JP2013151654A - Graft copolymer, and thermoplastic resin composition - Google Patents
Graft copolymer, and thermoplastic resin composition Download PDFInfo
- Publication number
- JP2013151654A JP2013151654A JP2012275344A JP2012275344A JP2013151654A JP 2013151654 A JP2013151654 A JP 2013151654A JP 2012275344 A JP2012275344 A JP 2012275344A JP 2012275344 A JP2012275344 A JP 2012275344A JP 2013151654 A JP2013151654 A JP 2013151654A
- Authority
- JP
- Japan
- Prior art keywords
- weight
- parts
- polymer
- conjugated diene
- graft copolymer
- 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
Links
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Graft Or Block Polymers (AREA)
Abstract
Description
本発明は、耐候性だけでなく、耐衝撃性、及び発色性に優れた熱可塑性樹脂組成物を構成するグラフト共重合体及び該グラフト共重合体から得られた熱可塑性樹脂組成物に関する。 The present invention relates to a graft copolymer constituting a thermoplastic resin composition excellent in not only weather resistance but also impact resistance and color developability, and a thermoplastic resin composition obtained from the graft copolymer.
ＡＢＳ樹脂は、耐衝撃性及び加工性のバランスに優れた樹脂であり、自動車等の車両用内外装部品、各種の家電製品やＯＡ機器のハウジング、その他雑貨分野等、幅広い分野に使用されている。しかし、ＡＢＳ樹脂は、そのゴム成分として使用するブタジエン系ゴム重合体が紫外線等により分解され易いことから、耐候性に劣るという欠点を有している。そこで、ＡＢＳ樹脂中のゴム成分をアクリルゴムに置換することで耐候性を改良した、ＡＳＡ樹脂が実用化されている。しかし、ＡＳＡ樹脂は耐候性に優れているものの、その反面、耐衝撃性、発色性に劣るという欠点を有している。 ABS resin is a resin with an excellent balance between impact resistance and workability, and is used in a wide range of fields such as interior and exterior parts for vehicles such as automobiles, housings for various home appliances and OA equipment, and other miscellaneous goods. . However, the ABS resin has a disadvantage that the weather resistance is inferior because the butadiene rubber polymer used as the rubber component is easily decomposed by ultraviolet rays or the like. Then, the ASA resin which improved the weather resistance by substituting the rubber component in ABS resin for acrylic rubber is put into practical use. However, although ASA resin is excellent in weather resistance, it has a disadvantage that it is inferior in impact resistance and color development.
特許文献１には耐衝撃性、耐候性、成形加工性が改良された熱可塑性樹脂組成物として、特定の分子量を有するジエン系ゴムとアクリル酸エステル系重合体とで構成される複合ゴムを用いた熱可塑性樹脂組成物が提案されている。しかし、発色性が不十分であるという問題がある。 Patent Document 1 uses a composite rubber composed of a diene rubber having a specific molecular weight and an acrylate ester polymer as a thermoplastic resin composition having improved impact resistance, weather resistance and molding processability. A thermoplastic resin composition has been proposed. However, there is a problem that the color developability is insufficient.
また、特許文献２には耐熱性、耐候性、成形加工性、さらには成形品の表面外観が改良された熱可塑性樹脂組成物として、共役ジエン系ゴム状重合体とアクリル酸エステル系ゴム状重合体からなる複合ゴムを使用したグラフト共重合体とマレイミド系共重合体から構成される熱可塑性樹脂組成物が提案されている。しかし、発色性が不十分であるという問題がある。 Further, Patent Document 2 discloses a conjugated diene rubber polymer and an acrylate rubber rubber as a thermoplastic resin composition having improved heat resistance, weather resistance, moldability, and surface appearance of a molded product. There has been proposed a thermoplastic resin composition composed of a graft copolymer using a composite rubber made of a coalescence and a maleimide copolymer. However, there is a problem that the color developability is insufficient.
本発明の目的は耐候性だけでなく、耐衝撃性、及び発色性に優れた熱可塑性樹脂組成物を構成するグラフト共重合体及び該グラフト共重合体から得られた熱可塑性樹脂組成物を提供することにある。 An object of the present invention is to provide a graft copolymer constituting a thermoplastic resin composition excellent in not only weather resistance but also impact resistance and color developability, and a thermoplastic resin composition obtained from the graft copolymer There is to do.
本発明者らは、従来技術の問題点を解決するために鋭意検討した結果、特定のゴム形態を有する複合ゴムに、シアン化ビニル系単量体、芳香族ビニル系単量体等の単量体混合物を重合して得られるグラフト共重合体を用いることにより、上記目的を達成できることを見出し、本発明に到達した。 As a result of intensive investigations to solve the problems of the prior art, the present inventors have found that the composite rubber having a specific rubber form is a single monomer such as a vinyl cyanide monomer or an aromatic vinyl monomer. The inventors have found that the above object can be achieved by using a graft copolymer obtained by polymerizing a body mixture, and have reached the present invention.
すなわち、本発明は共役ジエン系ゴム状重合体５〜５０重量％と架橋アクリル酸エステル系重合体５０〜９５重量％から構成される複合ゴム１０〜８０重量部に、芳香族ビニル系単量体、シアン化ビニル系単量体及びこれらと共重合可能な他のビニル系単量体から選ばれた少なくとも一種の単量体２０〜９０重量部をグラフト重合して得られるグラフト共重合体（Ａ）であって、複合ゴムは多層構造を有しており、内層が共役ジエン系ゴム状重合体もしくは共役ジエン系ゴム状重合体と架橋アクリル酸エステル系重合体を主成分とし、外層が架橋アクリル酸エステル系重合体を主成分とするだけでなく、内層は重量平均粒子径が５０〜３００ｎｍである共役ジエン系ゴム状重合体を２個以上内包し、外層の平均厚さが５〜１００ｎｍであることを特徴とするグラフト共重合体（Ａ）及び該グラフト共重合体（Ａ）から得られた熱可塑性樹脂組成物に関するものである。 That is, the present invention relates to an aromatic vinyl monomer in 10 to 80 parts by weight of a composite rubber composed of 5 to 50% by weight of a conjugated diene rubbery polymer and 50 to 95% by weight of a crosslinked acrylate polymer. A graft copolymer (A) obtained by graft polymerization of 20 to 90 parts by weight of at least one monomer selected from vinyl cyanide monomers and other vinyl monomers copolymerizable therewith The composite rubber has a multilayer structure, the inner layer is mainly composed of a conjugated diene rubber-like polymer or a conjugated diene rubber-like polymer and a crosslinked acrylate polymer, and the outer layer is a crosslinked acrylic. In addition to the acid ester polymer as a main component, the inner layer contains two or more conjugated diene rubber polymers having a weight average particle diameter of 50 to 300 nm, and the average thickness of the outer layer is 5 to 100 nm. Arco It relates graft copolymer (A) and the thermoplastic resin composition obtained from the graft copolymer (A), characterized in.
本発明により耐候性だけでなく、耐衝撃性、及び発色性に優れた熱可塑性樹脂組成物を構成するグラフト共重合体（Ａ）及び該グラフト共重合体（Ａ）から得られた熱可塑性樹脂組成物を提供することが出来る。 Graft copolymer (A) constituting thermoplastic resin composition excellent in not only weather resistance but also impact resistance and color developability according to the present invention, and thermoplastic resin obtained from the graft copolymer (A) A composition can be provided.
以下、本発明を詳しく説明する。
本発明のグラフト共重合体（Ａ）は、共役ジエン系ゴム状重合体と架橋アクリル酸エステル系重合体を主成分とする複合ゴムの存在下に芳香族ビニル系単量体、シアン化ビニル系単量体、及びこれらと共重合可能な他のビニル系単量体から選ばれた少なくとも一種の単量体をグラフト重合して得られた、グラフト共重合体である。
The present invention will be described in detail below.
The graft copolymer (A) of the present invention comprises an aromatic vinyl monomer and a vinyl cyanide monomer in the presence of a composite rubber mainly composed of a conjugated diene rubber polymer and a crosslinked acrylate polymer. A graft copolymer obtained by graft polymerization of a monomer and at least one monomer selected from other vinyl monomers copolymerizable therewith.
本発明で使用される複合ゴムは、共役ジエン系ゴム状重合体ラテックスの存在下で、架橋アクリル酸エステル系重合体を構成する単量体（混合物）を乳化重合することによって得ることができる。 The composite rubber used in the present invention can be obtained by emulsion polymerization of a monomer (mixture) constituting a crosslinked acrylate ester polymer in the presence of a conjugated diene rubbery polymer latex.
本発明で使用される複合ゴムを構成する共役ジエン系ゴム状重合体としては、ポリブタジエンゴム、スチレン−ブタジエンゴム（ＳＢＲ）、スチレン−ブタジエン−スチレン（ＳＢＳ）ブロックコポリマー、スチレン−（エチレン−ブタジエン）−スチレン（ＳＥＢＳ）ブロックコポリマー、アクリロニトリル−ブタジエンゴム（ＮＢＲ）、メチルメタクリレート−ブタジエンゴムが挙げられる。特に、ポリブタジエンゴム、スチレン−ブタジエンゴムが好ましい。 Examples of the conjugated diene rubber-like polymer constituting the composite rubber used in the present invention include polybutadiene rubber, styrene-butadiene rubber (SBR), styrene-butadiene-styrene (SBS) block copolymer, and styrene- (ethylene-butadiene). -Styrene (SEBS) block copolymer, acrylonitrile-butadiene rubber (NBR), methyl methacrylate-butadiene rubber. In particular, polybutadiene rubber and styrene-butadiene rubber are preferable.
本発明で使用される共役ジエン系ゴム状重合体は重量平均粒子径が５０〜３００ｎｍの共役ジエン系ゴム状重合体を凝集肥大化させることで重量平均粒子径を１５０〜８００ｎｍとした共役ジエン系ゴム状重合体を用いる事が好ましく、重量平均粒子径が２００〜６００ｎｍである凝集肥大化した共役ジエン系ゴム状重合体を用いる事が特に好ましい。 The conjugated diene rubbery polymer used in the present invention is a conjugated diene polymer having a weight average particle diameter of 150 to 800 nm by agglomerating and enlarging a conjugated diene rubbery polymer having a weight average particle diameter of 50 to 300 nm. It is preferable to use a rubbery polymer, and it is particularly preferable to use an agglomerated conjugated diene rubbery polymer having a weight average particle diameter of 200 to 600 nm.
本発明で使用される複合ゴムを構成する架橋アクリル酸エステル系重合体は、架橋剤の存在下にアルキル基の炭素数が１〜１６のアクリル酸エステル系単量体、例えばアクリル酸メチル、アクリル酸エチル、アクリル酸ブチル、アクリル酸２−エチルヘキシル等を一種又は二種以上、さらには必要に応じて他の共重合可能な単量体、例えばスチレン、アクリロニトリル、メタクリル酸メチル等を一種又は二種以上を重合して得られる重合体である。 The crosslinked acrylate polymer constituting the composite rubber used in the present invention is an acrylate monomer having an alkyl group having 1 to 16 carbon atoms in the presence of a crosslinking agent, such as methyl acrylate, acrylic. One or two or more kinds of ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, etc., and, if necessary, other copolymerizable monomers such as styrene, acrylonitrile, methyl methacrylate or the like It is a polymer obtained by polymerizing the above.
架橋アクリル酸エステル系重合体に用いられる架橋剤としては、例えばジビニルベンゼン、アリル（メタ）アクリレート、エチレングリコールジ（メタ）アクリレート、ジアリルフタレート、ジシクロペンタジエンジ（メタ）アクリレート、トリメチロールプロパントリ（メタ）アクリレート、ペンタエリスリトールヘキサ（メタ）アクリレート、１，４−ブタンジオールジ（メタ）アクリレート、１，６−ヘキサンジオールジ（メタ）アクリレート、トリアリルシアヌレート、トリアリルイソシアヌレート等が挙げられる。 Examples of the crosslinking agent used in the crosslinked acrylic ester polymer include divinylbenzene, allyl (meth) acrylate, ethylene glycol di (meth) acrylate, diallyl phthalate, dicyclopentadiene di (meth) acrylate, trimethylolpropane tri ( Examples include meth) acrylate, pentaerythritol hexa (meth) acrylate, 1,4-butanediol di (meth) acrylate, 1,6-hexanediol di (meth) acrylate, triallyl cyanurate, triallyl isocyanurate, and the like.
本発明で使用される複合ゴムを構成する、共役ジエン系ゴム状重合体と架橋アクリル酸エステル系重合体の比率は、共役ジエン系ゴム状重合体５〜５０重量％、架橋アクリル酸エステル系重合体５０〜９５重量％であることが必要であるが、耐候性、耐衝撃性、発色性とのバランスの観点から共役ジエン系ゴム状重合体が７〜４０重量％、架橋アクリル酸エステル系重合体が６０〜９３重量％であることが好ましく、共役ジエン系ゴム状重合体が１０〜３０重量％、架橋アクリル酸エステル系重合体７０〜９０重量％であることがより好ましい。 The ratio of the conjugated diene rubbery polymer to the crosslinked acrylate polymer constituting the composite rubber used in the present invention is 5 to 50% by weight of the conjugated diene rubbery polymer, and the crosslinked acrylate polymer weight. The blend needs to be 50 to 95% by weight, but from the viewpoint of the balance between weather resistance, impact resistance and color development, the conjugated diene rubbery polymer is 7 to 40% by weight, and the cross-linked acrylate weight The coalescence is preferably 60 to 93% by weight, more preferably 10 to 30% by weight of the conjugated diene rubbery polymer, and 70 to 90% by weight of the crosslinked acrylate polymer.
本発明で使用される複合ゴムは多層構造を有しているが、コア層とシェル層を有するいわゆるコアシェル構造である場合はコア層が内層に該当し、シェル層が外層に該当する。一方、層構造が３層以上である場合は、共役ジエン系ゴム状重合体を主成分とする内層以外の層を外層とする。 The composite rubber used in the present invention has a multilayer structure, but in the case of a so-called core-shell structure having a core layer and a shell layer, the core layer corresponds to the inner layer and the shell layer corresponds to the outer layer. On the other hand, when the layer structure is three or more layers, the layers other than the inner layer mainly composed of the conjugated diene rubber-like polymer are used as the outer layer.
本発明で使用される複合ゴムは、内層は共役ジエン系ゴム状重合体もしくは共役ジエン系ゴム状重合体と架橋アクリル酸エステル系重合体を主成分とし、外層は架橋アクリル酸エステル系重合体を主成分としている。さらに、複合ゴムは、内層は重量平均粒子径が５０〜３００ｎｍである共役ジエン系ゴム状重合体を２個以上内包し、外層の平均厚さが５〜１００ｎｍであることを特徴とする。 The composite rubber used in the present invention has a conjugated diene rubber-like polymer or a conjugated diene rubber-like polymer and a cross-linked acrylate ester polymer as main components in the inner layer, and an outer layer made of a cross-linked acrylate ester polymer. The main component. Furthermore, the composite rubber is characterized in that the inner layer contains two or more conjugated diene rubber-like polymers having a weight average particle diameter of 50 to 300 nm, and the outer layer has an average thickness of 5 to 100 nm.
内層が共役ジエン系ゴム状重合体の単独粒子を主成分としている場合、もしくは２個以上共役ジエン系ゴム状重合体粒子を内包していても、重量平均粒子径が５０〜３００ｎｍの範囲から外れる場合は耐衝撃性と発色性などの物性バランスに劣る。共役ジエン系ゴム状重合体の重量平均粒子径は７０〜２００ｎｍであることが好ましく、８０〜１５０ｎｍであることがより好ましい。また、架橋アクリル酸エステル系重合体を主成分とする外層の平均厚さが５ｎｍ未満の場合は、共役ジエン系ゴム状重合体部分が紫外線等により分解され易いことから、耐候性が劣り、１００ｎｍを超える場合は、発色性が劣る結果となる。外層の平均厚さは７〜８０ｎｍであることが好ましく、１０〜７０ｎｍであることがより好ましい。 When the inner layer is mainly composed of single particles of a conjugated diene rubber-like polymer, or even when two or more conjugated diene rubber-like polymer particles are included, the weight average particle diameter is out of the range of 50 to 300 nm. In some cases, the balance of physical properties such as impact resistance and color developability is poor. The weight average particle diameter of the conjugated diene rubbery polymer is preferably 70 to 200 nm, and more preferably 80 to 150 nm. Further, when the average thickness of the outer layer mainly composed of a crosslinked acrylate polymer is less than 5 nm, the conjugated diene rubber-like polymer portion is easily decomposed by ultraviolet rays or the like, so that the weather resistance is inferior, and 100 nm. If it exceeds 1, the color developability is inferior. The average thickness of the outer layer is preferably 7 to 80 nm, and more preferably 10 to 70 nm.
架橋アクリル酸エステル系重合体を主成分とする外層の厚さは、共役ジエン系ゴム状重合体にアクリル酸エステル系単量体を乳化重合する際に、共役ジエン系ゴム状重合体粒子中のアクリル酸エステル系単量体の膨潤度を変化させたり、重合途中で重合開始剤を水溶性のものから油溶性のものに置換したり、又は重合途中で開始剤濃度を変化させることで適宜調製することが可能である。具体的には重合初期にアクリル酸エステル系単量体の添加量を多くして共役ジエン系ゴム状重合体粒子に含浸させる方法や、２段重合法において、１段目重合時に油溶性開始剤を使用し、２段目重合時に水溶性開始剤に変更させる方法や、１段目と２段目重合時との開始剤濃度を変更するなどの方法が有効的である。 The thickness of the outer layer mainly composed of a cross-linked acrylic ester polymer is determined by the amount of the conjugated diene rubber-like polymer particles in the conjugated diene rubber-like polymer particles during emulsion polymerization of the acrylate monomer. It is prepared as appropriate by changing the degree of swelling of the acrylic ester monomer, replacing the polymerization initiator from water-soluble to oil-soluble during polymerization, or changing the initiator concentration during polymerization. Is possible. Specifically, in the method of increasing the amount of acrylate monomer added at the initial stage of polymerization and impregnating the conjugated diene rubber-like polymer particles, or in the two-stage polymerization method, an oil-soluble initiator during the first-stage polymerization. And a method of changing to a water-soluble initiator during the second stage polymerization and a method of changing the initiator concentration between the first stage and the second stage polymerization are effective.
上述の複合ゴムを重合する際、使用する重合開始剤としては、過硫酸カリウム、過硫酸ナトリウム、過硫酸アンモニウム等の水溶性重合開始剤、クメンハイドロパーオキサイド、過酸化ベンゾイル、t−ブチルハイドロパーオキサイド、アセチルパーオキサイド、ジイソプロピルベンゼンハイドロパーオキサイド、１，１，３，３−テトラメチルブチルハイドロパーオキサイド等の油溶性重合開始剤を適宜用いることができる。さらに、本発明において好ましく用いられる還元剤の具体例としては、硫酸第一鉄７水塩、亜硫酸塩、亜硫酸水素塩、ピロ亜硫酸塩、亜ニチオン酸塩、ニチオン酸塩、チオ硫酸塩、ホルムアルデヒドスルホン酸塩、ベンズアルデヒドスルホン酸塩、また、Ｌ−アスコルビン酸、酒石酸、クエン酸などのカルボン酸類、更にはラクトース、デキストロース、サッカロースなどの還元糖類、更にはジメチルアニリン、トリエタノールアミンなどのアミン類が挙げられる。またキレート剤としては、ピロリン酸四ナトリウム、エチレンジアミン四酢酸ナトリウムなどが挙げられる。 When polymerizing the above-mentioned composite rubber, the polymerization initiator used includes water-soluble polymerization initiators such as potassium persulfate, sodium persulfate, and ammonium persulfate, cumene hydroperoxide, benzoyl peroxide, and t-butyl hydroperoxide. Oil-soluble polymerization initiators such as acetyl peroxide, diisopropylbenzene hydroperoxide, 1,1,3,3-tetramethylbutyl hydroperoxide can be appropriately used. Furthermore, specific examples of the reducing agent preferably used in the present invention include ferrous sulfate heptahydrate, sulfite, bisulfite, pyrosulfite, nitrite, nithionate, thiosulfate, formaldehyde sulfone. Acid salts, benzaldehyde sulfonates, carboxylic acids such as L-ascorbic acid, tartaric acid and citric acid, and reducing sugars such as lactose, dextrose and saccharose, and amines such as dimethylaniline and triethanolamine. It is done. Examples of the chelating agent include tetrasodium pyrophosphate and sodium ethylenediaminetetraacetate.
本発明のグラフト共重合体（Ａ）は、上述の複合ゴムの存在下に、芳香族ビニル系単量体、シアン化ビニル系単量体、及びこれらと共重合可能な他のビニル系単量体から選ばれた少なくとも一種の単量体をグラフト重合して得られるグラフト共重合体である。 The graft copolymer (A) of the present invention comprises an aromatic vinyl monomer, a vinyl cyanide monomer, and other vinyl monomers copolymerizable therewith in the presence of the above composite rubber. A graft copolymer obtained by graft polymerization of at least one monomer selected from the body.
本発明のグラフト共重合体（Ａ）は該グラフト共重合体（Ａ）１００重量部中に複合ゴムが１０〜８０重量部含まれている必要がある。複合ゴムが１０重量部より少ないと耐衝撃性に劣る。また、８０重量部を超えると発色性に劣る。グラフト共重合体（Ａ）中の複合ゴムの含有量は３０〜７０重量部であることが好ましく、４０〜６０重量部であることがより好ましい。 The graft copolymer (A) of the present invention needs to contain 10 to 80 parts by weight of composite rubber in 100 parts by weight of the graft copolymer (A). If the composite rubber is less than 10 parts by weight, the impact resistance is poor. Moreover, when it exceeds 80 weight part, it is inferior to color developability. The content of the composite rubber in the graft copolymer (A) is preferably 30 to 70 parts by weight, and more preferably 40 to 60 parts by weight.
グラフト共重合体（Ａ）を構成する芳香族ビニル系単量体としては、スチレン、α−メチルスチレン、パラメチルスチレン、ブロムスチレン等が挙げられ、一種又は二種以上用いることができる。特にスチレン、α−メチルスチレンが好ましい。 Examples of the aromatic vinyl monomer constituting the graft copolymer (A) include styrene, α-methylstyrene, paramethylstyrene, bromostyrene, and the like, and one or more of them can be used. In particular, styrene and α-methylstyrene are preferable.
グラフト共重合体（Ａ）を構成するシアン化ビニル系単量体としては、アクリロニトリル、メタクリロニトリル、エタクリロニトリル、フマロニトリル等が挙げられ、一種又は二種以上用いることができる。特にアクリロニトリルが好ましい。 Examples of the vinyl cyanide monomer constituting the graft copolymer (A) include acrylonitrile, methacrylonitrile, ethacrylonitrile, fumaronitrile and the like, and one or more of them can be used. Particularly preferred is acrylonitrile.
共重合可能な他のビニル系単量体としては、（メタ）アクリル酸エステル系単量体、マレイミド系単量体、アミド系単量体等が挙げられ、一種又は二種以上用いることができる。（メタ）アクリル酸エステル系単量体としては（メタ）アクリル酸メチル、（メタ）アクリル酸エチル、（メタ）アクリル酸プロピル、（メタ）アクリル酸ブチル、アクリル酸２−エチルヘキシル、（メタ）アクリル酸フェニル、（メタ）アクリル酸４−ｔ−ブチルフェニル、（メタ）アクリル酸（ジ）ブロモフェニル、（メタ）アクリル酸クロルフェニル等を例示でき、マレイミド系単量体としてはＮ−フェニルマレイミド、Ｎ−シクロヘキシルマレイミド等を例示でき、アミド系単量体としてはアクリルアミド、メタクリルアミド等を例示できる。 Examples of other copolymerizable vinyl monomers include (meth) acrylic acid ester monomers, maleimide monomers, amide monomers, and the like, and one or more can be used. . (Meth) acrylic acid ester monomers include methyl (meth) acrylate, ethyl (meth) acrylate, propyl (meth) acrylate, butyl (meth) acrylate, 2-ethylhexyl acrylate, (meth) acrylic Examples include phenyl acid, 4-t-butylphenyl (meth) acrylate, (di) bromophenyl (meth) acrylic acid, chlorophenyl (meth) acrylate, and the maleimide monomer includes N-phenylmaleimide, N-cyclohexylmaleimide and the like can be exemplified, and examples of the amide monomer include acrylamide and methacrylamide.
複合ゴムとグラフト重合する、上述の単量体の組成比率に特に制限はないが、芳香族ビニル系単量体６０〜９０重量％、シアン化ビニル系単量体１０〜４０重量％及び共重合可能な他のビニル系単量体０〜３０重量％の組成比率、芳香族ビニル系単量体３０〜８０重量％、（メタ）アクリル酸エステル系単量体２０〜７０重量％及び共重合可能な他のビニル系単量体０〜５０重量％の組成比率、芳香族ビニル系単量体２０〜７０重量％、（メタ）アクリル酸エステル系単量体２０〜７０重量％、シアン化ビニル系単量体１０〜６０重量％及び共重合可能な他のビニル系単量体０〜３０重量％の組成比率等であることが好ましい。 There is no particular limitation on the composition ratio of the above-mentioned monomer that is graft-polymerized with the composite rubber, but the aromatic vinyl-based monomer is 60 to 90% by weight, the vinyl cyanide-based monomer is 10 to 40% by weight, and copolymerization Possible composition ratio of 0-30% by weight of other vinyl monomers, 30-80% by weight of aromatic vinyl monomers, 20-70% by weight of (meth) acrylate monomers, and copolymerizable Other vinyl monomer composition ratio of 0 to 50% by weight, aromatic vinyl monomer 20 to 70% by weight, (meth) acrylic acid ester monomer 20 to 70% by weight, vinyl cyanide The composition ratio is preferably 10 to 60% by weight of the monomer and 0 to 30% by weight of another copolymerizable vinyl monomer.
本発明のグラフト共重合体（Ａ）を重合するための手法に特に制限はなく、乳化重合法、懸濁重合法、塊状重合法等を用いることが出来る。乳化重合法を用いた場合、上述の複合ゴムに上述の単量体をグラフト重合することによって、グラフト共重合体（Ａ）のラテックスを得ることが出来る。グラフト共重合体（Ａ）のラテックスは、公知の方法により凝固され、洗浄、脱水、乾燥工程を経ることでグラフト共重合体（Ａ）のパウダーを得ることができる。 There is no restriction | limiting in particular in the method for superposing | polymerizing the graft copolymer (A) of this invention, An emulsion polymerization method, suspension polymerization method, block polymerization method, etc. can be used. When the emulsion polymerization method is used, a latex of the graft copolymer (A) can be obtained by graft polymerization of the above-described monomer to the above-described composite rubber. The latex of the graft copolymer (A) is coagulated by a known method, and the powder of the graft copolymer (A) can be obtained through washing, dehydration, and drying steps.
本発明のグラフト共重合体（Ａ）のグラフト率（グラフト共重合体のアセトン可溶分量と不溶分量及びグラフト共重合体中の複合ゴムの重量から求める。）、及びアセトン可溶分の還元粘度（０．４ｇ/１００ｃｃ、Ｎ，Ｎジメチルホルムアミド溶液として３０℃で測定）に特に制限はなく、要求性能によって任意の構造のものを使用することができるが、物性バランスの観点から、グラフト率は１０〜１３０％であることが好ましく、還元粘度は０．２〜２．０ｄｌ／ｇであることが好ましい。 Graft ratio of graft copolymer (A) of the present invention (determined from the amount of acetone-soluble and insoluble components of the graft copolymer and the weight of the composite rubber in the graft copolymer), and the reduced viscosity of the acetone-soluble component. (0.4 g / 100 cc, measured at 30 ° C. as a N, N dimethylformamide solution) There is no particular limitation, and any structure can be used depending on the required performance, but from the viewpoint of balance of physical properties, the graft ratio is It is preferably 10 to 130%, and the reduced viscosity is preferably 0.2 to 2.0 dl / g.
また、得られたグラフト共重合体（Ａ）は単独で使用できるが、必要に応じて芳香族ビニル系単量体、シアン化ビニル系単量体、必要に応じてその他の共重合可能な他のビニル系単量体を共重合することで得られる共重合体（Ｂ）と混合し、熱可塑性樹脂組成物として使用することもできる。共重合体（Ｂ）と混合する場合は熱可塑性樹脂組成物中の複合ゴム含有量が５〜５０重量％とすることが物性バランスの観点から好ましく、１０〜３０重量％とすることがより好ましい。 The obtained graft copolymer (A) can be used alone, but if necessary, an aromatic vinyl monomer, a vinyl cyanide monomer, or other copolymerizable other if necessary. It can also be used as a thermoplastic resin composition by mixing with a copolymer (B) obtained by copolymerizing the vinyl monomer. In the case of mixing with the copolymer (B), the content of the composite rubber in the thermoplastic resin composition is preferably 5 to 50% by weight from the viewpoint of balance of physical properties, more preferably 10 to 30% by weight. .
本発明の熱可塑性樹脂組成物は、必要に応じてヒンダードアミン系の光安定剤、ヒンダードフェノール系、含硫黄有機化合物系、含リン有機化合物系等の酸化防止剤、フェノール系、アクリレート系等の熱安定剤、ベンゾエート系、ベンゾトリアゾール系、ベンゾフェノン系、サリシレート系の紫外線吸収剤、有機ニッケル系、高級脂肪酸アミド類等の滑剤、リン酸エステル類等の可塑剤、ポリブロモフェニルエーテル、テトラブロモビスフェノール−Ａ、臭素化エポキシオリゴマー、臭素化等の含ハロゲン系化合物、リン系化合物、三酸化アンチモン等の難燃剤・難燃助剤、臭気マスキング剤、カーボンブラック、酸化チタン、顔料、及び染料等を添加することもできる。更に、タルク、炭酸カルシウム、水酸化アルミニウム、ガラス繊維、ガラスフレーク、ガラスビーズ、炭素繊維、金属繊維等の補強剤や充填剤を添加することもできる。 The thermoplastic resin composition of the present invention includes hindered amine-based light stabilizers, hindered phenol-based, sulfur-containing organic compound-based, phosphorus-containing organic compound-based antioxidants, phenol-based, acrylate-based and the like as necessary. Thermal stabilizer, benzoate, benzotriazole, benzophenone, salicylate UV absorbers, organic nickel, lubricants such as higher fatty acid amides, plasticizers such as phosphate esters, polybromophenyl ether, tetrabromobisphenol -A, brominated epoxy oligomers, halogenated compounds such as brominated compounds, phosphorus compounds, flame retardants and flame retardants such as antimony trioxide, odor masking agents, carbon black, titanium oxide, pigments, dyes, etc. It can also be added. Furthermore, reinforcing agents and fillers such as talc, calcium carbonate, aluminum hydroxide, glass fiber, glass flake, glass bead, carbon fiber, and metal fiber can be added.
本発明の熱可塑性樹脂組成物は、上述の成分を混合することで得ることができる。混合するために、例えば、押出し機、ロール、バンバリーミキサー、ニーダー等の公知の混練装置を用いることができる。 The thermoplastic resin composition of the present invention can be obtained by mixing the above-described components. In order to mix, well-known kneading apparatuses, such as an extruder, a roll, a Banbury mixer, a kneader, can be used, for example.
以下に実施例を示して本発明を具体的に説明するが、本発明はこれらによって何ら制限されるものではない。なお、実施例中にて示す「部」及び「％」は重量に基づくものである。 EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples. In the examples, “parts” and “%” are based on weight.
表１に示す複合ゴムを用いてグラフト共重合体（Ａ）を作成した。表１で示す各成分は以下の通りである。 A graft copolymer (A) was prepared using the composite rubber shown in Table 1. Each component shown in Table 1 is as follows.
共役ジエン系ゴム状重合体ラテックスの製造
小粒子径スチレン−ブタジエンゴムラテックスの製造
１０リットルの耐圧容器の内部を窒素で置換後、１，３−ブタジエン９７重量部、スチレン３重量部、ｎ−ドデシルメルカプタン０．４５重量部、過硫酸カリウム０．３重量部、不均化ロジン酸ナトリウム１．８５重量部、水酸化ナトリウム０．１重量部、脱イオン水１５５重量部を仕込み、攪拌しつつ７０℃で８時間反応させた。その後、不均化ロジン酸ナトリウム０．２１重量部、水酸化ナトリウム０．１重量部及び脱イオン水５重量部を添加した。さらに温度を７０℃に維持しながら６時間攪拌を継続して反応を終了した。その後、減圧して残存している１，３−ブタジエンを除去し、スチレン−ブタジエンゴムラテックスを得た。得られたスチレン−ブタジエンゴムラテックスを、四酸化オスミウム（ＯｓＯ４）で染色し、乾燥後に透過型電子顕微鏡で写真撮影した。画像解析処理装置（装置名：旭化成（株）製 ＩＰ−１０００ＰＣ）を用いて８００個のゴム粒子の面積を計測し、その円相当径（直径）を求め、スチレン−ブタジエンゴムの重量平均粒子径を算出した結果、重量平均粒子径は１０５ｎｍであった。
Production of conjugated diene rubbery polymer latex
Manufacture of small particle size styrene-butadiene rubber latex After replacing the inside of a 10 liter pressure vessel with nitrogen, 97 parts by weight of 1,3-butadiene, 3 parts by weight of styrene, 0.45 parts by weight of n-dodecyl mercaptan, potassium persulfate 0.3 parts by weight, 1.85 parts by weight of disproportionated sodium rosin acid, 0.1 part by weight of sodium hydroxide, and 155 parts by weight of deionized water were charged and reacted at 70 ° C. for 8 hours while stirring. Thereafter, 0.21 parts by weight of disproportionated sodium rosinate, 0.1 parts by weight of sodium hydroxide and 5 parts by weight of deionized water were added. Further, stirring was continued for 6 hours while maintaining the temperature at 70 ° C. to complete the reaction. Thereafter, the remaining 1,3-butadiene was removed under reduced pressure to obtain a styrene-butadiene rubber latex. The obtained styrene-butadiene rubber latex was dyed with osmium tetroxide (OsO 4 ), dried, and photographed with a transmission electron microscope. The area of 800 rubber particles was measured using an image analysis processor (apparatus name: IP-1000PC, manufactured by Asahi Kasei Co., Ltd.), the equivalent circle diameter (diameter) was obtained, and the weight average particle diameter of styrene-butadiene rubber As a result, the weight average particle size was 105 nm.
凝集肥大化スチレン−ブタジエンゴムラテックス（１）の製造
１０リットルの耐圧容器に、重合水１８５重量部、小粒子径スチレン−ブタジエンゴムラテックス１００重量部（固形分）、ドデシルベンゼンスルホン酸ナトリウム０．０２重量部を添加して１０分間攪拌混合した後、５％リン酸水溶液２０重量部を１０分間にわたり添加した。次いで１０％水酸化カリウム水溶液１０重量部を添加し、凝集肥大化したスチレン−ブタジエンゴムラテックス（１）を得た。
上述の方法で、凝集肥大化スチレン−ブタジエンゴムの重量平均粒子径を算出した結果、重量平均粒子径は４５０ｎｍであった。
Production of Agglomerated Styrene-Butadiene Rubber Latex (1) In a 10 liter pressure vessel, 185 parts by weight of polymerized water, 100 parts by weight of small particle size styrene-butadiene rubber latex (solid content), 0.02 sodium dodecylbenzenesulfonate After adding parts by weight and stirring and mixing for 10 minutes, 20 parts by weight of 5% phosphoric acid aqueous solution was added over 10 minutes. Subsequently, 10 parts by weight of a 10% aqueous potassium hydroxide solution was added to obtain an agglomerated styrene-butadiene rubber latex (1).
As a result of calculating the weight average particle size of the agglomerated styrene-butadiene rubber by the above-described method, the weight average particle size was 450 nm.
凝集肥大化スチレン−ブタジエンゴムラテックス（２）の製造
１０リットルの耐圧容器に、重合水１８５重量部、小粒子径スチレン−ブタジエンゴムラテックス１００重量部（固形分）、ドデシルベンゼンスルホン酸ナトリウム０．０５重量部を添加して１０分間攪拌混合した後、５％リン酸水溶液２０重量部を１０分間にわたり添加した。次いで１０％水酸化カリウム水溶液１０重量部を添加し、凝集肥大化したスチレン−ブタジエンゴムラテックス（２）を得た。
上述の方法で、凝集肥大化スチレン−ブタジエンゴムの重量平均粒子径を算出した結果、重量平均粒子径は２３３ｎｍであった。
Production of Agglomerated Styrene-Butadiene Rubber Latex (2) In a 10-liter pressure vessel, 185 parts by weight of polymerized water, 100 parts by weight of a small particle size styrene-butadiene rubber latex (solid content), sodium dodecylbenzenesulfonate 0.05 After adding parts by weight and stirring and mixing for 10 minutes, 20 parts by weight of 5% phosphoric acid aqueous solution was added over 10 minutes. Next, 10 parts by weight of a 10% aqueous potassium hydroxide solution was added to obtain an agglomerated styrene-butadiene rubber latex (2).
As a result of calculating the weight average particle size of the agglomerated styrene-butadiene rubber by the above-described method, the weight average particle size was 233 nm.
非凝集肥大化スチレン−ブタジエンゴムラテックス（３）の製造
１０リットルの耐圧容器の内部を窒素で置換後、１，３−ブタジエン９０重量部、スチレン１０重量部、ｎ−ドデシルメルカプタン０．３重量部、過硫酸カリウム０．３１重量部、不均化ロジン酸ナトリウム０．２０重量部、水酸化ナトリウム０．１０重量部、脱イオン水７３重量部を仕込み、攪拌しつつ６５℃で反応させた。１０時間目、２０時間目、３０時間目、４０時間目にそれぞれ不均化ロジン酸ナトリウム０．３５重量部、水酸化ナトリウム０．１０重量部及び脱イオン水７．５重量部を添加し４５時間反応させた。その後、不均化ロジン酸ナトリウム０．２重量部、水酸化ナトリウム０．１重量部及び脱イオン水５重量部を添加した。さらに温度を７０℃に維持しながら７時間攪拌を継続して反応を終了した。その後、減圧して残存している１，３−ブタジエンを除去し、スチレン−ブタジエンゴムラテックス（３）を得た。上述の方法で、重量平均粒子径を算出した結果、重量平均粒子径は４２０ｎｍであった。
Production of non-aggregated enlarged styrene-butadiene rubber latex (3) After replacing the inside of a 10 liter pressure vessel with nitrogen, 90 parts by weight of 1,3-butadiene, 10 parts by weight of styrene, 0.3 parts by weight of n-dodecyl mercaptan Then, 0.31 part by weight of potassium persulfate, 0.20 part by weight of disproportionated sodium rosinate, 0.10 part by weight of sodium hydroxide and 73 parts by weight of deionized water were charged and reacted at 65 ° C. with stirring. At 10 hours, 20 hours, 30 hours, and 40 hours, 0.35 parts by weight of disproportionated sodium rosinate, 0.10 parts by weight of sodium hydroxide, and 7.5 parts by weight of deionized water were added. Reacted for hours. Thereafter, 0.2 parts by weight of disproportionated sodium rosinate, 0.1 parts by weight of sodium hydroxide and 5 parts by weight of deionized water were added. Further, stirring was continued for 7 hours while maintaining the temperature at 70 ° C. to complete the reaction. Thereafter, the remaining 1,3-butadiene was removed under reduced pressure to obtain a styrene-butadiene rubber latex (3). As a result of calculating the weight average particle diameter by the above-mentioned method, the weight average particle diameter was 420 nm.
複合ゴムの製造
複合ゴムラテックス（ａ−１）の製造
１０Ｌのガラスリアクターに、上記の凝集肥大化スチレン−ブタジエンゴムラテックス（１）を２０重量部（固形分）、脱イオン水を１００重量部仕込み、窒素置換を行った。窒素置換後、槽内を昇温し４５℃に到達したところで脱イオン水２０重量部にラクトース０．３重量部、ピロリン酸四ナトリウム０．０８重量部及び硫酸第１鉄・７水和物０．００１重量部を溶解した水溶液を添加した。さらに、アクリル酸ブチル３０重量部、メタクリル酸アリル０．１重量部を添加した。槽内の温度が４８℃に到達した後、そのまま１時間保持した。さらに１段目重合として槽内の温度が５０℃に到達した後、クメンハイドロパーオキサイド０．２重量部を一括添加し、脱イオン水２０重量部にアルケニルコハク酸ジカリウム０．９重量部、ホルムアルデヒドナトリウムスルホシレート０．０８重量部を溶解した水溶液とアクリル酸ブチル３０重量部、メタクリル酸アリル０．０５重量部を２時間かけて連続的に滴下した。滴下後、１時間保持して、１段目重合を終了した。さらに２段目重合として槽内の温度が６５℃に到達した後、ホルムアルデヒドナトリウムスルホシレート０．０４重量部を一括添加し、脱イオン水２０重量部に過硫酸カリウム０．４重量部を溶解した水溶液とアクリル酸ブチル２０重量部、メタクリル酸アリル０．０５重量部を４時間かけて連続的に滴下した。滴下後、転化率が９７％以上のところで重合を終了した。凝集肥大化スチレン−ブタジエンゴム（１）と架橋アクリル酸ブチル重合体から構成される複合ゴムラテックス（a−１）を得た。
Manufacture of composite rubber
Manufacture of composite rubber latex (a-1) A 10 L glass reactor is charged with 20 parts by weight (solid content) of the above-mentioned agglomerated styrene-butadiene rubber latex (1) and 100 parts by weight of deionized water, and nitrogen replacement is performed. went. After nitrogen substitution, when the temperature inside the tank reached 45 ° C, 0.3 parts by weight of lactose, 0.08 parts by weight of tetrasodium pyrophosphate, and ferrous sulfate and heptahydrate 0 were added to 20 parts by weight of deionized water. An aqueous solution in which 0.001 part by weight was dissolved was added. Furthermore, 30 parts by weight of butyl acrylate and 0.1 parts by weight of allyl methacrylate were added. After the temperature in the tank reached 48 ° C., it was kept for 1 hour. Furthermore, after the temperature in the tank reaches 50 ° C. as the first stage polymerization, 0.2 parts by weight of cumene hydroperoxide is added all at once, 0.9 parts by weight of dipotassium alkenyl succinate and 20 parts by weight of deionized water, formaldehyde An aqueous solution in which 0.08 part by weight of sodium sulfosylate was dissolved, 30 parts by weight of butyl acrylate, and 0.05 part by weight of allyl methacrylate were continuously added dropwise over 2 hours. After the dropwise addition, the first stage polymerization was completed by holding for 1 hour. Furthermore, as the second stage polymerization, after the temperature in the tank reached 65 ° C., 0.04 part by weight of sodium formaldehyde sulfosylate was added all at once, and 0.4 part by weight of potassium persulfate was dissolved in 20 parts by weight of deionized water. The resulting aqueous solution, 20 parts by weight of butyl acrylate, and 0.05 parts by weight of allyl methacrylate were continuously added dropwise over 4 hours. After dropping, the polymerization was terminated when the conversion rate was 97% or more. A composite rubber latex (a-1) composed of agglomerated and enlarged styrene-butadiene rubber (1) and a crosslinked butyl acrylate polymer was obtained.
複合ゴム（ａ−１）の外層の厚さの計測は、以下に記載する方法で行った。表２の実施例１に示す組成割合を有する熱可塑性樹脂組成物のペレットを、クライオミクロトームを用いて−８５℃の低温で切り出すことで、超薄切片を得た。得られた超薄切片を四酸化ルテニウム（ＲｕＯ４）で染色し、透過電子顕微鏡（ＪＥＭ−１４００：日本電子製）を用いて観察及び写真撮影した。得られた写真は複合ゴム粒子の外層と内層の境界線が濃い色で表されるため、画像解析装置（旭化成 ＩＰ−１０００ＰＣ）を用いて、個々の複合ゴム粒子について、外層を含む面積の計測から、複合ゴム粒子の円相当径（半径）を求め、更に外層を除く内層部分についても、同様に円相当径（半径）を求めた。両者の差が外層の厚さを示すことになる。本発明でいう外層の平均厚さは、複合ゴム粒子１５個以上について測定した平均値である。画像解析を行った結果、複合ゴム（ａ−１）の外層の平均厚さは４８ｎｍであった。 The thickness of the outer layer of the composite rubber (a-1) was measured by the method described below. The pellet of the thermoplastic resin composition having the composition ratio shown in Example 1 in Table 2 was cut out at a low temperature of −85 ° C. using a cryomicrotome to obtain an ultrathin slice. The obtained ultrathin sections were stained with ruthenium tetroxide (RuO 4 ), and observed and photographed using a transmission electron microscope (JEM-1400: manufactured by JEOL Ltd.). Since the obtained photograph shows the boundary line between the outer layer and inner layer of the composite rubber particles in a dark color, the area including the outer layer is measured for each composite rubber particle using an image analysis device (Asahi Kasei IP-1000PC). From this, the equivalent circle diameter (radius) of the composite rubber particles was obtained, and the equivalent circle diameter (radius) was similarly obtained for the inner layer portion excluding the outer layer. The difference between them indicates the thickness of the outer layer. The average thickness of the outer layer referred to in the present invention is an average value measured for 15 or more composite rubber particles. As a result of image analysis, the average thickness of the outer layer of the composite rubber (a-1) was 48 nm.
複合ゴムラテックス（ａ−２）の製造
１０Ｌのガラスリアクターに、上記の凝集肥大化スチレン−ブタジエンゴムラテックス（１）を２０重量部（固形分）、脱イオン水を１００重量部仕込み、窒素置換を行った。窒素置換後、槽内を昇温し４５℃に到達したところで脱イオン水２０重量部にラクトース０．３５重量部、ピロリン酸四ナトリウム０．０９重量部及び硫酸第１鉄・７水和物０．００３重量部、β‐ナフタレンスルホン酸ホルマリン縮合物ナトリウム塩０．００１重量部を溶解した水溶液を添加した。さらに、アクリル酸ブチル２０重量部、メタクリル酸アリル０．１重量部を添加した。槽内の温度が４８℃に到達した後、そのまま０．５時間保持した。さらに１段目重合として槽内の温度が５０℃に到達した後、クメンハイドロパーオキサイド０．１５重量部を一括添加し、脱イオン水２０重量部にアルケニルコハク酸ジカリウム０．９重量部、ホルムアルデヒドナトリウムスルホシレート０．０８重量部を溶解した水溶液とアクリル酸ブチル２５重量部、メタクリル酸アリル０．１重量部を２時間かけて連続的に滴下した。滴下後、１時間保持して、１段目重合を終了した。さらに２段目重合として槽内の温度が６５℃に到達した後、ホルムアルデヒドナトリウムスルホシレート０．０５重量部を一括添加し、脱イオン水２０重量部に過硫酸カリウム０．５重量部を溶解した水溶液とアクリル酸ブチル３５重量部、メタクリル酸アリル０．１５重量部を４時間かけて連続的に滴下した。滴下後、転化率が９７％以上のところで重合を終了した。凝集肥大化スチレン−ブタジエンゴム（１）と架橋アクリル酸ブチル重合体から構成される複合ゴムラテックス（a−２）を得た。表２の実施例４に示す組成割合を有する熱可塑性樹脂組成物のペレットを用いた以外は、複合ゴム（ａ−１）と同様の方法で外層の平均厚さを求めた。外層の平均厚さは８２ｎｍであった。
Manufacture of composite rubber latex (a-2) A 10-liter glass reactor is charged with 20 parts by weight (solid content) of the above-mentioned agglomerated styrene-butadiene rubber latex (1) and 100 parts by weight of deionized water, and nitrogen replacement is performed. went. After nitrogen substitution, when the temperature inside the tank reached 45 ° C., 20 parts by weight of deionized water, 0.35 parts by weight of lactose, 0.09 parts by weight of tetrasodium pyrophosphate and ferrous sulfate / pentahydrate 0 An aqueous solution in which 0.003 part by weight and 0.001 part by weight of β-naphthalenesulfonic acid formalin condensate sodium salt were dissolved was added. Furthermore, 20 parts by weight of butyl acrylate and 0.1 parts by weight of allyl methacrylate were added. After the temperature in the tank reached 48 ° C., it was kept as it was for 0.5 hour. Furthermore, after the temperature in the tank reaches 50 ° C. as the first stage polymerization, 0.15 parts by weight of cumene hydroperoxide is added all at once, 0.9 parts by weight of dipotassium alkenyl succinate is added to 20 parts by weight of deionized water, and formaldehyde. An aqueous solution in which 0.08 part by weight of sodium sulfosylate was dissolved, 25 parts by weight of butyl acrylate, and 0.1 part by weight of allyl methacrylate were continuously added dropwise over 2 hours. After the dropwise addition, the first stage polymerization was completed by holding for 1 hour. Further, as the second stage polymerization, after the temperature in the tank reaches 65 ° C., 0.05 part by weight of sodium formaldehyde sulfosylate is added all at once, and 0.5 part by weight of potassium persulfate is dissolved in 20 parts by weight of deionized water. The aqueous solution, 35 parts by weight of butyl acrylate, and 0.15 parts by weight of allyl methacrylate were continuously added dropwise over 4 hours. After dropping, the polymerization was terminated when the conversion rate was 97% or more. A composite rubber latex (a-2) composed of agglomerated and enlarged styrene-butadiene rubber (1) and a crosslinked butyl acrylate polymer was obtained. The average thickness of the outer layer was determined in the same manner as for the composite rubber (a-1) except that pellets of the thermoplastic resin composition having the composition ratio shown in Example 4 of Table 2 were used. The average thickness of the outer layer was 82 nm.
複合ゴムラテックス（ａ−３）の製造
１０Ｌのガラスリアクターに、上記の凝集肥大化スチレン−ブタジエンゴムラテックス（１）を４８重量部（固形分）、脱イオン水を１００重量部仕込み、窒素置換を行った。窒素置換後、槽内を昇温し４５℃に到達したところで脱イオン水２０重量部にラクトース０．３５重量部、ピロリン酸四ナトリウム０．０９重量部及び硫酸第１鉄・７水和物０．００３重量部を溶解した水溶液を添加した。さらに、アクリル酸ブチル２２重量部、メタクリル酸アリル０．０５重量部を添加した。槽内の温度が４８℃に到達した後、そのまま１時間保持した。さらに１段目重合として槽内の温度が５２℃に到達した後、クメンハイドロパーオキサイド０．１５重量部を一括添加し、脱イオン水１９重量部にアルケニルコハク酸ジカリウム０．４５重量部、ホルムアルデヒドナトリウムスルホシレート０．０８重量部を溶解した水溶液とアクリル酸ブチル２０重量部、メタクリル酸アリル０．０５重量部を２時間かけて連続的に滴下した。滴下後、１時間保持して、１段目重合を終了した。さらに２段目重合として槽内の温度が６５℃に到達した後、ホルムアルデヒドナトリウムスルホシレート０．０２重量部を一括添加し、脱イオン水２０重量部にｔ−ブチルハイドロパーオキサイド０．１重量部、アルケニルコハク酸ジカリウム０．２５重量部を溶解した水溶液とアクリル酸ブチル１０重量部、メタクリル酸アリル０．０１重量部を５時間かけて連続的に滴下した。滴下後、転化率が９７％以上のところで重合を終了した。凝集肥大化スチレン−ブタジエンゴム（１）と架橋アクリル酸ブチル重合体から構成される複合ゴムラテックス（a−３）を得た。表２の実施例５に示す組成割合を有する熱可塑性樹脂組成物のペレットを用いた以外は、複合ゴム（ａ−１）と同様の方法で外層の平均厚さを求めた。外層の平均厚さは１０ｎｍであった。
Manufacture of composite rubber latex (a-3) A 10 L glass reactor is charged with 48 parts by weight (solid content) of the above-mentioned agglomerated styrene-butadiene rubber latex (1) and 100 parts by weight of deionized water, and nitrogen replacement is performed. went. After nitrogen substitution, when the temperature inside the tank reached 45 ° C., 20 parts by weight of deionized water, 0.35 parts by weight of lactose, 0.09 parts by weight of tetrasodium pyrophosphate and ferrous sulfate / pentahydrate 0 An aqueous solution having 0.003 parts by weight dissolved therein was added. Furthermore, 22 parts by weight of butyl acrylate and 0.05 parts by weight of allyl methacrylate were added. After the temperature in the tank reached 48 ° C., it was kept for 1 hour. Further, as the first stage polymerization, after the temperature in the tank reached 52 ° C., 0.15 parts by weight of cumene hydroperoxide was added all at once, and 0.45 parts by weight of dipotassium alkenyl succinate was added to 19 parts by weight of deionized water. An aqueous solution in which 0.08 part by weight of sodium sulfosylate was dissolved, 20 parts by weight of butyl acrylate, and 0.05 part by weight of allyl methacrylate were continuously added dropwise over 2 hours. After the dropwise addition, the first stage polymerization was completed by holding for 1 hour. Furthermore, after the temperature in the tank reaches 65 ° C. as the second stage polymerization, 0.02 part by weight of sodium formaldehyde sulfosylate is added all at once, and 0.1 part by weight of t-butyl hydroperoxide is added to 20 parts by weight of deionized water. Parts, an aqueous solution in which 0.25 parts by weight of dipotassium alkenyl succinate was dissolved, 10 parts by weight of butyl acrylate, and 0.01 parts by weight of allyl methacrylate were continuously added dropwise over 5 hours. After dropping, the polymerization was terminated when the conversion rate was 97% or more. A composite rubber latex (a-3) composed of agglomerated and enlarged styrene-butadiene rubber (1) and a crosslinked butyl acrylate polymer was obtained. The average thickness of the outer layer was determined in the same manner as for the composite rubber (a-1) except that the thermoplastic resin composition pellets having the composition ratio shown in Example 5 of Table 2 were used. The average thickness of the outer layer was 10 nm.
複合ゴムラテックス（ａ−４）の製造
１０Ｌのガラスリアクターに、上記の凝集肥大化スチレン−ブタジエンゴムラテックス（２）を２０重量部（固形分）、脱イオン水を１００重量部仕込み、窒素置換を行った。窒素置換後、槽内を昇温し４５℃に到達したところで脱イオン水２０重量部にラクトース０．３重量部、ピロリン酸四ナトリウム０．０８重量部及び硫酸第１鉄・７水和物０．００１重量部を溶解した水溶液を添加した。さらに、アクリル酸ブチル３０重量部、メタクリル酸アリル０．１重量部を添加した。槽内の温度が４８℃に到達した後、そのまま１時間保持した。さらに１段目重合として槽内の温度が５０℃に到達した後、クメンハイドロパーオキサイド０．２重量部を一括添加し、脱イオン水２０重量部にアルケニルコハク酸ジカリウム０．５５重量部、ホルムアルデヒドナトリウムスルホシレート０．０８重量部を溶解した水溶液とアクリル酸ブチル３０重量部、メタクリル酸アリル０．０５重量部を２時間かけて連続的に滴下した。滴下後、１時間保持して、１段目重合を終了した。さらに２段目重合として槽内の温度が６５℃に到達した後、ホルムアルデヒドナトリウムスルホシレート０．０４重量部を一括添加し、脱イオン水２０重量部にｔ−ブチルハイドロパーオキサイド０．２５重量部、アルケニルコハク酸ジカリウム０．３５重量部を溶解した水溶液とアクリル酸ブチル２０重量部、メタクリル酸アリル０．０５重量部を４時間かけて連続的に滴下した。滴下後、転化率が９７％以上のところで重合を終了した。凝集肥大化スチレン−ブタジエンゴム（２）と架橋アクリル酸ブチル重合体から構成される複合ゴムラテックス（a−４）を得た。表２の実施例６に示す組成割合を有する熱可塑性樹脂組成物のペレットを用いた以外は、複合ゴム（ａ−１）と同様の方法で外層の平均厚さを求めた。外層の平均厚さは３３ｎｍであった。
Manufacture of composite rubber latex (a-4) A 10 L glass reactor is charged with 20 parts by weight (solid content) of the above-mentioned agglomerated styrene-butadiene rubber latex (2) and 100 parts by weight of deionized water, and nitrogen replacement is performed. went. After nitrogen substitution, when the temperature inside the tank reached 45 ° C, 0.3 parts by weight of lactose, 0.08 parts by weight of tetrasodium pyrophosphate, and ferrous sulfate and heptahydrate 0 were added to 20 parts by weight of deionized water. An aqueous solution in which 0.001 part by weight was dissolved was added. Furthermore, 30 parts by weight of butyl acrylate and 0.1 parts by weight of allyl methacrylate were added. After the temperature in the tank reached 48 ° C., it was kept for 1 hour. Furthermore, after the temperature in the tank reaches 50 ° C. as the first stage polymerization, 0.2 part by weight of cumene hydroperoxide is added all at once, 0.55 part by weight of dipotassium alkenyl succinate is added to 20 parts by weight of deionized water, and formaldehyde. An aqueous solution in which 0.08 part by weight of sodium sulfosylate was dissolved, 30 parts by weight of butyl acrylate, and 0.05 part by weight of allyl methacrylate were continuously added dropwise over 2 hours. After the dropwise addition, the first stage polymerization was completed by holding for 1 hour. Further, as the second stage polymerization, after the temperature in the tank reached 65 ° C., 0.04 parts by weight of sodium formaldehyde sulfosylate was added all at once, and 0.25 weight of t-butyl hydroperoxide was added to 20 parts by weight of deionized water. Parts, an aqueous solution in which 0.35 parts by weight of dipotassium alkenyl succinate was dissolved, 20 parts by weight of butyl acrylate, and 0.05 parts by weight of allyl methacrylate were continuously added dropwise over 4 hours. After dropping, the polymerization was terminated when the conversion rate was 97% or more. A composite rubber latex (a-4) composed of agglomerated and enlarged styrene-butadiene rubber (2) and a crosslinked butyl acrylate polymer was obtained. The average thickness of the outer layer was determined in the same manner as for the composite rubber (a-1) except that pellets of the thermoplastic resin composition having the composition ratio shown in Example 6 of Table 2 were used. The average thickness of the outer layer was 33 nm.
複合ゴムラテックス（ａ−５）の製造
１０Ｌのガラスリアクターに、上記の凝集肥大化スチレン−ブタジエンゴムラテックス（１）を２０重量部（固形分）、脱イオン水を１００重量部仕込み、窒素置換を行った。窒素置換後、槽内を昇温し４５℃に到達したところで脱イオン水２０重量部にラクトース０．３重量部、ピロリン酸四ナトリウム０．０８重量部及び硫酸第１鉄・７水和物０．００１重量部を溶解した水溶液を添加した。さらに、アクリル酸ブチル３０重量部、メタクリル酸アリル０．１重量部を添加した。槽内の温度が４８℃に到達した後、そのまま１時間保持した。さらに１段目重合として槽内の温度が５０℃に到達した後、過硫酸カリウム０．２重量部を一括添加し、脱イオン水２０重量部にアルケニルコハク酸ジカリウム０．９重量部、ホルムアルデヒドナトリウムスルホシレート０．０８重量部を溶解した水溶液とアクリル酸ブチル３０重量部、メタクリル酸アリル０．０５重量部を２時間かけて連続的に滴下した。滴下後、１時間保持して、１段目重合を終了した。さらに２段目重合として槽内の温度が６５℃に到達した後、ホルムアルデヒドナトリウムスルホシレート０．０４重量部を一括添加し、脱イオン水２０重量部に過硫酸カリウム０．６５重量部を溶解した水溶液とアクリル酸ブチル２０重量部、メタクリル酸アリル０．０５重量部を４時間かけて連続的に滴下した。滴下後、転化率が９７％以上のところで重合を終了した。凝集肥大化スチレン−ブタジエンゴム（１）と架橋アクリル酸ブチル重合体から構成される複合ゴムラテックス（a−５）を得た。表２の実施例７に示す組成割合を有する熱可塑性樹脂組成物のペレットを用いた以外は、複合ゴム（ａ−１）と同様の方法で外層の平均厚さを求めた。外層の平均厚さは６１ｎｍであった。
Manufacture of composite rubber latex (a-5) A 10 L glass reactor is charged with 20 parts by weight (solid content) of the above-mentioned agglomerated styrene-butadiene rubber latex (1) and 100 parts by weight of deionized water. went. After nitrogen substitution, when the temperature inside the tank reached 45 ° C, 0.3 parts by weight of lactose, 0.08 parts by weight of tetrasodium pyrophosphate, and ferrous sulfate and heptahydrate 0 were added to 20 parts by weight of deionized water. An aqueous solution in which 0.001 part by weight was dissolved was added. Furthermore, 30 parts by weight of butyl acrylate and 0.1 parts by weight of allyl methacrylate were added. After the temperature in the tank reached 48 ° C., it was kept for 1 hour. Furthermore, after the temperature in the tank reaches 50 ° C. as the first stage polymerization, 0.2 part by weight of potassium persulfate is added all at once, 0.9 part by weight of dipotassium alkenyl succinate, 20 parts by weight of deionized water, sodium formaldehyde An aqueous solution in which 0.08 parts by weight of sulfosylate was dissolved, 30 parts by weight of butyl acrylate, and 0.05 parts by weight of allyl methacrylate were continuously added dropwise over 2 hours. After the dropwise addition, the first stage polymerization was completed by holding for 1 hour. Further, as the second stage polymerization, after the temperature in the tank reaches 65 ° C., 0.04 part by weight of sodium formaldehyde sulfosylate is added all at once, and 0.65 part by weight of potassium persulfate is dissolved in 20 parts by weight of deionized water. The resulting aqueous solution, 20 parts by weight of butyl acrylate, and 0.05 parts by weight of allyl methacrylate were continuously added dropwise over 4 hours. After dropping, the polymerization was terminated when the conversion rate was 97% or more. A composite rubber latex (a-5) composed of agglomerated and enlarged styrene-butadiene rubber (1) and a crosslinked butyl acrylate polymer was obtained. The average thickness of the outer layer was determined in the same manner as for the composite rubber (a-1) except that the pellets of the thermoplastic resin composition having the composition ratio shown in Example 7 of Table 2 were used. The average thickness of the outer layer was 61 nm.
複合ゴムラテックス（ａ−６）の製造
凝集肥大化スチレン−ブタジエンゴムラテックス（１）を非凝集肥大化スチレン−ブタジエンゴムラテックス（３）に変更した以外は、複合ゴムラテックス（a−１）を得る重合方法と同様にして複合ゴムラテックス（a−６）を得た。表２の比較例１に示す組成割合を有する熱可塑性樹脂組成物のペレットを用いた以外は、複合ゴム（ａ−１）と同様の方法で外層の平均厚さを求めた。外層の平均厚さは４４ｎｍであった。
Manufacture of composite rubber latex (a-6) The composite rubber latex (a-1) is obtained except that the agglomerated enlarged styrene-butadiene rubber latex (1) is changed to a non-agglomerated enlarged styrene-butadiene rubber latex (3). A composite rubber latex (a-6) was obtained in the same manner as in the polymerization method. The average thickness of the outer layer was determined in the same manner as the composite rubber (a-1) except that the pellets of the thermoplastic resin composition having the composition ratio shown in Comparative Example 1 in Table 2 were used. The average thickness of the outer layer was 44 nm.
複合ゴムラテックス（ａ−７）の製造
１０Ｌのガラスリアクターに、上記の凝集肥大化スチレン−ブタジエンゴムラテックス（１）を２０重量部（固形分）、脱イオン水を１１０重量部仕込み、窒素置換を行った。窒素置換後、槽内を昇温し４５℃に到達したところで脱イオン水２０重量部にラクトース０．３重量部、ピロリン酸四ナトリウム０．０８重量部及び硫酸第１鉄・７水和物０．００１重量部を溶解した水溶液を添加した。さらに、アクリル酸ブチル５０重量部、メタクリル酸アリル０．１重量部を添加した。槽内の温度が４８℃に到達した後、そのまま２時間保持した。さらに１段目重合として槽内の温度が４８℃で、クメンハイドロパーオキサイド０．４重量部を一括添加し、脱イオン水２０重量部にアルケニルコハク酸ジカリウム０．８重量部、ホルムアルデヒドナトリウムスルホシレート０．１重量部を溶解した水溶液とアクリル酸ブチル２７重量部、メタクリル酸アリル０．１重量部を６時間かけて連続的に滴下した。滴下後、３時間保持して、１段目重合を終了した。さらに２段目重合として槽内の温度が６５℃に到達した後、クメンハイドロパーオキサイド０．４重量部を一括添加し、脱イオン水１０重量部にホルムアルデヒドナトリウムスルホシレート０．０２５重量部、アルケニルコハク酸ジカリウム０．１重量部を溶解した水溶液とアクリル酸ブチル３重量部を０．５時間かけて連続的に滴下した。滴下後、転化率が９７％以上のところで重合を終了した。凝集肥大化スチレン−ブタジエンゴム（１）と架橋アクリル酸ブチル重合体から構成される複合ゴムラテックス（a−７）を得た。表２の比較例２に示す組成割合を有する熱可塑性樹脂組成物のペレットを用いた以外は、複合ゴム（ａ−１）と同様の方法で外層の平均厚さを求めた。外層の平均厚さは４ｎｍであった。
Manufacture of composite rubber latex (a-7) A 10 L glass reactor is charged with 20 parts by weight (solid content) of the above-mentioned agglomerated styrene-butadiene rubber latex (1) and 110 parts by weight of deionized water, and nitrogen replacement is performed. went. After nitrogen substitution, when the temperature inside the tank reached 45 ° C, 0.3 parts by weight of lactose, 0.08 parts by weight of tetrasodium pyrophosphate, and ferrous sulfate and heptahydrate 0 were added to 20 parts by weight of deionized water. An aqueous solution in which 0.001 part by weight was dissolved was added. Furthermore, 50 parts by weight of butyl acrylate and 0.1 parts by weight of allyl methacrylate were added. After the temperature in the tank reached 48 ° C., it was kept as it was for 2 hours. Further, as the first stage polymerization, the temperature in the tank is 48 ° C., 0.4 parts by weight of cumene hydroperoxide is added all at once, 0.8 parts by weight of dipotassium alkenyl succinate, 20 parts by weight of deionized water, sodium formaldehyde An aqueous solution in which 0.1 parts by weight of the rate had been dissolved, 27 parts by weight of butyl acrylate, and 0.1 parts by weight of allyl methacrylate were continuously added dropwise over 6 hours. After the dropwise addition, the first stage polymerization was completed by maintaining for 3 hours. Furthermore, after the temperature in the tank reached 65 ° C. as the second stage polymerization, 0.4 parts by weight of cumene hydroperoxide was added all at once, 0.025 parts by weight of formaldehyde sodium sulfosylate in 10 parts by weight of deionized water, An aqueous solution in which 0.1 parts by weight of dipotassium alkenyl succinate was dissolved and 3 parts by weight of butyl acrylate were continuously added dropwise over 0.5 hours. After dropping, the polymerization was terminated when the conversion rate was 97% or more. A composite rubber latex (a-7) composed of agglomerated and enlarged styrene-butadiene rubber (1) and a crosslinked butyl acrylate polymer was obtained. The average thickness of the outer layer was determined in the same manner as for the composite rubber (a-1) except that the pellets of the thermoplastic resin composition having the composition ratio shown in Comparative Example 2 of Table 2 were used. The average thickness of the outer layer was 4 nm.
複合ゴムラテックス（ａ−８）の製造
１０Ｌのガラスリアクターに、上記の凝集肥大化スチレン−ブタジエンゴムラテックス（１）を２０重量部（固形分）、脱イオン水を１００重量部仕込み、窒素置換を行った。窒素置換後、槽内を昇温し４５℃に到達したところで脱イオン水２０重量部にラクトース０．３重量部、ピロリン酸四ナトリウム０．０８重量部及び硫酸第１鉄・７水和物０．００１重量部を溶解した水溶液を添加した。さらに、アクリル酸ブチル３重量部、メタクリル酸アリル０．０５重量部を添加した。槽内の温度が４８℃に到達した後、そのまま０．１時間保持した。さらに１段目重合として槽内の温度が５０℃に到達した後、過硫酸カリウム０．２重量部を一括添加し、脱イオン水２０重量部にアルケニルコハク酸ジカリウム０．９重量部、ホルムアルデヒドナトリウムスルホシレート０．０８重量部を溶解した水溶液とアクリル酸ブチル３０重量部、メタクリル酸アリル０．０５重量部を２時間かけて連続的に滴下した。滴下後、１時間保持して、１段目重合を終了した。さらに２段目重合として槽内の温度が６５℃に到達した後、ホルムアルデヒドナトリウムスルホシレート０．０５重量部を一括添加し、脱イオン水２０重量部に過硫酸カリウム０．６５重量部を溶解した水溶液とアクリル酸ブチル４７重量部、メタクリル酸アリル０．１５重量部を４時間かけて連続的に滴下した。滴下後、転化率が９７％以上のところで重合を終了した。凝集肥大化スチレン−ブタジエンゴム（１）と架橋アクリル酸ブチル重合体から構成される複合ゴムラテックス（a−８）を得た。表２の比較例３に示す組成割合を有する熱可塑性樹脂組成物のペレットを用いた以外は、複合ゴム（ａ−１）と同様の方法で外層の平均厚さを求めた。外層の平均厚さは１０５ｎｍであった。
Manufacture of composite rubber latex (a-8) A 10-liter glass reactor is charged with 20 parts by weight (solid content) of the above-mentioned agglomerated styrene-butadiene rubber latex (1) and 100 parts by weight of deionized water, and nitrogen replacement is performed. went. After nitrogen substitution, when the temperature inside the tank reached 45 ° C, 0.3 parts by weight of lactose, 0.08 parts by weight of tetrasodium pyrophosphate, and ferrous sulfate and heptahydrate 0 were added to 20 parts by weight of deionized water. An aqueous solution in which 0.001 part by weight was dissolved was added. Furthermore, 3 parts by weight of butyl acrylate and 0.05 parts by weight of allyl methacrylate were added. After the temperature in the tank reached 48 ° C., it was kept as it was for 0.1 hour. Furthermore, after the temperature in the tank reaches 50 ° C. as the first stage polymerization, 0.2 part by weight of potassium persulfate is added all at once, 0.9 part by weight of dipotassium alkenyl succinate, 20 parts by weight of deionized water, sodium formaldehyde An aqueous solution in which 0.08 parts by weight of sulfosylate was dissolved, 30 parts by weight of butyl acrylate, and 0.05 parts by weight of allyl methacrylate were continuously added dropwise over 2 hours. After the dropwise addition, the first stage polymerization was completed by holding for 1 hour. Further, as the second stage polymerization, after the temperature in the tank reaches 65 ° C., 0.05 part by weight of sodium formaldehyde sulfosylate is added all at once, and 0.65 part by weight of potassium persulfate is dissolved in 20 parts by weight of deionized water. The aqueous solution, 47 parts by weight of butyl acrylate and 0.15 parts by weight of allyl methacrylate were continuously added dropwise over 4 hours. After dropping, the polymerization was terminated when the conversion rate was 97% or more. A composite rubber latex (a-8) composed of agglomerated and enlarged styrene-butadiene rubber (1) and a crosslinked butyl acrylate polymer was obtained. The average thickness of the outer layer was determined in the same manner as for the composite rubber (a-1) except that the pellets of the thermoplastic resin composition having the composition ratio shown in Comparative Example 3 of Table 2 were used. The average thickness of the outer layer was 105 nm.
複合ゴムラテックス（ａ−９）の製造
１０Ｌのガラスリアクターに、上記の凝集肥大化スチレン−ブタジエンゴムラテックス（１）を６０重量部（固形分）、脱イオン水を１００重量部仕込み、窒素置換を行った。窒素置換後、槽内を昇温し４５℃に到達したところで脱イオン水２０重量部にラクトース０．３重量部、ピロリン酸四ナトリウム０．０８重量部及び硫酸第１鉄・７水和物０．００１重量部を溶解した水溶液を添加した。さらに、アクリル酸ブチル１０重量部、メタクリル酸アリル０．１重量部を添加した。槽内の温度が４８℃に到達した後、そのまま１時間保持した。さらに１段目重合として槽内の温度が５０℃に到達した後、クメンハイドロパーオキサイド０．２重量部を一括添加し、脱イオン水２０重量部にアルケニルコハク酸ジカリウム０．５重量部、ホルムアルデヒドナトリウムスルホシレート０．０８重量部を溶解した水溶液とアクリル酸ブチル２５重量部、メタクリル酸アリル０．０５重量部を２時間かけて連続的に滴下した。滴下後、１時間保持して、１段目重合を終了した。さらに２段目重合として槽内の温度が６５℃に到達した後、ホルムアルデヒドナトリウムスルホシレート０．０４重量部を一括添加し、脱イオン水２０重量部に過硫酸カリウム０．４重量部を溶解した水溶液とアクリル酸ブチル５重量部、メタクリル酸アリル０．０５重量部を０．５時間かけて連続的に滴下した。滴下後、転化率が９７％以上のところで重合を終了した。凝集肥大化スチレン−ブタジエンゴム（１）と架橋アクリル酸ブチル重合体から構成される複合ゴムラテックス（a−９）を得た。表２の比較例４に示す組成割合を有する熱可塑性樹脂組成物のペレットを用いた以外は、複合ゴム（ａ−１）と同様の方法で外層の平均厚さを求めた。外層の平均厚さは１０ｎｍであった。
Manufacture of composite rubber latex (a-9) A 10 L glass reactor is charged with 60 parts by weight (solid content) of the above-mentioned agglomerated styrene-butadiene rubber latex (1) and 100 parts by weight of deionized water, and nitrogen replacement is performed. went. After nitrogen substitution, when the temperature inside the tank reached 45 ° C, 0.3 parts by weight of lactose, 0.08 parts by weight of tetrasodium pyrophosphate, and ferrous sulfate and heptahydrate 0 were added to 20 parts by weight of deionized water. An aqueous solution in which 0.001 part by weight was dissolved was added. Furthermore, 10 parts by weight of butyl acrylate and 0.1 parts by weight of allyl methacrylate were added. After the temperature in the tank reached 48 ° C., it was kept for 1 hour. Furthermore, after the temperature in the tank reaches 50 ° C. as the first stage polymerization, 0.2 parts by weight of cumene hydroperoxide is added all at once, 0.5 parts by weight of dipotassium alkenyl succinate is added to 20 parts by weight of deionized water, and formaldehyde. An aqueous solution in which 0.08 parts by weight of sodium sulfosylate was dissolved, 25 parts by weight of butyl acrylate, and 0.05 parts by weight of allyl methacrylate were continuously added dropwise over 2 hours. After the dropwise addition, the first stage polymerization was completed by holding for 1 hour. Furthermore, as the second stage polymerization, after the temperature in the tank reached 65 ° C., 0.04 part by weight of sodium formaldehyde sulfosylate was added all at once, and 0.4 part by weight of potassium persulfate was dissolved in 20 parts by weight of deionized water. The aqueous solution, 5 parts by weight of butyl acrylate, and 0.05 parts by weight of allyl methacrylate were continuously added dropwise over 0.5 hours. After dropping, the polymerization was terminated when the conversion rate was 97% or more. A composite rubber latex (a-9) composed of agglomerated and enlarged styrene-butadiene rubber (1) and a crosslinked butyl acrylate polymer was obtained. The average thickness of the outer layer was determined in the same manner as the composite rubber (a-1) except that the pellets of the thermoplastic resin composition having the composition ratio shown in Comparative Example 4 in Table 2 were used. The average thickness of the outer layer was 10 nm.
複合ゴムラテックス（ａ−１０）の製造
１０Ｌのガラスリアクターに、上記の凝集肥大化スチレン−ブタジエンゴムラテックス（１）を５重量部（固形分）、脱イオン水を１００重量部仕込み、窒素置換を行った。窒素置換後、槽内を昇温し４５℃に到達したところで脱イオン水２０重量部にラクトース０．３重量部、ピロリン酸四ナトリウム０．０８重量部及び硫酸第１鉄・７水和物０．００１重量部を溶解した水溶液を添加した。さらに、アクリル酸ブチル３０重量部、メタクリル酸アリル０．１重量部を添加した。槽内の温度が４８℃に到達した後、そのまま１時間保持した。さらに１段目重合として槽内の温度が５０℃に到達した後、クメンハイドロパーオキサイド０．２重量部を一括添加し、脱イオン水２０重量部にアルケニルコハク酸ジカリウム０．９重量部、ホルムアルデヒドナトリウムスルホシレート０．０８重量部を溶解した水溶液とアクリル酸ブチル３０重量部、メタクリル酸アリル０．０５重量部を２時間かけて連続的に滴下した。滴下後、１時間保持して、１段目重合を終了した。さらに２段目重合として槽内の温度が６５℃に到達した後、ホルムアルデヒドナトリウムスルホシレート０．０４重量部を一括添加し、脱イオン水２０重量部に過硫酸カリウム０．４重量部を溶解した水溶液とアクリル酸ブチル３５重量部、メタクリル酸アリル０．０５重量部を４時間かけて連続的に滴下した。滴下後、転化率が９７％以上のところで重合を終了した。凝集肥大化スチレン−ブタジエンゴム（１）と架橋アクリル酸ブチル重合体から構成される複合ゴムラテックス（a−１０）を得た。表２の比較例５に示す組成割合を有する熱可塑性樹脂組成物のペレットを用いた以外は、複合ゴム（ａ−１）と同様の方法で外層の平均厚さを求めた。外層の平均厚さは１１０ｎｍであった。
Manufacture of composite rubber latex (a-10) A 10-liter glass reactor is charged with 5 parts by weight (solid content) of the above-mentioned agglomerated styrene-butadiene rubber latex (1) and 100 parts by weight of deionized water, and nitrogen replacement is performed. went. After nitrogen substitution, when the temperature inside the tank reached 45 ° C, 0.3 parts by weight of lactose, 0.08 parts by weight of tetrasodium pyrophosphate, and ferrous sulfate and heptahydrate 0 were added to 20 parts by weight of deionized water. An aqueous solution in which 0.001 part by weight was dissolved was added. Furthermore, 30 parts by weight of butyl acrylate and 0.1 parts by weight of allyl methacrylate were added. After the temperature in the tank reached 48 ° C., it was kept for 1 hour. Furthermore, after the temperature in the tank reaches 50 ° C. as the first stage polymerization, 0.2 parts by weight of cumene hydroperoxide is added all at once, 0.9 parts by weight of dipotassium alkenyl succinate and 20 parts by weight of deionized water, formaldehyde An aqueous solution in which 0.08 part by weight of sodium sulfosylate was dissolved, 30 parts by weight of butyl acrylate, and 0.05 part by weight of allyl methacrylate were continuously added dropwise over 2 hours. After the dropwise addition, the first stage polymerization was completed by holding for 1 hour. Furthermore, as the second stage polymerization, after the temperature in the tank reached 65 ° C., 0.04 part by weight of sodium formaldehyde sulfosylate was added all at once, and 0.4 part by weight of potassium persulfate was dissolved in 20 parts by weight of deionized water. The aqueous solution, 35 parts by weight of butyl acrylate, and 0.05 parts by weight of allyl methacrylate were continuously added dropwise over 4 hours. After dropping, the polymerization was terminated when the conversion rate was 97% or more. A composite rubber latex (a-10) composed of agglomerated and enlarged styrene-butadiene rubber (1) and a crosslinked butyl acrylate polymer was obtained. The average thickness of the outer layer was determined in the same manner as for the composite rubber (a-1) except that the pellets of the thermoplastic resin composition having the composition ratio shown in Comparative Example 5 in Table 2 were used. The average thickness of the outer layer was 110 nm.
グラフト共重合体の製造
グラフト共重合体（Ａ−１）の製造
ガラスリアクターに、複合ゴムラテックス（ａ−１）４５重量部（固形分）を仕込み窒素置換を行った。窒素置換後、槽内を昇温し６３℃に到達したところで、アクリロニトリル１重量部、スチレン３重量部、ラクトース０．２重量部、無水ピロリン酸ナトリウム０．１重量部及び硫酸第１鉄０．００５重量部を脱イオン水１５重量部に溶解した水溶液を添加した。７０℃に到達後、アクリロニトリル１５重量部、スチレン３６重量部、ターシャリードデシルメルカプタン０．０９部の混合液及び脱イオン水２０重量部にオレイン酸カリウム１．０重量部、クメンハイドロパーオキサイド０．１８部、を溶解した乳化剤水溶液を４時間かけて連続的に滴下した。滴下後、３時間保持してグラフト共重合体ラテックス（Ａ−１）を得た。その後、塩析・脱水・乾燥し、グラフト重合体（Ａ−１）のパウダーを得た。
Production of graft copolymers
Production of Graft Copolymer (A-1) Into a glass reactor, 45 parts by weight (solid content) of the composite rubber latex (a-1) was charged and nitrogen substitution was performed. After nitrogen substitution, when the temperature in the tank was increased to 63 ° C., 1 part by weight of acrylonitrile, 3 parts by weight of styrene, 0.2 part by weight of lactose, 0.1 part by weight of anhydrous sodium pyrophosphate, and ferrous sulfate 0. An aqueous solution having 005 parts by weight dissolved in 15 parts by weight of deionized water was added. After reaching 70 ° C., a mixture of 15 parts by weight of acrylonitrile, 36 parts by weight of styrene, 0.09 part of terrestrial decyl mercaptan and 20 parts by weight of deionized water, 1.0 part by weight of potassium oleate, 0. An aqueous emulsifier solution in which 18 parts were dissolved was continuously dropped over 4 hours. After dropping, the mixture was held for 3 hours to obtain a graft copolymer latex (A-1). Thereafter, salting out, dehydration, and drying were performed to obtain a powder of the graft polymer (A-1).
グラフト共重合体（Ａ−２）〜（Ａ−１０）の製造
複合ゴムラテックス（ａ−１）から複合ゴムラテックス（ａ−２）〜（ａ−１０）に変更した以外はグラフト共重合体（Ａ−１）と同様に製造し、グラフト共重合体ラテックス（Ａ−２）〜（Ａ−１０）を得た。その後、塩析・脱水・乾燥し、グラフト重合体（Ａ−２）〜（Ａ−１０）のパウダーを得た。
Production of Graft Copolymer (A-2) to (A-10) Graft copolymer (A- 1) except that the composite rubber latex (a-1) was changed to the composite rubber latex (a-2) to (a-10). It manufactured similarly to A-1) and obtained graft copolymer latex (A-2)-(A-10). Thereafter, salting out, dehydration, and drying were performed to obtain powders of graft polymers (A-2) to (A-10).
共重合体（Ｂ）の製造
窒素置換したガラスリアクターに、脱イオン水１４９重量部、スチレン７重量部、アクリロニトリル３重量部、ターシャリードデシルメルカプタン０．０３重量部、オレイン酸カリウム１．０重量部及び過硫酸カリウム０．３重量部を仕込み、６５℃で１時間重合した。その後、スチレン６３重量部、アクリロニトリル２７重量部、ターシャリードデシルメルカプタン０．１５重量部及びオレイン酸カリウム１．５重量部を含む乳化剤水溶液２９重量部を各々３時間かけて連続的に滴下した。滴下後２時間保持して、共重合体ラテックス（Ｂ）を得た。その後、塩析・脱水・乾燥し、共重合体（Ｂ）のパウダーを得た。
Production of Copolymer (B) In a nitrogen-replaced glass reactor, 149 parts by weight of deionized water, 7 parts by weight of styrene, 3 parts by weight of acrylonitrile, 0.03 part by weight of tarlead decyl mercaptan, 1.0 part by weight of potassium oleate And 0.3 part by weight of potassium persulfate was charged and polymerized at 65 ° C. for 1 hour. Thereafter, 29 parts by weight of an emulsifier aqueous solution containing 63 parts by weight of styrene, 27 parts by weight of acrylonitrile, 0.15 parts by weight of tartarid decyl mercaptan and 1.5 parts by weight of potassium oleate were continuously added dropwise over 3 hours. After dropping, the mixture was held for 2 hours to obtain a copolymer latex (B). Thereafter, salting out, dehydration and drying were performed to obtain a powder of the copolymer (B).
添加剤
光安定剤：ＡＤＥＫＡ（株）製 アデカスタブ ＬＡ７７Ｙ
紫外線吸収剤：住友化学（株）製 スミソーブ２００
Additives Light stabilizer: ADEKA Corporation ADK STAB LA77Y
UV absorber: Sumitomo 200 manufactured by Sumitomo Chemical Co., Ltd.
＜実施例１〜７及び比較例１〜５＞
表２に示すグラフト共重合体（Ａ）、共重合体（Ｂ）、添加剤を混合した後、東芝ＴＥＭ−３５Ｂ二軸押出機を用いて２４０℃にて溶融混練して実施例１〜７及び比較例１〜５のペレットを得た。各実施例及び比較例で得られたペレットを用いて以下の評価に供した。その結果を表２に示す。
<Examples 1-7 and Comparative Examples 1-5>
Examples 1 to 7 were prepared by mixing the graft copolymer (A), copolymer (B), and additives shown in Table 2 and then kneading at 240 ° C. using a Toshiba TEM-35B twin screw extruder. And the pellet of Comparative Examples 1-5 was obtained. It used for the following evaluation using the pellet obtained by each Example and the comparative example. The results are shown in Table 2.
耐衝撃性
各実施例及び比較例で得られたペレットを用いＩＳＯ試験方法２９４に準拠して各種試験片を成形し、耐衝撃性を測定した。
耐衝撃性はＩＳＯ１７９に準拠し、４ｍｍ厚みで、ノッチ付きシャルピー衝撃値を測定した。単位：ｋＪ／ｍ２
Impact Resistance Various test pieces were molded according to ISO test method 294 using the pellets obtained in each Example and Comparative Example, and impact resistance was measured.
The impact resistance was in conformity with ISO 179, and a Charpy impact value with a notch was measured at a thickness of 4 mm. Unit: kJ / m 2
発色性
発色性の評価には、各実施例及び比較例で得られたペレットを、射出成形機（日本製鋼所製 Ｊ−１５０ＥＰ シリンダー温度：２３０℃ 金型温度：６０℃）にて成形された成形品（６０ｍｍ×６０ｍｍ×２ｍｍ）を用いた。ＪＩＳ−Ｚ８７２９に準拠した色相測定により得られた成形品の白バック、黒バックの色相差を、成形品の発色性の尺度とした（値が大きいほど発色性に優れる）。分光光度計は、（株）村上色彩研究所社製 ＣＭＳ−３５ＳＰを用いた。
For evaluation of color developability, the pellets obtained in each Example and Comparative Example were molded by an injection molding machine (J-150EP, cylinder temperature: 230 ° C., mold temperature: 60 ° C., manufactured by Nippon Steel). A molded product (60 mm × 60 mm × 2 mm) was used. The hue difference between the white background and the black background of the molded product obtained by hue measurement according to JIS-Z8729 was used as a measure of the color developability of the molded product (the larger the value, the better the color developability). The spectrophotometer used was CMS-35SP manufactured by Murakami Color Research Co., Ltd.
耐候性
耐候性の評価には、各実施例及び比較例で得られたペレットを用い、射出成形機（山城精機製作所製 ＳＡＶ−３０−３０ シリンダー温度：２１０℃ 金型温度：５０℃）にて成形された成形品（９０ｍｍ×５５ｍｍ×２．５ｍｍ）を用いた。スガ試験機（株）製サンシャインスーパーロングライフウェザーメーター、ＷＥＬ−ＳＵＮ−ＨＣＨ−Ｂを使用し、６５℃、雨ありの条件下で５００時間の加速曝露試験を行った。その後測色計を用い、曝露前と曝露後の色差（ΔＥ）を測定した（値が小さいほど耐候性に優れる）。
For evaluation of weather resistance, the pellets obtained in each of Examples and Comparative Examples were used, and injection molding machine (SAV-30-30 manufactured by Yamashiro Seiki Seisakusho, cylinder temperature: 210 ° C, mold temperature: 50 ° C) was used. A molded product (90 mm × 55 mm × 2.5 mm) was used. Using a Sunshine Super Long Life Weather Meter, WEL-SUN-HCH-B manufactured by Suga Test Instruments Co., Ltd., an accelerated exposure test was conducted for 500 hours under conditions of 65 ° C. and rain. Thereafter, the color difference (ΔE) before and after exposure was measured using a colorimeter (the smaller the value, the better the weather resistance).
表２に示すように、実施例１〜７は本発明に関わる熱可塑性樹脂組成物の例であり、耐候性だけでなく耐衝撃性、及び発色性に優れていた。 As shown in Table 2, Examples 1 to 7 are examples of the thermoplastic resin composition according to the present invention, and were excellent not only in weather resistance but also in impact resistance and color development.
表２に示すように、比較例１は複合ゴムの内層が共役ジエン系ゴム状重合体粒子単独で構成されていたため、耐衝撃性と発色性に劣った。比較例２は複合ゴム粒子の外層の平均厚さが４ｎｍであったため耐候性に劣った。比較例３は複合ゴム粒子の外層の平均厚さが１００ｎｍを超えていたため発色性に劣った。比較例４は複合ゴム中の共役ジエン系ゴム状重合体の含有量が６０重量％であったため耐候性に劣った。比較例５は複合ゴム中の共役ジエン系ゴム状重合体の含有量が５重量％であったため耐衝撃性と発色性に劣った。 As shown in Table 2, Comparative Example 1 was inferior in impact resistance and color developability because the inner layer of the composite rubber was composed of conjugated diene rubbery polymer particles alone. In Comparative Example 2, since the average thickness of the outer layer of the composite rubber particles was 4 nm, the weather resistance was inferior. In Comparative Example 3, since the average thickness of the outer layer of the composite rubber particle exceeded 100 nm, the color development was inferior. Comparative Example 4 was inferior in weather resistance because the content of the conjugated diene rubbery polymer in the composite rubber was 60% by weight. In Comparative Example 5, since the content of the conjugated diene rubbery polymer in the composite rubber was 5% by weight, the impact resistance and color developability were poor.
本発明のグラフト共重合体を用いた熱可塑性樹脂組成物は、耐候性だけでなく耐衝撃性、及び発色性に優れるため車輌用外装部品、屋外で使用される製品等への利用価値が高い。 The thermoplastic resin composition using the graft copolymer of the present invention is excellent not only in weather resistance but also in impact resistance and color development, and thus has high utility value for exterior parts for vehicles, products used outdoors, and the like. .
１：外層
２：外層と内層の境界面
３：重量平均粒子径が５０〜３００ｎｍである共役ジエン系ゴム状重合体の粒子
1: outer layer 2: boundary surface between outer layer and inner layer 3: particles of a conjugated diene rubbery polymer having a weight average particle diameter of 50 to 300 nm
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2012275344A JP5453512B2 (en) | 2011-12-27 | 2012-12-18 | Graft copolymer and thermoplastic resin composition |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2011286505 | 2011-12-27 | ||
| JP2011286505 | 2011-12-27 | ||
| JP2012275344A JP5453512B2 (en) | 2011-12-27 | 2012-12-18 | Graft copolymer and thermoplastic resin composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2013151654A true JP2013151654A (en) | 2013-08-08 |
| JP5453512B2 JP5453512B2 (en) | 2014-03-26 |
Family
ID=49048250
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2012275344A Active JP5453512B2 (en) | 2011-12-27 | 2012-12-18 | Graft copolymer and thermoplastic resin composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP5453512B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015086305A (en) * | 2013-10-31 | 2015-05-07 | ユーエムジー・エービーエス株式会社 | Graft copolymer and thermoplastic resin composition |
| WO2023140382A1 (en) * | 2022-01-24 | 2023-07-27 | 株式会社クラレ | Curable resin composition, adhesive, molding material, cured article |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001220487A (en) * | 1999-12-01 | 2001-08-14 | Mitsubishi Rayon Co Ltd | Thermoplastic resin composition |
| JP2002080684A (en) * | 2000-09-07 | 2002-03-19 | Nippon A & L Kk | Thermoplastic resin composition and various parts |
-
2012
- 2012-12-18 JP JP2012275344A patent/JP5453512B2/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001220487A (en) * | 1999-12-01 | 2001-08-14 | Mitsubishi Rayon Co Ltd | Thermoplastic resin composition |
| JP2002080684A (en) * | 2000-09-07 | 2002-03-19 | Nippon A & L Kk | Thermoplastic resin composition and various parts |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015086305A (en) * | 2013-10-31 | 2015-05-07 | ユーエムジー・エービーエス株式会社 | Graft copolymer and thermoplastic resin composition |
| WO2023140382A1 (en) * | 2022-01-24 | 2023-07-27 | 株式会社クラレ | Curable resin composition, adhesive, molding material, cured article |
Also Published As
| Publication number | Publication date |
|---|---|
| JP5453512B2 (en) | 2014-03-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5096460B2 (en) | Resin composition with excellent scratch resistance | |
| WO2013008829A1 (en) | Graft copolymer, thermoplastic resin composition, molding, and method for producing graft copolymer | |
| JP5453511B2 (en) | Graft copolymer, thermoplastic resin composition, and method for producing graft copolymer | |
| JP5547793B2 (en) | Thermoplastic resin composition and molded article | |
| JP5453512B2 (en) | Graft copolymer and thermoplastic resin composition | |
| KR102354837B1 (en) | Method for preparing graft copolymer powder | |
| JP5457499B2 (en) | Thermoplastic resin composition | |
| JP2013018950A (en) | Rubber-reinforced thermoplastic resin composition | |
| JP5329702B1 (en) | Graft copolymer, thermoplastic resin composition, and method for producing graft copolymer | |
| JP5547826B2 (en) | Flame retardant thermoplastic resin composition and resin molded product | |
| JP5547795B2 (en) | Thermoplastic resin composition and molded article | |
| JP5547828B2 (en) | Thermoplastic resin composition and extruded product | |
| JPH11217411A (en) | Rubber-modified styrene-based resin composition | |
| JP2999944B2 (en) | Thermoplastic resin composition | |
| JP5457573B2 (en) | Thermoplastic resin composition and molded article | |
| JP5547796B2 (en) | Thermoplastic resin composition and molded article | |
| JP5457518B2 (en) | Thermoplastic resin composition for vehicle lamp and molded product | |
| JP6214939B2 (en) | Thermoplastic resin composition for extrusion molding and extrusion molding | |
| JP5547794B2 (en) | Thermoplastic resin composition and extruded product | |
| JP6041381B2 (en) | Thermoplastic resin composition for vehicle lamp and molded product | |
| JP6707817B2 (en) | Thermoplastic resin composition and method for producing the same | |
| CN111868168A (en) | Thermoplastic resin composition and molded article thereof | |
| JP5786079B1 (en) | Thermoplastic resin composition | |
| JP2013018949A (en) | Graft copolymer and thermoplastic resin composition | |
| WO2017104508A1 (en) | Thermoplastic resin composition |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A871 | Explanation of circumstances concerning accelerated examination |
Free format text: JAPANESE INTERMEDIATE CODE: A871 Effective date: 20130911 |
|
| A975 | Report on accelerated examination |
Free format text: JAPANESE INTERMEDIATE CODE: A971005 Effective date: 20131003 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20131015 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20131224 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20140106 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 5453512 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |