JPS638982B2 - - Google Patents
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- Publication number
- JPS638982B2 JPS638982B2 JP55088592A JP8859280A JPS638982B2 JP S638982 B2 JPS638982 B2 JP S638982B2 JP 55088592 A JP55088592 A JP 55088592A JP 8859280 A JP8859280 A JP 8859280A JP S638982 B2 JPS638982 B2 JP S638982B2
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- JP
- Japan
- Prior art keywords
- resin
- weight
- vinyl chloride
- parts
- abs
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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- Compositions Of Macromolecular Compounds (AREA)
Description
本発明はABS系樹脂(ABS樹脂又はMABS樹
脂)と塩化ビニル系樹脂およびアルキルアクリレ
ート又はアルキルメタクリレート系重合体とから
なり、加工性、耐衝撃性、成形機内での樹脂置換
性に優れた難燃性樹脂組成物、さらに詳しくは、
ジエン系ゴム質重合体の存在下でシアン化ビニ
ル、芳香族ビニルアルキルメタアクリレート系の
共重合を行なう際にアルキル(メタ)アクリレー
ト系の成分を加えてなる共重合体と、塩化ビニル
系樹脂とをブレンドしてなり、加工性、耐衝撃性
に優れ、又かかる樹脂組成物を加工する成形機の
シリンダー、スクリユー、ダイス、ノズル等金属
面への溶融樹脂の粘着が少く成形機内での樹脂置
換性に優れ、さらに溶融樹脂の粘着が少いことか
ら樹脂の部分的滞留がほとんどなく滞留部分の熱
劣化が減少し、熱安定性の面からも優れた特性を
有する樹脂組成物に係わるものである。
合成樹脂の種々の特性の中でも特に、高い難燃
特性が望まれるようになつてきた。その難燃化の
指標として米国のUL規格が用いられることが多
い。その規格の中でも射出成形、押出成形等の分
野で多く用いられている比較的高度な難燃性を有
している樹脂は、ABS樹脂等の易燃性樹脂に難
燃剤等を添加した添加型と一般的に呼ばれている
ものと、同じくABS等の易燃性樹脂と塩化ビニ
ル系樹脂とをブレンドした塩ビブレンド型と一般
的に呼ばれているものの2つに大別される。この
2者のうち経済的に有利なこともあつて塩ビブレ
ンド型が一般的な用途では可成り大きな割合をし
めている。この塩ビブレンド型樹脂は、一般的に
行なわれている成形方法である射出成形におい
て、その加工温度が塩ビニル系樹脂の分解温度に
ほぼ近いところで行なわれているため、塩化ビニ
ル樹脂の分解に起因する熱安定性の面での欠点が
ある。この熱安定性の問題は、樹脂温度が最も高
くなる成形機のノズル又は成形体のゲートにおけ
る熱劣化と、成形機内の部分的滞留による長時間
の熱履歴による劣化に大別される。
塩ビブレンド型樹脂のこの欠点を改良する試み
がいくつか提案され実施されている。1つの方法
として、分子量のより小さい塩化ビニル樹脂を用
いる方法があるが、実用的機械強度の低下、熱安
定性の低下等があり、用いる塩化ビニル樹脂の分
子量には限界がある。他の方法として、可塑剤や
滑剤を多量に添加する方法があるが、添加剤が成
形体表面にブリードしたり、成形体に剥離現象が
現われたり、耐熱変形性が低下する等の欠点があ
る。また他の方法として、塩化ビニルとエチレ
ン、プロピレン等の不飽和炭化水素化合物やアル
キルアクリレート又はアルキルメタアクリレート
を共重合、グラフト重合又は疑似グラフト重合し
て塩化ビニル部分の溶融粘度を下げるか又は滑性
を持たせる等して加工性を改良する方法もある。
この加工性改良方法は、ブラベンダープラストグ
ラフによる熱分解までの時間を長くできる。従つ
て、主にノズル又はゲート部分の熱劣化を改良す
る方法としては有効であるが、成形機内の部分的
滞留による長時間の熱履歴による劣化を改良する
に至つていない。
本発明者らは、鋭意検討した結果、金属面への
粘着が塩化ビニル樹脂はもちろんABS樹脂にも
帰因しやすいこと、また高温では特にABS樹脂
による粘着が大きいことを明らかにし、従つてア
ルキルアクリレート化合物又はアルキルメタクリ
レート化合物を主成分とする重合体連鎖をABS
樹脂に緊密に接触させて存在させることが上記の
部分的滞留による熱劣化を改良するに有効である
ことを知つた。そして
加工性と耐衝撃性にすぐれ、また成形機のシリ
ンダー、スクリユー、ダイス、ノズル等金属面へ
の溶融樹脂の粘着が少なく成形機内での樹脂置換
性に優れ、さらに溶融樹脂の粘着が少ないので、
樹脂の部分的滞留による熱劣化も大巾に少ない塩
ビブレンド型樹脂組成物を見出した。即ち本発明
は、ABS樹脂又はメチルメタアクリレート成分
を含むMABS樹脂〔A〕20〜70重量%と塩化ビ
ニル系樹脂〔B〕80〜30重量%からなる組成物
100重量部に対して、アルキル(メタ)アクリレ
ート化合物の1種又は2種以上を主成分として含
む重合体〔C〕1〜10重量部を、上記のポリブタ
ジエン系ゴム質重合体を用いてABS樹脂又は
MABS樹脂を製造する際にラテツクス粒子の状
態で混合することを特徴とする衝撃性、加工性、
熱安定性、樹脂置換性に優れた樹脂組成物を内容
とする。以下詳細説明する。
樹脂成分〔A〕の含量は30〜65重量%である。
30重量%未満では加工性に難点が生ずる傾向がで
るし、65重量%をこえると難燃性の保持が困難と
なる。
ポリブタジエン系ゴム質重合体は、ポリブタジ
エン又は50重量%以上のポリブタジエン及びこれ
と共重合し得る50重量%以下のモノオレフイン単
量体例えばスチレン等の芳香族ビニル化合物、メ
チルアクリレート、エチルアクリレート、ブチル
アクリレート等のアルキルアクリレート;メチル
メタアクリレート、エチルメタアクリレート、ブ
チルメタアクリレート等のアルキルメタアクリレ
ート;アクリロニトリル等のシアン化ビニル化合
物等との共重合体である。
共重合体〔C〕は、メチルアクリレート、エチ
ルアクリレート、2―エチルヘキシルアクリレー
ト、ブチルアクリレート、シクロヘキシルアクリ
レート等のアルキルアクリレート;エチルメタア
クリレート、2―エチルヘキシルメタアクリレー
ト、ブチルメタアクリレート等のアルキルメタア
クリレートより選ばれる1種又は2種以上の単量
体100〜50重量%とスチレン、α―メチルスチレ
ン等の芳香族ビニル化合物より選ばれる1種又は
2種以上の単量体0〜50重量%を重合してなる共
重合体である。アルキル(メタ)アクリレートが
50重量%より少ない場合は溶融樹脂の金属面への
粘着が大きく樹脂置換性の効果が得られにくい。
この共重合体〔C〕は、樹脂〔A〕と樹脂〔B〕
からなる組成物100重量部に対して、1〜10重量
部、殊に1.5〜5重量部が好ましい。1重量部よ
り少ないと溶融樹脂の金属面への粘着が大きく樹
脂置換性の効果が得られず、10重量部をこえると
塩化ビニル樹脂との混和性が悪くなること、また
成形品の耐熱変形性も低下するので好ましくな
い。
共重合体〔C〕は、ポリブタジエン系ゴム質重
合体を用いてABS又はMABS樹脂〔A〕を製造
する際にグラフト重合の開始時、又は途中、或い
は終了時のいずれかの時点においてラテツクスの
状態で混合することが重要である。
本発明によれば、製造プロセス上、コストは従
来のABS樹脂と比べて殆んど変らないものとす
ることができるのも1つの特徴である。
塩化ビニル系樹脂〔B〕は、ポリ塩化ビニル又
は90重量%以上の塩化ビニルとこれと共重合し得
る10重量%以下のモノオレフイン単量体例えば酢
酸ビニル、塩化ビニリデン、アクリロニトリル等
との共重合体であり、目的とする樹脂組成物の加
工性、耐衝撃性の点からは重合度は300〜1000で
あることが好ましく、400〜750であることがさら
に好ましい。
本発明の樹脂組成物は、各種添加剤を添加した
形で実用に供されるが、安定剤としては錫系安定
剤・鉛系安定剤が熱安定性の面で好ましい。
次に、本発明の実施例を示すが、本発明は以下
の例に限定されるものではない。
実施例及び比較例
重合体〔C〕の製造
第1表の仕込比にもとずき60℃で乳化重合を行
なつて重合体〔C〕―1,〔C〕―2を得た。
The present invention is made of ABS resin (ABS resin or MABS resin), vinyl chloride resin, and alkyl acrylate or alkyl methacrylate polymer, and is flame retardant and has excellent processability, impact resistance, and resin replacement ability in the molding machine. The resin composition, more specifically,
A copolymer obtained by adding an alkyl (meth)acrylate component during the copolymerization of vinyl cyanide and aromatic vinyl alkyl methacrylate in the presence of a diene rubbery polymer, and a vinyl chloride resin. It has excellent processability and impact resistance, and there is less adhesion of the molten resin to metal surfaces such as cylinders, screws, dies, nozzles, etc. of the molding machine that processes this resin composition, making it easy to replace the resin in the molding machine. This relates to a resin composition that has excellent properties in terms of thermal stability, as well as low adhesion of the molten resin, so there is almost no local retention of the resin, reducing thermal deterioration in the retained area. be. Among the various properties of synthetic resins, high flame retardant properties have become particularly desirable. The American UL standard is often used as an indicator of flame retardancy. Among the standards, resins with relatively high flame retardancy that are often used in fields such as injection molding and extrusion molding are additive-type resins that are made by adding flame retardants to easily flammable resins such as ABS resin. It is broadly divided into two types: what is commonly called a PVC blend type, and what is generally called a PVC blend type, which is a blend of easily flammable resin such as ABS and vinyl chloride resin. Of these two types, the vinyl chloride blend type accounts for a considerably larger proportion in general use, partly because it is economically advantageous. In injection molding, which is a commonly used molding method, this PVC blend type resin is processed at a temperature close to the decomposition temperature of the PVC resin. There is a drawback in terms of thermal stability. This thermal stability problem can be roughly divided into thermal deterioration at the nozzle of the molding machine or at the gate of the molded article, where the resin temperature is highest, and deterioration due to long-term thermal history due to partial retention in the molding machine. Several attempts have been proposed and implemented to improve this drawback of vinyl chloride blend type resins. One method is to use a vinyl chloride resin with a smaller molecular weight, but there is a decrease in practical mechanical strength, a decrease in thermal stability, etc., and there is a limit to the molecular weight of the vinyl chloride resin to be used. Another method is to add large amounts of plasticizers or lubricants, but these have drawbacks such as the additives bleeding onto the surface of the molded product, peeling phenomena appearing on the molded product, and reduced heat deformation resistance. . Another method is to copolymerize, graft polymerize, or pseudo-graft polymerize vinyl chloride with an unsaturated hydrocarbon compound such as ethylene or propylene, or an alkyl acrylate or alkyl methacrylate to lower the melt viscosity of the vinyl chloride portion or to improve the lubricating properties. There is also a method to improve workability, such as by adding
This processability improvement method can lengthen the time until thermal decomposition by Brabender plastography. Therefore, although it is effective as a method for improving the thermal deterioration of the nozzle or gate portion, it has not yet been able to improve the deterioration caused by long-term thermal history due to partial retention in the molding machine. As a result of intensive studies, the present inventors have found that adhesion to metal surfaces is likely to be caused by not only vinyl chloride resin but also ABS resin, and that the adhesion caused by ABS resin is particularly large at high temperatures. ABS is a polymer chain mainly composed of acrylate compounds or alkyl methacrylate compounds.
It has been found that allowing the resin to exist in close contact with the resin is effective in improving the thermal deterioration caused by the above-mentioned partial retention. It has excellent processability and impact resistance, and has low adhesion of molten resin to metal surfaces such as cylinders, screws, dies, nozzles, etc. of the molding machine, and has excellent resin replacement properties in the molding machine. ,
We have found a vinyl chloride blend type resin composition that has significantly less thermal deterioration due to partial retention of the resin. That is, the present invention provides a composition comprising 20 to 70% by weight of ABS resin or MABS resin [A] containing a methyl methacrylate component and 80 to 30% by weight of vinyl chloride resin [B].
Based on 100 parts by weight, 1 to 10 parts by weight of a polymer [C] containing one or more alkyl (meth)acrylate compounds as a main component is added to ABS resin using the above polybutadiene-based rubbery polymer. or
When manufacturing MABS resin, it is mixed in the form of latex particles, which improves impact properties and processability.
Contains a resin composition with excellent thermal stability and resin substitution properties. The details will be explained below. The content of resin component [A] is 30 to 65% by weight.
If it is less than 30% by weight, there will be a tendency for difficulties in processability to occur, and if it exceeds 65% by weight, it will be difficult to maintain flame retardancy. Polybutadiene-based rubbery polymers include polybutadiene or 50% by weight or more of polybutadiene and 50% by weight or less of monoolefin monomers that can be copolymerized with this, such as aromatic vinyl compounds such as styrene, methyl acrylate, ethyl acrylate, butyl acrylate. Alkyl acrylates such as methyl methacrylate, ethyl methacrylate, and butyl methacrylate; copolymers with vinyl cyanide compounds such as acrylonitrile. Copolymer [C] is selected from alkyl acrylates such as methyl acrylate, ethyl acrylate, 2-ethylhexyl acrylate, butyl acrylate, and cyclohexyl acrylate; and alkyl methacrylates such as ethyl methacrylate, 2-ethylhexyl methacrylate, and butyl methacrylate. By polymerizing 100 to 50% by weight of one or more monomers and 0 to 50% by weight of one or more monomers selected from aromatic vinyl compounds such as styrene and α-methylstyrene. It is a copolymer. Alkyl (meth)acrylate
If it is less than 50% by weight, the molten resin will stick to the metal surface so much that it will be difficult to obtain the effect of resin substitution.
This copolymer [C] consists of resin [A] and resin [B]
It is preferably 1 to 10 parts by weight, particularly 1.5 to 5 parts by weight, based on 100 parts by weight of the composition. If it is less than 1 part by weight, the molten resin will stick to the metal surface and the effect of resin replacement will not be obtained, and if it exceeds 10 parts by weight, the miscibility with vinyl chloride resin will be poor, and the molded product will not undergo heat deformation. This is not preferable because it also reduces performance. Copolymer [C] is the state of latex at the beginning, during, or at the end of graft polymerization when producing ABS or MABS resin [A] using a polybutadiene-based rubbery polymer. It is important to mix at According to the present invention, one of the features is that the cost can be made almost the same in terms of manufacturing process compared to conventional ABS resin. Vinyl chloride resin [B] is polyvinyl chloride or a copolymer of 90% by weight or more of vinyl chloride and 10% by weight or less of a monoolefin monomer that can be copolymerized therewith, such as vinyl acetate, vinylidene chloride, acrylonitrile, etc. The degree of polymerization is preferably from 300 to 1000, more preferably from 400 to 750, from the viewpoint of processability and impact resistance of the desired resin composition. The resin composition of the present invention is put to practical use with various additives added thereto, and as the stabilizer, tin-based stabilizers and lead-based stabilizers are preferred in terms of thermal stability. Next, examples of the present invention will be shown, but the present invention is not limited to the following examples. Examples and Comparative Examples Production of Polymer [C] Emulsion polymerization was carried out at 60°C based on the charging ratios shown in Table 1 to obtain Polymers [C]-1 and [C]-2.
【表】
オキシレート
ABS樹脂またはMABS樹脂と共重合体〔C〕
の混合物の製造
第2表の仕込み比にもとずき60℃で乳化重合を
行なつて重合体〔D〕―1〜4,ABS―を得
た。[Table] Oxylate
ABS resin or MABS resin and copolymer [C]
Production of a mixture Emulsion polymerization was carried out at 60°C based on the charging ratio shown in Table 2 to obtain polymers [D]-1 to 4, ABS-.
【表】
PVC―の製造
ポリ塩化ビニル樹脂粉末(カネビニルS―500,
鐘淵化学製)100重量部に水300重量部を加え、次
に過酸化ベンゾイル0.02重量部を含むブチルアク
リレート6.2重量部を加えて撹拌しながら室温で
塩化ビニル樹脂に十分含浸吸収させた後、85℃で
18時間重合を行なつた。得られた重合体を脱水、
水洗した後、メタノール洗浄を行ない未反応の単
量体を除去後、乾燥を行なつた。ブチルアクリレ
ートのグラフト量は塩化ビニル樹脂100重量部に
対して6.0重量部であつた。
ABS樹脂又はMABS樹脂と塩化ビニル樹脂の
混合樹脂組成物100重量部あたり第3表に示す添
加剤を加えて40mm単軸押出機を用いてペレツト化
し、その後5オンス射出成形機により成形を行な
い第4表に示す結果を得た。〔D〕―5は、第2
表中ABS―の重合を終了したラテツクス(ポ
リマー固型分100重量部)に重合体〔C〕―1の
ラテツクス(ポリマー固型分6重量部)を加えた
ものである。[Table] Manufacturing of PVC Polyvinyl chloride resin powder (Kanevinyl S-500,
300 parts by weight of water was added to 100 parts by weight (manufactured by Kanebuchi Chemical Co., Ltd.), and then 6.2 parts by weight of butyl acrylate containing 0.02 parts by weight of benzoyl peroxide was added and the mixture was sufficiently impregnated and absorbed into the vinyl chloride resin at room temperature while stirring. at 85℃
Polymerization was carried out for 18 hours. Dehydrate the obtained polymer,
After washing with water, washing with methanol was performed to remove unreacted monomers, and then drying was performed. The grafting amount of butyl acrylate was 6.0 parts by weight based on 100 parts by weight of vinyl chloride resin. Add the additives shown in Table 3 per 100 parts by weight of a mixed resin composition of ABS resin or MABS resin and vinyl chloride resin, pelletize it using a 40 mm single screw extruder, and then mold it using a 5 oz injection molding machine. The results shown in Table 4 were obtained. [D]-5 is the second
In the table, a latex of Polymer [C]-1 (polymer solid content: 6 parts by weight) was added to a latex (polymer solid content: 100 parts by weight) after completing the polymerization of ABS-.
【表】
用いた塩化ビニル樹脂はカネビニールS―500
(=550)である。[Table] The vinyl chloride resin used is Kanevinyl S-500.
(=550).
【表】
この表の実施例から判る様に、ブラベンダーの
分解時間が長く、分解後の掃除難易性、成形機の
樹脂置換性が良く、Izod衝撃値、高化式フロー値
も重合体〔C〕のないもの(比較例1)に比べて
大巾に改良されている。比較例2は、重合体
〔C〕を10重量部を越えて用いたものであるが、
ブラベンダー分解時間は長く、掃除難易性、成形
機の樹脂置換性、高化式フロー値はよいが、熱変
形温度が大巾に低下する。比較例3はブチルアク
リレートを含浸重合した塩化ビニル樹脂を用いた
ものであるが、ブラベンダーの掃除難易性、成形
機の樹脂置換性の改良程度が実施例1〜4に比べ
て小さく、熱変形温度の低下が大きい。[Table] As can be seen from the examples in this table, Brabender takes a long time to disassemble, is easy to clean after disassembly, is easy to replace with resin in the molding machine, and has a higher Izod impact value and higher flow value than the polymer. C] is greatly improved compared to the one without (Comparative Example 1). Comparative Example 2 used polymer [C] in an amount exceeding 10 parts by weight,
The Brabender decomposition time is long, and although it is easy to clean, has good resin replacement properties in the molding machine, and has good flow values, the heat distortion temperature decreases significantly. Comparative Example 3 uses vinyl chloride resin impregnated and polymerized with butyl acrylate, but the degree of improvement in the difficulty of cleaning the Brabender and the resin replacement property of the molding machine is smaller than in Examples 1 to 4, and thermal deformation is small. The temperature drop is large.
Claims (1)
を含むMABS樹脂〔A〕30〜65重量%と塩化ビ
ニル系樹脂〔B〕70〜35重量%からなる組成物
100重量部に対し、アルキルアクリレート化合物
又はアルキルメタアクリレート化合物の1種又は
2種以上を主成分として含む重合体〔C〕1〜10
重量部を、上記ABS樹脂又はMABS樹脂の製造
時にラテツクス粒子の状態で混合することにより
得られる〔A〕、〔B〕及び〔C〕からなる難燃性
樹脂組成物。[Claims] 1. A composition comprising 30 to 65% by weight of ABS resin or MABS resin [A] containing a methyl methacrylate component and 70 to 35% by weight of vinyl chloride resin [B]
Polymer [C] 1 to 10 containing one or more alkyl acrylate compounds or alkyl methacrylate compounds as a main component per 100 parts by weight
A flame-retardant resin composition consisting of [A], [B] and [C] obtained by mixing parts by weight in the form of latex particles during the production of the above-mentioned ABS resin or MABS resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8859280A JPS5714638A (en) | 1980-06-27 | 1980-06-27 | Flame-retardant resin composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8859280A JPS5714638A (en) | 1980-06-27 | 1980-06-27 | Flame-retardant resin composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5714638A JPS5714638A (en) | 1982-01-25 |
| JPS638982B2 true JPS638982B2 (en) | 1988-02-25 |
Family
ID=13947098
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8859280A Granted JPS5714638A (en) | 1980-06-27 | 1980-06-27 | Flame-retardant resin composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5714638A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5933342A (en) * | 1982-08-18 | 1984-02-23 | Mitsubishi Rayon Co Ltd | Vinyl chloride resin composition |
| JPS5998153A (en) * | 1982-11-09 | 1984-06-06 | Mitsubishi Rayon Co Ltd | Vinyl chloride resin composition |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3929700A (en) * | 1974-04-29 | 1975-12-30 | Hooker Chemicals Plastics Corp | Polyvinyl chloride composition |
| JPS5914067B2 (en) * | 1976-07-09 | 1984-04-03 | 日産化学工業株式会社 | Vinyl chloride resin composition |
-
1980
- 1980-06-27 JP JP8859280A patent/JPS5714638A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5714638A (en) | 1982-01-25 |
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