on resin substrate surface |
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Country | Link |
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JP (1) | JP3452332B2 (en) |
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JP5083778B2 (en) * | 2009-09-02 | 2012-11-28 | 富士フイルム株式会社 | Method for recovering cellulose ester |
WO2021199895A1 (en) * | 2020-03-31 | 2021-10-07 | 三菱ケミカル株式会社 | Polyester film recovery method, recycled polyester product, recovery device, and functional layer removal agent |
CN115362201B (en) * | 2020-03-31 | 2024-04-02 | 三菱化学株式会社 | Recycling system and recycling method of polyester |
-
1994
- 1994-03-28 JP JP05776294A patent/JP3452332B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH07266337A (en) | 1995-10-17 |
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