JPS59187012A - Manufacture of thermoplastic resin - Google Patents
Manufacture of thermoplastic resinInfo
- Publication number
- JPS59187012A JPS59187012A JP5915883A JP5915883A JPS59187012A JP S59187012 A JPS59187012 A JP S59187012A JP 5915883 A JP5915883 A JP 5915883A JP 5915883 A JP5915883 A JP 5915883A JP S59187012 A JPS59187012 A JP S59187012A
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- Prior art keywords
- parts
- refractive index
- mixture
- rubber
- monomer mixture
- 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.)
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- Graft Or Block Polymers (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は優れた耐候性、耐衝撃性および透明性を有する
熱可塑性樹脂の製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a thermoplastic resin having excellent weather resistance, impact resistance and transparency.
ポリメタクリル酸メチル(PMMA)樹脂は優れた透明
樹脂として広汎な分野に使用されているが衝撃強度が低
いという欠点がある。これらの透明樹脂に耐衝撃性を付
与する方法としては、ポリブタジェン(PBD)などの
ジエン系ゴムの存在下に、メタクリル酸メチル、スチレ
ンおよびアクリロニトリルなどからなるビニル系単量体
混合物を、ジエン系ゴムの屈折率とビニル系単量体混合
物を単独で重合して得られる重合体の屈折率が実質的に
一致するようにビニル系単量体混合物の組成を選択して
重合する方法(特公昭42−19248号公報、特公昭
44−19547号公報および特公昭44−2229号
公報など)が知られており、例えばメタクリル酸メチル
−ブタジェン−スチレン共重合体樹脂(M B S樹脂
)やメタクリル酸メチ/L=−7り+)ロニトリルーブ
タジエンースチレン共重合体樹脂[vfABS樹脂)と
して種々の分野に使われているが、これらの樹脂は紫外
線や空気中の酸素によって劣化し、変色するなど、いわ
ゆる耐候性が悪いという致命的な欠点がある。Although polymethyl methacrylate (PMMA) resin is used in a wide range of fields as an excellent transparent resin, it has the drawback of low impact strength. As a method for imparting impact resistance to these transparent resins, a vinyl monomer mixture consisting of methyl methacrylate, styrene, acrylonitrile, etc. is added to a diene rubber in the presence of a diene rubber such as polybutadiene (PBD). A method of polymerizing by selecting the composition of a vinyl monomer mixture so that the refractive index of the vinyl monomer mixture and the refractive index of the polymer obtained by polymerizing the vinyl monomer mixture alone are substantially the same (Japanese Patent Publication No. 42 19248, Japanese Patent Publication No. 44-19547, and Japanese Patent Publication No. 44-2229), for example, methyl methacrylate-butadiene-styrene copolymer resin (MBS resin) and methacrylic acid methyl /L=-7ri+) Ronitrile-butadiene-styrene copolymer resin (vfABS resin) is used in various fields, but these resins deteriorate and discolor due to ultraviolet rays and oxygen in the air. However, it has a fatal drawback of poor weather resistance.
一方、耐衝撃性樹脂に耐候性を付与する方法としては、
ベースゴムとしてジエン系ゴムの代、9にエチレン−プ
ロピレン−非共役ジエン共重合体ゴム(以降、EPDM
ゴムと略す)を用いる方法が数多く知られており、たと
えばE、PDMゴムの存在下に芳香族ビニル系単量体、
/アン化ビニル系単量体、メタクリル酸アルキルエステ
ル系単量体などからな不穏々の組成のビニル系単量体混
合物を重合することによって耐候性のすぐれた耐衝撃性
樹脂を製造する方法(たとえば特公昭52−30549
号公報、特公昭52−18751号報、特開昭56−5
0906号公報)および耐熱老化性や耐オゾン性をさら
に高めることを目的として、EPDMゴムの存在下にメ
タクリル酸メチルに代表されるメタクリル酸アルキルエ
ステル系単量体を重合する方法(特公報51−4748
6号公報および特公昭52−15112号公報)などが
提案されている。しかしながらこれらの方法で得られる
グラフト共重合体は耐衝撃性および耐候性こそすぐれる
ものの、単量体混合物またはメタ2IJ )し酸アルキ
ルエステル系単量体のみからなる重合体の屈折率が、E
PDMの屈折率に比し著しく高いために透明性が劣り、
透明性が要求される用途には使用できないという欠点が
ある。On the other hand, as a method of imparting weather resistance to impact-resistant resin,
The base rubber is a diene rubber, and 9 is an ethylene-propylene-nonconjugated diene copolymer rubber (hereinafter referred to as EPDM).
A number of methods are known, for example, using aromatic vinyl monomers in the presence of E, PDM rubber.
/ A method for producing an impact-resistant resin with excellent weather resistance by polymerizing a vinyl monomer mixture with an unstable composition, such as an annated vinyl monomer and a methacrylic acid alkyl ester monomer ( For example, Tokuko Sho 52-30549
Publication No. 52-18751, Japanese Patent Publication No. 56-56
0906) and a method of polymerizing a methacrylic acid alkyl ester monomer represented by methyl methacrylate in the presence of EPDM rubber for the purpose of further increasing heat aging resistance and ozone resistance (Japanese Patent Publication No. 51-0906). 4748
6 and Japanese Patent Publication No. 52-15112) have been proposed. However, although the graft copolymers obtained by these methods have excellent impact resistance and weather resistance, the refractive index of a polymer consisting only of a monomer mixture or a meta-acid alkyl ester monomer is
The refractive index is significantly higher than that of PDM, resulting in inferior transparency.
It has the disadvantage that it cannot be used in applications that require transparency.
そこで本発明者らは耐候性、耐衝撃性および透明性が均
衡にすぐれた熱可塑性樹脂の開発を目的として鋭意検討
した結果、EPDMコ゛ムをベースとし、これにアクリ
ル酸アルキルエステル系単量体を必須成分として含有し
、かつ特定の条件を満足するビニル系単量体混合物をグ
ラフト重合することにより、上記目的に十分合致した熱
可塑性樹脂が得られることを見出し本発明に到達した。Therefore, the present inventors conducted extensive research with the aim of developing a thermoplastic resin with an excellent balance of weather resistance, impact resistance, and transparency. As a result, the present inventors developed a thermoplastic resin based on an EPDM coating and an acrylic acid alkyl ester monomer. The inventors have discovered that a thermoplastic resin that fully meets the above objectives can be obtained by graft polymerizing a vinyl monomer mixture that is contained as an essential component and satisfies specific conditions, and has thus arrived at the present invention.
すなわち、本発明は(a) E P D Mゴム10〜
70重量部の存在下に(b)アクリル酸アルキルエステ
ル系単量体およびこれと共重合可能な他のビニル単量体
からなる単量体混合物90〜30重量部をグラフト重合
するに際し、(+))単量体混合物のみを重合してなる
重合体の屈折率と(a)EPDMゴム9屈折率の差が、
0.005以下となるように(b)単量体混合物の組成
を選択することを特徴とする熱可塑性樹脂の製造方法を
提供するものである。That is, the present invention provides (a) EPDM rubber 10 to
When graft polymerizing 90 to 30 parts by weight of a monomer mixture consisting of (b) an acrylic acid alkyl ester monomer and another vinyl monomer copolymerizable therewith in the presence of 70 parts by weight, (+ )) The difference between the refractive index of the polymer obtained by polymerizing only the monomer mixture and the refractive index of (a) EPDM rubber 9 is
The present invention provides a method for producing a thermoplastic resin, characterized in that the composition of (b) the monomer mixture is selected so that the ratio is 0.005 or less.
EPDMゴムをベースゴムとして用いる場合、従来行な
われているように芳香族ビニル系単量体、シアン化ビニ
ル系単量体およびメタアクリル酸アルキルエステル系単
量体などの通常のビニル系単量体のみを単量体成分とし
て用いても、EPDMゴムの屈折率がマトリックス樹脂
成分の屈折率に比べて著しく低いため、両者の組合せか
ら透明樹脂を製造することができないが、アクリル酸ア
ルキルエステル系単量体からなる重合体の屈折率は、上
記通常のマトリックス樹脂成分の屈折率よシもきわめて
低いため、本発明においてはビニル系単量体混合物の必
須成分としてアクリル酸アルキルエステル系単量体を用
いることによって、EPDMゴムの屈折率とマトリック
ス樹脂成分の屈折率を実質的に一致させることが可能と
なり、その結果、透明性が良好で、しかも耐候性と耐衝
撃性がすぐれた熱可塑性樹脂の製造が可能となる。When EPDM rubber is used as a base rubber, conventional vinyl monomers such as aromatic vinyl monomers, vinyl cyanide monomers, and alkyl methacrylate monomers are used. Even if only EPDM rubber is used as a monomer component, the refractive index of EPDM rubber is significantly lower than that of the matrix resin component, so it is not possible to produce a transparent resin from a combination of the two. Since the refractive index of the polymer consisting of the above-mentioned polymer is extremely lower than that of the above-mentioned ordinary matrix resin component, in the present invention, an acrylic acid alkyl ester monomer is used as an essential component of the vinyl monomer mixture. By using this, it is possible to substantially match the refractive index of the EPDM rubber and the refractive index of the matrix resin component, and as a result, a thermoplastic resin with good transparency and excellent weather resistance and impact resistance can be created. Manufacturing becomes possible.
本発明で使用するEPDMゴムとしては通常エチレン2
0〜90モルチ、プロピレフ9陶80
合からなる共重合体ゴムが適当である。これらEPDM
ゴムのムーニー粘度は、20〜200が好ましい。なお
ここで非共役ジエンとしては、ノルボルネン類、シクロ
ペンタジェン類の環状ジエン類、するいはt4−ヘキサ
ジエンなどの非共役鎖状ジエン類が用いられる。The EPDM rubber used in the present invention is usually ethylene 2
A copolymer rubber consisting of 0 to 90 moles of propylene and 80 moles of propylev is suitable. These EPDM
The Mooney viscosity of the rubber is preferably 20 to 200. Here, as the non-conjugated diene, cyclic dienes such as norbornenes and cyclopentadiene, or non-conjugated chain dienes such as t4-hexadiene are used.
本発明で用いるアクリル酸アルキルエステル(式中几は
炭素原子数1〜8個のアルキルを示す。)
で示され、具体例としてはアクリル酸メチル、アクリル
酸エチル、アクリル酸プロピル、アクリル酸ブチル、ア
クリル酸ペンチル、アクリル酸へキイ残、アクリル酸ヘ
プチルおよびアクリこともでき、≠+中でも特にアクリ
ル
酸nプロピル、アクリル−参←酸ブチルの使用が好まし
い。The acrylic acid alkyl ester used in the present invention (in the formula represents alkyl having 1 to 8 carbon atoms), and specific examples include methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, It is also possible to use pentyl acrylate, heptyl acrylate, heptyl acrylate and acrylic acid, among which n-propyl acrylate and butyl acrylate are particularly preferred.
またアクリル酸アルキルエステル系単量体と共重合可能
な他のビニル単量体としては、例えばスチレン、α−メ
チルスチレン、ビニルトルエンなどの芳香族ビニル系単
量体、アクリロニトリルやメタクリロニトリルなどのシ
アン化ビニル系単量体およびメタクリル酸メチルやメタ
クリル酸エチルなどのメタクリル酸エステル系単量体な
どが挙げられる。Examples of other vinyl monomers that can be copolymerized with the acrylic acid alkyl ester monomer include aromatic vinyl monomers such as styrene, α-methylstyrene, and vinyltoluene, and acrylonitrile and methacrylonitrile. Examples include vinyl cyanide monomers and methacrylic acid ester monomers such as methyl methacrylate and ethyl methacrylate.
本発明においてEPDMゴムとグラフト重合するビニル
系単量体としてアクリル酸アルキルエステル系単量体の
みを用いる場合には、マトリックス樹脂成分の屈折率が
EPDMの屈折率よシも小さいため透明な熱可塑性樹脂
が得られず、上記の他のビニル系単量体とアクリル酸ア
ルキルエステル系単量体を混合使用することによりマト
リックス樹脂の屈折率とEPDMの屈折率の差が0.0
05以下となるように単量体混合物の組成を適宜選−択
する必要がある。ここで両者の屈折率の差が0.005
を越える場合には得られる熱可塑性樹脂の透明性が低下
するため好ましくない。なお単量体混合物のみからなる
マ) IJラックス脂の屈折率は理論式からの計算かま
たは予めその組成からなる単量体混合物を重合して得た
樹脂の屈折率を測定することにより知ることができる。In the present invention, when only an acrylic acid alkyl ester monomer is used as a vinyl monomer to be graft-polymerized with EPDM rubber, the refractive index of the matrix resin component is smaller than that of EPDM, so that transparent thermoplastic When a resin is not obtained, the difference between the refractive index of the matrix resin and the refractive index of EPDM is 0.0 by using a mixture of the other vinyl monomers and the acrylic acid alkyl ester monomers mentioned above.
It is necessary to appropriately select the composition of the monomer mixture so that it is 0.05 or less. Here, the difference in refractive index between the two is 0.005
If it exceeds 20%, the transparency of the thermoplastic resin obtained will decrease, which is not preferable. The refractive index of the IJ lux resin, which is composed only of a monomer mixture, can be calculated from a theoretical formula or can be known by measuring the refractive index of a resin obtained by polymerizing a monomer mixture having the same composition in advance. I can do it.
本発明の熱可塑性樹脂を製造する際の(a) E PD
Mゴムと(b)単量体混合物の割合は(a) 10〜
70重量部、とくに15〜50重量部に対しくb) 9
0〜60重量部、とくに85〜50重量部(合計100
重量部)が好ましく 、(a) E P D Mが10
重量部未満ではグラフト率が低く耐衝撃性の不十分な樹
脂しか得られず、また70重量部を越えると樹脂の成形
性や透明性が低下するため好1しくない。(a) E PD when producing the thermoplastic resin of the present invention
The ratio of M rubber and (b) monomer mixture is (a) 10~
70 parts by weight, especially 15 to 50 parts by weight b) 9
0 to 60 parts by weight, especially 85 to 50 parts by weight (total 100 parts by weight)
(parts by weight) is preferred, and (a) EPDM is 10
If it is less than 70 parts by weight, the grafting rate is low and a resin with insufficient impact resistance is obtained, and if it exceeds 70 parts by weight, the moldability and transparency of the resin deteriorate, which is not preferable.
本発明の熱可塑性樹脂を製造するための重合方法として
は溶液重合法、懸濁重合法、塊状重合法および乳化重合
法などの公知の方法が採用できるが、なかでもたとえば
芳香族炭化水素溶媒や芳香族/脂肪族炭化水素混合溶媒
を用いる溶液重合法および懸濁重合法が好ましい。As the polymerization method for producing the thermoplastic resin of the present invention, known methods such as solution polymerization, suspension polymerization, bulk polymerization, and emulsion polymerization can be employed. Solution polymerization methods and suspension polymerization methods using aromatic/aliphatic hydrocarbon mixed solvents are preferred.
かくして得られる本発明の熱可塑性樹脂は耐候性、耐衝
撃性および透明性が均衡してすぐれており、これらの特
性を生かした種々の用途に使用が期待されるが、この熱
可塑性樹脂に他のビニル系重合体、たとえばスチレン−
アクリロニトリル−メタクリル酸メチル共重合体、ポリ
ツタクリル酸メチル、ポリアクリル酸ブチル、アクリル
酸ブチル−メタクリル酸メチル共重合体、スチレン−ア
クリル酸ブチル−メタクリル酸メチル共重合体、スチレ
ン−アクリロニトリル−アクリル酸ブチル共重合体、メ
タクリル酸メチル−アクリロニトリル共重合体、スチレ
ン−メタクリル酸メチル共重合体、スチレン−アクリル
酸ブチル共重合体およびスチレン−アクリロニトリル−
メタクリル酸メチル−アクリル酸ブチル共重合体などを
配合した組成物の形で実用に供することもできる。ただ
しここで用いるビニル系重合体は、本発明で得られる熱
可塑性樹脂とその屈折率の差が0.0’ 05以下の範
囲にあるものが好ましく、この条件を満足しない場合に
は透明な組成物を得ることができない。The thermoplastic resin of the present invention thus obtained has excellent weather resistance, impact resistance, and transparency in a well-balanced manner, and is expected to be used in various applications that take advantage of these properties. vinyl polymers, such as styrene
Acrylonitrile-methyl methacrylate copolymer, polymethyl methacrylate, polybutyl acrylate, butyl acrylate-methyl methacrylate copolymer, styrene-butyl acrylate-methyl methacrylate copolymer, styrene-acrylonitrile-butyl acrylate copolymer Polymers, methyl methacrylate-acrylonitrile copolymer, styrene-methyl methacrylate copolymer, styrene-butyl acrylate copolymer and styrene-acrylonitrile-
It can also be put to practical use in the form of a composition containing a methyl methacrylate-butyl acrylate copolymer or the like. However, the vinyl polymer used here preferably has a refractive index difference of 0.0'05 or less from the thermoplastic resin obtained in the present invention, and if this condition is not satisfied, a transparent composition is used. can't get things.
またこの場合の本発明の熱可塑性樹脂とビニル系重合体
の配合割合は5〜95重量部/95〜5重量部の広い範
囲が採用し得る。Further, in this case, the blending ratio of the thermoplastic resin of the present invention and the vinyl polymer may be in a wide range of 5 to 95 parts by weight/95 to 5 parts by weight.
なお本発明の熱可塑性樹脂およびこれを用いた上記組成
物にはヒンダードフエノール基、リン系および硫黄系な
どの酸化防止剤、ヒンダードアミン系などの光安定剤、
紫外線吸収剤、滑剤、着色剤、難燃剤、補強剤および充
填剤などの通常の添加剤を、その透明性を阻害しない範
囲で含有せしめて実用に供することもできる。The thermoplastic resin of the present invention and the composition using the same may contain hindered phenol groups, phosphorus-based and sulfur-based antioxidants, hindered amine-based light stabilizers, etc.
Conventional additives such as ultraviolet absorbers, lubricants, colorants, flame retardants, reinforcing agents, and fillers can also be incorporated to the extent that they do not impede transparency.
以下に参考例および実施例によって本発明をさらに説明
する。なお、本実施例中、アイゾツト衝撃強度はAST
M D−256−56MethodAに従って測定し
た。屈折率は、アツベ屈折計によシ20℃で測定した。The present invention will be further explained below using reference examples and examples. In this example, the Izod impact strength is AST
Measured according to MD-256-56 Method A. The refractive index was measured at 20° C. using an Atsube refractometer.
光透過率は厚さ1馴シ−トをプレス成形し、分光光度計
によシ光波長5807nμで測定し7た。The light transmittance was determined by press-molding a sheet with a thickness of 1, and measuring it with a spectrophotometer at a light wavelength of 5807 nm.
耐候性試験は、サン7ヤインウエザーメーター(スガ試
験磯■製WEL−8UN−HC型)を用い、400時間
暴露後の1/8″アイゾツト衝撃強度の保持率〔400
時間暴露後の衝撃強度/暴露前の衝撃強度Xl00.1
で示し、1/8〃アイゾツト衝撃強度は、ASTM
I)−256−5−6に準じて測定した。The weather resistance test was carried out using a Sun 7 Yain Weather Meter (WEL-8UN-HC model manufactured by Suga Tenken Iso), and the retention rate of 1/8" Izotsu impact strength after 400 hours of exposure [400
Impact strength after time exposure/Impact strength before exposure Xl00.1
The 1/8 Izot impact strength is ASTM
Measured according to I)-256-5-6.
実施例1 次の各処方により重合体A−Fを製造した。Example 1 Polymers A to F were produced using the following formulations.
(1) E P D Mゴム(三井石油化学製E P
T≠3045)25部をトルエン250部中に溶解し
たのち、系内を窒素置換し、アクリル酸11−ブチル6
7.5部、メチレフ15部およびベンゾイルパーオキサ
イド0.5部を添加して80℃で15時間重合を行なっ
た。重合終了後、ポリマ溶液をメチルアルコール中に投
じて未反応物を抽出除去し、メチルアルコールで洗浄、
乾燥後グラフト共重合体を得た。(1) E PDM rubber (Mitsui Petrochemical E P
After dissolving 25 parts of T≠3045) in 250 parts of toluene, the system was replaced with nitrogen and 11-butyl acrylate 6
7.5 parts of methyleph, 15 parts of methylene ref, and 0.5 part of benzoyl peroxide were added, and polymerization was carried out at 80° C. for 15 hours. After polymerization is complete, the polymer solution is poured into methyl alcohol to extract and remove unreacted substances, washed with methyl alcohol,
After drying, a graft copolymer was obtained.
Δ
(2)EPDMゴム(三井石油化学製E P T≠40
70)15部をベンセン100部およびn−へブタン1
00部の混合溶媒に溶解したのち、系内を窒素置換し、
次いでアクリル酸n−ブチル595部、スチレン4.2
5部、アクリロニトリル21.25部およびベンゾイル
パーオキサイド05部を添加して、80℃で8時間重合
を行なった。重合終了後、ポリマ溶液をメチルアルコー
ル中に投じ、未反応物を抽出除去して、メチルアルコー
ルで洗浄、乾燥後、グラフト共重合体Bを得た。Δ (2) EPDM rubber (Mitsui Petrochemicals EP T≠40
70) 15 parts to 100 parts of benzene and 1 part of n-hebutane
After dissolving in 00 parts of mixed solvent, the system was replaced with nitrogen,
Next, 595 parts of n-butyl acrylate, 4.2 parts of styrene
5 parts of acrylonitrile, 21.25 parts of acrylonitrile, and 05 parts of benzoyl peroxide were added, and polymerization was carried out at 80° C. for 8 hours. After the polymerization was completed, the polymer solution was poured into methyl alcohol, unreacted substances were extracted and removed, and after washing with methyl alcohol and drying, a graft copolymer B was obtained.
(3)ll?!オートクレーブにE I) D Mゴム
(三井石油化学製E P T≠3045)40部および
トルエン250部を仕込み、ゴムを完全溶解したのち、
系内を窒素置換し、次いでアクリル酸エチル42部、メ
タクリル酸メチル18部およびジークミルパーオキザイ
ド0.5部を添加して110℃で20時間重合を行なっ
た。(3)ll? ! 40 parts of E I) DM rubber (EP T≠3045 manufactured by Mitsui Petrochemicals) and 250 parts of toluene were placed in an autoclave, and after completely dissolving the rubber,
The inside of the system was purged with nitrogen, and then 42 parts of ethyl acrylate, 18 parts of methyl methacrylate, and 0.5 part of dicumyl peroxide were added, and polymerization was carried out at 110° C. for 20 hours.
重合終了後、ポリマ溶液をメチルアルコールに投じ、未
反応物を抽出除去して、メチルアルコールで洗浄、乾燥
後、グラフト共重合体Cを得た。After the polymerization was completed, the polymer solution was poured into methyl alcohol, unreacted substances were extracted and removed, and after washing with methyl alcohol and drying, a graft copolymer C was obtained.
(4) オートクレーブ中でEPDMゴム(三井石油
化学製EPT−≠3045)20部をトルエン66.7
部およびn−へキサン66.6部に混合溶解し、この溶
液にアクリル酸メチル72部、スチレン1.6部、アク
リロニトリル6.4部およびベンゾイルパーオキサイド
05部を添加して均一に混合した。一方、純水200部
にメタクリル酸メチル/アクリルアミド−20780の
共重合体03部、燐酸/ナトリウム0.05部を溶解し
オートクレーブ中に仕込み、気相とN2ガスで置換して
激しく攪拌しながら90℃6時間、さらに100℃で1
時間重合して、平均粒状0.5〜0.8 mynの無色
透明のビーズ状重合体りを得た。(4) In an autoclave, 20 parts of EPDM rubber (EPT-≠3045 manufactured by Mitsui Petrochemicals) was mixed with 66.7 g of toluene.
72 parts of methyl acrylate, 1.6 parts of styrene, 6.4 parts of acrylonitrile and 05 parts of benzoyl peroxide were added to this solution and mixed uniformly. Separately, 03 parts of methyl methacrylate/acrylamide-20780 copolymer and 0.05 parts of phosphoric acid/sodium were dissolved in 200 parts of pure water and charged into an autoclave. °C for 6 hours, then at 100 °C for 1 hour.
Polymerization was carried out for a period of time to obtain a colorless and transparent bead-like polymer having an average particle size of 0.5 to 0.8 myn.
(5) オートクレーブ中においてE P D M
コム(三井石油化学製EPT≠4070125部を27
750部およびローへブタン50部に混合溶解したのち
系内をN、ガスで置換し、この溶液にアクリル酸メチル
60.0部、アクリロニトリル15部およびベンゾイル
パーオキサイド0.5部を添加して均一に混合した。(5) E PDM in autoclave
com (Mitsui Petrochemical EPT≠4070125 parts 27
After mixing and dissolving 750 parts of methyl acrylate and 50 parts of rhohebutane, the system was replaced with N and gas, and 60.0 parts of methyl acrylate, 15 parts of acrylonitrile, and 0.5 parts of benzoyl peroxide were added to this solution to homogenize. mixed with.
一方、純水200部にメタクリル酸メチル/アクリルア
ミド−2o、’a OQ共重合体0.3部および燐酸/
ナトリウム0.05部を溶融してオートクレーブ中に仕
込み激しく攪拌しながら90℃で6時間、さらに100
℃1時間重合して、ビーズ状重合体Eを得た。On the other hand, 0.3 parts of methyl methacrylate/acrylamide-2o,'a OQ copolymer and phosphoric acid/
Melt 0.05 part of sodium, charge it into an autoclave, and heat it at 90°C for 6 hours with vigorous stirring.
C. for 1 hour to obtain bead-like polymer E.
(6) オートクレーブ中にE J) D Mゴム(
三井石油化学製E I) T−≠ろ045)20部ケト
ルエン66.7部および1]−へブタン6ろ、6部を仕
込んで均一溶解したのち、系内を窒素で置換し、この溶
液にアクリル酸11−ブチル60.0部、メタクリル酸
メチル16部、スチレン4部およびベンゾイルパーオキ
サイド0.5部を混合溶解した。次に懸濁安定剤として
メタクリル酸メチル/アクリルアミド−2D/80共重
合体0.3部、燐酸1ナトリウム0.05部および純水
200部を混ぜて添加し、攪拌しながら90℃で6時間
、さらに100℃で1時間重合した。重合終了後続いて
水蒸気蒸留より未反応物および溶媒を留去したのち、水
洗脱水、乾燥して、ビーズ状の重合体Fを得た。(6) E J) D M rubber (
Mitsui Petrochemical Co., Ltd. E I) T-≠RO045) 20 parts 66.7 parts of ketoluene and 6 parts of 1]-hebutane were charged and dissolved uniformly, then the system was replaced with nitrogen and this solution was 60.0 parts of 11-butyl acrylate, 16 parts of methyl methacrylate, 4 parts of styrene, and 0.5 part of benzoyl peroxide were mixed and dissolved. Next, as a suspension stabilizer, 0.3 parts of methyl methacrylate/acrylamide-2D/80 copolymer, 0.05 parts of monosodium phosphate, and 200 parts of pure water were mixed and added, and the mixture was heated at 90°C for 6 hours with stirring. , and further polymerized at 100°C for 1 hour. After the polymerization was completed, unreacted substances and the solvent were removed by steam distillation, followed by washing with water, dehydration, and drying to obtain bead-shaped polymer F.
得られた各重合体A−Fを押出機によって樹脂温度22
0℃で押出し、それぞれペレット化した。次いで各ペレ
ットについてシリンダ一温度230℃、金型温度50℃
の条件での射出成形に供し、各試験片を作製し、それに
ついて特性の評価を行なった。結果を表1に示した。Each of the obtained polymers A-F was heated to a resin temperature of 22°C using an extruder.
Each sample was pelletized by extrusion at 0°C. Then, for each pellet, the cylinder temperature was 230°C and the mold temperature was 50°C.
Each test piece was prepared by injection molding under the following conditions, and its characteristics were evaluated. The results are shown in Table 1.
比較例1
ポリブタジェン・ラテックス20部(固形分として)の
存在下にスチレン24部およびメタクリル酸メチル56
部を乳化グラフト重合することによりグラフト共重合体
CG)を得た。Comparative Example 1 24 parts of styrene and 56 parts of methyl methacrylate in the presence of 20 parts of polybutadiene latex (as solids)
A graft copolymer CG) was obtained by emulsion graft polymerization.
捷だ表1に示したEPDMゴムの存在下に、表−1に示
しだ組成の単量体または単量体混合物を実施例1のグラ
フト共重合体(A)の溶液重合法と同様な重合処方で重
合し、グラフト共重合体(H+〜(N)を調製した。In the presence of the EPDM rubber shown in Table 1, monomers or monomer mixtures having the composition shown in Table 1 were polymerized in the same manner as in the solution polymerization method of graft copolymer (A) in Example 1. Graft copolymers (H+ to (N)) were prepared by polymerization according to the recipe.
これらのグラフト共重合体(1−I)〜(N)について
実施例1と同様に射出成形により試験片を作成し、その
特性を評価した結果を表−1に併せて示す。Test pieces of these graft copolymers (1-I) to (N) were prepared by injection molding in the same manner as in Example 1, and the properties of the test pieces were evaluated. Table 1 also shows the results.
以下余白
表−1から明らかなように、本発明の方法1得られたク
ラフト共重合体(A)〜(F’)はいずrも透明性、耐
衝撃性および耐候性が均衡してづぐれている。一方、E
PDMの代りにポリブ多ジエンを用いたグラフト共重合
体(G)は耐候伯が極めて劣り、単量体混合物にアクリ
ル酸アノ1キル工ステル単量体の代シにメクアクリル酸
メチルを含有させた場合(H,I、M)およびフクリル
酸エステル単量体を含有しても、単量付混合物のみから
なる共重合体の屈折率とEPDI’vの屈折率の差が0
.005以上の場合(J−L。As is clear from Table 1 below, all of the kraft copolymers (A) to (F') obtained by method 1 of the present invention have a balance of transparency, impact resistance, and weather resistance. ing. On the other hand, E
The graft copolymer (G) using polybutylene diene instead of PDM had extremely poor weathering resistance, and the monomer mixture contained methyl methacrylate instead of the monokylated acrylic ester monomer. In case (H, I, M) and even if the fucryl ester monomer is contained, the difference between the refractive index of the copolymer consisting only of the monomer mixture and the refractive index of EPDI'v is 0.
.. 005 or more (J-L.
N)のグラフト共重合体はいずれも透明性がqる。All of the graft copolymers (N) have good transparency.
実施例2
懸濁重合法により、表−2に示した共重合糸・成および
屈折率を有する6種類のビニル系共重合体(a)〜(f
)を調製した。Example 2 By a suspension polymerization method, six types of vinyl copolymers (a) to (f
) was prepared.
□
次にこれらビニル系共重合体(a)〜(f)i−よび実
施例1で得たグラフト共重合体(5)〜(F) ヲそレ
ソれ表−6の割合で混合し、4Qvungt押出機(2
20℃)でベレット化した後、さらに射出成形により試
験片を作成してその特性を評価した。□ Next, these vinyl copolymers (a) to (f) i- and the graft copolymers (5) to (F) obtained in Example 1 were mixed in the proportions shown in Table 6. Extruder (2)
After pelletizing at 20° C.), test pieces were prepared by injection molding and their properties were evaluated.
これらの結果を表−3に併せて示す。These results are also shown in Table-3.
以下余白
表−6の結果から明らかなように本発明の方法で得た熱
可塑性樹脂と透明なビニル系重合体とその屈折率の差が
0.005以内となるように配合した組成物においても
、透明性、耐衝撃性および耐候性が均衡にすぐれている
。As is clear from the results in Margin Table 6 below, even in compositions in which the thermoplastic resin obtained by the method of the present invention and the transparent vinyl polymer are blended so that the difference in refractive index between them is within 0.005, , has an excellent balance of transparency, impact resistance, and weather resistance.
特許出願人 東し株式会社Patent applicant: Toshi Co., Ltd.
Claims (1)
ム10〜70重量部の存在下に(b)アクリル酸アルキ
ルエステル系単量体およびこれと共重合可能な他のビニ
ル単量体からなる単量体混合物90〜30重量部をグラ
フト重合するに際し、(b)単量体混合物のみを重合し
て々る重合体の屈折率と(a)エチレン−プロピレン−
非共役ジエン共重合体ゴムの屈折率の差が、0005以
下となるように(b)単量体混合物の組成を選択するこ
とを特徴とする熱可塑性樹脂の製造方法。(a) In the presence of 10 to 70 parts by weight of ethylene-propylene-nonconjugated diene copolymer rubber, (b) a monomer consisting of an acrylic acid alkyl ester monomer and another vinyl monomer copolymerizable therewith. When graft polymerizing 90 to 30 parts by weight of the monomer mixture, (b) the refractive index of the polymer obtained by polymerizing only the monomer mixture and (a) ethylene-propylene-
A method for producing a thermoplastic resin, comprising selecting the composition of (b) the monomer mixture so that the difference in refractive index of the non-conjugated diene copolymer rubber is 0005 or less.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5915883A JPS59187012A (en) | 1983-04-06 | 1983-04-06 | Manufacture of thermoplastic resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5915883A JPS59187012A (en) | 1983-04-06 | 1983-04-06 | Manufacture of thermoplastic resin |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59187012A true JPS59187012A (en) | 1984-10-24 |
Family
ID=13105274
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5915883A Pending JPS59187012A (en) | 1983-04-06 | 1983-04-06 | Manufacture of thermoplastic resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59187012A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004359832A (en) * | 2003-06-05 | 2004-12-24 | Techno Polymer Co Ltd | Soft polymer |
WO2022196121A1 (en) * | 2021-03-16 | 2022-09-22 | 三菱ケミカル株式会社 | Acryl-olefin composite resin composition, nonaqueous resin composition, nonaqueous resin composition production method, acryl-olefin composite resin composition production method, coating composition, ink composition, adhesive agent composition, film, and forming material |
-
1983
- 1983-04-06 JP JP5915883A patent/JPS59187012A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004359832A (en) * | 2003-06-05 | 2004-12-24 | Techno Polymer Co Ltd | Soft polymer |
WO2022196121A1 (en) * | 2021-03-16 | 2022-09-22 | 三菱ケミカル株式会社 | Acryl-olefin composite resin composition, nonaqueous resin composition, nonaqueous resin composition production method, acryl-olefin composite resin composition production method, coating composition, ink composition, adhesive agent composition, film, and forming material |
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