JPH0227123B2 - - Google Patents

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Publication number
JPH0227123B2
JPH0227123B2 JP16313685A JP16313685A JPH0227123B2 JP H0227123 B2 JPH0227123 B2 JP H0227123B2 JP 16313685 A JP16313685 A JP 16313685A JP 16313685 A JP16313685 A JP 16313685A JP H0227123 B2 JPH0227123 B2 JP H0227123B2
Authority
JP
Japan
Prior art keywords
synthetic resin
thermoplastic synthetic
resin particles
multicolored
colored fine
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
Application number
JP16313685A
Other languages
Japanese (ja)
Other versions
JPS6223716A (en
Inventor
Kenro Hatsutori
Masanori Nagano
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Achilles Corp
Original Assignee
Achilles Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Achilles Corp filed Critical Achilles Corp
Priority to JP16313685A priority Critical patent/JPS6223716A/en
Publication of JPS6223716A publication Critical patent/JPS6223716A/en
Publication of JPH0227123B2 publication Critical patent/JPH0227123B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は多色合成樹脂粒及びその製造方法に関
し、詳しくは床材等に使用される合成樹脂シート
の製造の際に使用されるものであつて、流れ模様
を有する合成樹脂シートを製造する際に使用され
る多色合成樹脂粒及びその製造方法に関する。 〔従来の技術〕 従来から大理石模様等の数種類の色が入り乱れ
て配置された所謂流れ模様を有するシートの形成
方法として、塩化ビニール系樹脂の如き熱可塑性
合成樹脂材に顔料を混練してシート状とすると共
にこのシート面に上記顔料添加と混練による流れ
模様を形成し、このシート素材の表面に顔料を塗
布するか又は色素地シートを貼合わせたものを角
形等の立方体小片に細断し、この細断素材を無定
形にプレス型箱内に充填し、熱圧を加えてプレス
型箱内の細断素材の流動を促し、流動状態の下に
之を冷却固定化して板状体としたものを研削する
ことにより、大理石模様を始めとする各種の立体
的柄模様を有する合成樹脂シートを得る方法(特
公昭38−4684号公報)等が知られており、上記し
たような細断素材が流れ模様を有するシートの形
成に使用されている。 〔発明が解決しようとする問題点〕 しかしながら、上記した従来の細断素材は立方
体形状をなしており、熱プレスするに際して層状
に配列する際に均一な平面を有する如く層状に形
成するのがはなはだ困難であり、又、各素材を密
に層状化することも困難であり、その結果細断素
材を重ねて層の厚みを厚くすることによりそれら
の欠点を補う工夫が必要となり、得られるシート
がどうしても厚くなり薄いシートが得られ難いと
いう欠点があつた。又、上記素材を得るために熱
可塑性合成樹脂に顔料を混練してシート状とする
と共にシート面に顔料添加と混練による流れ模様
を形成するので混練のコントロールが非常に難し
く、例えば、混練し過ぎると極端な場合一色に変
化してしまい流れ模様の形成が不可能となる場合
があり、又、混練の程度が少ないと充分な流れ模
様が得られない虞が生じる不具合があつた。 本発明は、流れ模様を有するシートを形成する
に当たり、層状に配列することが容易に出来しか
も単層に容易に配列することが出来、その結果厚
みの厚いものはもとより厚みの薄いシートを容易
に形成することが出来、しかも良好な流れ模様を
形成することが出来る多色合成樹脂粒を提供する
ことを目的とする。 本発明のいま一つは、上記のような多色合成樹
脂粒を混練のコントロールミスがなく均一で良好
な多色合成樹脂粒を得ることができる多色合成樹
脂粒の製造方法を提供することを目的とする。 〔問題点を解決するための手段〕 本発明者等は上記課題を解決するため鋭意研究
した結果、複数種類の着色微粒状熱可塑性合成樹
脂を高速回転翼型ミキサー内にて撹拌造粒してな
る多色合成樹脂粒が上記課題を解決するととも
に、又、少なくとも2種類以上の着色微粒状熱可
塑性合成樹脂を高速回転翼型ミキサー内で撹拌造
粒する多色合成樹脂粒の製造方法が、均一で良好
な樹脂粒を得られることを見出し本発明を完成す
るに至つた。 即ち、本発明の一つは、着色微粒状熱可塑性合
成樹脂を複数種類高速回転翼型ミキサー内にて撹
拌造粒してなり、複数の色彩が合成樹脂粒の表面
及び内部において入り乱れた流れ模様を形成して
なる多色合成樹脂粒を要旨とするものである。 又、本発明のいま一つは、少なくとも2種類以
上の着色微粒状熱可塑性合成樹脂を高速回転翼型
ミキサー内に投入した後、該ミキサー内にて加熱
撹拌し、しかる後冷却し、複数の色彩が合成樹脂
粒の表面及び内部において入り乱れた流れ模様を
形成してなる多色合成樹脂粒を得ることを特徴と
する多色合成樹脂粒の製造方法を要旨とするもの
である。 本発明の多色合成樹脂粒は着色微粒状熱可塑性
合成樹脂を複数種類高速回転翼型ミキサー内にて
撹拌造粒してなる球状粒子で、少なくとも2種類
以上の色が粒子の表面はもとよりその内部にまで
入り乱れて存在するものである。 本発明にいう微粒状熱可塑性合成樹脂とは、平
均粒径が0.2〜5mm程度のもの、好ましくは0.5〜
3mm程度のものを指し、その形状は球状のもので
も或いは楕円状のものでも円柱状のものでもどの
様なものでも使用可能である。 上記熱可塑性合成樹脂としてはポリ塩化ビニル
樹脂、酢酸ビニル樹脂、ポリエチレン、ポリプロ
ピレン、アクリル樹脂等の単独重合体或いは共重
合体等の一般に使用される熱可塑性合成樹脂であ
ればいずれのものも単独又は混合して使用可能で
ある。 上記着色微粒状熱可塑性合成樹脂は、例えば、
熱可塑性合成樹脂の粉末を着色剤、可塑剤ととも
に高速回転翼型ミキサー内に投入し、加熱撹拌す
ることにより得られたもの、又、シート状または
棒状に形成された着色合成樹脂を粉砕もしくは切
断して製造したものが使用され、これらのうちで
色の相違する複数種類のものが使用される。 上記着色剤としては、従来から熱可塑性合成樹
脂の着色に使用されているものであればどの様な
ものでも使用可能である。 又、上記可塑剤としては、ジオクチルフタレー
ト、ジブチルフタレート、ブチルベンジルフタレ
ート、ジオクチルアジペート、トリクレジルフオ
スフエート等の汎用可塑剤の他、DAP、アクリ
ル系モノマー、アクリル系オリゴマー等の反応性
可塑剤、トリブトキシエチルフオスフエート、ブ
チルジグリコールアジペート、サンソサイザーC
−1100(新日本理化製)等の帯電防止性可塑剤、
ドデシルベンゼン誘導体等の二次可塑剤等が挙げ
られる。可塑剤の添加量は樹脂100重量部に対し
10〜100重量部が好ましい。 又、必要に応じて安定剤、滑剤、充填剤、発泡
剤、帯電防止剤、防カビ剤等通常使用される添加
剤が使用される。 特に充填剤は高速回転翼型ミキサーでの撹拌時
の熱可塑性合成樹脂組成物の粘着による流動性低
下を改良し、粗大粒子の発生を抑える効果があり
支障のない範囲で添加することが好ましい。又、
このような目的以外に、コストダウン、軽量化等
の目的で炭酸カルシウム、クレー、シリカ、シラ
スバルーン、ガラスバルーン、木粉、コルク粉等
の軽量充填剤、導電性や帯電防止性付与の目的で
カーボン粉末、炭素繊維や銀、銅、ニツケル、ア
ルミニウム、ステンレス、鉄等の金属よりなる粉
末や短繊維などの導電性粉末充填剤や導電性短繊
維、耐摩耗性や防滑性付与の目的で珪砂粒、珪酸
化合物粒子、ガラス粉末、陶磁器粉砕粒、カーボ
ンランダム、アランダムなどの硬質粉粒体、寸法
安定性付与の目的でガラス短繊維、チタン酸カリ
ウムの短繊維、MOS(カルシウムメタシリケー
ト)短繊維などの無機物短繊維等が使用できる。 導電性粉末充填剤は粒系が0.5〜1000μが好まし
く導電性短繊維は径が4〜600μで長さが0.5〜20
mmの範囲が好ましい。添加量は目的とする抵抗値
により適宜設定する必要があるが、導電性粉末充
填剤の場合で約2重量%以上、導電性短繊維の場
合で約1重量%以上の添加が必要である。 硬質粉粒体は径が10〜1000μが好ましく、添加
量は5重量%以上の添加が好ましい。他の添加
剤、充填剤等は使用目的により適当量添加使用す
る。 これらの添加剤は単独で使用しても良いし、2
種以上を混合使用しても何等さしつかえないもの
である。 本発明では、上記着色微粒状熱可塑性合成樹脂
を複数種類高速回転翼型ミキサー内にて撹拌造粒
して多色合成樹脂粒を得る。 特に上記したような導電性充填剤や導電性繊維
を添加した導電性微粒状熱可塑性合成樹脂と非導
電性微粒状熱可塑性合成樹脂とを高速回転翼型ミ
キサーで撹拌造粒することにより部分的に導電性
流れ模様を有する導電性合成樹脂粒を得ることが
できる。この場合導電性微粒熱可塑性合成樹脂は
非導電性微粒状熱可塑性合成樹脂100重量部に対
し1重量部以上添加することが好ましい。 本発明において使用される高速回転翼型ミキサ
ーは従来から一般に使用されているものが使用で
き、例えば、ヘンシエルミキサー(三井三池化工
機製)、スーパーミキサー(川田製作所製)、ニユ
ーグラマシン(大和化工機製)等が使用可能であ
る。 高速回転翼型ミキサー内に投入された複数種類
の着色微粒状熱可塑性合成樹脂は該ミキサー内で
加熱撹拌され粒子体積を増加するとともに球状に
形成され、各色の入り乱れた多色合成樹脂粒が形
成される。この際、着色微粒状熱可塑性合成樹脂
の少なくとも1種類のものは他の着色微粒状熱可
塑性合成樹脂の溶融温度より低い溶融温度を有す
るものを使用することが好ましい。そうすること
により、溶融温度の低い着色微粒状熱可塑性合成
樹脂が加熱撹拌した際により流動性を増し、他の
微粒状熱可塑性合成樹脂の付着性を向上すること
で粒子の成長が容易となるとともに、得られる樹
脂粒の各色の配色がより装飾性を増加する。 本発明において、高速回転翼型ミキサー内に所
定の着色微粒状熱可塑性合成樹脂を投入し、回転
翼の回転速度を約20〜50m/secで撹拌すると同
時に、ミキサーのジヤケツトに蒸気を通じ加熱を
開始する。これによりミキサー内壁面からの熱伝
達と着色微粒状熱可塑性合成樹脂同士の高速撹拌
に伴う摩擦熱の発生により、該微粒状熱可塑性合
成樹脂の温度が上昇し造粒が開始する。 合成樹脂が望みの粒径に到達した後、加熱を停
止し、ミキサーの回転翼の回転速度を約5〜
20m/secに下げ、造粒物を破壊しない程度の低
速度で冷却撹拌し、しかる後多色合成樹脂粒を取
り出す。以上の操作は、通常加熱撹拌を加熱ミキ
サーで行い、所望の粒径になつた時直ちに冷却ミ
キサーに移し、粒子を破壊しない程度の低速度で
冷却撹拌する方法で行われる。 加熱停止時の温度は使用する樹脂の溶融温度、
得られる多色合成樹脂粒の希望する粒径等により
種々変更可能であるが、一般に100〜250℃程度が
好ましい。 本発明で得られる多色合成樹脂粒の粒径は必要
に応じて種々選択することができるが、一般に1
〜20mm程度である。得られる多色合成樹脂粒の粒
径が大きいものを必要とする場合には高速回転翼
型ミキサーに投入する着色微粒状熱可塑性合成樹
脂を平均粒径の大きいものを使用し、又、粒径の
小さい多色合成樹脂粒を必要とする場合には高速
回転翼型ミキサー内に投入する着色微粒状合成樹
脂を平均粒径の小さいものを使用すればよい。 本発明においては、着色剤の添加量、混合する
着色微粒状熱可塑性合成樹脂の粒径、使用する樹
脂の溶融温度または流動特性等を変化させること
で種々のながれ模様を有する多色合成樹脂粒を得
ることができる。また、着色微粒状熱可塑性合成
樹脂に目的に応じた添加剤を添加することで種々
の機能性を付与した多色合成樹脂粒を得ることが
できる。 〔実施例〕 以下、本発明を実施例を挙げて更に詳細に説明
するが、本発明はこれら実施例に限定されるもの
ではない。 実施例 1 下記第1表に示す配合(1)、配合(2)により各々黒
色微粒状熱可塑性合成樹脂、黄色微粒状熱可塑性
合成樹脂を製造する。
[Industrial Application Field] The present invention relates to multicolored synthetic resin particles and a method for producing the same, and more specifically, the present invention relates to multicolored synthetic resin particles that are used in the production of synthetic resin sheets used for flooring, etc., and that have a flowing pattern. The present invention relates to multicolored synthetic resin particles used in producing synthetic resin sheets and a method for producing the same. [Prior Art] Conventionally, as a method of forming a sheet having a so-called flow pattern, such as a marble pattern, in which several types of colors are arranged in a jumbled manner, pigments are kneaded into a thermoplastic synthetic resin material such as vinyl chloride resin, and the sheet is formed into a sheet. At the same time, a flow pattern is formed on the surface of this sheet by adding the pigment and kneading, and the pigment is applied to the surface of this sheet material, or the colored base sheet is pasted together, and the sheet is shredded into cubes such as squares. This shredded material was filled into a press mold box in an amorphous shape, heat and pressure was applied to promote the flow of the shredded material inside the press mold box, and the material was cooled and fixed in a fluid state to form a plate-shaped body. A method of obtaining synthetic resin sheets with various three-dimensional patterns including marble patterns by grinding objects is known (Japanese Patent Publication No. 38-4684). is used to form sheets with flow patterns. [Problems to be Solved by the Invention] However, the conventional shredded materials described above have a cubic shape, and it is extremely difficult to form them into layers so that they have a uniform plane when they are arranged in layers during hot pressing. It is also difficult to layer each material densely, and as a result, it is necessary to make up for these shortcomings by stacking the shredded materials to increase the thickness of the layer, and the resulting sheet is The drawback was that it inevitably became thicker and it was difficult to obtain a thin sheet. Furthermore, in order to obtain the above-mentioned material, pigment is kneaded into a thermoplastic synthetic resin to form a sheet, and a flow pattern is formed on the sheet surface by adding the pigment and kneading, so it is very difficult to control the kneading, such as over-kneading. In extreme cases, the color may change to one color, making it impossible to form a flowing pattern, and if the degree of kneading is too low, there is a risk that a sufficient flowing pattern may not be obtained. In forming a sheet having a flowing pattern, the present invention can easily arrange it in layers, and can also easily arrange it in a single layer, and as a result, it is possible to easily form not only thick sheets but also thin sheets. It is an object of the present invention to provide multicolored synthetic resin particles that can be formed and that can form a good flow pattern. Another object of the present invention is to provide a method for producing multicolored synthetic resin particles as described above, which can produce uniform and good multicolored synthetic resin particles without any mis-control of kneading. With the goal. [Means for Solving the Problems] As a result of intensive research in order to solve the above problems, the present inventors have developed a method by stirring and granulating multiple types of colored fine-grained thermoplastic synthetic resins in a high-speed rotary vane type mixer. The multicolored synthetic resin particles solve the above problems, and the method for producing the multicolored synthetic resin particles includes stirring and granulating at least two or more types of colored fine-grained thermoplastic synthetic resins in a high-speed rotary blade mixer. The present invention was completed by discovering that uniform and good resin particles can be obtained. That is, one aspect of the present invention is that a plurality of colored fine-grained thermoplastic synthetic resins are agitated and granulated in a high-speed rotary vane type mixer, and a flow pattern in which a plurality of colors are mixed on the surface and inside of the synthetic resin particles is created. The gist is multicolored synthetic resin particles formed by forming. Another aspect of the present invention is to charge at least two or more kinds of colored fine-grained thermoplastic synthetic resins into a high-speed rotary vane type mixer, heat and stir in the mixer, and then cool them. The gist of the present invention is to provide a method for producing multicolored synthetic resin particles, which is characterized by obtaining multicolored synthetic resin particles in which colors form a mixed flow pattern on the surface and inside of the synthetic resin particles. The multicolored synthetic resin particles of the present invention are spherical particles made by agitating and granulating a plurality of colored fine-grained thermoplastic synthetic resins in a high-speed rotary vane type mixer, and at least two or more types of colors are present not only on the surface of the particles but also on their surfaces. It exists in a state of confusion even inside. The fine particulate thermoplastic synthetic resin referred to in the present invention is one with an average particle size of about 0.2 to 5 mm, preferably 0.5 to 5 mm.
It refers to a material of about 3 mm, and any shape can be used, including spherical, elliptical, and cylindrical. The above-mentioned thermoplastic synthetic resin may be any commonly used thermoplastic synthetic resin such as homopolymers or copolymers such as polyvinyl chloride resin, vinyl acetate resin, polyethylene, polypropylene, acrylic resin, etc., alone or Can be used in combination. The colored fine particulate thermoplastic synthetic resin is, for example,
Thermoplastic synthetic resin powder is put into a high-speed rotary blade mixer together with a colorant and plasticizer, and the resulting mixture is heated and stirred, or the colored synthetic resin formed into a sheet or rod shape is crushed or cut. Among these, a plurality of types with different colors are used. As the colorant, any colorant that has been conventionally used for coloring thermoplastic synthetic resins can be used. In addition, the above-mentioned plasticizers include general-purpose plasticizers such as dioctyl phthalate, dibutyl phthalate, butylbenzyl phthalate, dioctyl adipate, and tricresyl phosphate, as well as reactive plasticizers such as DAP, acrylic monomers, and acrylic oligomers. , tributoxyethyl phosphate, butyl diglycol adipate, Sansocizer C
Antistatic plasticizers such as −1100 (manufactured by New Nippon Rika),
Examples include secondary plasticizers such as dodecylbenzene derivatives. The amount of plasticizer added is based on 100 parts by weight of resin.
10 to 100 parts by weight is preferred. Additionally, commonly used additives such as stabilizers, lubricants, fillers, foaming agents, antistatic agents, and fungicides may be used as required. In particular, the filler is effective in improving fluidity reduction due to adhesion of the thermoplastic synthetic resin composition during stirring with a high-speed rotary blade mixer and suppressing the generation of coarse particles, and is preferably added within a range that does not cause any problems. or,
In addition to these purposes, we also use lightweight fillers such as calcium carbonate, clay, silica, shirasu balloons, glass balloons, wood powder, and cork powder for the purpose of cost reduction and weight reduction, and for the purpose of imparting conductivity and antistatic properties. Conductive powder fillers and conductive short fibers such as carbon powder, powders and short fibers made of carbon fiber, metals such as silver, copper, nickel, aluminum, stainless steel, and iron, and silica sand for the purpose of imparting wear resistance and anti-slip properties. Hard powder particles such as grains, silicate compound particles, glass powder, crushed ceramic particles, carbon random, and alundum, short glass fibers, potassium titanate short fibers, and MOS (calcium metasilicate) short fibers for the purpose of providing dimensional stability. Inorganic short fibers such as fibers can be used. The conductive powder filler preferably has a grain size of 0.5 to 1000 μm, and the conductive short fibers have a diameter of 4 to 600 μm and a length of 0.5 to 20 μm.
A range of mm is preferred. The amount added needs to be set appropriately depending on the desired resistance value, but it is necessary to add about 2% by weight or more in the case of a conductive powder filler, and about 1% by weight or more in the case of conductive short fibers. The hard powder particles preferably have a diameter of 10 to 1000 μm, and the amount added is preferably 5% by weight or more. Other additives, fillers, etc. are added in appropriate amounts depending on the purpose of use. These additives may be used alone or in combination with
There is no problem in using a mixture of more than one species. In the present invention, multicolor synthetic resin particles are obtained by agitating and granulating a plurality of kinds of the colored fine-grained thermoplastic synthetic resins in a high-speed rotary vane type mixer. Particularly, by agitating and granulating conductive fine particulate thermoplastic synthetic resin containing conductive filler or conductive fiber as described above and non-conductive fine particulate thermoplastic synthetic resin with a high-speed rotary blade mixer, partial granulation can be achieved. Conductive synthetic resin particles having a conductive flow pattern can be obtained. In this case, it is preferable to add 1 part by weight or more of the conductive fine-grained thermoplastic synthetic resin to 100 parts by weight of the non-conductive fine-grained thermoplastic synthetic resin. The high-speed rotary vane type mixer used in the present invention can be one that has been commonly used in the past, such as the Hensiel mixer (manufactured by Mitsui Miike Kakoki), the super mixer (manufactured by Kawada Manufacturing Co., Ltd.), and the Newgra Machine (manufactured by Daiwa Kakoki Co., Ltd.). Machine-made) etc. can be used. Multiple types of colored fine-grained thermoplastic synthetic resins put into a high-speed rotary vane type mixer are heated and stirred in the mixer to increase the particle volume and form into spherical shapes, forming multicolored synthetic resin particles with a mixture of colors. be done. At this time, it is preferable to use at least one type of colored fine-grained thermoplastic synthetic resin having a melting temperature lower than the melting temperature of the other colored fine-grained thermoplastic synthetic resins. By doing so, the colored fine-grained thermoplastic synthetic resin with a low melting temperature increases its fluidity when heated and stirred, and the adhesion of other fine-grained thermoplastic synthetic resins improves, making particle growth easier. At the same time, the color scheme of the resulting resin particles becomes more decorative. In the present invention, a predetermined colored fine-grained thermoplastic synthetic resin is put into a high-speed rotary vane type mixer, and the rotary vane is stirred at a rotational speed of about 20 to 50 m/sec, and at the same time steam is passed through the jacket of the mixer to start heating. do. As a result, the temperature of the finely divided thermoplastic synthetic resin increases due to heat transfer from the inner wall surface of the mixer and generation of frictional heat due to high-speed stirring of the colored finely divided thermoplastic synthetic resin, and granulation begins. After the synthetic resin reaches the desired particle size, stop heating and reduce the rotation speed of the mixer rotor to about 5~
The speed was lowered to 20 m/sec, and the mixture was cooled and stirred at a low speed that would not destroy the granules, and then the multicolored synthetic resin particles were taken out. The above operation is usually carried out by heating and stirring using a heating mixer, and immediately transferring the particles to a cooling mixer when the desired particle size is reached, followed by cooling and stirring at a low speed that does not destroy the particles. The temperature when heating is stopped is the melting temperature of the resin used,
Although various changes can be made depending on the desired particle size of the resulting multicolored synthetic resin particles, the temperature is generally preferably about 100 to 250°C. The particle size of the multicolored synthetic resin particles obtained in the present invention can be selected from various sizes as required, but generally 1
~20mm. If the obtained multicolored synthetic resin particles are required to have a large particle size, use a colored fine-grained thermoplastic synthetic resin that is charged into a high-speed rotary vane type mixer and have a large average particle size. When multicolored synthetic resin particles with a small size are required, the colored fine-grained synthetic resin charged into the high-speed rotary vane type mixer may have a small average particle size. In the present invention, multicolored synthetic resin particles having various flowing patterns can be produced by changing the amount of coloring agent added, the particle size of the colored finely divided thermoplastic synthetic resin to be mixed, the melting temperature or flow characteristics of the resin used, etc. can be obtained. Furthermore, by adding additives depending on the purpose to the colored fine-grained thermoplastic synthetic resin, it is possible to obtain multicolored synthetic resin particles with various functionalities. [Examples] Hereinafter, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited to these Examples. Example 1 A black fine-grained thermoplastic synthetic resin and a yellow fine-grained thermoplastic synthetic resin were produced according to formulations (1) and (2) shown in Table 1 below, respectively.

〔発明の効果〕〔Effect of the invention〕

本発明多色合成樹脂粒は着色微粒状熱可塑性合
成樹脂を複数種類高速回転翼型ミキサー内にて撹
拌造粒したものであるから、該合成樹脂粒を使用
して流れ模様を有するシートを形成する場合、容
易に層形成でき作業能率の良いシート形成が可能
となる。又、本発明樹脂粒は複数の色が粒子の表
面はもとよりその内部にまで入り乱れて存在する
ものであり、該粒子を用いてシートを形成すれば
方向性のない模様が形成でき、装飾性豊なシート
が形成できる。 又、本発明製造方法では、各着色微粒状熱可塑
性合成樹脂の有する色が鮮明に且つ入り乱れた状
態で配置された樹脂粒が形成でき、従来のように
混練コントロールが難しいというような不具合は
なく、しかも任意の粒度の樹脂粒を容易に得るこ
とができ、また、種々の充填剤が容易にしかも多
量に混合でき、充填剤の種類に応じて種々の機能
を付与したシート形成用樹脂粒を簡単に得ること
ができる等種々の効果を有するものである。
The multicolored synthetic resin particles of the present invention are obtained by stirring and granulating a plurality of types of colored fine-grained thermoplastic synthetic resins in a high-speed rotary vane type mixer, so the synthetic resin particles can be used to form a sheet with a flow pattern. In this case, layers can be easily formed and sheets can be formed with high work efficiency. Furthermore, in the resin particles of the present invention, a plurality of colors exist in a disordered manner not only on the surface of the particles but also inside the particles, and if a sheet is formed using the particles, a pattern without directionality can be formed, and it is highly decorative. A sheet can be formed. In addition, in the production method of the present invention, resin particles can be formed in which the colors of each colored particulate thermoplastic synthetic resin are clearly arranged in a disordered manner, and there is no problem such as difficulty in controlling kneading as in the past. Moreover, resin particles of any particle size can be easily obtained, various fillers can be easily mixed in large amounts, and resin particles for sheet formation can be provided with various functions depending on the type of filler. It has various effects such as being easily obtainable.

Claims (1)

【特許請求の範囲】 1 着色微粒状熱可塑性合成樹脂を複数種類高速
回転翼型ミキサー内にて撹拌造粒してなり、複数
の色彩が合成樹脂粒の表面及び内部において入り
乱れた流れ模様を形成してなる多色合成樹脂粒。 2 少なくとも2種類以上の着色微粒状熱可塑性
合成樹脂を高速回転翼型ミキサー内に投入した
後、該ミキサー内にて加熱撹拌し、しかる後冷却
し、複数の色彩が合成樹脂粒の表面及び内部にお
いて入り乱れた流れ模様を形成してなる多色合成
樹脂粒を得ることを特徴とする多色合成樹脂粒の
製造方法。 3 上記2種類以上の着色微粒状熱可塑性合成樹
脂のうち少なくとも1種類の着色微粒状熱可塑性
合成樹脂の溶融温度が他の着色微粒状熱可塑性合
成樹脂の溶融温度よりも低温である特許請求の範
囲第2項記載の多色合成樹脂粒の製造方法。
[Scope of Claims] 1. A product made by stirring and granulating a plurality of types of colored fine-grained thermoplastic synthetic resins in a high-speed rotary vane type mixer, and forming a flow pattern in which a plurality of colors are mixed on the surface and inside of the synthetic resin particles. Multicolored synthetic resin particles. 2. At least two or more types of colored fine-grained thermoplastic synthetic resins are put into a high-speed rotary vane type mixer, heated and stirred in the mixer, and then cooled so that multiple colors appear on the surface and inside of the synthetic resin particles. 1. A method for producing multicolored synthetic resin granules, which comprises obtaining multicolored synthetic resin granules that form a mixed flow pattern. 3. A patent claim in which the melting temperature of at least one colored fine-grained thermoplastic synthetic resin among the two or more types of colored fine-grained thermoplastic synthetic resins is lower than the melting temperature of the other colored fine-grained thermoplastic synthetic resins. A method for producing multicolored synthetic resin particles according to Scope 2.
JP16313685A 1985-07-24 1985-07-24 Preparation of multi-color synthetic resin particle Granted JPS6223716A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16313685A JPS6223716A (en) 1985-07-24 1985-07-24 Preparation of multi-color synthetic resin particle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16313685A JPS6223716A (en) 1985-07-24 1985-07-24 Preparation of multi-color synthetic resin particle

Publications (2)

Publication Number Publication Date
JPS6223716A JPS6223716A (en) 1987-01-31
JPH0227123B2 true JPH0227123B2 (en) 1990-06-14

Family

ID=15767882

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16313685A Granted JPS6223716A (en) 1985-07-24 1985-07-24 Preparation of multi-color synthetic resin particle

Country Status (1)

Country Link
JP (1) JPS6223716A (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4923657A (en) * 1984-09-24 1990-05-08 Davidson Textron Inc. Method for making plastic parts
JPS6262710A (en) * 1985-09-13 1987-03-19 Achilles Corp Manufacture of synthetic resin granule
JPH0647039Y2 (en) * 1989-12-18 1994-11-30 株式会社タジマ Decoration material
JP2531225Y2 (en) * 1992-09-11 1997-04-02 有限会社勝製作所 Stirring vessel for synthetic resin raw materials
JP3746436B2 (en) 2001-05-10 2006-02-15 ミサワホーム株式会社 Wood-like molded product manufacturing method and wood-like molded product manufacturing apparatus
JP4664526B2 (en) * 2001-05-23 2011-04-06 太平洋セメント株式会社 Method for producing powdered cement dispersant

Also Published As

Publication number Publication date
JPS6223716A (en) 1987-01-31

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