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JP4770182B2 - Disassembly method of artificial marble - Google Patents
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JP4770182B2 - Disassembly method of artificial marble - Google Patents

Disassembly method of artificial marble Download PDF

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JP4770182B2
JP4770182B2 JP2005016887A JP2005016887A JP4770182B2 JP 4770182 B2 JP4770182 B2 JP 4770182B2 JP 2005016887 A JP2005016887 A JP 2005016887A JP 2005016887 A JP2005016887 A JP 2005016887A JP 4770182 B2 JP4770182 B2 JP 4770182B2
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artificial marble
resin
thermosetting resin
inorganic filler
water
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JP2006206638A (en
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清史 守田
尚治 中川
豊之 卜部
哲也 前川
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Panasonic Corp
Panasonic Electric Works Co Ltd
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Panasonic Corp
Matsushita Electric Works 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
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

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Description

本発明は、浴室用材やキッチンのカウンター材、家具材、内装材、外装材をはじめとする建材等として利用されている人造大理石、特に廃棄物の人造大理石から有価物を回収するための分解方法に関するものである。   The present invention relates to an artificial marble used as a building material including bathroom materials, kitchen counter materials, furniture materials, interior materials, exterior materials, and the like, and in particular, a decomposition method for recovering valuable materials from waste artificial marble. It is about.

従来、人造大理石を含むプラスチック廃棄物はその殆どが埋立処分あるいは焼却処理されており、資源として有効活用されていない。また埋立処分では埋立用地の確保の困難や埋立後の地盤の不安定化という問題があり、焼却処理では炉の損傷、有害ガスや悪臭の発生、CO排出といった問題がある。このため、2001年4月施行の資源有効利用促進法で、プラスチック、人造大理石を多く使用している浴室ユニット、システムキッチンを特定再利用促進製品に指定するなど、各種リサイクル法の施行に伴って人造大理石を含むプラスチック製品の回収リサイクルへの流れは加速する傾向にある。 Conventionally, most plastic waste containing artificial marble has been landfilled or incinerated, and has not been effectively utilized as a resource. In addition, landfill disposal has problems such as difficulty in securing a landfill site and instability of the ground after landfilling, and incineration treatment has problems such as furnace damage, generation of harmful gases and odors, and CO 2 emissions. For this reason, in accordance with the Law for Promotion of Effective Utilization of Resources in April 2001, various recycling laws such as bathroom units that use a lot of plastic and artificial marble, and system kitchens are designated as specific reuse promotion products. The trend toward collection and recycling of plastic products including artificial marble tends to accelerate.

これらの状況に合わせて、近年、プラスチック廃棄物を再資源化することが試みられており、その一つとして、超臨界水を反応媒体とする反応により、プラスチック廃棄物を分解油化し、有用な油状物を回収する方法が提案されており、また、各種構造材料に使用される繊維強化プラスチックについては、超臨界水又は亜臨界水を用いて樹脂成分を分解し、ガラス繊維や炭素繊維等の繊維を回収し、再利用する方法が提案されている(例えば、特許文献1−5参照)。   In recent years, attempts have been made to recycle plastic waste in accordance with these situations, and as one of them, plastic waste is decomposed into oil by a reaction using supercritical water as a reaction medium. Methods for recovering oily substances have been proposed, and for fiber reinforced plastics used in various structural materials, resin components are decomposed using supercritical water or subcritical water, and glass fibers, carbon fibers, etc. A method of collecting and reusing fibers has been proposed (see, for example, Patent Documents 1-5).

これらの方法では、加水分解を受けやすいエステル結合を多く含むポリエステル樹脂のような樹脂であるならば原料となるモノマー成分を回収できる。しかし、ビニルエステル樹脂に代表される人造大理石の熱硬化性樹脂の場合、エステル結合が非常に少なく、樹脂成分はランダムに熱分解により低分子化し、多種成分からなる油状成分となり、これを主に液体燃料として再利用することになる。このため、ゼオライトに代表される触媒を用いて油質の改質を行なうことなどの後処理が必要となってコスト高になり、また改質した生成油においても灯油や軽油などの石油製品そのものにすることは困難であるので、実用化には至っていない。   In these methods, a monomer component as a raw material can be recovered if the resin is a resin such as a polyester resin that contains many ester bonds that are susceptible to hydrolysis. However, in the case of artificial marble thermosetting resins represented by vinyl ester resins, there are very few ester bonds, and the resin component is randomly reduced in molecular weight by thermal decomposition to become an oily component consisting of various components. It will be reused as liquid fuel. For this reason, post-treatment such as reforming oil quality using a catalyst typified by zeolite is required, resulting in high costs, and even in the reformed product oil, petroleum products such as kerosene and light oil itself Since it is difficult to achieve this, it has not been put into practical use.

石油資源の枯渇、二酸化炭素による地球温暖化といった地球環境全体の問題に鑑みると、熱硬化性樹脂を含有する人造大理石の分解及び再利用の抜本的な対策が必要であるというのが現状である。
特開平10−237215号公報 特開平8−85736号公報 特開2000−53801号公報 特開2000−61423号公報 特開2001−170603号公報
Considering the problems of the entire global environment such as the depletion of petroleum resources and global warming due to carbon dioxide, it is necessary to take drastic measures to disassemble and reuse artificial marble containing thermosetting resins. .
JP-A-10-237215 JP-A-8-85736 JP 2000-53801 A JP 2000-61423 A JP 2001-170603 A

本発明は、上記のとおりの背景から、従来の技術の問題点を解消し、人造大理石を、無機充填剤、熱硬化性樹脂ともに、人造大理石の原料として再利用できるように分解することができる、新しい人造大理石の分解方法を提供することを課題としている。   The present invention eliminates the problems of the prior art from the background described above, and can decompose artificial marble so that both inorganic fillers and thermosetting resins can be reused as raw materials for artificial marble. Therefore, it is an object to provide a new method for decomposing artificial marble.

本発明の人造大理石の分解方法は、上記の課題を解決するものとして、以下のことを特徴としている。   The method for decomposing artificial marble of the present invention is characterized by the following as a solution to the above problems.

第1:無機充填剤と熱硬化性樹脂を主として含有し、前記無機充填剤が水酸化アルミニウムであり前記熱硬化性樹脂がビニルエステル樹脂であるビニルエステル系人造大理石を、180℃〜280℃の温度範囲の亜臨界水で処理し、この亜臨界水処理物を固液分離することにより前記熱硬化性樹脂由来の高分子の有価物を含む水可溶成分と、前記無機充填剤由来のべーマイトを含む固形残渣とを回収し、原料として再利用可能な有価物を得る。 First: containing mainly an inorganic filler and a thermosetting resin, the inorganic filler is aluminum hydroxide vinyl ester artificial marble wherein the thermosetting resin is a vinyl ester resin, of 180 ° C. ~ 280 ° C. It is treated with subcritical water in the temperature range, and this subcritical water treated product is subjected to solid-liquid separation to thereby separate a water-soluble component containing a valuable polymer material derived from the thermosetting resin and a material derived from the inorganic filler. -Collect solid residue containing mitite to obtain valuable materials that can be reused as raw materials.

第2亜臨界水にアルカリを共存させる。 Second : Alkaline coexists in subcritical water .

第3:共存させるアルカリが第1A族(アルカリ金属)、第2A族(アルカリ土類金属)、および塩基性リン酸塩のうちの少くともいずれかである。 Third : The coexisting alkali is at least one of Group 1A (alkali metal), Group 2A (alkaline earth metal), and basic phosphate.

上記のとおりの第1の発明によれば、簡便、かつ効率的に人造大理石を、無機充填剤、熱硬化性樹脂ともに、人造大理石の原料として再利用できるように分解することが可能とされる。亜臨界水の温度を180℃〜280℃の範囲とすることで、熱硬化性樹脂由来の有価物をより選択的に回収することができる。またベーマイトを回収することができる。そして亜臨界水とすることで、取扱い、回収、コスト等の点において優れた分解方法が実現される。 According to the first invention as described above, simple and convenient, and efficient artificial marble, the inorganic filler, both thermosetting resin, is it possible to decompose for reuse as terrazzo material The By setting the temperature of the subcritical water in the range of 180 ° C. to 280 ° C., valuable materials derived from the thermosetting resin can be collected more selectively. Boehmite can be recovered. By using subcritical water, an excellent decomposition method is realized in terms of handling, recovery, cost, and the like.

ルカリを添加する第2の発明によれば加水分解反応が促進されて樹脂溶解率が向上し、より効率的な分解が可能とされ、アルカリとして第3の発明のようにアルカリ金属、アルカリ土類金属もしくは塩基性リン酸塩を用いることで、この効率はより高められることになる According to a second aspect of the invention for adding A alkali hydrolysis reaction is promoted to improve the resin dissolution rate, it is to enable more efficient decomposition, alkali metals, alkaline earth as in the third invention as an alkali This efficiency can be further increased by using a similar metal or basic phosphate .

本発明は上記のとおりの特徴をもつものであるが、以下にその実施の形態を説明する。   The present invention has the features as described above, and an embodiment thereof will be described below.

本発明において分解の対象として用いる人造大理石は、その組成が主として無機充填剤と熱硬化性樹脂からなり、このような人造大理石としては、無機充填剤として水酸化アルミニウム、熱硬化性樹脂としてエポキシアクリレート系樹脂(ビニルエステル樹脂とも呼ばれている)を用いているビニルエステル系人造大理石を挙げることができる。 Artificial marble used as a decomposition of the target in the present invention, the composed composition mainly inorganic filler and a thermosetting resin, as such artificial marble, aluminum hydroxide as a non-machine filler, an epoxy thermosetting resin A vinyl ester artificial marble using an acrylate resin (also called a vinyl ester resin) can be given.

そして、本発明では、このような人造大理石(主に廃棄物)に水や有機溶媒等を加え、温度及び圧力を上昇させて、亜臨界状態下で、熱硬化性樹脂を溶解させて有価物を分離・回収すると同時に、無機充填剤由来の有価物は固形分残渣として分離・回収する。人造大理石と水や有機溶媒等の亜臨界状態となる溶媒の比率は特に制限されるものではないが、人造大理石100質量部に対して100〜500質量部の範囲に設定するのが好ましい。   And in this invention, water, an organic solvent, etc. are added to such artificial marble (mainly waste), temperature and pressure are raised, a thermosetting resin is dissolved under a subcritical state, and valuable resources are obtained. At the same time, the valuable material derived from the inorganic filler is separated and collected as a solid residue. The ratio of the artificial marble and the solvent that becomes a subcritical state such as water or an organic solvent is not particularly limited, but is preferably set in the range of 100 to 500 parts by mass with respect to 100 parts by mass of the artificial marble.

一般に亜臨界流体による熱硬化性樹脂の分解は、熱分解反応及び加水分解反応によって起こると考えられる。つまり、熱硬化性樹脂としてエポキシアクリレート系樹脂(ビニルエステル系樹脂)を用いている人造大理石においても同様であるが、亜臨界流体を接触させた場合には、エステル結合部分の加水分解反応がまず起こり、これが引き金となって熱分解反応が起こりやすくなり、モノマー或いは更に分解された化合物となり、これらを分離・回収することで、有価物を得ることができる。これと同時に、固形残渣として残った無機充填剤由来の有価物も得ることができるものである。 Generally, it is considered that the thermosetting resin is decomposed by the subcritical fluid by a thermal decomposition reaction and a hydrolysis reaction. That is the same also in the artificial marble and a thermosetting resin is used et Po carboxymethyl acrylate resin (vinyl ester resin), when contacted with subcritical fluids, the ester bond portion of the hydrolysis reaction First, this triggers a thermal decomposition reaction, which becomes a monomer or a further decomposed compound, and valuable materials can be obtained by separating and recovering them. At the same time, valuable materials derived from inorganic fillers remaining as solid residues can be obtained.

分解反応の温度は180〜370℃の範囲に設定するのが好ましい。温度が180℃未満であると分解に多大な時間がかかり、処理コストが高くなる恐れがある。また、180〜280℃の範囲では熱硬化性樹脂の過度な熱分解反応が抑制されることにより熱硬化性樹脂製造原料として再利用が容易に可能な高分子の有価物が主に回収される。280〜370℃の範囲では、熱硬化性樹脂が溶解しやすく、無機充填剤と熱硬化性樹脂の分離ができ、無機充填剤の再利用に有効である。370℃を超えると熱硬化性樹脂の過度な熱分解が起こりやすく、熱硬化性樹脂由来の有価物の回収量が減少する。   The temperature of the decomposition reaction is preferably set in the range of 180 to 370 ° C. If the temperature is lower than 180 ° C., it takes a long time for decomposition, which may increase the processing cost. Also, in the range of 180 to 280 ° C., polymer valuables that can be easily reused as a thermosetting resin production raw material are mainly recovered by suppressing excessive thermal decomposition reaction of the thermosetting resin. . In the range of 280 to 370 ° C., the thermosetting resin is easily dissolved, and the inorganic filler and the thermosetting resin can be separated, which is effective for reuse of the inorganic filler. When it exceeds 370 ° C., excessive thermal decomposition of the thermosetting resin tends to occur, and the recovery amount of valuable materials derived from the thermosetting resin decreases.

分解のための溶媒としては、水やアルコール、エーテル等の有機溶媒、CO、そしてそれらの混合物が適宜に用いられるが、その取扱い、回収、そしてコスト等の点において水を用いることがより好ましい。 As a solvent for decomposition, water, an organic solvent such as alcohol and ether, CO 2 , and a mixture thereof are appropriately used, but it is more preferable to use water in terms of handling, recovery, cost, and the like. .

さらにまた、亜臨界流体にアルカリを共存させることにより、加水分解反応が促進されて樹脂溶解率を向上させることができる。ここで、アルカリの添加量は特に限定されるものではないが、人造大理石100質量部に対して0.01〜50質量部の範囲が好ましい。また、添加するアルカリの種類は第1A族(アルカリ金属)、第2A族(アルカリ土類金属)、塩基性リン酸塩のうちの1種以上のアルカリが好適なものとして考慮される。なかでも、KOHやNaOHが望ましい。   Furthermore, by allowing alkali to coexist in the subcritical fluid, the hydrolysis reaction is promoted and the resin dissolution rate can be improved. Here, although the addition amount of an alkali is not specifically limited, The range of 0.01-50 mass parts is preferable with respect to 100 mass parts of artificial marble. Moreover, the kind of alkali to add is considered that the 1 or more types of alkali of 1A group (alkali metal), 2A group (alkaline earth metal), and basic phosphate is suitable. Of these, KOH and NaOH are desirable.

また、分解反応の時間は、反応温度などの条件によって異なるが、0.1〜10時間が望ましい。反応時間が短い方が処理コストは少なくなるのでより好ましい。分解反応の際の圧力については、特に限定されるものではないが、2〜17Mpa程度の範囲に設定するのが好ましい。   The time for the decomposition reaction varies depending on the reaction temperature and other conditions, but is preferably 0.1 to 10 hours. A shorter reaction time is more preferable because the processing cost is reduced. The pressure during the decomposition reaction is not particularly limited, but is preferably set in the range of about 2 to 17 MPa.

そこで以下に実施例を示し、さらに詳しく説明する。もちろん以下の例によって発明が限定されることはない。   Therefore, an example will be shown below and will be described in more detail. Of course, the invention is not limited by the following examples.

(実施例1)
ビニルエステル系人造大理石は、熱硬化性樹脂としてビニルエステル樹脂(ジャパンコンポジット社製)を、無機充填として水酸化アルミニウム(住友化学社製)を用いて作製した。
Example 1
Vinyl ester artificial marble, vinyl ester resin (manufactured by Japan Composite Co., Ltd.) as the thermosetting resin, produced by using aluminum hydroxide as an inorganic filler (manufactured by Sumitomo Chemical Co., Ltd.).

ビニルエステル系人造大理石粉砕物(3mmメッシュ)を3.8g、純水15.2gを計量し反応管に密閉した。これを230℃の恒温槽に浸漬し、反応管内を亜臨界状態にして、4時間浸漬したまま放置し、人造大理石の分解処理を4時間行なった。この後、反応管を恒温槽から取り出して、冷却槽に浸漬し、急冷して室温まで戻した。   3.8 g of vinyl ester-based artificial marble ground (3 mm mesh) and 15.2 g of pure water were weighed and sealed in a reaction tube. This was immersed in a constant temperature bath at 230 ° C., the inside of the reaction tube was placed in a subcritical state, left standing for 4 hours, and the artificial marble was decomposed for 4 hours. Thereafter, the reaction tube was taken out from the thermostatic bath, immersed in a cooling bath, rapidly cooled to room temperature.

分解処理後の反応管の内容物は、水可溶成分と固形残渣であり、この内容物をろ過することにより固形分を分離して反応管から回収した。この固形残渣から人造大理石に含まれる樹脂成分の溶解率を算出した。この樹脂成分の溶解率は以下の式で算出した。   The content of the reaction tube after the decomposition treatment was a water-soluble component and a solid residue, and the content was filtered to separate the solid content and collect it from the reaction tube. The dissolution rate of the resin component contained in the artificial marble was calculated from the solid residue. The dissolution rate of this resin component was calculated by the following formula.

樹脂成分溶解率(%)=〔処理前含有樹脂量(g)−固形残渣中含有樹脂量(g)〕/処理前含有樹脂量(g)×100
また、水可溶成分はGC−MSにより定性分析を行なった。得られた結果は表1に示した。
参考例1
アクリル系人造大理石は、熱硬化性樹脂として熱硬化性のアクリル樹脂を、無機充填材として溶融シリカを用いている、アクリルシロップ(ルーサイトジャパン社製)を用いて作製した。
Resin component dissolution rate (%) = [Amount of resin contained before treatment (g) −Amount of resin contained in solid residue (g)] / Amount of resin contained before treatment (g) × 100
The water-soluble component was qualitatively analyzed by GC-MS. The results obtained are shown in Table 1.
( Reference Example 1 )
The acrylic artificial marble was produced using acrylic syrup (manufactured by Lucite Japan) using thermosetting acrylic resin as the thermosetting resin and fused silica as the inorganic filler.

この後、用いた人造大理石をアクリル系人造大理石とした他は、実施例1と同様にして分解処理を行なうとともに、樹脂溶解率を算出し、定性分析を行なった。
(実施例
実施例1の純水を1N KOHにした他は、実施例1と同様にして分解処理を行なうとともに、樹脂溶解率を算出し、定性分析を行なった。
(実施例
実施例1の純水を1N NaOHとした他は、実施例1と同様にして分解処理を行うとともに、樹脂溶解率を算出し、定性分析を行なった。
参考例2
参考例1の純水を1N KOHとした他は、参考例1と同様にして分解処理を行なうとともに、樹脂溶解率を算出した。
参考例3
参考例1の純水を1N NaOHとした他は、参考例1と同様にして分解処理を行なうとともに、樹脂溶解率を算出した。
(実施例
実施例1のビニルエステル系人造大理石粉砕物(3mmメッシュ)仕込み量を2.88g、純水仕込み量を11.6g、温度を350℃、分解処理時間を2時間とした他は、実施例1と同様にして分解処理を行なうとともに、樹脂溶解率を算出した。
参考例4
参考例1のアクリル系人造大理石粉砕物(3mmメッシュ)仕込み量を2.88g、純水仕込み量を11.5g、温度を350℃、分解処理時間を2時間とした他は、参考例1と同様にして分解処理を行なうとともに、樹脂溶解率を算出した。
(実施例
実施例の純水を1N KOHとした他は、実施例と同様にして分解処理を行なうとともに、樹脂溶解率を算出した。
参考例5
参考例4の純水を1N KOHとした他は、参考例4と同様にして分解処理を行なうとともに、樹脂溶解率を算出した。
(比較例1)
実施例1において、処理温度を170℃とした。
(比較例2)
参考例2において、処理温度を170℃とした。
(比較例3)
参考例4において、処理温度を380℃とした。
(比較例4)
実施例において、処理温度を380℃とした。
(評価)
実施例1〜5、参考例1〜5と比較例1〜4の結果を各々、表1および表2に示した。
Thereafter, a decomposition treatment was performed in the same manner as in Example 1 except that the artificial marble used was an acrylic artificial marble, a resin dissolution rate was calculated, and a qualitative analysis was performed.
(Example 2 )
A decomposition treatment was performed in the same manner as in Example 1 except that the pure water of Example 1 was changed to 1N KOH, a resin dissolution rate was calculated, and a qualitative analysis was performed.
(Example 3 )
A decomposition treatment was performed in the same manner as in Example 1 except that the pure water of Example 1 was changed to 1N NaOH, and a resin dissolution rate was calculated and a qualitative analysis was performed.
( Reference Example 2 )
The decomposition treatment was performed in the same manner as in Reference Example 1 except that the pure water of Reference Example 1 was changed to 1N KOH, and the resin dissolution rate was calculated.
( Reference Example 3 )
The decomposition treatment was performed in the same manner as in Reference Example 1 except that the pure water of Reference Example 1 was changed to 1N NaOH, and the resin dissolution rate was calculated.
(Example 4 )
Example 1 except that the amount of charged vinyl ester-based artificial marble (3 mm mesh) in Example 1 was 2.88 g, the amount of pure water was 11.6 g, the temperature was 350 ° C., and the decomposition treatment time was 2 hours. In the same manner as above, decomposition treatment was performed, and the resin dissolution rate was calculated.
( Reference Example 4 )
Reference Example 1 of the acrylic artificial marble ground product (3mm mesh) were charged amount 2.88 g, pure water was charged amount 11.5 g, 350 ° C. The temperature, except that the decomposition treatment time 2 hours Reference Example 1 Similarly, the decomposition treatment was performed and the resin dissolution rate was calculated.
(Example 5 )
The decomposition treatment was performed in the same manner as in Example 4 except that the pure water of Example 4 was changed to 1N KOH, and the resin dissolution rate was calculated.
( Reference Example 5 )
The decomposition treatment was performed in the same manner as in Reference Example 4 except that the pure water of Reference Example 4 was changed to 1N KOH, and the resin dissolution rate was calculated.
(Comparative Example 1)
In Example 1, the processing temperature was 170 ° C.
(Comparative Example 2)
In Reference Example 2 , the treatment temperature was 170 ° C.
(Comparative Example 3)
In Reference Example 4 , the treatment temperature was 380 ° C.
(Comparative Example 4)
In Example 5 , the treatment temperature was 380 ° C.
(Evaluation)
The results of Examples 1 to 5, Reference Examples 1 to 5 and Comparative Examples 1 to 4 are shown in Table 1 and Table 2, respectively.

実施例1、2、3にて回収されたビニルエステル系樹脂由来可溶化物は、スチレン−メタクリル酸共重合体、エポキシ骨格であった。また、固形残渣のX線回折分析から水酸化アルミニウムはベーマイト化していることが確認できた。これは、水酸化アルミニウムが脱水され生成したもので、熱可塑性樹脂の無機性難燃フィラーとして利用可能である。 The vinyl ester resin-derived solubilized product recovered in Examples 1, 2 , and 3 was a styrene-methacrylic acid copolymer and an epoxy skeleton. Moreover, it was confirmed from the X-ray diffraction analysis of the solid residue that the aluminum hydroxide was converted to boehmite. This is produced by dehydration of aluminum hydroxide and can be used as an inorganic flame retardant filler for thermoplastic resins.

参考例1〜3にて回収されたアクリル系樹脂由来可溶化物は、メタクリル酸であった。また、固形残渣のX線回折分析からシリカ(SiO)が残存していることが確認できた。 The solubilized product derived from the acrylic resin recovered in Reference Examples 1 to 3 was methacrylic acid. Moreover, it was confirmed from the X-ray diffraction analysis of the solid residue that silica (SiO 2 ) remained.

実施例4〜5では、いずれもビニルエステル系樹脂由来可溶化物はエタノール、イソ酪酸、フェノール、イソプロペニルフェニールが生成していることが確認できた。また、固形残渣のX線回折分析から水酸化アルミニウムはベーマイト化していることが確認できた。 In each of Examples 4 to 5 , it was confirmed that ethanol, isobutyric acid, phenol, and isopropenyl phenyl were produced in the solubilizate derived from the vinyl ester resin. Moreover, it was confirmed from the X-ray diffraction analysis of the solid residue that the aluminum hydroxide was converted to boehmite.

参考例4〜5では、メタノール、エタノール、クロロホルムが生成していることが確認できたが、ごく少量であり、回収・再利用するのは困難である。また、固形残渣のX線回折分析からシリカ(SiO)が残存していることが確認できた。 In Reference Examples 4 to 5 , it was confirmed that methanol, ethanol, and chloroform were produced, but the amount was very small, and it was difficult to recover and reuse. Moreover, it was confirmed from the X-ray diffraction analysis of the solid residue that silica (SiO 2 ) remained.

以上の結果より、本発明によりビニルエステル系人造大理石においては、樹脂由来のスチレン−メタクリル酸共重合体、エポキシ骨格、或いは無機充填剤由来のベーマイトを回収再利用できる。また、アクリル系人造大理石においては、樹脂由来のメタクリル酸、或いは無機充填剤のシリカを回収再利用できる。   From the above results, in the vinyl ester-based artificial marble according to the present invention, resin-derived styrene-methacrylic acid copolymer, epoxy skeleton, or boehmite derived from an inorganic filler can be recovered and reused. In acrylic artificial marble, methacrylic acid derived from resin or silica as an inorganic filler can be recovered and reused.

実施例と比較例1〜4との対比より明らかなように、処理温度が180℃未満の170℃の場合、そして370℃を超える380℃の場合には回収率が顕著に低下していることがわかる。   As is clear from the comparison between the Examples and Comparative Examples 1 to 4, the recovery rate is remarkably reduced when the treatment temperature is 170 ° C. less than 180 ° C. and when the treatment temperature is 380 ° C. exceeding 370 ° C. I understand.

Figure 0004770182
Figure 0004770182

Figure 0004770182
Figure 0004770182

Claims (3)

無機充填剤と熱硬化性樹脂を主として含有し、前記無機充填剤が水酸化アルミニウムであり前記熱硬化性樹脂がビニルエステル樹脂であるビニルエステル系人造大理石を、180℃〜280℃の温度範囲の亜臨界水で処理し、この亜臨界水処理物を固液分離することにより前記熱硬化性樹脂由来の高分子の有価物を含む水可溶成分と、前記無機充填剤由来のべーマイトを含む固形残渣とを回収することを特徴とする人造大理石の分解方法。 A vinyl ester-based artificial marble mainly containing an inorganic filler and a thermosetting resin, wherein the inorganic filler is aluminum hydroxide and the thermosetting resin is a vinyl ester resin, in a temperature range of 180 ° C. to 280 ° C. A water-soluble component containing a valuable material of a polymer derived from the thermosetting resin and a boehmite derived from the inorganic filler by treating with subcritical water and solid-liquid separation of the treated subcritical water. A method for decomposing artificial marble, comprising collecting solid residue . 亜臨界水にアルカリを共存させることを特徴とする請求項1の人造大理石の分解方法。 Artificial marble decomposition method according to claim 1, characterized in Rukoto coexist alkali subcritical water. 共存させるアルカリが第1A族(アルカリ金属)、第2A族(アルカリ土類金属)、および塩基性リン酸塩のうちの少なくともいずれかであることを特徴とする請求項2の人造大理石の分解方法。 Alkali Group 1A coexist (alkali metal), Group 2A (alkaline earth metals), and degradation of the artificial marble according to claim 2, wherein at least one Der Rukoto of basic phosphate Method.
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