JP5022578B2 - Modified styrene-fumaric acid copolymer, unsaturated polyester resin composition, unsaturated polyester resin molded article, and method of using waste plastic - Google Patents

Modified styrene-fumaric acid copolymer, unsaturated polyester resin composition, unsaturated polyester resin molded article, and method of using waste plastic Download PDF

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JP5022578B2
JP5022578B2 JP2005215931A JP2005215931A JP5022578B2 JP 5022578 B2 JP5022578 B2 JP 5022578B2 JP 2005215931 A JP2005215931 A JP 2005215931A JP 2005215931 A JP2005215931 A JP 2005215931A JP 5022578 B2 JP5022578 B2 JP 5022578B2
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unsaturated polyester
polyester resin
fumaric acid
acid copolymer
styrene
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毅 吉村
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Matsushita Electric Industrial Co Ltd
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    • 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
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Description

本発明は、浴室部材に代表される家庭用品又は航空機等の部材に使用される不飽和ポリエステル樹脂を含むプラスチックを再利用した変性スチレン−フマル酸共重合体、これを用いた不飽和ポリエステル樹脂組成物、不飽和ポリエステル樹脂成型品及び廃プラスチックの利用方法に関する。 The present invention relates to a modified styrene- fumaric acid copolymer that reuses a plastic containing an unsaturated polyester resin that is used for a household product represented by a bathroom member or an aircraft member, and an unsaturated polyester resin composition using the same. Product, unsaturated polyester resin molded product, and waste plastics.

プラスチックは、軽量、高強度であり、錆や腐食に強く、着色が自由、電気絶縁性に優れ、成形が容易であり、さらに大量生産が可能であるという利点を有することから、浴室部材に代表される家庭用品、自動車、航空機などの各部材として多用されている。プラスチックの使用量の増加に伴いプラスチックの廃棄量も増加する傾向にあり、環境への負荷を軽減するために、廃プラスチックをリサイクルする技術が盛んに開発されている。   Plastic is representative of bathroom materials because it has the advantages of light weight, high strength, resistance to rust and corrosion, free coloring, excellent electrical insulation, easy molding, and mass production. It is widely used as a member for household goods, automobiles, airplanes and the like. As the amount of plastic used increases, the amount of plastic discarded tends to increase. In order to reduce the burden on the environment, technologies for recycling waste plastic have been actively developed.

例えば、廃プラスチックを亜臨界水により高速で分解、油化して、廃プラスチックを大量に処理する方法が開示されている(特許文献1参照)。この方法によれば、廃プラスチックを分解して生成された低分子化した油状成分を液体燃料として回収し、回収した液体燃料を火力発電ボイラの燃料として再利用している。しかし、回収された液体燃料を火力発電ボイラの燃料として再利用しても、CO2の排出が抑制されないことから、環境への負荷を軽減することができなかった。 For example, a method of treating waste plastic in a large amount by decomposing and plasticizing waste plastic at high speed with subcritical water has been disclosed (see Patent Document 1). According to this method, a low molecular weight oily component generated by decomposing waste plastic is recovered as a liquid fuel, and the recovered liquid fuel is reused as a fuel for a thermal power generation boiler. However, even if the recovered liquid fuel is reused as the fuel for the thermal power generation boiler, the CO 2 emission is not suppressed, and the environmental load cannot be reduced.

そこで、強力な加水分解能力を有する亜臨界水を用いて、熱硬化性樹脂を含むプラスチックを加水分解する技術が提案されている。すなわち、熱硬化性樹脂を亜臨界水により加水分解して生成された熱硬化性樹脂の原料モノマを回収し、原料モノマを樹脂原料として再利用している(特許文献2参照)。この方法を用いて、多価アルコール(グリコール)と不飽和脂肪酸(フマル酸)とから形成される不飽和ポリエステル部と、不飽和ポリエステル部を架橋する架橋部とから構成される不飽和ポリエステル樹脂を処理すると、原料モノマを得ることができる。
特開平10−67991号公報 特開平10−24274号公報
Therefore, a technique for hydrolyzing a plastic containing a thermosetting resin using subcritical water having a strong hydrolytic ability has been proposed. That is, a raw material monomer of a thermosetting resin produced by hydrolyzing a thermosetting resin with subcritical water is recovered, and the raw material monomer is reused as a resin raw material (see Patent Document 2). Using this method, an unsaturated polyester resin composed of an unsaturated polyester part formed from a polyhydric alcohol (glycol) and an unsaturated fatty acid (fumaric acid) and a cross-linking part that crosslinks the unsaturated polyester part is obtained. When processed, raw material monomers can be obtained.
Japanese Patent Laid-Open No. 10-67991 Japanese Patent Laid-Open No. 10-24274

しかしながら、上述した熱硬化性樹脂を加水分解して回収しても、回収された分解物をそのまま樹脂原料として再利用すると、得られる樹脂は収縮し、さらには脆く、劣化する恐れを有していた。このため、加水分解により回収した樹脂を変性させて、樹脂原料として再利用することが望まれている。   However, even if the above-mentioned thermosetting resin is hydrolyzed and recovered, if the recovered decomposition product is reused as it is as a raw material for the resin, the resulting resin shrinks, becomes brittle, and may deteriorate. It was. For this reason, it is desired to modify the resin recovered by hydrolysis and reuse it as a resin raw material.

本発明は、上記課題を解決するためになされたものであり、すなわち、本発明の変性スチレン−フマル酸共重合体は、不飽和ポリエステル樹脂を亜臨界水により分解して得られるスチレン−フマル酸共重合体に、アルコール又はフェノール類を脱水反応させて得られたことを要旨とする。 The present invention has been made to solve the above problems, i.e., modified styrene of the present invention - fumaric acid copolymer, styrene obtained by decomposing the subcritical water unsaturated polyester resin - fumaric acid The gist is obtained by dehydrating a copolymer with alcohol or phenol.

本発明の不飽和ポリエステル樹脂組成物は、スチレン−フマル酸共重合体にアルコール又はフェノール類を脱水反応させて得られた変性スチレン−フマル酸共重合体と、スチレンと、不飽和ポリエステルと、ラジカル開始剤とを含むことを要旨とする。 Unsaturated polyester resin composition of the present invention, styrene - fumaric acid copolymer alcohols or phenols by dehydration reaction with resultant modified styrene - fumaric acid copolymer, a styrene, an unsaturated polyester, a radical The gist is to include an initiator.

本発明の不飽和ポリエステル樹脂成型品は、上記不飽和ポリエステル樹脂組成物を成型して得られたものである。   The unsaturated polyester resin molded product of the present invention is obtained by molding the unsaturated polyester resin composition.

本発明の廃プラスチックの利用方法は、不飽和ポリエステル樹脂を亜臨界水により加水分解して得られるスチレン−フマル酸共重合体に、アルコール又はフェノール類を脱水反応させて変性スチレン−フマル酸共重合体とし、得られた変性スチレン−フマル酸共重合体と、スチレンと、不飽和ポリエステルと、ラジカル開始剤とを混合した樹脂組成物を成型して樹脂成型品とすることを要旨とする。 The method of using the waste plastic of the present invention is a modified styrene- fumaric acid copolymer obtained by subjecting a styrene- fumaric acid copolymer obtained by hydrolyzing an unsaturated polyester resin with subcritical water to a dehydration reaction of alcohol or phenols. The gist is to form a resin composition by molding a resin composition in which the resulting modified styrene- fumaric acid copolymer , styrene, unsaturated polyester, and radical initiator are mixed.

本発明の変性スチレン−フマル酸共重合体によれば、廃プラスチックを低収縮剤として再利用できるため、資源を有効に活用することができる。 According to the modified styrene- fumaric acid copolymer of the present invention, the waste plastic can be reused as a low shrinkage agent, so that resources can be effectively utilized.

本発明の不飽和ポリエステル樹脂組成物によれば、低収縮率を維持することができる。   According to the unsaturated polyester resin composition of the present invention, a low shrinkage rate can be maintained.

本発明の不飽和ポリエステル樹脂成型品によれば、寸法精度を高めることができる。   According to the unsaturated polyester resin molded product of the present invention, the dimensional accuracy can be increased.

本発明の廃プラスチックの利用方法によれば、廃プラスチックを再利用して、低収縮性の樹脂成型品を得ることができる。   According to the method for using waste plastic of the present invention, a resin molded product having low shrinkage can be obtained by reusing waste plastic.

以下、本発明の実施の形態に係る変性スチレン−フマル酸共重合体、これを用いた不飽和ポリエステル樹脂組成物、不飽和ポリエステル樹脂成型品及び廃プラスチックの利用方法を説明する。 Hereinafter, a modified styrene- fumaric acid copolymer according to an embodiment of the present invention, an unsaturated polyester resin composition using the same, an unsaturated polyester resin molded product, and a method of using waste plastic will be described.

本発明の実施の形態に係る変性スチレン−フマル酸共重合体は、以下のようにして得ることができる。 The modified styrene- fumaric acid copolymer according to the embodiment of the present invention can be obtained as follows.

まず、不飽和ポリエステル部とその架橋部からなる不飽和ポリエステル樹脂を含むプラスチックを、不飽和ポリエステル樹脂が熱分解される温度未満とした亜臨界水(280℃未満、7MPa以下)を用いて加水分解する。すると、グリコール水溶液が得られる。   First, a plastic containing an unsaturated polyester resin composed of an unsaturated polyester portion and a cross-linked portion thereof is hydrolyzed using subcritical water (below 280 ° C., 7 MPa or less) that is below the temperature at which the unsaturated polyester resin is thermally decomposed. To do. Then, an aqueous glycol solution is obtained.

グリコール水溶液中には、不飽和ポリエステル樹脂の原料モノマである多価アルコール(グリコール)及び有機酸(フマル酸)と、不飽和ポリエステル樹脂中の架橋部と有機酸の化合物(スチレンとフマル酸の共重合体)と、が少なくとも含まれる。スチレン−フマル酸共重合体は、化1に示す構造を有し、親水基と疎水基を併せ持ち、界面活性剤のような性質を有する。

Figure 0005022578
During glycol solution, a polyhydric alcohol which is a raw material monomer of the unsaturated polyester resin (glycol) and organic acids (fumaric acid), compounds of the bridge and an organic acid unsaturated polyester resin (scan styrene and fumaric acid Copolymer). The styrene-fumaric acid copolymer has the structure shown in Chemical Formula 1, has both a hydrophilic group and a hydrophobic group, and has properties such as a surfactant.
Figure 0005022578

上記加水分解の具体的方法としては、例えば、不飽和ポリエステル樹脂を含むプラスチックと、純水と、水酸化カリウムとを反応管に仕込み、反応管の内部を希ガスにより置換封入する。反応管を恒温槽(約230℃)に浸漬した後、亜臨界水により4時間加水分解をする。加水分解後の内容物を濾過、分離した後、さらに酸(例えば、塩酸、硫酸など)を加えて、スチレンとフマル酸の共重合体を回収する。 As a specific method of the hydrolysis, for example, a plastic containing an unsaturated polyester resin, pure water, and potassium hydroxide are charged into a reaction tube, and the inside of the reaction tube is replaced and sealed with a rare gas. After immersing the reaction tube in a thermostatic chamber (about 230 ° C), it is hydrolyzed with subcritical water for 4 hours. After filtering and separating the hydrolyzed contents, an acid (for example, hydrochloric acid, sulfuric acid, etc.) is further added to recover a copolymer of styrene and fumaric acid .

さらに、回収されたスチレン−フマル酸共重合体と、アルコール又はフェノール類とを脱水反応させて、変性スチレン−フマル酸共重合体とする。ここで用いるアルコールとしては、一価アルコール又は多価アルコールを挙げることができ、例えば、一価アルコールとしては、メチルアルコール、エチルアルコール、プロピルアルコール、ブチルアルコールなどが好ましく、多価アルコールとしては、エチレングリコール、ジエチレングリコール、プロピレングリコール、ジプロピレングリコールなどのグリコール類が好ましい。また、フェノール類としては、例えば、フェノール、サリチル酸、ナフトール、カテコール、レジルシノール、ヒドロキノンなどが好ましい。 Further, the recovered styrene- fumaric acid copolymer is subjected to a dehydration reaction with alcohol or phenol to obtain a modified styrene- fumaric acid copolymer . Examples of the alcohol used herein include monohydric alcohols and polyhydric alcohols. For example, monohydric alcohols are preferably methyl alcohol, ethyl alcohol, propyl alcohol, butyl alcohol, etc., and polyhydric alcohols are ethylene. Glycols such as glycol, diethylene glycol, propylene glycol and dipropylene glycol are preferred. Further, as the phenols, for example, phenol, salicylic acid, naphthol, catechol, resilcinol, hydroquinone and the like are preferable.

得られた変性スチレン−フマル酸共重合体は、樹脂中に配合させて、低収縮剤として再利用される。 The obtained modified styrene- fumaric acid copolymer is mixed in the resin and reused as a low shrinkage agent.

以下、さらに具体的に実施例を用いて説明する。なお、実施例を説明する前に基準例を説明する。   Hereinafter, more specific description will be given using examples. Prior to describing the examples, a reference example will be described.

基準例
グリコールとしてプロピレングリコール、有機酸として無水マレイン酸を用いて、両者を等モル量として縮重合して、重量平均分子量4000〜5000の不飽和ポリエステル樹脂とした。この不飽和ポリエステル樹脂のワニス(溶媒なし)に、スチレンとラジカル開始剤としてメチルエチルケトンパーオキサイドと無機フィラーとして炭酸カルシウムを不飽和ポリエステル樹脂1に対して1:0.02:2の重量比で配合し、更に組成物全量に対し、10重量%になる様に低収縮材としてポリスチレンを添加し、硬化させて硬化物とした。
Reference Example Using propylene glycol as the glycol and maleic anhydride as the organic acid, both were subjected to polycondensation in equimolar amounts to obtain an unsaturated polyester resin having a weight average molecular weight of 4000 to 5000. This unsaturated polyester resin varnish (without solvent) is blended with styrene, methyl ethyl ketone peroxide as radical initiator and calcium carbonate as inorganic filler in a weight ratio of 1: 0.02: 2 to unsaturated polyester resin 1, and further Polystyrene was added as a low shrinkage material so as to be 10% by weight with respect to the total amount of the composition, and cured to obtain a cured product.

実施例1
まず、上記基準例の硬化物3g、純水15g、水酸化カリウム0.84g、を反応管に仕込み、反応管の内部をアルゴンガスで置換封入した。この反応管を230℃の恒温槽に浸漬し、水を亜臨界状態にして4時間加水分解を行った。その後、反応管内部の内容物を濾過、分離し、さらに塩酸を加えてスチレン−フマル酸共重合体を回収した。
Example 1
First, 3 g of the cured product of the above reference example, 15 g of pure water, and 0.84 g of potassium hydroxide were charged into a reaction tube, and the inside of the reaction tube was replaced with argon gas. This reaction tube was immersed in a thermostatic bath at 230 ° C., and water was hydrolyzed for 4 hours in a subcritical state. Thereafter, the contents inside the reaction tube were filtered and separated, and hydrochloric acid was further added to recover a styrene- fumaric acid copolymer .

上記の作業を繰り返して、得られたスチレン−フマル酸共重合体50gをメタノール100gに溶解して15分間攪拌した。その後、環流条件下で18時間反応させた後、蒸留水100gを加えて、変性樹脂を析出させた。これを低収縮剤とした。 The above operation was repeated, and 50 g of the obtained styrene- fumaric acid copolymer was dissolved in 100 g of methanol and stirred for 15 minutes. Thereafter, the mixture was reacted for 18 hours under reflux conditions, and then 100 g of distilled water was added to precipitate the modified resin. This was a low shrinkage agent.

次に、基準例で用いた不飽和ポリエステル樹脂のワニスにスチレンをほぼ当量混合し、炭酸カルシウムを添加して得られたワニス/スチレン/炭酸カルシウム配合系を用い、この配合系に対して、上記変性樹脂が10重量部となるように配合した後、硬化させて硬化物とした。   Next, the varnish of the unsaturated polyester resin used in the reference example was mixed in an approximately equivalent amount with styrene, and a varnish / styrene / calcium carbonate blending system obtained by adding calcium carbonate was used. The modified resin was blended so as to be 10 parts by weight and then cured to obtain a cured product.

比較例
まず、上記基準例の硬化物3g、純水15g、水酸化カリウム0.84g、を反応管に仕込み、反応管の内部をアルゴンガスで置換封入した。この反応管を230℃の恒温槽に浸漬し、水を亜臨界状態にして4時間分解反応を行った。その後、反応管内部の内容物を濾過、分離し、さらに塩酸を加えてスチレン−フマル酸共重合体を回収した。
Comparative Example First, 3 g of the cured product of the above reference example, 15 g of pure water, and 0.84 g of potassium hydroxide were charged into a reaction tube, and the inside of the reaction tube was replaced with argon gas. This reaction tube was immersed in a constant temperature bath at 230 ° C., and the decomposition reaction was carried out for 4 hours with water in a subcritical state. Thereafter, the contents inside the reaction tube were filtered and separated, and hydrochloric acid was further added to recover a styrene- fumaric acid copolymer .

上記の操作を繰り返して、得られたスチレン−フマル酸共重合体を低収縮剤とした。 By repeating the above operation, the resulting styrene- fumaric acid copolymer was used as a low shrinkage agent.

次に、基準例で用いた不飽和ポリエステル樹脂のワニスにスチレンをほぼ当量混合し、炭酸カルシウムを添加して得られたワニス/スチレン/炭酸カルシウム配合系を用い、この配合系に対して、上記スチレン−フマル酸共重合体が10重量部となるように配合した後、硬化させて硬化物とした。 Next, the varnish of the unsaturated polyester resin used in the reference example was mixed in an approximately equivalent amount with styrene, and a varnish / styrene / calcium carbonate blending system obtained by adding calcium carbonate was used. After blending so that the styrene- fumaric acid copolymer would be 10 parts by weight, it was cured to obtain a cured product.

上記実施例、比較例及び基準例から得られた各硬化物について、以下の測定方法を用いて、反応率、収縮率、曲げ弾性率、曲げ強度、アイゾット衝撃値をそれぞれ測定し、硬化物の物性を評価した。   For each cured product obtained from the above Examples, Comparative Examples, and Reference Examples, the following measurement methods were used to measure the reaction rate, shrinkage rate, flexural modulus, bending strength, and Izod impact value. Physical properties were evaluated.

反応率は、熱水環流抽出により回収される未反応量から算出した。   The reaction rate was calculated from the amount of unreacted recovered by hot water reflux extraction.

収縮率は、100mm角の型に配合樹脂を流し込み、硬化させた後の寸法変化から算出した。   The shrinkage was calculated from the dimensional change after the compounded resin was poured into a 100 mm square mold and cured.

曲げ強さと曲げ弾性率は、JIS-K7017に準じた。具体的には、試験片中央の圧子の変異に伴う強力を計測し、変異と強力の直線関係が成り立つ弾性率を求めて、降伏点での強力から曲げ強さを求めた。なお、ここで使用した試験片の寸法は、厚さ2 mm、巾12 mm、長さ80mmとし、支点間距離を50mmとし、試験速度を2mm/minとした。   The bending strength and flexural modulus were in accordance with JIS-K7017. Specifically, the strength associated with the variation of the indenter at the center of the test piece was measured, the elastic modulus at which the linear relationship between the variation and the strength was established was determined, and the bending strength was determined from the strength at the yield point. The dimensions of the test piece used here were a thickness of 2 mm, a width of 12 mm, a length of 80 mm, a fulcrum distance of 50 mm, and a test speed of 2 mm / min.

アイゾット衝撃試験は、JIS-K7062に準じた。具体的には、試験片の片側を固定した後、ハンマーで打撃して破断に要したエネルギから衝撃性を評価した。なお、ここで使用した試験片の寸法は、厚さ2 mm、巾12 mm、長さ80mmとした。   The Izod impact test conformed to JIS-K7062. Specifically, after fixing one side of the test piece, the impact property was evaluated from the energy required for breaking by hitting with a hammer. The dimensions of the test piece used here were 2 mm thick, 12 mm wide, and 80 mm long.

得られた結果を表1に示す。

Figure 0005022578
The obtained results are shown in Table 1.
Figure 0005022578

表1に示す結果から、アルコール又はフェノール類によって脱水反応をしないスチレン−フマル酸共重合体を低収縮剤として用いた比較例は、外観観察をすると、硬化物の表面に多数のダマが見受けられ、さらに、収縮率が4%と高く、樹脂を硬化させる時に収縮してしまうことから、得られた樹脂の特性が低下することが判明した。これに対して、実施例の硬化物の表面には、ダマも無く、収縮率をはじめ、曲げ弾性率、曲げ強度、アイゾット衝撃値も基準例と何ら遜色のない硬化物が得られることが確認された。 From the results shown in Table 1, in the comparative example using a styrene- fumaric acid copolymer that does not undergo a dehydration reaction with alcohol or phenols as a low shrinkage agent, a number of lumps are found on the surface of the cured product when the appearance is observed. Furthermore, the shrinkage rate was as high as 4%, and it was found that the properties of the obtained resin deteriorated because it shrinks when the resin is cured. On the other hand, on the surface of the cured product of the example, it was confirmed that a cured product having no lumps, a shrinkage rate, a bending elastic modulus, a bending strength, and an Izod impact value, which is comparable to the reference example, can be obtained. It was done.

以上説明したように、本発明の実施の形態によれば、不飽和ポリエステル樹脂を含む廃プラスチックを亜臨界水により加水分解して得られたスチレン−フマル酸共重合体をアルコール又はフェノール類により脱水反応させた上で、低収縮剤として利用することにより、廃プラスチックを再利用することができ、さらに得られる樹脂の低収縮性を維持できることが判明した。 As described above, according to the embodiment of the present invention, the styrene- fumaric acid copolymer obtained by hydrolyzing the waste plastic containing the unsaturated polyester resin with subcritical water is dehydrated with alcohol or phenols. It was found that waste plastic can be reused by using it as a low shrinkage agent after reaction, and the low shrinkage of the resulting resin can be maintained.

Claims (4)

不飽和ポリエステル樹脂を亜臨界水により加水分解して得られるスチレン−フマル酸共重合体に、アルコール又はフェノール類を脱水反応させて得られたことを特徴とする変性スチレン−フマル酸共重合体A modified styrene- fumaric acid copolymer obtained by subjecting a styrene- fumaric acid copolymer obtained by hydrolyzing an unsaturated polyester resin with subcritical water to a dehydration reaction of alcohol or phenol. スチレン−フマル酸共重合体にアルコール又はフェノール類を脱水反応させて得られた変性スチレン−フマル酸共重合体と、スチレンと、不飽和ポリエステルと、ラジカル開始剤とを含むことを特徴とする不飽和ポリエステル樹脂組成物。 A modified styrene- fumaric acid copolymer obtained by dehydrating a styrene- fumaric acid copolymer with alcohol or phenol, styrene, an unsaturated polyester, and a radical initiator. Saturated polyester resin composition. 請求項2に記載の不飽和ポリエステル樹脂組成物を成型して得られた不飽和ポリエステル樹脂成型品。   An unsaturated polyester resin molded product obtained by molding the unsaturated polyester resin composition according to claim 2. 不飽和ポリエステル樹脂を亜臨界水により加水分解して得られるスチレン−フマル酸共重合体に、アルコール又はフェノール類を脱水反応させて変性スチレン−フマル酸共重合体とし、
得られた前記変性スチレン−フマル酸共重合体と、スチレンと、不飽和ポリエステルと、ラジカル開始剤とを混合した樹脂組成物を成型して樹脂成型品とすることを特徴とする廃プラスチックの利用方法。
A styrene- fumaric acid copolymer obtained by hydrolyzing an unsaturated polyester resin with subcritical water is subjected to a dehydration reaction of alcohol or phenol to obtain a modified styrene- fumaric acid copolymer ,
Use of a waste plastic characterized by molding a resin composition obtained by mixing the resulting modified styrene- fumaric acid copolymer , styrene, unsaturated polyester, and radical initiator into a resin molded product Method.
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