JP2009057410A - Production method for methacrylic resin molding material - Google Patents
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- JP2009057410A JP2009057410A JP2007223701A JP2007223701A JP2009057410A JP 2009057410 A JP2009057410 A JP 2009057410A JP 2007223701 A JP2007223701 A JP 2007223701A JP 2007223701 A JP2007223701 A JP 2007223701A JP 2009057410 A JP2009057410 A JP 2009057410A
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
- C08J7/04—Coating
- C08J7/06—Coating with compositions not containing macromolecular substances
- C08J7/065—Low-molecular-weight organic substances, e.g. absorption of additives in the surface of the article
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/16—Nitrogen-containing compounds
- C08K5/20—Carboxylic acid amides
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L33/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
- C08L33/04—Homopolymers or copolymers of esters
- C08L33/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, which oxygen atoms are present only as part of the carboxyl radical
- C08L33/10—Homopolymers or copolymers of methacrylic acid esters
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2333/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
- C08J2333/04—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters
- C08J2333/06—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters of esters containing only carbon, hydrogen, and oxygen, the oxygen atom being present only as part of the carboxyl radical
- C08J2333/10—Homopolymers or copolymers of methacrylic acid esters
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- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Description
本発明は、メタクリル樹脂成形材料を製造する方法に関するものである。 The present invention relates to a method for producing a methacrylic resin molding material.
メタクリル樹脂は、その優れた透明性や耐候性を活かして、従来から車両のランプカバー、照明カバー、看板、光学レンズ、導光体、透明食器等に使用されている。また最近では、その透明性を活かして、比較的肉厚の厚い置物や容器、アクセサリー等にも用いられている。これらメタクリル樹脂成形体の製造は、射出成形法により行われることが多く、その成形材料として、メタクリル樹脂は、ペレットに加工され、供給されている。 Methacrylic resins have been used for vehicle lamp covers, lighting covers, signboards, optical lenses, light guides, transparent tableware and the like, taking advantage of their excellent transparency and weather resistance. Moreover, recently, taking advantage of its transparency, it is also used for relatively thick figurines, containers and accessories. Production of these methacrylic resin molded bodies is often performed by an injection molding method, and methacrylic resin is processed into pellets and supplied as a molding material.
ここで、典型的な射出成形法について概略を説明すると、このために用いる射出成形装置は、金型と、この金型を型閉じ方向又は型開き方向に駆動する型締め装置と、型締めされた金型に溶融樹脂を射出する射出装置とで構成される。金型は、可動側型板と固定側型板とで構成され、固定側型板には、溶融樹脂を通過させるためのスプルーが形成され、可動側型板と固定側型板とのパーティングラインに沿ってランナーとゲートが形成され、両型板の間に製品を成形するためのキャビティーが形成されている。また、固定側型板には、溶融樹脂を保温したまま通過させるためのホットランナーを設置し、さらにホットチップを通じて、溶融樹脂がパーティングラインに沿って形成されたゲートまで達するように構成する方法もある。可動側型板には、形成された成形品を取り出すための突出し手段が設けられる。射出装置は、成形材料を可塑化溶融させ、金型のキャビティー内に射出充填するためのものであって、シリンダー、その中で回転駆動するように設けられたスクリュー、シリンダーの先端部に取り付けられた射出ノズル、シリンダーに成形材料を供給するホッパー、スクリューを回転駆動するモーター、スクリューを前進駆動するラム機構等で構成されている。そして、シリンダーの外周部には、内部の成形材料を溶融するためにヒーターが設けられている。 Here, an outline of a typical injection molding method will be described. An injection molding apparatus used for this purpose is a mold, a mold clamping device that drives the mold in a mold closing direction or a mold opening direction, and a mold clamping. And an injection device for injecting molten resin into the mold. The mold is composed of a movable side mold plate and a fixed side mold plate. The fixed side mold plate is formed with a sprue for allowing molten resin to pass through. The parting of the movable side mold plate and the fixed side mold plate is performed. A runner and a gate are formed along the line, and a cavity for forming a product is formed between the two mold plates. In addition, a hot runner for allowing the molten resin to pass through while maintaining the temperature is installed in the fixed side template, and further, the molten resin reaches the gate formed along the parting line through the hot tip. There is also. The movable mold plate is provided with a protruding means for taking out the formed product. The injection device is for plasticizing and melting the molding material and injection filling it into the cavity of the mold. The injection device is attached to the cylinder, the screw provided to rotate in it, and the tip of the cylinder. The injection nozzle, the hopper for supplying the molding material to the cylinder, the motor for rotationally driving the screw, the ram mechanism for driving the screw forward, and the like. A heater is provided on the outer periphery of the cylinder to melt the molding material inside.
成形材料は、スクリューの回転駆動によりシリンダー内に供給され、通電されたヒーターにより加熱され、またスクリューの回転による剪断摩擦熱や加圧作用を受けて、溶融混練され、スクリューの先端に送られて蓄積される。そのとき溶融樹脂がスクリュー先端に蓄積された樹脂圧力によってスクリューは徐々に後方へ下がり、所望の位置に達すると停止する。スクリューが徐々に回転しながら後方へ下がる時には、適度の背圧をスクリュー後方から加圧することにより、溶融樹脂の分解ガスや巻き込んだ空気、水蒸気等を後方へ排気しホッパー部から脱気する。次いで、ラム機構によりスクリューを前進駆動して、ノズルから金型のキャビティーに溶融樹脂を射出充填し、そして溶融樹脂の冷却固化に伴う体積収縮分を補うための保圧力を付与する。その後引き続いて、成形品の金型内での冷却と次の成形のための溶融樹脂の計量を併行して行う。冷却完了後、可動側型板を移動させ、金型を開いて成形品を取り出す。 The molding material is supplied into the cylinder by the rotational drive of the screw, heated by an energized heater, melted and kneaded under shear frictional heat and pressure action due to the rotation of the screw, and sent to the tip of the screw. Accumulated. At that time, the screw gradually descends backward due to the resin pressure accumulated in the tip of the molten resin, and stops when the desired position is reached. When the screw descends while gradually rotating, an appropriate back pressure is applied from the rear of the screw to exhaust the molten resin decomposition gas, entrained air, water vapor, and the like to the rear and deaerate it from the hopper. Next, the screw is driven forward by the ram mechanism, the molten resin is injected and filled from the nozzle into the cavity of the mold, and a holding pressure for compensating the volume shrinkage accompanying cooling and solidification of the molten resin is applied. Subsequently, the cooling of the molded product in the mold and the measurement of the molten resin for the next molding are performed simultaneously. After completion of cooling, the movable side mold plate is moved, the mold is opened, and the molded product is taken out.
このような射出成形法では、比較的肉厚の厚い又は製品体積の大きい成形体を製造する場合、成形材料を上記のようにスクリューの先端に送って蓄積する工程(可塑化工程)で、多量に溶融樹脂としてシリンダー内に蓄積する必要があり、長い時間をかけて計量することになる。また金型内に充填された溶融樹脂を金型表面との熱交換によって冷却するときに、成形体の中心層まで充分に冷却固化させないで取り出すと、メタクリル樹脂の成形収縮によって所定の寸法が得られないことがあるため、長時間の冷却時間が必要となり、1サイクルの時間が長くなる。 In such an injection molding method, when a molded product having a relatively large thickness or a large product volume is produced, a large amount of the molding material is sent to the tip of the screw and accumulated as described above (plasticization step). It is necessary to accumulate in the cylinder as a molten resin, and it takes a long time to measure. Also, when the molten resin filled in the mold is cooled by heat exchange with the mold surface, if the molten resin is taken out to the center layer of the molded body without sufficiently cooling and solidifying, a predetermined dimension can be obtained by molding shrinkage of the methacrylic resin. Since it may not be possible, a long cooling time is required and the time for one cycle becomes long.
こうして成形材料を溶融状態で長時間シリンダー内に蓄積すると、成形材料が全体として必要以上に溶融するので、スクリューの溝に滞留している半溶融成形材料(ソリッド)とシリンダー内壁との粘着が上がり、溶融樹脂の前方への移送がし難くなる。またスクリューの供給ゾーンでは早期に成形材料が溶融するので溶融被膜がスクリュー外周に形成され易くなって、計量中の分解ガスや水蒸気を後方へ脱気し難くなる。すると、移送が遅れることでより成形材料の分解が促進されてガスの発生が著しく上昇し、脱気不足により分解ガスや空気を巻き込み包含したまま、スクリュー先端部に溶融樹脂が蓄積されることになる。そして、そのような溶融樹脂を金型内に充填すると、成形体の内部に気泡が発生したり、成形体の表面に気泡に由来するシルバーと呼ばれる銀条に光って見える欠陥が生じたりすることがある。 If the molding material is accumulated in the cylinder for a long time in a molten state in this way, the molding material will melt more than necessary, and the adhesion between the semi-molten molding material (solid) staying in the screw groove and the cylinder inner wall will increase. It becomes difficult to transfer the molten resin forward. Further, since the molding material is melted at an early stage in the screw supply zone, a molten coating is easily formed on the outer periphery of the screw, and it is difficult to degas the cracked gas and water vapor during measurement. Then, the decomposition of the molding material is accelerated by delaying the transfer, and the generation of gas is remarkably increased, and the molten resin is accumulated at the tip of the screw while containing the decomposition gas and air due to insufficient degassing. Become. And when such a molten resin is filled in the mold, bubbles may be generated inside the molded body, or defects that appear to shine on the silver strip called silver derived from the bubbles may be generated on the surface of the molded body. There is.
このような問題を解決するため、例えば、特開平8−217945号公報(特許文献1)には、メタクリル樹脂ペレットの表面にアミド化合物を添着させ、該添着後の安息角を所定範囲に調整したものを、成形材料として用いることが提案されている。しかしながら、得られるメタクリル樹脂成形材料の安息角が均一になり難く、該成形材料を射出成形に適用した場合に、気泡やシルバーの発生を抑制する効果が安定して得られ難いという問題があった。 In order to solve such problems, for example, in JP-A-8-217945 (Patent Document 1), an amide compound is attached to the surface of a methacrylic resin pellet, and the angle of repose after the attachment is adjusted to a predetermined range. It has been proposed to use those as molding materials. However, the angle of repose of the obtained methacrylic resin molding material is difficult to be uniform, and there is a problem that when the molding material is applied to injection molding, it is difficult to stably obtain the effect of suppressing the generation of bubbles and silver. .
そこで、本発明の目的は、安息角の均一性が高いメタクリル樹脂成形材料を製造しうる方法を提供することにある。 Accordingly, an object of the present invention is to provide a method capable of producing a methacrylic resin molding material having high repose angle uniformity.
本発明者らは、鋭意研究を行った結果、メタクリル樹脂ペレットの表面に所定の温度以上でアミド化合物を添着させることにより、上記目的を達成できることを見出し、本発明を完成するに至った。 As a result of intensive studies, the present inventors have found that the above object can be achieved by attaching an amide compound to the surface of a methacrylic resin pellet at a predetermined temperature or higher, and have completed the present invention.
すなわち、本発明は、メタクリル樹脂ペレットの表面に35℃以上でアミド化合物を添着させることを特徴とするメタクリル樹脂成形材料の製造方法を提供するものである。 That is, the present invention provides a method for producing a methacrylic resin molding material, characterized in that an amide compound is attached to the surface of a methacrylic resin pellet at 35 ° C. or higher.
本発明によれば、安息角の均一性が高いメタクリル樹脂成形材料を製造することができる。 According to the present invention, a methacrylic resin molding material with high repose angle uniformity can be manufactured.
以下、本発明を詳細に説明する。本発明で原料に用いるメタクリル樹脂ペレットは、メタクリル樹脂又はこれに離型剤、紫外線吸収剤、顔料、酸化防止剤、難燃剤等が配合されてなるメタクリル樹脂組成物のペレット(粒状物)である。 Hereinafter, the present invention will be described in detail. The methacrylic resin pellet used as a raw material in the present invention is a methacrylic resin or a pellet (granular material) of a methacrylic resin composition in which a release agent, an ultraviolet absorber, a pigment, an antioxidant, a flame retardant, and the like are blended. .
メタクリル樹脂は、メタクリル酸メチルを主成分とする単量体、具体的にはメタクリル酸メチル50重量%以上を含む単量体を重合させて得られる重合体であって、メタクリル酸メチルの単独重合体であってもよいし、メタクリル酸メチル50重量%以上とこれ以外の単量体50重量%以下との共重合体であってもよい。メタクリル酸メチル以外の単量体としては、例えば、メタクリル酸エチル、メタクリル酸プロピル、メタクリル酸ブチル、メタクリル酸ベンジル、メタクリル酸2−エチルヘキシル、メタクリル酸シクロヘキシル、メタクリル酸ボルニル、メタクリル酸アダマンチル、メタクリル酸シクロペンタジエニルのようなメタクリル酸エステル類;アクリル酸メチル、アクリル酸エチル、アクリル酸プロピル、アクリル酸ブチル、アクリル酸ベンジル、アクリル酸2−エチルヘキシル、アクリル酸シクロヘキシル、アクリル酸ボルニル、アクリル酸アダマンチル、アクリル酸シクロペンタジエニルのようなアクリル酸エステル類;アクリル酸、メタクリル酸、マレイン酸、イタコン酸、無水マレイン酸、無水イタコン酸のような不飽和カルボン酸やその酸無水物;アクリル酸2−ヒドロキシエチル、アクリル酸2−ヒドロキシプロピル、アクリル酸モノグリセロール、メタクリル酸2−ヒドロキシエチル、メタクリル酸2−ヒドロキシプロピル、メタクリル酸モノグリセロールのようなヒドロキシル基含有単量体;アクリルアミド、メタクリルアミド、アクリルニトリル、メタクリロニトリル、ジアセトンアクリルアミド、メタクリル酸ジメチルアミノエチルのような窒素含有単量体;アリルグリシジルエーテル、アクリル酸グリシジル、メタクリル酸グリシジルのようなエポキシ基含有単量体;スチレン、α−メチルスチレンのようなスチレン系単量体等が挙げられる。 A methacrylic resin is a polymer obtained by polymerizing a monomer containing methyl methacrylate as a main component, specifically, a monomer containing 50% by weight or more of methyl methacrylate. It may be a coalescence or a copolymer of 50% by weight or more of methyl methacrylate and 50% by weight or less of other monomers. Examples of monomers other than methyl methacrylate include, for example, ethyl methacrylate, propyl methacrylate, butyl methacrylate, benzyl methacrylate, 2-ethylhexyl methacrylate, cyclohexyl methacrylate, bornyl methacrylate, adamantyl methacrylate, and cyclohexane methacrylate. Methacrylic acid esters such as pentadienyl; methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, benzyl acrylate, 2-ethylhexyl acrylate, cyclohexyl acrylate, bornyl acrylate, adamantyl acrylate, acrylic Acrylic esters such as cyclopentadienyl; unsaturated carboxylic acids such as acrylic acid, methacrylic acid, maleic acid, itaconic acid, maleic anhydride, itaconic anhydride, Acid anhydrides; hydroxyl group-containing monomers such as 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, monoglycerol acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl methacrylate, monoglycerol methacrylate Nitrogen-containing monomers such as acrylamide, methacrylamide, acrylonitrile, methacrylonitrile, diacetone acrylamide, and dimethylaminoethyl methacrylate; Epoxy group-containing monomers such as allyl glycidyl ether, glycidyl acrylate, and glycidyl methacrylate Body; styrene-based monomers such as styrene and α-methylstyrene.
メタクリル樹脂の製造は、例えば塊状重合法により行うことができ、中でも連続塊状重合法により行うことが好ましい。連続混合重合法によれば、不純物を極力減らし透明性を向上させたメタクリル樹脂を製造することができ、これを成形して得られるストランドを切断することによりメタクリル樹脂ペレットを製造することができる。この場合の成形は、例えば、一軸押出機、二軸押出機又は脱気押出機のような、加熱可能なシリンダーとその内に回転するスクリューを有する押出成形機の出口に複数の孔を有するダイを設置した装置を用いて行うことができる。 The production of the methacrylic resin can be performed, for example, by a bulk polymerization method, and among them, it is preferably performed by a continuous bulk polymerization method. According to the continuous mixed polymerization method, it is possible to produce a methacrylic resin having as few impurities as possible and improving the transparency, and it is possible to produce a methacrylic resin pellet by cutting a strand obtained by molding this. The molding in this case is a die having a plurality of holes at the outlet of an extruder having a heatable cylinder and a screw rotating in the same, such as a single screw extruder, a twin screw extruder or a degassing extruder. Can be carried out using an apparatus in which
こうして得られる溶融状態のストランドは、例えば、水流ストランドカット方式により冷却され、切断されて、直径が2〜4mmで長さが2〜5mmのペレット(成形材料)となる。ここで用いる水流ストランドカット方式とは、溶融状態のストランドを、冷却水によって水膜が形成された流下シュート上を流下させて冷却し、これを切断してペレットとする方法である。 The melted strand thus obtained is cooled and cut by, for example, a water stream strand cutting method to form pellets (molding material) having a diameter of 2 to 4 mm and a length of 2 to 5 mm. The water stream strand cutting method used here is a method in which a melted strand is cooled by flowing down a flowing chute on which a water film is formed with cooling water, and then cut into pellets.
また、メタクリル樹脂を押出成形機で溶融混練した後、ダイ孔から押し出し、該押出物が所定長さになったときに切断する方法により、メタクリル樹脂ペレットを製造してもよい。 Alternatively, the methacrylic resin pellets may be produced by a method in which the methacrylic resin is melt-kneaded with an extruder and then extruded from a die hole and cut when the extrudate reaches a predetermined length.
こうして得られるメタクリル樹脂ペレットの表面に、アミド化合物を添着させることにより、メタクリル樹脂成形材料を製造するが、本発明では、その添着温度を35℃以上とする。このように所定の温度以上でメタクリル樹脂ペレット表面にアミド化合物を添着させることにより、得られるメタクリル樹脂成形材料の安息角の均一性を高めることができ、ひいては該成形材料を射出成形に適用したとき、気泡やシルバーの発生を抑制する効果を安定して得ることができる。添着温度は、好ましくは40〜100℃であり、より好ましくは40〜80℃である。 A methacrylic resin molding material is produced by adhering an amide compound to the surface of the methacrylic resin pellet thus obtained. In the present invention, the adhering temperature is set to 35 ° C. or higher. By attaching an amide compound to the surface of the methacrylic resin pellets at a predetermined temperature or more in this way, the uniformity of the angle of repose of the resulting methacrylic resin molding material can be improved, and as a result, when the molding material is applied to injection molding The effect of suppressing the generation of bubbles and silver can be stably obtained. The adhesion temperature is preferably 40 to 100 ° C, more preferably 40 to 80 ° C.
アミド化合物は、例えば、モノアミド化合物であってもよいし、ビスアミド化合物であってもよいが、ビスアミド化合物が好ましく用いられる。モノアミド化合物としては、RCONH2(Rは1価の脂肪族炭化水素基を表す)で示される脂肪族モノアミド化合物が好ましく用いられ、その例としては、ステアリン酸アミド、パルミチン酸アミド、オレイン酸アミド、エルカ酸アミド等が挙げられる。また、ビスアミド化合物としては、R1CONH−R2−NHCOR3(R1及びR3はそれぞれ1価の脂肪族炭化水素基を表し、R2は2価の脂肪族炭化水素基を表す)で示される脂肪族ビスアミド化合物が好ましく用いられ、その例としては、メチレンビスステアリン酸アミド、エチレンビスステアリン酸アミド、エチレンビスオレイン酸アミド、ヘキサメチレンビスステアリン酸アミド、メチレンビスステアリン酸アミド、エチレンビスステアリン酸アミド等が挙げられる。 The amide compound may be, for example, a monoamide compound or a bisamide compound, but a bisamide compound is preferably used. As the monoamide compound, an aliphatic monoamide compound represented by RCONH 2 (R represents a monovalent aliphatic hydrocarbon group) is preferably used. Examples thereof include stearic acid amide, palmitic acid amide, oleic acid amide, And erucic acid amide. The bisamide compound is R 1 CONH—R 2 —NHCOR 3 (R 1 and R 3 each represent a monovalent aliphatic hydrocarbon group, and R 2 represents a divalent aliphatic hydrocarbon group). The aliphatic bisamide compounds shown are preferably used, and examples thereof include methylene bis stearamide, ethylene bis stearamide, ethylene bis oleate amide, hexamethylene bis stearamide, methylene bis stearamide, ethylene bis stearamide. Examples include acid amides.
アミド化合物の使用量は、メタクリル樹脂ペレット100重量部に対し、通常0.003〜0.5重量部、好ましくは0.008〜0.015重量部である。アミド化合物の使用量があまり少ないと、得られるメタクリル樹脂成形材料を射出成形に適用したとき、気泡やシルバーの発生を抑制する効果が得られ難くなる。また、アミド化合物の使用量があまり多いと、得られるメタクリル樹脂成形材料を射出成形に適用したとき、滑り過ぎて計量し難くなる。 The amount of the amide compound used is usually 0.003 to 0.5 parts by weight, preferably 0.008 to 0.015 parts by weight, based on 100 parts by weight of the methacrylic resin pellets. If the amount of the amide compound used is too small, when the resulting methacrylic resin molding material is applied to injection molding, it is difficult to obtain the effect of suppressing the generation of bubbles and silver. If the amount of the amide compound used is too large, when the resulting methacrylic resin molding material is applied to injection molding, it is too slippery to measure.
また、アミド化合物は、その融点が30〜200℃であるのが好ましく、70〜170℃であるのがより好ましい。この融点があまり低いと、得られるメタクリル樹脂成形材料がべたつき易くなる。また、この融点があまり高いと、メタクリル樹脂ペレットに添着させ難くなる。 Moreover, it is preferable that the melting point of an amide compound is 30-200 degreeC, and it is more preferable that it is 70-170 degreeC. If this melting point is too low, the resulting methacrylic resin molding material will be sticky. Moreover, when this melting | fusing point is too high, it will become difficult to attach to a methacryl resin pellet.
メタクリル樹脂ペレットの表面にアミド化合物を添着させる方法としては、例えば、メタクリル樹脂ペレットとアミド化合物を攪拌等により混合する方法や、メタクリル樹脂ペレットにアミド化合物を噴霧する方法等が挙げられる。その際、アミド化合物としては、その水溶液を用いてもよく、この場合、添着後に乾燥を行うのがよい。また、添着は、メタクリル樹脂を射出成形機のホッパー等に蓄積する前に行ってもよいし、蓄積した後に行ってもよい。 Examples of the method of attaching the amide compound to the surface of the methacrylic resin pellet include a method of mixing the methacrylic resin pellet and the amide compound by stirring, a method of spraying the amide compound on the methacrylic resin pellet, and the like. At that time, as the amide compound, an aqueous solution thereof may be used. Further, the attachment may be performed before the methacrylic resin is accumulated in the hopper of the injection molding machine or after the accumulation.
添着温度は、例えば、添着前にメタクリル樹脂ペレット及び/又はアミド化合物を加熱することにより調整してもよいし、添着系内の雰囲気ガスを加熱することにより調整してもよく、これらの加熱を、添着時のペレット温度、具体的にはペレットの表面温度が、上記所定の添着温度になるように行えばよい。なお、添着時間は適宜調整されるが、通常10秒〜10分程度である。 The adhesion temperature may be adjusted, for example, by heating the methacrylic resin pellets and / or the amide compound before the adhesion, or may be adjusted by heating the atmospheric gas in the adhesion system. The pellet temperature at the time of attachment, specifically, the surface temperature of the pellet may be set to the predetermined attachment temperature. The attaching time is appropriately adjusted, but is usually about 10 seconds to 10 minutes.
こうして得られるメタクリル樹脂成形材料は、必要に応じて予備乾燥等の前処理に付した後、射出成形を始めとする溶融成形用の材料として、好適に用いることができる。特に比較的肉厚の厚い(例えば3mm以上)又は製品体積の大きい成形体を製造するための射出成形用の材料として、好適に用いることができる。 The methacrylic resin molding material thus obtained can be suitably used as a material for melt molding including injection molding after being subjected to pretreatment such as preliminary drying as necessary. In particular, it can be suitably used as a material for injection molding for producing a molded product having a relatively large thickness (for example, 3 mm or more) or a large product volume.
以下、本発明の実施例を示すが、本発明はこれらによって限定されるものではない。 Examples of the present invention will be described below, but the present invention is not limited thereto.
実施例1〜3、比較例1
メタクリル樹脂ペレットとして、住友化学株式会社製の“スミペックスLG2”(透明)を使用した。また、アミド化合物として、花王株式会社製の“カオーワックスEB−FF”(エチレンビスステアリン酸アミド、融点141.5〜146.5℃)を使用した。
Examples 1-3, Comparative Example 1
As a methacrylic resin pellet, “SUMIPEX LG2” (transparent) manufactured by Sumitomo Chemical Co., Ltd. was used. As the amide compound, “Kao wax EB-FF” (ethylene bis stearamide, melting point: 141.5 to 146.5 ° C.) manufactured by Kao Corporation was used.
メタクリル樹脂ペレット3000gを、オーブンで表1に示す温度に加熱した後、ポリ袋に入れ、次いでアミド化合物0.36gを添加し、ポリ袋の口を閉じて30秒間振り混ぜた。このときのポリ袋内のペレットの温度を測定し、添着温度として表1に示した。 After 3000 g of methacrylic resin pellets were heated in an oven to the temperature shown in Table 1, they were put in a plastic bag, 0.36 g of an amide compound was added, and the mouth of the plastic bag was closed and shaken for 30 seconds. The temperature of the pellet in the plastic bag at this time was measured and shown in Table 1 as the attaching temperature.
ポリ袋の中からアミド化合物が添着されたペレットを300gずつ8回採取し、各サンプルを室温にて一晩(約15時間)放置した後、各サンプルから200gを採取し、その安息角を回転式安息角測定器を用いて測定した。各サンプルの安息角を、その平均値及び標準偏差と共に表1に示した。なお、アミド化合物未添着のペレットの安息角は36°であった。 Collect 300g of pellets each containing amide compound from a plastic bag 8 times, leave each sample overnight at room temperature (about 15 hours), then collect 200g from each sample and rotate its angle of repose It measured using the type | formula repose angle measuring device. The angle of repose of each sample is shown in Table 1 together with its average value and standard deviation. The angle of repose of the pellets not attached with the amide compound was 36 °.
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Citations (8)
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JPH0284454A (en) * | 1988-09-20 | 1990-03-26 | Nippon Steel Chem Co Ltd | Resin pellet and production thereof |
JPH04501089A (en) * | 1988-10-19 | 1992-02-27 | ザ ダウ ケミカル カンパニー | Plastic pellets coated with processing aids and coating method |
JPH08500549A (en) * | 1992-09-01 | 1996-01-23 | イー・アイ・デュポン・ドゥ・ヌムール・アンド・カンパニー | Lubricant-containing pellets of thermoplastics, method of making and use thereof |
JPH08217945A (en) * | 1995-02-15 | 1996-08-27 | Asahi Chem Ind Co Ltd | Methacrylic resin molding material excellent in molding stability |
JP2000302937A (en) * | 1999-04-23 | 2000-10-31 | Kanegafuchi Chem Ind Co Ltd | Flexible resin pellet |
JP2003320528A (en) * | 2002-04-30 | 2003-11-11 | Mitsubishi Chemicals Corp | Thermoplastic resin pellet |
JP2004169027A (en) * | 2002-11-08 | 2004-06-17 | Asahi Kasei Chemicals Corp | Manufacturing method of thermoplastic resin pellet containing additive |
JP2004168056A (en) * | 2002-11-08 | 2004-06-17 | Asahi Kasei Chemicals Corp | Manufacturing method for additive-containing thermoplastic resin pellet |
-
2007
- 2007-08-30 JP JP2007223701A patent/JP5272354B2/en not_active Expired - Fee Related
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2008
- 2008-08-14 SG SG200806093-1A patent/SG150473A1/en unknown
- 2008-08-21 KR KR1020080081826A patent/KR101551977B1/en active IP Right Grant
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH0284454A (en) * | 1988-09-20 | 1990-03-26 | Nippon Steel Chem Co Ltd | Resin pellet and production thereof |
JPH04501089A (en) * | 1988-10-19 | 1992-02-27 | ザ ダウ ケミカル カンパニー | Plastic pellets coated with processing aids and coating method |
JPH08500549A (en) * | 1992-09-01 | 1996-01-23 | イー・アイ・デュポン・ドゥ・ヌムール・アンド・カンパニー | Lubricant-containing pellets of thermoplastics, method of making and use thereof |
JPH08217945A (en) * | 1995-02-15 | 1996-08-27 | Asahi Chem Ind Co Ltd | Methacrylic resin molding material excellent in molding stability |
JP2000302937A (en) * | 1999-04-23 | 2000-10-31 | Kanegafuchi Chem Ind Co Ltd | Flexible resin pellet |
JP2003320528A (en) * | 2002-04-30 | 2003-11-11 | Mitsubishi Chemicals Corp | Thermoplastic resin pellet |
JP2004169027A (en) * | 2002-11-08 | 2004-06-17 | Asahi Kasei Chemicals Corp | Manufacturing method of thermoplastic resin pellet containing additive |
JP2004168056A (en) * | 2002-11-08 | 2004-06-17 | Asahi Kasei Chemicals Corp | Manufacturing method for additive-containing thermoplastic resin pellet |
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KR101551977B1 (en) | 2015-09-09 |
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