JPH04117447A - Styrene resin composition - Google Patents

Styrene resin composition

Info

Publication number
JPH04117447A
JPH04117447A JP23444890A JP23444890A JPH04117447A JP H04117447 A JPH04117447 A JP H04117447A JP 23444890 A JP23444890 A JP 23444890A JP 23444890 A JP23444890 A JP 23444890A JP H04117447 A JPH04117447 A JP H04117447A
Authority
JP
Japan
Prior art keywords
rubber
styrene
weight
less
resin
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.)
Granted
Application number
JP23444890A
Other languages
Japanese (ja)
Other versions
JPH07119347B2 (en
Inventor
Yutaka Tsubokura
豊 坪倉
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.)
Idemitsu Petrochemical Co Ltd
Original Assignee
Idemitsu Petrochemical 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 Idemitsu Petrochemical Co Ltd filed Critical Idemitsu Petrochemical Co Ltd
Priority to JP2234448A priority Critical patent/JPH07119347B2/en
Publication of JPH04117447A publication Critical patent/JPH04117447A/en
Publication of JPH07119347B2 publication Critical patent/JPH07119347B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To improve the balance among heat resistance, impart strength, and mold releasability by compounding a specific rubber-modified styrene resin with a specific mold release agent. CONSTITUTION:The title compsn. comprises a rubber-modified styrene resin which is obtd. by the copolymn. of styrene with a rubberlike polymer and consists of a matrix polystyrene resin having a mol.wt. of 16X10<4>-24X10<4> and contg. 4.0-8.0wt.% particulate rubberlike polymer having a particle size of 1.0-4.0mum, 0.5wt.% or lower in total styrene dimer and trimer and 500ppm or lower residual volatile components, and 500-3000ppm (based on the compsn.) mold release agent consisting of at least one compd. selected from the group consisting of a satd. higher fatty acid and a metal salt thereof and contg. 50wt.% or lower compd. having an m.p. of 100 deg.C or lower.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は家電、OA分野において好適に利用される耐熱
性、耐衝撃性、離型性に優れたゴム変性のスチレン系樹
脂組成物に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a rubber-modified styrenic resin composition that has excellent heat resistance, impact resistance, and mold release properties and is suitably used in the fields of home appliances and OA.

[従来の技術] スチレン系樹脂の耐熱性を向上させるために、スチレン
にα−メチルスチレン、無水マレイン酸、メタクリル酸
などのコモノマーを共重合する方法が一般に行われてい
る。しかしながら得られた共重合体はコモノマーの価格
が高いため価格が高く、また流動性が低い、吸湿性が高
いなどの問題が在り、用途に制限を受けている。
[Prior Art] In order to improve the heat resistance of styrenic resins, a method of copolymerizing styrene with a comonomer such as α-methylstyrene, maleic anhydride, or methacrylic acid is generally used. However, the obtained copolymers are expensive due to the high cost of comonomers, and they also have problems such as low fluidity and high hygroscopicity, which limits their uses.

芳香族モノビニル重合体中にゴム状重合体を分散粒子と
して含有する耐熱性、耐衝撃性、離型性を兼ね備えたゴ
ム変性スチレン系樹脂組成物が特開平1−247446
号公報に開示されているが、芳香族モノビニル重合体の
分子量が小さく耐熱性が十分でないという問題点がある
A rubber-modified styrenic resin composition containing a rubbery polymer as dispersed particles in an aromatic monovinyl polymer and having heat resistance, impact resistance, and mold release properties is disclosed in JP-A-1-247446.
However, there is a problem that the aromatic monovinyl polymer has a small molecular weight and does not have sufficient heat resistance.

[発明が解決しようとする課題] 本発明は上記の問題点を解消した耐熱性、耐衝撃性、離
型性のバランスに優れたゴム変性のスチレン系樹脂組成
物を提供することを目的とするものである。
[Problems to be Solved by the Invention] An object of the present invention is to provide a rubber-modified styrenic resin composition that solves the above-mentioned problems and has an excellent balance of heat resistance, impact resistance, and mold release properties. It is something.

[課題を解決するための手段] 本発明者らは前記問題点を解決するために鋭意研究を重
ねた結果、特定な分子量のマトリックスポリスチレン系
樹脂中に特定なゴム状重合体を含有し、スチレン2量体
とスチレン3量体の総量及び残留揮発成分の総量が特定
量未満であるゴム変性スチレン系樹脂に特定の離型剤を
特定量含有させてなるスチレン系樹脂組成物により前記
目的が達成されることを見出し、この知見に基づいて本
発明を完成するに至った。
[Means for Solving the Problems] As a result of extensive research in order to solve the above-mentioned problems, the present inventors have found that a specific rubber-like polymer is contained in a matrix polystyrene resin having a specific molecular weight, and styrene The above object is achieved by a styrenic resin composition comprising a rubber-modified styrenic resin in which the total amount of dimer and styrene trimer and the total amount of residual volatile components are less than a specific amount and a specific amount of a specific mold release agent. Based on this knowledge, the present invention was completed.

すなわち、本発明は、分子量が16×104〜24×1
04のマトリックスポリスチレン系樹脂中に粒径1.0
〜4.0μmの粒子状のゴム状重合体を4.0〜8.0
重量%、スチレン2量体とスチレン3量体を総量で0.
5重量%以下、残留揮発成分を総量で500 pprn
以下含有するスチレンとゴム状重合一体を重合して得ら
れたゴム変性スチレン系樹脂(A)及び組成物に対して
500〜3000ppmの飽和高級脂肪族のカルボン酸
及びそれらの金属塩から選ばれる1種又は2種以上の化
合物からなり、融点100’C以下の化合物が50重量
%以下である離型剤(B)からなることを特徴とするス
チレン系樹脂組成物を提供するものである。
That is, in the present invention, the molecular weight is 16 x 104 to 24 x 1
Particle size 1.0 in matrix polystyrene resin of 04
~4.0μm particulate rubbery polymer from 4.0 to 8.0μm
Weight%, total amount of styrene dimer and styrene trimer is 0.
5% by weight or less, total residual volatile components 500 pprn
1 selected from saturated higher aliphatic carboxylic acids and metal salts thereof in an amount of 500 to 3000 ppm based on the rubber-modified styrenic resin (A) obtained by polymerizing the styrene and rubber-like polymerized monomer containing the following: The present invention provides a styrenic resin composition characterized by comprising a mold release agent (B) comprising a species or two or more kinds of compounds, and a compound having a melting point of 100'C or less accounts for 50% by weight or less.

本発明におけるゴム変性スチレン系樹脂(A)はスチレ
ンとゴム状重合体を重合して得られるものであり、従来
のゴム変性スチレン系樹脂の製造において慣用されてい
る方法、例えば乳化重合法、塊状重合法、塊状−懸濁重
合法、懸濁重合法なと、いずれの方法によっても製造す
ることができるが、本発明においては、経済的に有利な
点から、塊状−懸濁重合法又は連続塊状重合法による製
造方法が選ばれる。
The rubber-modified styrenic resin (A) in the present invention is obtained by polymerizing styrene and a rubbery polymer, and can be obtained by a method commonly used in the production of conventional rubber-modified styrenic resins, such as emulsion polymerization, bulk polymerization, etc. Although it can be produced by any method such as polymerization method, bulk-suspension polymerization method, or suspension polymerization method, in the present invention, from an economically advantageous point, bulk-suspension polymerization method or continuous polymerization method is used. A manufacturing method based on bulk polymerization is selected.

次に、本発明のゴム変性スチレン系樹脂の製造方法の一
例について説明する。まず、ゴム状重合体を、スチレン
及び所望に応じて用いられる他の共重合可能な単量体を
含む混合溶液に加え、20〜700C程度の温度におい
て溶解したのち、この溶液を攪拌機付の1段以上、好ま
しくは2段以上の重合器に供給して重合を行い、重合の
最終段から固形成分と未反応単量体及び溶剤などの揮発
成分とを分離する脱揮発成分工程を経て、所望の樹脂が
得られる。
Next, an example of the method for producing the rubber-modified styrenic resin of the present invention will be described. First, a rubber-like polymer is added to a mixed solution containing styrene and other copolymerizable monomers used as desired, and dissolved at a temperature of about 20 to 700 C. Polymerization is carried out by supplying the polymer to a polymerization vessel having more than one stage, preferably two or more stages, and from the final stage of the polymerization, the desired amount is removed through a devolatilizing component step in which solid components and volatile components such as unreacted monomers and solvents are separated. of resin is obtained.

この方法においては、第1段目の重合器には、単量体に
溶解したゴム状重合体が供給され、また、単量体及び所
望に応じて用いられる重合開始剤や連鎖移動剤は、任意
の段階で重合器に供給してもよい。
In this method, a rubber-like polymer dissolved in a monomer is supplied to the first stage polymerization vessel, and the monomer and a polymerization initiator and chain transfer agent used as desired are It may be supplied to the polymerization vessel at any stage.

この重合方法において、所望に応じて用いられる重合開
始剤としては、例えばt−ブチルヒドロペルオキシド、
ジ−t−ブチルペルオキシド、クメンヒドロペルオキシ
ド、ジクミルペルオキシド、ベンゾイルペルオキシド、
1,1−ビス(t−ブチルペルオキシ)シクロヘキサン
、2,5−ジメチル−2,5−ジ(t−ブチルペルオキ
シ)ヘキサン、1.1−ビス(t−ブチルペルオキシ)
3.3.5−トリメチルシクロヘキサン、2,2−ビス
(4,4−ジ−t−ブチルペルオキシシクロヘキサン)
プロパノンなどの有機過酸化物、アゾビスイソブチロニ
トリル、アゾビス−2,4−ジメチルバレロニトリル、
アゾビスシクロヘキサンカルボニトリル、アゾビスイソ
酪酸メチル、アゾビスシアノ吉草酸などのアゾ化合物な
どが挙げられる。これらは単独で又は2種以上を混合し
て使用することができるが、半減期温度温度(10時間
)が100℃以下のものと100℃以上のものを混合し
て使用することが好ましい。
In this polymerization method, examples of the polymerization initiator used as desired include t-butyl hydroperoxide,
di-t-butyl peroxide, cumene hydroperoxide, dicumyl peroxide, benzoyl peroxide,
1,1-bis(t-butylperoxy)cyclohexane, 2,5-dimethyl-2,5-di(t-butylperoxy)hexane, 1,1-bis(t-butylperoxy)
3.3.5-Trimethylcyclohexane, 2,2-bis(4,4-di-t-butylperoxycyclohexane)
Organic peroxides such as propanone, azobisisobutyronitrile, azobis-2,4-dimethylvaleronitrile,
Examples include azo compounds such as azobiscyclohexanecarbonitrile, methyl azobisisobutyrate, and azobiscyanovaleric acid. These can be used alone or in combination of two or more, but it is preferable to use a mixture of those with a half-life temperature (10 hours) of 100° C. or lower and one with a half-life temperature of 100° C. or higher.

また、所望に応じて用いられる連鎖移動剤としては、例
えばn−ドデシルメルカプタン、t−ドデシルメルカプ
タンなどのメルカプタン類や、α−メチルスチレンダイ
マー、1−フェニル−ブテン−2−フルオレン、チルピ
ノール、クロロホルムなどが挙げられる。
Chain transfer agents that can be used as desired include, for example, mercaptans such as n-dodecylmercaptan and t-dodecylmercaptan, α-methylstyrene dimer, 1-phenyl-butene-2-fluorene, tilpinol, and chloroform. can be mentioned.

スチレン単量体を重合して得られるマトリックス成分の
スチレン系樹脂は、スチレン単独重合体又はスチレンと
共重合可能な単量体との共重合体であり、共重合可能な
単量体としては、例えばα−メチルスチレン、ビニルト
ルエン、ビニルエチルベンゼン、ビニルキシレン、p−
t−ブチルスチレン、α−メチル−p−メチルスチレン
、ビニルナフタレンなとの芳香族モノビニル化合物、ア
クリロニトリル、メタクリル酸メチル、アクリル酸メチ
ル、メタクリル酸、アクルリル酸、無水マレイン酸、フ
ェニルマレイミドなどを挙げることができる。これらの
単量体は1種用いてもよいし、2種以上を組み合わせて
用いてもよいが、スチレンを含む全単量体に対して、通
常50重量%以下、好ましくは40重量%以下の割合で
用いられる。
The styrenic resin as a matrix component obtained by polymerizing styrene monomers is a styrene homopolymer or a copolymer of a monomer copolymerizable with styrene, and the copolymerizable monomers include: For example, α-methylstyrene, vinyltoluene, vinylethylbenzene, vinylxylene, p-
Aromatic monovinyl compounds such as t-butylstyrene, α-methyl-p-methylstyrene, vinylnaphthalene, acrylonitrile, methyl methacrylate, methyl acrylate, methacrylic acid, acrylic acid, maleic anhydride, phenylmaleimide, etc. I can do it. These monomers may be used alone or in combination of two or more types, but they usually account for 50% by weight or less, preferably 40% by weight or less, based on the total monomers containing styrene. Used in percentages.

ゴム状重合体の種類については特に制限はなく、従来ゴ
ム変性スチレン系樹脂に慣用されているもの、例えば天
然ゴムや、ポリブタジェンゴム、ポリイソプレンゴム、
スチレン−ブタジェン共重合体ゴム、スチレン−イソプ
レン共重合体ゴム、ブチルゴム、エチレン−プロピレン
共重合体ゴムなとの合成ゴム、あるいはこれらのゴムと
スチレンとのグラフト共重合体ゴムなどが用いられる。
There are no particular restrictions on the type of rubber-like polymer, and those conventionally used in rubber-modified styrenic resins, such as natural rubber, polybutadiene rubber, polyisoprene rubber,
Synthetic rubbers such as styrene-butadiene copolymer rubber, styrene-isoprene copolymer rubber, butyl rubber, ethylene-propylene copolymer rubber, or graft copolymer rubbers of these rubbers and styrene are used.

上記のようにして得られたゴム変性スチレン系樹脂中の
ゴム状重合体の量は仕込ゴム濃度と樹脂の最終転化率か
ら計算により求められる。また、ゴム状重合体の粒径は
ゴム状重合体の面積平均粒子径(直径)  (DS)と
して次のようにして求められる。すなわち、配向の小さ
いゴム変性スチレン系樹脂のペレットを3重量%の四酸
化オスミウム水溶液にて処理したものを超ミクロトーム
により薄片化したのち、このものの透過型電子顕微鏡像
を得、画像上のゴム状重合体粒子の長径方向の直径(D
)を約1000個の粒子について測定し、その面積平均
値を次式に従って求めることにより、ゴム状重合体の面
積平均粒子径(直径)  (Ds)が得られる。
The amount of the rubbery polymer in the rubber-modified styrenic resin obtained as described above is determined by calculation from the charged rubber concentration and the final conversion rate of the resin. Further, the particle size of the rubbery polymer is determined as the area average particle size (diameter) (DS) of the rubbery polymer as follows. Specifically, pellets of a rubber-modified styrenic resin with a small degree of orientation were treated with a 3% by weight osmium tetroxide aqueous solution, and then sliced into thin sections using an ultramicrotome. A transmission electron microscope image of this pellet was obtained, and the rubber-like appearance in the image was obtained. The diameter of the polymer particles in the major axis direction (D
) is measured for about 1000 particles, and the area average value is determined according to the following formula to obtain the area average particle size (diameter) (Ds) of the rubbery polymer.

(nは直径りのゴム状重合体粒子の個数。)ゴム状重合
体の含有量は4.O〜8.0重量%であることが必要で
、4.0重量%未満では耐衝撃性が低下し、8.0重量
%を超えると耐熱性が低下する。好ましい範囲は4. 
0〜7.5重量%である。またゴム状重合体の粒径は1
.  O〜4゜0μmであることが必要で1.0μm未
満では耐衝撃性が低下し、4. 0μmを超えると耐衝
撃性及び耐熱性が低下する。好ましい範囲は1.2〜3
.6μmである。
(n is the number of rubbery polymer particles in diameter.) The content of the rubbery polymer is 4. It is necessary that the content is 0 to 8.0% by weight; if it is less than 4.0% by weight, the impact resistance will decrease, and if it exceeds 8.0% by weight, the heat resistance will decrease. The preferred range is 4.
It is 0 to 7.5% by weight. Also, the particle size of the rubbery polymer is 1
.. It is necessary that the thickness is 0 to 4°0 μm; if it is less than 1.0 μm, the impact resistance will decrease. If it exceeds 0 μm, impact resistance and heat resistance will decrease. The preferred range is 1.2-3
.. It is 6 μm.

次に、マトリックスポリスチレン系樹脂の分子量は次の
ようにして求められる。すなわち、ゴム変性スチレン系
樹脂をメチルエチルケトンに溶解後、ゲル成分を除去す
るために遠心分離し、マトリックス成分を含む上澄み液
を乾燥した。その後、テトラヒドロフランを溶媒として
マトリックス成分の0. 2重量%溶液を調製し、ウォ
ータース社製GPC150Cを使用して、重量平均分子
量(M w)を、ポリスチレン換算で求めた。マトリッ
クスポリスチレン系樹脂の分子量は16X104〜24
×104の範囲にあることが必要で、16×104未満
であると耐衝撃性及び耐熱性が低下し、24×104を
超えると流動性が低下する。
Next, the molecular weight of the matrix polystyrene resin is determined as follows. That is, after dissolving the rubber-modified styrene resin in methyl ethyl ketone, it was centrifuged to remove the gel component, and the supernatant containing the matrix component was dried. Thereafter, 0.0% of the matrix component was prepared using tetrahydrofuran as a solvent. A 2% by weight solution was prepared, and the weight average molecular weight (Mw) was determined in terms of polystyrene using GPC150C manufactured by Waters. The molecular weight of the matrix polystyrene resin is 16X104~24
It is necessary to be in the range of ×104, and if it is less than 16×104, impact resistance and heat resistance will decrease, and if it exceeds 24×104, fluidity will decrease.

好ましい範囲は17×104〜23×104である。The preferred range is 17x104 to 23x104.

さらに本発明のゴム変性スチレン系樹脂は、樹脂中のス
チレン2量体及び3量体の総量が0.5重量%以下であ
ることが必要である。この総量か0.5重量%を超える
と耐熱性が低下する。好ましい範囲は0. 4重量%以
下である。また、本発明のゴム変性スチレン系樹脂は、
樹脂中の残留揮発成分の総量が500 ppm以下であ
ることが必要である。この総量が500 ppmを超え
ると耐熱性が低下する。好ましい範囲は400 ppm
以下である。残留揮発成分としてはスチレン、イソプロ
ピルベンゼン、n−プロピルベンゼン、エチルベンゼン
及び重合に使用した溶剤なとがある。
Furthermore, the rubber-modified styrenic resin of the present invention requires that the total amount of styrene dimers and trimers in the resin be 0.5% by weight or less. If the total amount exceeds 0.5% by weight, heat resistance will decrease. The preferred range is 0. It is 4% by weight or less. Furthermore, the rubber-modified styrenic resin of the present invention is
It is necessary that the total amount of residual volatile components in the resin is 500 ppm or less. If this total amount exceeds 500 ppm, heat resistance will decrease. Preferred range is 400 ppm
It is as follows. The remaining volatile components include styrene, isopropylbenzene, n-propylbenzene, ethylbenzene, and the solvent used in the polymerization.

上記スチレン2量体及び3量体の総量、残留揮発成分の
総量は島津製作所製のガスクロマトグラフィーGC−3
BFを使用して求めた。
The total amount of the above styrene dimer and trimer and the total amount of residual volatile components were measured using a gas chromatography GC-3 manufactured by Shimadzu Corporation.
It was determined using BF.

次に、(B)成分として用いられる飽和高級脂肪族のカ
ルボン酸としては炭素数12〜42程度の直鎖飽和モノ
カルボン酸が用いられる。例えば、ラウリン酸(44℃
)、ミリスチン酸(54℃)、パルミチン酸(636C
)、ステアリン酸(70℃)ベヘン酸(81℃)、モン
タン酸(89℃)などが挙げられる。これらの金属塩の
金属としては、リチウム、ナトリウム、カリウム、マグ
ネシウム、カルシウム、アルミニウム、亜鉛などがあり
、代表的な高級脂肪族のカルボン酸の金属塩としては、
ステアリン酸マグネシウム(132℃)、ステアリン酸
アルミニウム(103℃)、ステアリン酸カルシウム(
180℃)、ステアリン酸亜鉛(140℃)などが挙げ
られる(かっこ内は融点を表す)。
Next, as the saturated higher aliphatic carboxylic acid used as component (B), a linear saturated monocarboxylic acid having about 12 to 42 carbon atoms is used. For example, lauric acid (44℃
), myristic acid (54℃), palmitic acid (636C
), stearic acid (70°C), behenic acid (81°C), and montanic acid (89°C). The metals of these metal salts include lithium, sodium, potassium, magnesium, calcium, aluminum, zinc, etc. Typical metal salts of higher aliphatic carboxylic acids include:
Magnesium stearate (132℃), aluminum stearate (103℃), calcium stearate (
(180°C), zinc stearate (140°C), etc. (The melting point is shown in parentheses).

本発明の組成物において、離型剤(B)は上記飽和高級
脂肪酸及びそれらの金属塩から選ばれる1種又は2種以
上の化合物からなり、融点100℃以下の化合物が50
重量%以下であることが必要である。融点100℃以下
の化合物が50重量%を超えると耐熱性が低下する。ま
た、離型剤の量は組成物に対して500〜3000pp
mであることが必要である。500 ppm未満である
と離型性が低下し、3000ppmを超えると耐熱性が
低下する。好ましい範囲は1000〜2500ppmで
ある。
In the composition of the present invention, the mold release agent (B) is composed of one or more compounds selected from the above-mentioned saturated higher fatty acids and metal salts thereof, and the compound having a melting point of 100°C or less is
It is necessary that the amount is below % by weight. If the content of the compound having a melting point of 100° C. or lower exceeds 50% by weight, heat resistance will decrease. In addition, the amount of the mold release agent is 500 to 3000pp relative to the composition.
It is necessary that m. If it is less than 500 ppm, mold releasability will decrease, and if it exceeds 3000 ppm, heat resistance will decrease. The preferred range is 1000 to 2500 ppm.

離型剤の添加方法は特に制限はなくゴム変性スチレン系
樹脂の原料であるゴムを溶解したスチレン溶液中に添加
しても、あるいは重合工程、脱揮発成分工程に添加して
も、あるいは得られた樹脂ベレットに添加してもいずれ
でもよい。
There are no particular restrictions on the method of adding the mold release agent, and it can be added to a styrene solution in which rubber, which is a raw material for rubber-modified styrenic resin, is dissolved, or added to the polymerization process or devolatilization process, or it can be added to the styrene solution. It may be added to the resin pellet.

本発明のゴム変性スチレン系樹脂組成物には、所望に応
じて通常用いられている種々の添加剤、例えばエチレン
ビスステアロアミドなどの滑剤や有機ポリシロキサン、
ミネラルオイル等、また酸化防止剤として、例えば、ヒ
ンダードフェノール類、ヒンダードビスフェノール類、
ヒンダードトリスフェノール類等、また、例えば、2.
6−ジーt−ブチル−4−メチルフェノール、ステアリ
ル−β−(3,5−ジ−t−ブチル−4−ヒト七キシフ
ェニル)プロピオネート、トリエチレングリコール−ビ
ス−3−(3−t−ブチル−4−ヒドロキシ−6−メチ
ルフェニル)プロピオネート等、あるいは、リン化合物
、例えば、トリ(2゜4−ジ−t−ブチルフェニル)フ
ォスファイト、4.4′−ブチリデン−ビス−(3−メ
チル−6−t−ブチルフェニル−ジ−トリデシル)フォ
スファイト等を添加することができる。さらに必要に応
じて、安定剤、染料、顔料、充填剤、滑剤、可塑剤、帯
電防止剤などを添加することができる。
The rubber-modified styrenic resin composition of the present invention may contain various commonly used additives, such as lubricants such as ethylene bisstearamide, organic polysiloxane,
Mineral oil, etc., and antioxidants such as hindered phenols, hindered bisphenols, etc.
Hindered trisphenols, etc. Also, for example, 2.
6-di-t-butyl-4-methylphenol, stearyl-β-(3,5-di-t-butyl-4-human-7xyphenyl)propionate, triethylene glycol-bis-3-(3-t-butyl- 4-hydroxy-6-methylphenyl) propionate, etc., or phosphorus compounds such as tri(2°4-di-t-butylphenyl)phosphite, 4,4'-butylidene-bis-(3-methyl-6 -t-butylphenyl-di-tridecyl) phosphite, etc. can be added. Furthermore, stabilizers, dyes, pigments, fillers, lubricants, plasticizers, antistatic agents, etc. can be added as necessary.

また、本発明のスチレン系樹脂組成物は、所望により、
汎用ポリスチレン(GPPS)や他のポリマー、例えば
ポリフェニレンエーテル、ABSなどを配合することも
できる。
Furthermore, the styrenic resin composition of the present invention may optionally contain
General purpose polystyrene (GPPS) and other polymers such as polyphenylene ether, ABS, etc. can also be blended.

[実施例] 以下、本発明を実施例に基づいて説明するが、本発明は
これに限定されるものではない。なお、物性等の測定法
を下記に示す。
[Examples] The present invention will be described below based on Examples, but the present invention is not limited thereto. In addition, the measurement method of physical properties etc. is shown below.

(1)メルトインデックス(M I )J Is−に−
7210に準拠して測定。
(1) Melt index (M I ) J Is-
Measured in accordance with 7210.

(2)アイゾツト衝撃強度 J Is−に−7110(23℃、ノツチ付)に準拠し
て測定。
(2) Izot impact strength Measured according to J Is-7110 (23°C, with notch).

(3)ボールプレッシャー温度 試験片を恒温槽内に入れ、その上に直径が5mmの鋼玉
を用いて2ONの静加重を1時間加えたのち、鋼玉を除
去してただちに259C±5℃の水中で30分間冷却し
、へこんだ穴の直径を測定したとき、その直径が2mm
(深さで換算する場合は、0、 209mm)である温
度。
(3) Place the ball pressure temperature test piece in a constant temperature bath, apply a static load of 2ON for 1 hour using a steel ball with a diameter of 5mm, then remove the ball pressure test piece and immediately place it in water at 259C ± 5C. After cooling for 30 minutes, the diameter of the hollow hole was measured to be 2 mm.
(If converted by depth, the temperature is 0.209mm).

(4)離型性 成形温度220℃にてリブ及びボス部分などの多くつい
た複雑な成形品を射出成形し、成形品の外観を次のラン
クにて評価した。
(4) Mold releasability Complex molded products with many ribs and bosses were injection molded at a molding temperature of 220° C., and the appearance of the molded products was evaluated using the following rankings.

◎:キズ、白化が全くないもの。◎: No scratches or whitening at all.

O:キズ、白化がほんの少しあるもの。O: There are slight scratches and whitening.

△:キズ、白化がかなりあるもの。△: There are considerable scratches and whitening.

×:キズ、白化があり、割れもあるもの。×: There are scratches, whitening, and cracks.

実施例1 毎時201の供給速度で次の組成の混合物を、容量23
ρの第一重合槽に連続的に送液した。
Example 1 A mixture of the following composition at a feed rate of 201/hr was fed into a volume of 23
The solution was continuously fed to the first polymerization tank of ρ.

ゴム状重合体:NF35AS (旭化成工業製 ポリブ
タジェン)          5.2重量%スチレン
          89.8重量%エチルベンゼン 
       5.0重量%n−ドデシルメルカプタン
     200 ppm1.1−ビス(t−ブチルペ
ルオキシ)3,3゜5−トリメチルシクロヘキサン  
300ppm2.5−ジメチル−2,5−ジ(t−ブチ
ルペルオキシ)ヘキサン        1100pp
第一重合槽の温度は115℃であり、回転数は150r
pmであった。
Rubber-like polymer: NF35AS (polybutadiene manufactured by Asahi Kasei Industries) 5.2% by weight styrene 89.8% by weight ethylbenzene
5.0% by weight n-dodecylmercaptan 200 ppm 1.1-bis(t-butylperoxy)3,3°5-trimethylcyclohexane
300ppm2.5-dimethyl-2,5-di(t-butylperoxy)hexane 1100pp
The temperature of the first polymerization tank is 115℃, and the rotation speed is 150r.
It was pm.

次いで容量331の第二重合槽、容量331の第三重合
槽に順次送液した。温度、回転数は各々、137℃,5
0rpm、 160℃、2Orpmであった。
Next, the liquid was sequentially sent to a second polymerization tank with a capacity of 331 and a third polymerization tank with a capacity of 331. Temperature and rotation speed are 137℃ and 5, respectively.
The temperature was 0 rpm, 160° C., and 2 Orpm.

また、第三重合槽出口の添加率は85重量%であった。Further, the addition rate at the outlet of the third polymerization tank was 85% by weight.

さらに、230〜280℃の温度に加熱した真空槽にて
揮発成分を除去して、ペレット状のゴム変性スチレン系
樹脂を得た。以下の運転条件を第1表に示す。
Furthermore, volatile components were removed in a vacuum chamber heated to a temperature of 230 to 280°C to obtain a pellet-shaped rubber-modified styrene resin. The following operating conditions are shown in Table 1.

このベレットにステアリン酸カルシウムを2500pp
m添加し、押出機にて練り込んだ。得られた樹脂組成物
の組成及び物性並びにゴム変性スチレン系樹脂の樹脂構
造を第2表に示す。
This pellet contains 2500pp of calcium stearate.
m was added and kneaded using an extruder. Table 2 shows the composition and physical properties of the resulting resin composition and the resin structure of the rubber-modified styrene resin.

実施例2〜4 実施例1において、運転条件を第1表に示す様に、離型
剤組成を第2表に示すように変更した。
Examples 2 to 4 In Example 1, the operating conditions were changed as shown in Table 1, and the release agent composition was changed as shown in Table 2.

得られた樹脂組成物の物性及びゴム変性スチレン系樹脂
の樹脂構造を第2表に示す。
Table 2 shows the physical properties of the obtained resin composition and the resin structure of the rubber-modified styrene resin.

比較例1〜5 実施例1において、運転条件を第1表に示す様に、離型
剤組成を第2表に示すように変更した。
Comparative Examples 1 to 5 In Example 1, the operating conditions were changed as shown in Table 1, and the release agent composition was changed as shown in Table 2.

得られた樹脂組成物の物性及びゴム変性スチレン系樹脂
の樹脂構造を第2表に示す。
Table 2 shows the physical properties of the obtained resin composition and the resin structure of the rubber-modified styrene resin.

[発明の効果] 本発明によれば耐熱性、耐衝撃性、離型性のバランスに
優れ、特に耐熱性に優れたスチレン系樹脂組成物を得る
ことができる。
[Effects of the Invention] According to the present invention, it is possible to obtain a styrenic resin composition that has an excellent balance of heat resistance, impact resistance, and mold releasability, and has particularly excellent heat resistance.

したがって、本発明のスチレン系樹脂組成物は家電、O
A分野の材料として好適に用いられ、その工業的価値は
極めて大である。
Therefore, the styrenic resin composition of the present invention can be used in home appliances, O
It is suitably used as a material in the A field, and its industrial value is extremely large.

Claims (1)

【特許請求の範囲】[Claims] 1、分子量が16×10^4〜24×10^4のマトリ
ックスポリスチレン系樹脂中に粒径1.0〜4.0μm
の粒子状のゴム状重合体を4.0〜8.0重量%、スチ
レン2量体とスチレン3量体を総量で0.5重量%以下
、残留揮発成分を総量で500ppm以下含有するスチ
レンとゴム状重合体を重合して得られたゴム変性スチレ
ン系樹脂(A)及び組成物に対して500〜3000p
pmの飽和高級脂肪族のカルボン酸及びそれらの金属塩
から選ばれる1種又は2種以上の化合物からなり、融点
100℃以下の化合物が50重量%以下である離型剤(
B)からなることを特徴とするスチレン系樹脂組成物。
1. Particle size of 1.0 to 4.0 μm in matrix polystyrene resin with molecular weight of 16 x 10^4 to 24 x 10^4
Styrene containing 4.0 to 8.0% by weight of a particulate rubbery polymer, 0.5% by weight or less of styrene dimer and styrene trimer in total, and 500ppm or less of residual volatile components in total. 500 to 3000 p to the rubber-modified styrenic resin (A) and composition obtained by polymerizing a rubbery polymer
A mold release agent consisting of one or more compounds selected from pm saturated higher aliphatic carboxylic acids and their metal salts, and containing 50% by weight or less of compounds with a melting point of 100°C or less (
A styrenic resin composition comprising B).
JP2234448A 1990-09-06 1990-09-06 Styrene resin composition Expired - Lifetime JPH07119347B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2234448A JPH07119347B2 (en) 1990-09-06 1990-09-06 Styrene resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2234448A JPH07119347B2 (en) 1990-09-06 1990-09-06 Styrene resin composition

Publications (2)

Publication Number Publication Date
JPH04117447A true JPH04117447A (en) 1992-04-17
JPH07119347B2 JPH07119347B2 (en) 1995-12-20

Family

ID=16971163

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2234448A Expired - Lifetime JPH07119347B2 (en) 1990-09-06 1990-09-06 Styrene resin composition

Country Status (1)

Country Link
JP (1) JPH07119347B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11323065A (en) * 1998-05-18 1999-11-26 Denki Kagaku Kogyo Kk Rubber-modified styrene-based resin composition and its blow molding product

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54127454A (en) * 1978-03-27 1979-10-03 Asahi Chem Ind Co Ltd Styrene resin composition
JPS5742654A (en) * 1980-08-26 1982-03-10 Ube Ind Ltd Preparation of dimethyl oxalate
JPS5876405A (en) * 1981-10-31 1983-05-09 Denki Kagaku Kogyo Kk Manufacture of styrene polymer
JPS59196349A (en) * 1983-04-05 1984-11-07 Dainippon Ink & Chem Inc Styrene resin composition
JPS60192755A (en) * 1984-03-15 1985-10-01 Asahi Chem Ind Co Ltd Rubber-modified styrene resin composition for thin- walled molding
JPS63159414A (en) * 1986-12-23 1988-07-02 Dainippon Ink & Chem Inc Preparation of rubber-modified styrene resin composition having excellent flow property
JPH01247446A (en) * 1988-03-29 1989-10-03 Idemitsu Petrochem Co Ltd Rubber-modified styrene resin composition

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54127454A (en) * 1978-03-27 1979-10-03 Asahi Chem Ind Co Ltd Styrene resin composition
JPS5742654A (en) * 1980-08-26 1982-03-10 Ube Ind Ltd Preparation of dimethyl oxalate
JPS5876405A (en) * 1981-10-31 1983-05-09 Denki Kagaku Kogyo Kk Manufacture of styrene polymer
JPS59196349A (en) * 1983-04-05 1984-11-07 Dainippon Ink & Chem Inc Styrene resin composition
JPS60192755A (en) * 1984-03-15 1985-10-01 Asahi Chem Ind Co Ltd Rubber-modified styrene resin composition for thin- walled molding
JPS63159414A (en) * 1986-12-23 1988-07-02 Dainippon Ink & Chem Inc Preparation of rubber-modified styrene resin composition having excellent flow property
JPH01247446A (en) * 1988-03-29 1989-10-03 Idemitsu Petrochem Co Ltd Rubber-modified styrene resin composition

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11323065A (en) * 1998-05-18 1999-11-26 Denki Kagaku Kogyo Kk Rubber-modified styrene-based resin composition and its blow molding product

Also Published As

Publication number Publication date
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