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JPH0319260B2 - - Google Patents
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JPH0319260B2 - - Google Patents

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Publication number
JPH0319260B2
JPH0319260B2 JP55079732A JP7973280A JPH0319260B2 JP H0319260 B2 JPH0319260 B2 JP H0319260B2 JP 55079732 A JP55079732 A JP 55079732A JP 7973280 A JP7973280 A JP 7973280A JP H0319260 B2 JPH0319260 B2 JP H0319260B2
Authority
JP
Japan
Prior art keywords
resin
pellets
molding
fatty acid
higher fatty
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 - Lifetime
Application number
JP55079732A
Other languages
Japanese (ja)
Other versions
JPS576712A (en
Inventor
Yozo Kitagawa
Hideyuki Hatsutori
Akio Matsuda
Minoru Maeda
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.)
JSR Corp
Original Assignee
Japan Synthetic Rubber Co Ltd
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 Japan Synthetic Rubber Co Ltd filed Critical Japan Synthetic Rubber Co Ltd
Priority to JP7973280A priority Critical patent/JPS576712A/en
Publication of JPS576712A publication Critical patent/JPS576712A/en
Publication of JPH0319260B2 publication Critical patent/JPH0319260B2/ja
Granted legal-status Critical Current

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  • Processes Of Treating Macromolecular Substances (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

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

本発明は熱可塑性樹脂ペレツトに関し、詳しく
はスチレン系熱可塑性樹脂のペレツト表面に極く
少量の特定の化合物を均一に付着させた状態で成
形品の成形に供する成形加工性に優れた熱可塑性
樹脂ペレツトに関するものである。更に詳しく
は、射出成形または押出成形時に於て、ペレツト
の流動性、樹脂溶融速度の不均一性,可塑化時の
剪断発熱等が原因となつて発生する、成形品のシ
ルバーストリーク、ガスリ、ヤケ等の現象を未然
に防ぐことのできるスチレン系熱可塑性樹脂ペレ
ツトを提供することにある。 従来、スチレン系熱可塑性樹脂の成形加工性を
改良する方法としては、樹脂ペレツト中に内部及
び外部滑性を有する化合物を練り込んで、成形機
シリンダー壁及びスクリユー表面と溶融樹脂の滑
性化並びに樹脂と樹脂との内部滑性化により加熱
混練り時の摩擦発熱の防止を図り、シルバースト
リーク,ガスリ,ヤケ等の不良現象を改善し、実
用に供してきた。しかし、近年、成形加工機の進
歩によりバレルとスクリユー間のクリアランスの
減少,ロングシリンダー化,スクリユー回転数の
増加等の、いわゆる高混練,高可塑化型の成形が
出現し、従来の滑剤練り込み型の樹脂ペレツトで
は摩擦発熱による樹脂の熱分解,スクリユー回転
時の空気の捲き込み、可塑化速度の不均一等の原
因によるシルバーストリーク,ガスリ,ヤケ等の
発生率が高くなるために、高性能成形機への樹脂
面からの対処が検討されはじめている。 滑剤練り込み型樹脂ペレツトに於ける対処法と
しては、滑剤添加量の増加がしばしば用いられる
が、増量による樹脂の耐熱性の低下、添加剤自体
の揮発成分の増加等により、シルバーストリー
ク,ヤケ,着色等の成形品外観の不良ばかりでな
く、物性低下も余儀無くされる。更に練り込み型
樹脂ペレツトに於いては樹脂と滑剤が同時に溶融
するため、ペレツトが溶融するまでの滑性が低
く、このためスクリユーのフイードゾーン及びコ
ンプレツシヨンゾーンの初期までの滑性を持たせ
るには多量の滑剤を添加する必要があり、増々総
合的な品質の低下となり、少量添加により効果の
著しい添加剤及び添加方法の出現が望まれてい
た。 本発明者等は少量の添加により上記の目的を達
成する添加剤及び添加方法について種々検討し、
本発明を完成した。即ち、本発明はスチレン系熱
可塑性樹脂ペレツト100重量部に対し、 (1) オルガノポリシロキサン、 (2) 脂肪族炭化水素系ワツクス、 (3) 高級脂肪酸と高級アルコールのエステルワツ
クス、 (4) 高級脂肪酸のビスアミド、および (5) 高級脂肪酸の金属塩 から選ばれた少なくとも1種の化合物0.01〜0.1
重量部を前記樹脂ペレツト表面に均一に付着させ
た状態でそのまま直接成形品の成形に供する成形
加工性に優れた熱可塑性樹脂ペレツトに関するも
のである。 本発明でいうスチレン系熱可塑性樹脂とは
ABS樹脂,AES樹脂,AAS樹脂,AS樹脂,ポ
リスチレン樹脂,耐衝撃性ポリスチレン樹脂等
で、通常、ペレツト粒子として取扱える硬度を有
するものである。またペレツトの大きさは20メツ
シユを通過しない大きさのものが良く、望ましく
は2〜10メツシユのものが適している。 本発明で用いる添加剤としてはポリジメチルシ
ロキサン,ポリジエチルシロキサン,ポリメチ
ル・フエニルシロキサンまたはそれらの変性物等
で代表されるオルガノポリシロキサン類,流動パ
ラフイン,合成パラフイン,ポリエチレンワツク
ス,ポリプロピレンワツクス等で代表される脂肪
族炭化水素系ワツクス類,カルナウバワツクス,
モンタンワツクス,蜜ロウ等に代表される高級脂
肪酸と高級アルコールのエステルワツクス類,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・バルミ
チン酸アミド,エチレンビス・オレイン酸アミド
等に代表される高級脂肪酸のビスアミド類,ラウ
リン酸バリウム,ミリスチン酸カドミウム,ステ
アリン酸カルシウム,ステアリン酸マグネシウ
ム,ステアリン酸アルミニウム等に代表される高
級脂肪酸の金属塩類等が挙げられる。一方、ステ
アリン酸ブチル,セバシン酸ジブチル,グリセリ
ン脂肪酸エステル等に代表される比較的炭素数の
少ないアルコールの脂肪酸エステル類,パルミチ
ルアルコール,ステアリルアルコール等に代表さ
れる脂肪族アルコール類,ラウリン酸,パルミチ
ン酸,ステアリン酸等で代表される脂肪酸等は本
発明の目的に対しては効果が小さい。 ペレツト表面に均一に付着させる様に添加する
添加剤の量はスチレン系熱可塑性樹脂ペレツト
100重量部に対して0.01〜0.1重量部の範囲であ
る。ここで添加量が0.01重量部に満たない場合は
成形加工性を向上させる効果が不充分であり、一
方0.1重量部を超えて添加すると、ペレツトがス
クリユーのフイードゾーンでスリツプしたり、混
練不充分となり、成形サイクルの遅延,品質の不
均一,更にはスクリユー回転時の空気の捲き込み
増加等により、逆に成形外観不良,生産性低下及
び品質低下となり、好ましい成形品が得られな
い。 ペレツト表面へ添加剤を均一に付着させる方法
としては、特別な装置を必要とせず、通常のヘン
シエル型ミキサー,タンブラー,リボンミキサ
ー,ワツクスブレンダー等を用いて樹脂ペレツト
と添加剤とを混合することによつて容易に実施で
きる。又通常用いられるジオクチルフタレート,
ジブチルフタレート,ブチルステアレート等の湿
潤剤をペレツト表面に付着させてから、上記添加
剤を付着させてもよい。かくして得られた成形加
工性の良好なスチレン系熱可塑性樹脂ペレツトは
そのまま直接成形機に供給され、成形品が成形さ
れる。本発明のかかる樹脂ペレツトを用いること
により、従来型の成形機だけでなく、高混練,高
可塑化型の成形機に於ても、ホツパーからスクリ
ユーフイードゾーンへの供給安定性及びフイード
ゾーンでのペレツト流動性が向上し、コンプレツ
シヨンゾーン及びメータリングゾーンでの均一可
塑化による捲き込み空気の減少並びに加熱混練り
時の摩擦発熱の低減を図ることにより、品質低
下,外観不良を発生させずに、成形サイクル短
縮,吐出量増加等の生産性を向上させることが可
能になつた。 以下、本発明を実施例により具体的に説明す
る。 実施例 1 ABS樹脂ペレツト(粒径2〜10メツシユ品)
100重量部に、下記の粉末化合物又は液状化合物
を各々所定量添加し、タンブラーで10分間撹拌混
合した後、ペレツトを80℃で2時間乾燥させ、
13pz射出成形機を用いて、200mm×250mm×3mmの
プレートを成形し、成形品外観の目視評価及びス
クリユー計量時間の測定を実施した。 成形条件としては不良現象の発生しやすい条
件、すなわち低シリンダー温度,低金型温度,高
射出圧力,低スクリユー背圧,及び高スクリユー
回転で実施した。結果を表−1に示した。 成形条件シリンダー温度200℃,金型温度30℃,
射出圧力1200Kg/cm2,スクリユー背圧2
Kg/cm2(ゲージ圧),スクリユー回転数
100rpm
The present invention relates to thermoplastic resin pellets, and more specifically to a thermoplastic resin with excellent moldability that is used to mold a molded article with a very small amount of a specific compound uniformly adhered to the surface of the styrenic thermoplastic resin pellet. It concerns pellets. More specifically, during injection molding or extrusion molding, silver streaks, gas marks, and burns on molded products occur due to pellet fluidity, non-uniform resin melting rate, shear heat generation during plasticization, etc. An object of the present invention is to provide a styrenic thermoplastic resin pellet that can prevent such phenomena from occurring. Conventionally, a method for improving the molding processability of styrenic thermoplastic resins involves kneading compounds with internal and external lubricity into resin pellets to make the molten resin lubricious between the molding machine cylinder wall and screw surface. By creating internal lubricity between the resins, frictional heat generation during heating and kneading has been prevented, and defective phenomena such as silver streaks, gas, and discoloration have been improved and the product has been put into practical use. However, in recent years, advances in molding machines have led to the emergence of so-called high-kneading, high-plasticization molding, which reduces the clearance between the barrel and the screw, makes the cylinder longer, and increases the screw rotation speed. With molded resin pellets, there is a high incidence of silver streaks, gas smudges, and discoloration due to thermal decomposition of the resin due to frictional heat generation, air entrainment during screw rotation, uneven plasticization speed, etc. Measures to deal with molding machines from the resin perspective are beginning to be considered. As a countermeasure for lubricant-mixed resin pellets, increasing the amount of lubricant added is often used, but increasing the amount will lower the heat resistance of the resin and increase the volatile components of the additive itself, resulting in silver streaks, discoloration, This not only causes defects in the appearance of the molded product such as coloring, but also leads to deterioration in physical properties. Furthermore, in kneaded resin pellets, the resin and lubricant are melted at the same time, so the lubricity until the pellets melt is low. However, it is necessary to add a large amount of lubricant, which leads to a further deterioration in overall quality.Therefore, it has been desired to develop an additive and an additive method that can be more effective even when added in small amounts. The present inventors have studied various additives and methods of addition that achieve the above objectives by adding small amounts,
The invention has been completed. That is, in the present invention, based on 100 parts by weight of styrene thermoplastic resin pellets, (1) organopolysiloxane, (2) aliphatic hydrocarbon wax, (3) ester wax of higher fatty acid and higher alcohol, (4) At least one compound selected from higher fatty acid bisamides and (5) higher fatty acid metal salts 0.01 to 0.1
The present invention relates to thermoplastic resin pellets which have excellent moldability and can be used directly to form molded products with the weight part uniformly adhered to the surface of the resin pellets. What is the styrenic thermoplastic resin referred to in the present invention?
These include ABS resin, AES resin, AAS resin, AS resin, polystyrene resin, impact-resistant polystyrene resin, etc., and usually have a hardness that allows them to be handled as pellet particles. The size of the pellets is preferably one that does not pass through 20 meshes, and preferably 2 to 10 meshes. Additives used in the present invention include organopolysiloxanes represented by polydimethylsiloxane, polydiethylsiloxane, polymethyl phenylsiloxane, or modified products thereof, liquid paraffin, synthetic paraffin, polyethylene wax, polypropylene wax, etc. Aliphatic hydrocarbon waxes represented by carnauba wax,
Montan waxes, ester waxes of higher fatty acids and higher alcohols such as beeswax, methylene bis stearamide, ethylene bis stearamide, ethylene bis valmitic acid amide, ethylene bis oleic acid amide, etc. Examples include metal salts of higher fatty acids such as bisamides of higher fatty acids, barium laurate, cadmium myristate, calcium stearate, magnesium stearate, and aluminum stearate. On the other hand, fatty acid esters of alcohols with a relatively small number of carbon atoms such as butyl stearate, dibutyl sebacate, and glycerin fatty acid esters, fatty alcohols such as palmityl alcohol and stearyl alcohol, lauric acid, and palmitin Acids, fatty acids such as stearic acid, etc. have little effect on the purpose of the present invention. The amount of additive added so that it is evenly attached to the pellet surface is the styrene thermoplastic resin pellet.
The amount ranges from 0.01 to 0.1 parts by weight per 100 parts by weight. If the amount added is less than 0.01 part by weight, the effect of improving molding processability is insufficient, while if it is added in excess of 0.1 part by weight, the pellets may slip in the feed zone of the screw, or the kneading may be insufficient. , a delay in the molding cycle, non-uniformity in quality, and an increase in air entrainment during screw rotation, conversely resulting in poor molding appearance, decreased productivity, and decreased quality, making it impossible to obtain a desirable molded product. A method for uniformly adhering the additive to the pellet surface is to mix the resin pellet and the additive using a normal Henschel type mixer, tumbler, ribbon mixer, wax blender, etc. without requiring any special equipment. It can be easily implemented by Also commonly used dioctyl phthalate,
The above additives may be applied after a wetting agent such as dibutyl phthalate or butyl stearate is applied to the pellet surface. The thus obtained styrenic thermoplastic resin pellets having good moldability are directly fed to a molding machine to form a molded article. By using the resin pellets of the present invention, not only conventional molding machines but also high-kneading, high-plasticization molding machines can achieve stable supply from the hopper to the screw feed zone and a stable feed zone. This improves the fluidity of the pellets, reduces entrained air through uniform plasticization in the compression zone and metering zone, and reduces frictional heat generation during heating and kneading, thereby preventing quality deterioration and appearance defects. It has become possible to improve productivity by shortening the molding cycle and increasing the amount of discharge. Hereinafter, the present invention will be specifically explained with reference to Examples. Example 1 ABS resin pellets (particle size 2-10 mesh product)
To 100 parts by weight, a predetermined amount of each of the following powder compounds or liquid compounds was added, and after stirring and mixing in a tumbler for 10 minutes, the pellets were dried at 80 ° C. for 2 hours.
A 200 mm x 250 mm x 3 mm plate was molded using a 13 pz injection molding machine, and the appearance of the molded product was visually evaluated and the screw metering time was measured. The molding conditions were such that defects are likely to occur, ie, low cylinder temperature, low mold temperature, high injection pressure, low screw back pressure, and high screw rotation. The results are shown in Table-1. Molding conditions cylinder temperature 200℃, mold temperature 30℃,
Injection pressure 1200Kg/cm 2 , screw back pressure 2
Kg/cm 2 (gauge pressure), screw rotation speed
100rpm

【表】 比較例 1 実施例1と全く同様の方法で、下記化合物につ
いて評価した。 結果を表−2に示した。
[Table] Comparative Example 1 The following compounds were evaluated in exactly the same manner as in Example 1. The results are shown in Table-2.

【表】 比較例 2 実施例1の添加剤が付着した各ペレツトをシリ
ンダー温度200℃の押出機に通し、添加剤をペレ
ツト内に練り込んだペレツトを得た。このペレツ
トを用いて実施例1と同様の方法でプレートを成
形し、評価した。評価結果を表−3に示す。 添加剤を練り込んだペレツト用いた比較例2に
おいてはシルバーストリーク、ヤケの改良はでき
なかつた。
[Table] Comparative Example 2 Each pellet to which the additive of Example 1 was attached was passed through an extruder with a cylinder temperature of 200°C to obtain pellets in which the additive was kneaded into the pellet. Using this pellet, a plate was molded in the same manner as in Example 1 and evaluated. The evaluation results are shown in Table-3. In Comparative Example 2, which used pellets mixed with additives, silver streaks and discoloration could not be improved.

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】 1 スチレン系熱可塑性樹脂ペレツト100重量部
に対し、 (1) オルガノポリシロキサン、 (2) 脂肪族炭化水素系ワツクス、 (3) 高級脂肪酸と高級アルコールのエステルワツ
クス、 (4) 高級脂肪酸のビスアミド、および (5) 高級脂肪酸の金属塩 から選ばれた少なくとも1種の化合物0.01〜0.1
重量部を前記樹脂ペレツト表面に均一に付着させ
た状態でそのまま直接成形品の成形に供する熱可
塑性樹脂ペレツト。
[Scope of Claims] 1 Based on 100 parts by weight of styrene thermoplastic resin pellets, (1) organopolysiloxane, (2) aliphatic hydrocarbon wax, (3) ester wax of higher fatty acid and higher alcohol, ( 4) at least one compound selected from higher fatty acid bisamides and (5) higher fatty acid metal salts 0.01 to 0.1
A thermoplastic resin pellet that is directly used for molding a molded product with the weight part uniformly attached to the surface of the resin pellet.
JP7973280A 1980-06-13 1980-06-13 Thermoplastic resin pellet Granted JPS576712A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7973280A JPS576712A (en) 1980-06-13 1980-06-13 Thermoplastic resin pellet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7973280A JPS576712A (en) 1980-06-13 1980-06-13 Thermoplastic resin pellet

Publications (2)

Publication Number Publication Date
JPS576712A JPS576712A (en) 1982-01-13
JPH0319260B2 true JPH0319260B2 (en) 1991-03-14

Family

ID=13698373

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7973280A Granted JPS576712A (en) 1980-06-13 1980-06-13 Thermoplastic resin pellet

Country Status (1)

Country Link
JP (1) JPS576712A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6037138B2 (en) * 1983-04-05 1985-08-24 大日本インキ化学工業株式会社 Styrenic resin composition
JPS61280913A (en) * 1986-06-06 1986-12-11 Dainippon Ink & Chem Inc Preparation of styrene resin hollow molding
JP2001342259A (en) * 2000-03-27 2001-12-11 Mitsui Chemicals Inc Method for producing resin pellet excellent in non- adhesiveness

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4847934A (en) * 1971-10-21 1973-07-07
JPS50113559A (en) * 1974-02-20 1975-09-05

Also Published As

Publication number Publication date
JPS576712A (en) 1982-01-13

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