JP4357930B2 - Method for producing thermoplastic resin pellets containing additives - Google Patents

Method for producing thermoplastic resin pellets containing additives Download PDF

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JP4357930B2
JP4357930B2 JP2003377982A JP2003377982A JP4357930B2 JP 4357930 B2 JP4357930 B2 JP 4357930B2 JP 2003377982 A JP2003377982 A JP 2003377982A JP 2003377982 A JP2003377982 A JP 2003377982A JP 4357930 B2 JP4357930 B2 JP 4357930B2
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additive
resin
pellet
thermoplastic resin
powder
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JP2004169027A (en
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克史 渡辺
政昭 荒巻
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Asahi Kasei Chemicals Corp
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本発明は、熱可塑性樹脂ペレット表面に添加剤を付着させ、添加剤を含有する熱可塑性樹脂ペレットを製造する方法に関する。   The present invention relates to a method for producing a thermoplastic resin pellet containing an additive by attaching the additive to the surface of the thermoplastic resin pellet.

熱可塑性樹脂材料からなる製品は、従来から射出成形などにより成形されている。この場合、ペレットは射出成形機の高温のシリンダー内に搬送(以下可塑化と称する場合がある)され、その後溶融した樹脂は各種製品の形状に加工された金型に射出、冷却、離型させることにより製品化される。近年、環境的及び経済的観点から、成形時間の短縮が求められている。
具体的には、例えば、シリンダーの温度を従来より高温に設定し、かつ金型の温度を従来より低温にして成形を行う。あるいはホットランナーを用いた成形、製品のリサイクルを行ったりする。また部品統合の観点から製品形状の大型化、薄肉化、複雑化してきている。ところが、前記の如く成形条件を変え成形時間の短縮を行ったとしても、可塑化しなかったり可塑化が不安定になったりして予想に反して成形時間が逆に長くなる。
ホットランナー法、製品のリサイクルでは、樹脂の熱劣化により得られた製品の性能が不十分であったり、熱分解成分の発生により製品外観に不具合を発生させる。また大型化、薄肉化あるいは複雑化した製品金型の末端まで溶融樹脂が流動しなかったり(すなわち流動性が不足の問題)、金型から製品が離型しない問題を発生させる。
A product made of a thermoplastic resin material has been conventionally molded by injection molding or the like. In this case, the pellets are conveyed into a high-temperature cylinder of an injection molding machine (hereinafter sometimes referred to as plasticization), and then the molten resin is injected, cooled, and released into molds processed into various product shapes. Product. In recent years, shortening of molding time has been demanded from an environmental and economic viewpoint.
Specifically, for example, the molding is performed with the temperature of the cylinder set higher than the conventional temperature and the temperature of the mold set lower than the conventional temperature. Or, molding using hot runners, recycling products. In addition, from the viewpoint of component integration, product shapes have become larger, thinner, and more complicated. However, even if the molding conditions are changed and the molding time is shortened as described above, the molding time will be longer than expected due to the lack of plasticization or unstable plasticization.
In the hot runner method and product recycling, the performance of the product obtained by thermal degradation of the resin is insufficient, or the appearance of the product is defective due to the generation of thermal decomposition components. In addition, the molten resin does not flow to the end of a product mold that is large, thin, or complicated (that is, the problem of insufficient fluidity), or the product does not release from the mold.

これらの問題を解決する方法として、従来よりヒンダードフェノール化合物、有機ホスファイト化合物などに代表される有機系熱安定剤や高級脂肪酸金属塩、高級脂肪酸アミド、高級脂肪酸エステルなどの滑剤を熱可塑性樹脂ペレットに含有させる技術が用いられている。特に前記の如く成形時の可塑化、離型、熱安定性を向上させるために、熱可塑性樹脂ペレット表面に有機系熱安定剤や滑剤を付着させる方法が用いられていることは当業界では周知の事実である。   As a method for solving these problems, organic heat stabilizers such as hindered phenol compounds and organic phosphite compounds, and lubricants such as higher fatty acid metal salts, higher fatty acid amides and higher fatty acid esters have been used as thermoplastic resins. A technique for inclusion in pellets is used. In particular, it is well known in the art that a method of attaching an organic heat stabilizer or a lubricant to the surface of a thermoplastic resin pellet is used in order to improve plasticization, mold release, and thermal stability during molding as described above. Is the fact of

例えば、タンブラーなどを用いて、熱可塑性樹脂ペレットとミネラルオイルと添加剤などを混合し、ペレット表面に滑剤を付着させる方法がある。しかしこの方法では、添加剤をペレット表面に均一に付着させることが難しくまた添加剤が脱落しやすく、可塑化、離型、熱安定性などの性能が低下したり、脱落した添加剤が成形機ホッパーに付着するコンタミや粉塵による作業環境の悪化の問題を引き起こす。
これらの問題を解決する方法として、添加剤の一部あるいは全部を溶融させ、溶融状態でペレット表面に付着させた後、添加剤を固化しペレット表面にフィルム状に均一に添加剤を付着させる方法が用いられている。この方法を行う装置として、例えば、ヘンシェルミキサーに代表される縦型チャンバーであって内部に水平方向の撹拌装置を具備する装置が用いられる。
For example, there is a method in which a thermoplastic resin pellet, mineral oil, an additive, and the like are mixed using a tumbler or the like, and a lubricant is adhered to the pellet surface. However, with this method, it is difficult to make the additive uniformly adhere to the pellet surface, and the additive tends to fall off, resulting in a decrease in performance such as plasticization, mold release, thermal stability, etc. It causes the problem of deterioration of work environment due to contamination and dust adhering to the hopper.
As a method for solving these problems, a method in which a part or all of the additive is melted and adhered to the pellet surface in a molten state, and then the additive is solidified and the additive is uniformly adhered to the pellet surface in a film form. Is used. As an apparatus for performing this method, for example, an apparatus that is a vertical chamber represented by a Henschel mixer and has a horizontal stirring device inside is used.

しかしながらこの方法では、装置上連続的に付着させることが困難でありバッチ法で行わなければならないという経済的問題が発生する。また撹拌翼の剪断によりペレットが一部粉体化するという問題が発生する。
また、流動床型の装置が開示されている例もある(例えば特許文献1参照)。しかしながらこの装置では、ペレットを流動させるため強力な送風を必要とするため、送風装置が大がかりなるという経済的な問題がある。また、強力な送風により溶融した添加剤がペレットにフィルム状に付着する前に固化しやすいため、特に融点、軟化点が高い添加剤を付着できない等の問題が発生する。
However, this method has an economical problem that it is difficult to deposit continuously on the apparatus and must be performed by a batch method. In addition, there is a problem that the pellets are partly powdered by the shearing of the stirring blade.
There is also an example in which a fluidized bed type apparatus is disclosed (for example, see Patent Document 1). However, this apparatus has an economical problem that a large blower is required because a strong blow is required to flow the pellets. In addition, since the additive melted by strong air blowing is easily solidified before adhering to the pellet in the form of a film, there arises a problem that an additive having a particularly high melting point and softening point cannot be adhered.

さらに、ペレットと潤滑剤を用いて、滑剤の融点より低い温度で組合せ混合し、相互衝突と剪断力を発生させペレット表面に潤滑剤のフィルムを形成させる方法が開示されている例もある(例えば特許文献2参照)。しかしながらこの方法では、付着が不十分であったり、融点、軟化点が高い添加剤を付着できない等の問題が発生する。
特開平8−239482号公報 特表平8−500549号公報
In addition, there is an example in which a method of forming a lubricant film on the pellet surface by using a pellet and a lubricant in combination and mixing at a temperature lower than the melting point of the lubricant to generate a mutual collision and a shearing force is also disclosed (for example, Patent Document 2). However, this method has problems such as insufficient adhesion and the inability to attach an additive having a high melting point and softening point.
JP-A-8-239482 Japanese National Patent Publication No. 8-500549

本発明は、熱可塑性樹脂ペレット表面に均一にフィルム状に添加剤をコーティングすることにより、ニューマーなどを用いた移送あるいは射出成形などの各種成形において添加剤の脱落などが少なく、かつ各種成形での可塑化性、離型性、熱安定性等の性能に優れる添加剤を含有する熱可塑性樹脂ペレットを製造する方法を提供することである。   In the present invention, the additive is uniformly coated on the surface of the thermoplastic resin pellet so that the additive does not fall off in various moldings such as transfer or injection molding using a newer and the like. An object of the present invention is to provide a method for producing a thermoplastic resin pellet containing an additive having excellent performance such as plasticization, releasability and thermal stability.

本発明者らは、上記本発明課題を解決すべく鋭意検討した結果、スキ型ショベル羽根を備えた横型チャンバー型の攪拌機に添加剤を加熱溶融噴霧する設備と粉体添加する設備を具備した装置を用いて、熱可塑性樹脂ペレット表面に添加剤を付着させることにより、上記課題を解決できることを見いだし、本発明を完成させるに至った。 As a result of intensive studies to solve the above-mentioned problems of the present invention, the present inventors have equipped a horizontal chamber type stirrer equipped with a skid type shovel blade with equipment for heating and spraying the additive and equipment for adding powder. The present inventors have found that the above-mentioned problems can be solved by attaching an additive to the surface of the thermoplastic resin pellet using the above, and have completed the present invention.

すなわち本発明は、
1. スキ型ショベル羽根を備えた横型チャンバー型の攪拌機に添加剤を加熱溶融噴霧する設備と粉体添加する設備を具備した装置を用いて、添加剤の加熱溶融噴霧添加および粉体添加を行い、熱可塑性樹脂ペレット表面に添加剤を付着させ、添加剤を含有する熱可塑性樹脂ペレットを得る製造方法。
.熱可塑性樹脂が、ポリアミド樹脂、ポリフェニレンエーテル樹脂、ポリオキシメチレン樹脂、芳香族ポリエステル樹脂、芳香族ポリカーボネート樹脂、ポリフェニレンスルフィド樹脂、ポリオレフィン樹脂、スチレン樹脂、アクリル樹脂、ゴムのいずれかから選ばれた少なくとも1種のペレットであることを特徴とする上記1に記載の製造方法、
.添加剤が、ヒンダードフェノール化合物、ヒンダードアミン化合物、有機ホスファイト化合物、高級脂肪酸金属塩、高級脂肪酸アミド、高級脂肪酸エステルから選ばれる少なくとも1種の化合物であることを特徴とする上記1または2に記載の製造方法、
である。
4. 添加剤の添加方法を、加熱溶融噴霧添加、粉体添加の順に行うことを特徴とする上記1〜3いずれかに記載の製造方法。
5. 粉体添加する添加剤が、加熱溶融噴霧添加する添加剤より高融点であることを特徴とする上記4記載の製造方法。
That is, the present invention
1. Using an apparatus equipped with a horizontal chamber type stirrer equipped with a skive type shovel blade and equipment for heating and spraying the additive and equipment for adding powder, the heat melting and spraying of the additive and powder addition are performed. A production method for obtaining a thermoplastic resin pellet containing an additive by attaching an additive to the surface of the plastic resin pellet.
2 . The thermoplastic resin is at least one selected from polyamide resin, polyphenylene ether resin, polyoxymethylene resin, aromatic polyester resin, aromatic polycarbonate resin, polyphenylene sulfide resin, polyolefin resin, styrene resin, acrylic resin, and rubber. The production method according to 1 above, which is a seed pellet,
3 . 3. The additive according to 1 or 2 above, wherein the additive is at least one compound selected from a hindered phenol compound, a hindered amine compound, an organic phosphite compound, a higher fatty acid metal salt, a higher fatty acid amide, and a higher fatty acid ester. Manufacturing method,
It is.
4. The method according to any one of 1 to 3 above, wherein the additive is added in the order of heat-melt spray addition and powder addition.
5). 5. The production method according to 4 above, wherein the additive to be powdered has a higher melting point than the additive to be added by hot melt spraying.

本発明の製造方法により、ニューマーなどを用いた移送あるいは射出成形などの各種成形において添加剤の脱落などが少なく、かつ各種成形での可塑化性、離型性、熱安定性等の性能やそれらのばらつきが少ないという優れた特徴を有する添加剤を付着させた熱可塑性樹脂ペレットを得ることができる。   By the production method of the present invention, there is little dropout of additives in various moldings such as transfer or injection molding using a pneumatic or the like, and the performance such as plasticizing property, releasability and thermal stability in various moldings and the like. It is possible to obtain a thermoplastic resin pellet to which an additive having an excellent feature that there is little variation is attached.

以下、本発明について詳細に説明する。
本発明で好ましく用いられる熱可塑性樹脂は、例えば、ポリアミド樹脂、ポリフェニレンエーテル樹脂、ポリオキシメチレン樹脂、芳香族ポリエステル樹脂、芳香族ポリカーボネート樹脂、ポリフェニレンスルフィド樹脂、ポリオレフィン樹脂、スチレン樹脂、アクリル樹脂、ゴム、あるいはアラミド、ポリイミド等の縮合系樹脂、ポリスルホン、ポリエーテルスルホン、ポリエーテルケトンなどのポリエーテル系樹脂、ポリ塩化ビニル、
ポリ塩化ビニリデン、ポリフッ化ビニル、ポリフッ化ビニリデンなどの含ハロゲンビニル化合物樹脂などから選ばれる少なくとも1種の樹脂を挙げることができる。
中でもポリアミド樹脂、ポリフェニレンエーテル樹脂、ポリオキシメチレン樹脂、芳香族ポリエステル樹脂、芳香族ポリカーボネート樹脂、ポリフェニレンスルフィド樹脂、ポリオレフィン樹脂、スチレン樹脂、アクリル樹脂、ゴムからなどから選ばれる少なくとも1種の樹脂を用いるのが好ましい。
Hereinafter, the present invention will be described in detail.
The thermoplastic resin preferably used in the present invention is, for example, polyamide resin, polyphenylene ether resin, polyoxymethylene resin, aromatic polyester resin, aromatic polycarbonate resin, polyphenylene sulfide resin, polyolefin resin, styrene resin, acrylic resin, rubber, Or condensation resins such as aramid and polyimide, polyether resins such as polysulfone, polyethersulfone and polyetherketone, polyvinyl chloride,
Examples thereof include at least one resin selected from halogen-containing vinyl compound resins such as polyvinylidene chloride, polyvinyl fluoride, and polyvinylidene fluoride.
Among them, at least one resin selected from polyamide resin, polyphenylene ether resin, polyoxymethylene resin, aromatic polyester resin, aromatic polycarbonate resin, polyphenylene sulfide resin, polyolefin resin, styrene resin, acrylic resin, rubber, etc. is used. Is preferred.

また、本発明の樹脂ペレット表面には本発明の目的を損なわない程度で慣用的に用いられるポリアルキレンエーテル類等の帯電防止剤を展着させても構わない。
本発明の添加剤は、ヒンダードフェノール化合物、ヒンダードアミン化合物、有機ホスファイト化合物、ヒンダードアミン化合物などの有機系熱安定剤や高級脂肪酸金属塩、高級脂肪酸アミド、高級脂肪酸エステルなどの滑剤を挙げることができる。高級脂肪酸金属塩としては、ステアリン酸カルシウム、ステアリン酸亜鉛、モノステアリン酸アルミニウム、ジステアリン酸アルミニウム、トリステアリン酸アルミニウム、モンタン酸カルシウムなどを例示することができる。
In addition, an antistatic agent such as polyalkylene ethers conventionally used may be spread on the surface of the resin pellets of the present invention to the extent that the object of the present invention is not impaired.
Examples of the additive of the present invention include organic heat stabilizers such as hindered phenol compounds, hindered amine compounds, organic phosphite compounds, hindered amine compounds, and lubricants such as higher fatty acid metal salts, higher fatty acid amides, and higher fatty acid esters. . Examples of the higher fatty acid metal salt include calcium stearate, zinc stearate, aluminum monostearate, aluminum distearate, aluminum tristearate, and calcium montanate.

高級脂肪酸アミドとしては、エチレンビスステアリルアミド、エルカ酸アミド、N-ステアリルエルカ酸アミド、N-パルミチルエルカ酸アミド、N-ステアリルステアリルアミド及びこれらの混合物などを例示することができる。高級脂肪酸エステルとしては、ステアリルステアレートを例示することができる。これら添加剤は1種で用いても良いし2種以上を混合して用いても良い。また、本発明の添加剤には、本発明の目的を損なわない程度で、慣用的に用いられる添加剤、例えば顔料および染料、難燃剤、蛍光漂白剤、可塑化剤、有機酸化防止剤、熱安定剤、紫外線吸収剤、核剤、ゴム、強化剤を配合してもかまわない。   Examples of higher fatty acid amides include ethylene bisstearyl amide, erucic acid amide, N-stearyl erucic acid amide, N-palmityl erucic acid amide, N-stearyl stearyl amide, and mixtures thereof. As the higher fatty acid ester, stearyl stearate can be exemplified. These additives may be used alone or in combination of two or more. In addition, the additives of the present invention include additives conventionally used to the extent that the object of the present invention is not impaired, such as pigments and dyes, flame retardants, fluorescent bleaching agents, plasticizers, organic antioxidants, heat Stabilizers, UV absorbers, nucleating agents, rubbers, and reinforcing agents may be blended.

本発明のスキ型ショベル羽根を備えた横型チャンバー型の攪拌機は、添加剤を加熱溶融噴霧する装置を備える。該添加剤を加熱溶融噴霧する装置は、加熱装置を兼ね備える。これにより低温から高温の融点あるいは軟化点を有する種々の添加剤を加熱溶融噴霧することが可能である。更に本発明の該攪拌機には、添加剤を粉体添加する装置も備える。これにより高い溶液粘度あるいは溶融粘度を有する種々の添加剤を付着させることが可能である。なお、上述した加熱溶融噴霧添加、粉体添加方法に関して特に順序の制限は無いが、より高融点の添加剤をペレットの外側に付着させ高温成形性を高めるために、加熱溶融噴霧添加、粉体添加の順に添加することが望ましい。 The horizontal chamber type stirrer provided with the skid type shovel blade of the present invention includes a device for heating and melting and spraying the additive. The apparatus for heating and melting and spraying the additive also has a heating apparatus. Thereby, various additives having a melting point or softening point from a low temperature to a high temperature can be heated and melt sprayed. Furthermore, the stirrer of the present invention is also provided with a device for adding additives in powder form. Thereby, various additives having high solution viscosity or melt viscosity can be adhered. In addition, there is no particular restriction on the order of the above-mentioned hot melt spray addition and powder addition method, but in order to adhere a higher melting point additive to the outside of the pellet and enhance high temperature formability, the heat melt spray addition, powder It is desirable to add in the order of addition.

本発明の装置を用いることにより、搬入口からチャンバー内に搬入された熱可塑性樹脂ペレットに、具備された添加剤加熱溶融噴霧装置から目的の添加剤を液状あるいは溶融状態にし噴霧し、更に粉体添加装置から目的の添加剤を粉末状で展着させる。添加剤を加熱溶融噴霧、展着されたペレットは、スキ型ショベル羽根を用いて均一にかつ効率良く撹拌され、ペレット表面に添加剤を付着させることができる。添加剤を付着させたペレットは、搬出口から連続して搬出される。
また必要に応じてバッチ法すなわち横型チャンバーにペレットを投入し、チャンバーの搬入口と搬出口を閉じた後、添加剤の加熱溶融噴霧、展着、撹拌して、ペレット全量を搬出するという方法でも、ペレット表面に添加剤を付着させることできる。本発明においては、均一にかつ効率良く添加剤をペレット表面に付着させるために、使用する添加剤に応じて、横型チャンバー内の温度を変化させることができる。
By using the apparatus of the present invention, the target additive is sprayed in a liquid or molten state from the additive heating melt spraying apparatus provided on the thermoplastic resin pellets carried into the chamber from the carry-in entrance, and further powdered The target additive is spread in powder form from the addition device. The pellet obtained by spraying and spreading the additive with heat melting can be uniformly and efficiently stirred using a skid type shovel blade to adhere the additive to the surface of the pellet. The pellets to which the additive has been adhered are continuously carried out from the carry-out port.
In addition, the batch method, that is, a method in which pellets are charged into a horizontal chamber as needed, the inlet and outlet of the chamber are closed, and then the additive is heated and melted sprayed, spread, and stirred to carry out the entire pellet amount. The additive can be attached to the pellet surface. In the present invention, in order to adhere the additive uniformly and efficiently to the pellet surface, the temperature in the horizontal chamber can be changed according to the additive used.

また、チャンバー内に窒素等の不活性ガスを流通させ、ペレットの色調等の低下を抑制してもかまわない。横型チャンバーの温度を種々変化させる方法は、加熱した不活性ガスを流通させ加熱する方法、あるいはヒーターで加熱する方法、ジャケットに具備させ熱媒など流通させ温度制御する方法等を例示することができる。本発明の縦方向に回転するスキ型ショベル羽根を備えた横型チャンバー型の攪拌としては、太平洋機工(株)製のプロシェアミキサ(バッチ式あるいは連続式)を例示することができる。   In addition, an inert gas such as nitrogen may be circulated in the chamber to suppress a decrease in the color tone of the pellet. Examples of the method for changing the temperature of the horizontal chamber in various ways include a method in which heated inert gas is circulated and heated, a method in which heating is performed with a heater, a method in which a jacket is provided in a jacket and a heat medium is circulated to control temperature. . Examples of the horizontal chamber type agitation provided with the skid type shovel blade rotating in the vertical direction of the present invention include a proshear mixer (batch type or continuous type) manufactured by Taiheiyo Kiko Co., Ltd.

前記の本発明の方法で得られた熱可塑性樹脂ペレットの表面には、添加剤が強固にかつ均一にフィルム状に付着するという特徴を持つ。該「強固にかつ均一にフィルム状」という形態は、本質的にペレット表面にワニスを均一に塗布した状態の如き形態を有する。この形態は、例えばブレンダー等を用いて熱可塑性樹脂ペレットとミネラルオイルと添加剤などを混合しペレット表面に滑剤を付着させる方法(ブレンド法)とは、得られるペレット表面と全く異なる。   The surface of the thermoplastic resin pellet obtained by the method of the present invention is characterized in that the additive adheres firmly and uniformly in the form of a film. The form of “strongly and uniformly in the form of a film” has such a form that the varnish is essentially uniformly applied to the pellet surface. This form is completely different from the pellet surface obtained by, for example, blending thermoplastic resin pellets, mineral oil and additives using a blender or the like to attach a lubricant to the pellet surface.

この形態の差異は、ペレット表面を光学顕微鏡あるいは走査型電子顕微鏡(SEM)等の観察により確認できる。具体的なペレット表面の形態の差異を述べると、本発明の製造方法により得られたペレット表面は、前述の如く添加剤の境界が識別できないほど均一、連続的に塗布されているのに対し、前記従来のブレンド方法は添加剤が粒状、不均一、不連続に付着しているという大きな差異である。従って、本発明のペレットには、強固にかつ均一にフィルム状に添加剤が付着しているため、ニューマーなどを用いた移送あるいは射出成形などの各種成形において添加剤の脱落などが少なく、かつ各種成形での可塑化性、離型性、熱安定性等の性能やそれらのばらつきが少ないという優れた特徴を有する。   This difference in form can be confirmed by observing the pellet surface with an optical microscope or a scanning electron microscope (SEM). To describe specific differences in the form of the pellet surface, the pellet surface obtained by the production method of the present invention is applied uniformly and continuously so that the boundary of the additive cannot be identified as described above, The conventional blending method is greatly different in that the additive is granular, non-uniform, and discontinuously attached. Therefore, the pellets of the present invention have a strong and uniform film-like additive, so that there is little dropout of the additive in various moldings such as transfer or injection molding using a newer, etc. It has excellent characteristics such as plasticizing properties, mold release properties, thermal stability, etc. in molding, and few variations thereof.

本発明の製造方法により得られた熱可塑性樹脂ペレットは、公知の成形方法、例えばプレス成形、射出成形、ガスアシスト射出成形、溶着成形、押出成形、吹込成形、フィルム成形、中空成形、多層成形、溶融紡糸など、一般に知られているプラスチック成形方法を用いても、良好に成形加工ができる。中でも、射出成形性に優れる。   The thermoplastic resin pellets obtained by the production method of the present invention are known molding methods such as press molding, injection molding, gas assist injection molding, welding molding, extrusion molding, blow molding, film molding, hollow molding, multilayer molding, Even if a generally known plastic molding method such as melt spinning is used, molding can be performed satisfactorily. Especially, it is excellent in injection moldability.

以下、本発明を実施例により更に詳細に説明するが、本発明はその要旨を越えない限り、以下の実施例に制限されるものではない。なお、以下の実施例、比較例において記載した物性評価は、以下のように行った。   EXAMPLES Hereinafter, although an Example demonstrates this invention still in detail, this invention is not restrict | limited to a following example, unless the summary is exceeded. In addition, the physical property evaluation described in the following examples and comparative examples was performed as follows.

[参考実施例1]
スキ型ショベル羽根を備えた横型チャンバー型の攪拌機として、プローシェアーミキサ(太平洋機工株式会社製WB−75型(バッチ式))を用いた。ジャケットにはスチームを流通させ、ジャケット温度を80℃に保った。また、チャンバーには180℃に加熱できる添加剤用噴霧装置を具備した。添加剤としては、ジステアリン酸アルミニウム(融点約150℃)を用いた。該チャンバー中にポリアミドペレット(旭化成(株)製レオナ1300)を投入し密閉し、しばらく撹拌した。この時ペレット温度は約60℃であった。
その後、加熱溶融したジステアリン酸アルミニウムを所定量噴霧し、約1分間経った後、ペレットを排出した。該ペレット及びジャケット内部には、ダストはほとんど観測されなかった。また、得られたペレット表面を走査型電子顕微鏡写真で観測したところ、強固、均一にフィルム状に付着した形態で有ることが観測された。
[ Reference Example 1]
A proshear mixer (WB-75 type (batch type) manufactured by Taiheiyo Kiko Co., Ltd.) was used as a horizontal chamber type stirrer equipped with ski type shovel blades. Steam was circulated through the jacket, and the jacket temperature was kept at 80 ° C. The chamber was also equipped with an additive spraying device that could be heated to 180 ° C. As an additive, aluminum distearate (melting point: about 150 ° C.) was used. Polyamide pellets (Leona 1300 manufactured by Asahi Kasei Co., Ltd.) were put into the chamber, sealed, and stirred for a while. At this time, the pellet temperature was about 60 ° C.
Thereafter, a predetermined amount of aluminum melted distearate was sprayed, and after about 1 minute, the pellets were discharged. Little dust was observed inside the pellets and jacket. Further, when the obtained pellet surface was observed with a scanning electron micrograph, it was observed that the pellet surface was firmly and uniformly attached to the film.

[参考実施例2]
添加剤として、ジステアリン酸アルミニウムとN−ステアリルエルカ酸アミド(融点約70℃)の重量比1/1の混合物を用いる以外は実施例1と同様にして実施した。得られたペレット表面を走査型電子顕微鏡写真で観測したところ、強固、均一にフィルム状に付着した形態で有ることが観測された。
[ Reference Example 2]
The same procedure as in Example 1 was performed except that a mixture of aluminum distearate and N-stearylerucamide (melting point: about 70 ° C.) in a weight ratio of 1/1 was used as an additive. When the obtained pellet surface was observed with a scanning electron micrograph, it was observed that the pellet surface was firmly and uniformly attached to the film.

[実施例3]
スキ型ショベル羽根を備えた横型チャンバー型の攪拌機として、プローシェアーミキサ(太平洋機工株式会社製WA-75型(連続式))を用いた。また、チャンバーには180℃に加熱できる添加剤用噴霧装置及び添加剤を粉体添加できる装置を具備した。添加剤としては、N-ステアリルエルカ酸アミド(N-パルミチルエルカ酸アミド含有物,融点約70℃)およびジステアリン酸アルミニウムを用いた。該チャンバー中にポリアミドペレット(旭化成(株)製レオナ1300)を連続的に投入し、帯電防止剤であるポリエチレングリコール(分子量400)を所定量液滴添加し、120℃に加熱溶融したN-ステアリルエルカ酸アミドを所定量噴霧し、直後にジステアリン酸アルミニウム粉末を所定量添加し、吐出量約1トン/hrでペレットを排出した。該ペレット及びジャケット内部には、ダストはほとんど観測されなかった。また、得られたペレット表面を走査型電子顕微鏡写真で観測したところ、固体粉末が浮き出ることなく、均一にフィルム状に付着した形態で有ることが観測された。
[Example 3]
A proshear mixer (WA-75 type (continuous type) manufactured by Taiheiyo Kiko Co., Ltd.) was used as a horizontal chamber type stirrer equipped with ski type shovel blades. Further, the chamber was equipped with an additive spraying apparatus that can be heated to 180 ° C. and an apparatus that can add powder of the additive. As additives, N-stearyl erucamide (containing N-palmitylerucamide, melting point: about 70 ° C.) and aluminum distearate were used. Polyamide pellets (Leona 1300 manufactured by Asahi Kasei Co., Ltd.) are continuously charged into the chamber, and a predetermined amount of a drop of polyethylene glycol (molecular weight 400) as an antistatic agent is added, and N-stearyl is heated and melted at 120 ° C. A predetermined amount of erucamide was sprayed, and immediately after that, a predetermined amount of aluminum distearate powder was added, and the pellets were discharged at a discharge rate of about 1 ton / hr. Little dust was observed inside the pellets and jacket. Further, when the obtained pellet surface was observed with a scanning electron micrograph, it was observed that the solid powder was uniformly attached in the form of a film without being raised.

[実施例4]
粉末添加する添加剤として、ジステアリン酸アルミニウム、Irganox1098(チバ・スペシャルティ・ケミカルズ(株)社製N,N‘-ヘキサン-1,6-ジイルビス[3-(3,5-ジ-tert-ブチル-4-ヒドロキシフェニル)プロピオアミド])の重量比1/1を用いる以外は実施例3と同様にして行った。該ペレット及びジャケット内部には、ダストはほとんど観測されなかった。また、得られたペレット表面を走査型電子顕微鏡写真で観測したところ、固体粉末が浮き出ることなく、均一にフィルム状に付着した形態で有ることが観測された。
[Example 4]
As an additive to be added as a powder, aluminum distearate, Irganox 1098 (Ciba Specialty Chemicals Co., Ltd. N, N'-hexane-1,6-diylbis [3- (3,5-di-tert-butyl-4) -Hydroxyphenyl) propioamide]) in the same manner as in Example 3 except that a weight ratio of 1/1 was used. Little dust was observed inside the pellets and jacket. Further, when the obtained pellet surface was observed with a scanning electron micrograph, it was observed that the solid powder was uniformly attached in the form of a film without being raised.

本発明の方法は、熱可塑性樹脂ペレット表面に添加剤を均一に付着させることに好適に利用できる。   The method of the present invention can be suitably used for uniformly attaching an additive to the surface of a thermoplastic resin pellet.

Claims (5)

スキ型ショベル羽根を備えた横型チャンバー型の攪拌機に添加剤を加熱溶融噴霧する設備と粉体添加する設備を具備した装置を用いて、添加剤の加熱溶融噴霧添加および粉体添加を行い、熱可塑性樹脂ペレット表面に添加剤を付着させ、添加剤を含有する熱可塑性樹脂ペレットを得る製造方法。 Using an apparatus equipped with a horizontal chamber type stirrer equipped with a skive type shovel blade and equipment for heating and spraying the additive and equipment for adding powder, the heat melting and spraying of the additive and powder addition are performed. A production method for obtaining a thermoplastic resin pellet containing an additive by attaching an additive to the surface of the plastic resin pellet. 熱可塑性樹脂が、ポリアミド樹脂、ポリフェニレンエーテル樹脂、ポリオキシメチレン樹脂、芳香族ポリエステル樹脂、芳香族ポリカーボネート樹脂、ポリフェニレンスルフィド樹脂、ポリオレフィン樹脂、スチレン樹脂、アクリル樹脂、ゴムのいずれかから選ばれた少なくとも1種のペレットであることを特徴とする請求項1に記載の製造方法。 The thermoplastic resin is at least one selected from polyamide resin, polyphenylene ether resin, polyoxymethylene resin, aromatic polyester resin, aromatic polycarbonate resin, polyphenylene sulfide resin, polyolefin resin, styrene resin, acrylic resin, and rubber. The production method according to claim 1, which is a seed pellet. 添加剤が、ヒンダードフェノール化合物、ヒンダードアミン化合物、有機ホスファイト化合物、高級脂肪酸金属塩、高級脂肪酸アミド、高級脂肪酸エステルから選ばれる少なくとも1種の化合物であることを特徴とする請求項1または2に記載の製造方法。 Additives, hindered phenol compounds, hindered amine compounds, organic phosphite compounds, higher fatty acid metal salts, higher fatty acid amides, that to claim 1 or 2, characterized in that at least one compound selected from higher fatty acid esters The manufacturing method as described. 添加剤の添加方法を、加熱溶融噴霧添加、粉体添加の順に行うことを特徴とする請求項1〜3いずれかに記載の製造方法。 The manufacturing method according to any one of claims 1 to 3 , wherein the additive is added in the order of hot melt spray addition and powder addition. 粉体添加する添加剤が、加熱溶融噴霧添加する添加剤より高融点であることを特徴とする請求項4記載の製造方法。The manufacturing method according to claim 4, wherein the additive to be added with a powder has a higher melting point than the additive to be added by heating and melt spraying.
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