JPS6354017B2 - - Google Patents
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- Publication number
- JPS6354017B2 JPS6354017B2 JP55098299A JP9829980A JPS6354017B2 JP S6354017 B2 JPS6354017 B2 JP S6354017B2 JP 55098299 A JP55098299 A JP 55098299A JP 9829980 A JP9829980 A JP 9829980A JP S6354017 B2 JPS6354017 B2 JP S6354017B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- parts
- component
- vinyl chloride
- polymer
- 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
Links
- 239000000203 mixture Substances 0.000 claims description 32
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 claims description 30
- 229920000642 polymer Polymers 0.000 claims description 21
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 18
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 12
- 238000006116 polymerization reaction Methods 0.000 claims description 12
- -1 acrylic ester Chemical class 0.000 claims description 8
- 229920001577 copolymer Polymers 0.000 claims description 8
- 239000011342 resin composition Substances 0.000 claims description 7
- 230000000379 polymerizing effect Effects 0.000 claims description 5
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 4
- 230000000704 physical effect Effects 0.000 claims description 3
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims 1
- 239000011347 resin Substances 0.000 description 15
- 229920005989 resin Polymers 0.000 description 15
- 238000002156 mixing Methods 0.000 description 11
- 238000001879 gelation Methods 0.000 description 10
- 230000000694 effects Effects 0.000 description 9
- 239000000178 monomer Substances 0.000 description 7
- 238000012545 processing Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 238000000465 moulding Methods 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 239000006057 Non-nutritive feed additive Substances 0.000 description 5
- 229920000915 polyvinyl chloride Polymers 0.000 description 5
- 239000004800 polyvinyl chloride Substances 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 4
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 description 4
- 239000012986 chain transfer agent Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 239000003995 emulsifying agent Substances 0.000 description 4
- 230000001771 impaired effect Effects 0.000 description 4
- 239000004014 plasticizer Substances 0.000 description 4
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 3
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 3
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 3
- 238000011088 calibration curve Methods 0.000 description 3
- 239000000314 lubricant Substances 0.000 description 3
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 3
- 239000004926 polymethyl methacrylate Substances 0.000 description 3
- 239000003381 stabilizer Substances 0.000 description 3
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 2
- ONBWNNUYXGJKKD-UHFFFAOYSA-N 1,4-bis(2-ethylhexoxy)-1,4-dioxobutane-2-sulfonic acid;sodium Chemical compound [Na].CCCCC(CC)COC(=O)CC(S(O)(=O)=O)C(=O)OCC(CC)CCCC ONBWNNUYXGJKKD-UHFFFAOYSA-N 0.000 description 2
- GGSRTHRSSCWGGK-UHFFFAOYSA-L 2,2-dibutyl-5-hydroxy-1,3,2-dioxastannepane-4,7-dione Chemical compound CCCC[Sn]1(CCCC)OC(=O)CC(O)C(=O)O1 GGSRTHRSSCWGGK-UHFFFAOYSA-L 0.000 description 2
- 239000004593 Epoxy Substances 0.000 description 2
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 239000004816 latex Substances 0.000 description 2
- 229920000126 latex Polymers 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 238000009864 tensile test Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- GOXQRTZXKQZDDN-UHFFFAOYSA-N 2-Ethylhexyl acrylate Chemical compound CCCCC(CC)COC(=O)C=C GOXQRTZXKQZDDN-UHFFFAOYSA-N 0.000 description 1
- CFVWNXQPGQOHRJ-UHFFFAOYSA-N 2-methylpropyl prop-2-enoate Chemical compound CC(C)COC(=O)C=C CFVWNXQPGQOHRJ-UHFFFAOYSA-N 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- 125000005396 acrylic acid ester group Chemical group 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000007720 emulsion polymerization reaction Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 125000005395 methacrylic acid group Chemical group 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- FBCQUCJYYPMKRO-UHFFFAOYSA-N prop-2-enyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC=C FBCQUCJYYPMKRO-UHFFFAOYSA-N 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Description
本発明は、良好な加工特性と物理特性とを有す
る塩化ビニル樹脂組成物に関する。
ポリ塩化ビニルは物理的、化学的性質に優れて
いるために広く用いられているが、加工温度が熱
分解温度に近く成形加工領域が狭いばかりでな
く、ゲル化速度が遅い等の種々の加工上の問題を
有している。
可塑剤の添加がこれらの欠点の一部を解決する
ことは良く知られているが、可塑剤の揮発逃散等
の問題がある他の成形品の機械的性質の低下をも
たらし、硬化ポリ塩化ビニルの用途の全面的解決
にはほど遠い。
塩化ビニル樹脂の成形加工時に樹脂のゲル化速
度をはやめたり、成形機の金属面への粘着性を低
下させたりすることによつて生産性を向上させ、
かつ成形品の表面を平滑にし、長期間連続成形し
ても成形品に変らぬ光沢を付与したり、成形品の
深絞りを可能にしたりする、いわゆる加工性の向
上を目的として、塩化ビニル樹脂と相溶性を有す
る共重合体のいくつかが加工助剤として検討され
ており、一部の用途では大きな成果を得ている。
現在市場で使用されている主なものとしては、メ
チルメタクリレートを主成分とする共重合体があ
る。これらはゲル化速度の促進効果が大きく、又
特に高温での引張り伸度を増大させるなどの二次
加工性を大巾に改善するが、一方では押出しフイ
ルムの光沢の欠如、未ゲル化物の発生(フイツシ
ユアイとも呼ばれる)等を生ぜしめる欠点を有し
ている。特にこれを軟質の塩化ビニル樹脂に配合
した場合は、相溶性をほとんど示さない為に無数
の未ゲル化物となつて点在し、商品価値を著しく
低下させ、この意味で軟質分野への適用は極めて
困難である。上記の問題点を一挙に解決する組成
物、すなわち塩化ビニル樹脂の透明性を維持し、
高温での伸度、深絞り成形などの二次加工性を向
上せしめ、しかも硬質塩化ビニル樹脂のみならず
軟質塩化ビニル樹脂に対しても優れた分散性と優
れた加工特性を付与する加工助剤も考案されてい
るが、生産性の向上、省エネルギー等の見地か
ら、塩化ビニル樹脂の加工時に、塩化ビニルに対
する分散性の良好であること、ゲル化が早いこ
と、又加工前のブレンド工程で、ヘンシエルミキ
サー等の中で混練時にトルクがかからないこと等
の要求が強くなつた。又塩化ビニルと加工助剤の
可塑剤に対する相溶性の差からくるブレンド時の
加工助剤の融着現象とそれによるフイルムシート
加工時の未ゲル化物の発生もあり、特に軟質塩化
ビニル樹脂での分散性を大巾に改善することが求
められており、上記組成物では限界があり、又配
合によつては、ブレンド時に器壁へ加工助剤が付
着することもあり、市場の要求を充分に満足して
いるとはいえない状態である。
本発明者らは以上の点を考慮しつつ、広範囲の
検討を行つた結果、前記ポリメチルメタクリレー
ト系が示す優れた加工特性を有しながら、優れた
軟質分散性をも有し、ゲル化速度が早くブレンド
時に器壁への付着、融着のない組成物を得ること
を目的として検討を重ね本発明に到達した。
本発明は()少なくとも80重量%が塩化ビニ
ル成分である塩化ビニル系重合体または共重合体
99.9〜70重量部と、()(A)少なくとも60重量%
がメチルメタクリレートであり、100mlのクロロ
ホルム中に0.1gの重合体を溶解した溶液につい
て25℃で測定した還元粘度(ηsp/C)が2以上
である重合体又は共重合体45重量部を超え〜70重
量部の存在下に、(B)スチレン30〜70重量%とアク
リル酸エステル70〜30重量%とからなる混合物5
重量部〜50重量部未満を(B)成分のηsp/Cが1以
上になるような条件で重合し、得られた(A)、(B)両
成分を含む重合体の存在下に、(C)メチルメタクリ
レートを少なくとも80重量%含む単量体または単
量体混合物5〜25重量部を(C)成分のηsp/Cが2
以上になるような条件で重合((A)、(B)、(C)成分の
和は100重量部)して得られる三段重合物0.1〜30
重量部とからなる良好な加工性と物理特性とを有
する新規な塩化ビニル系樹脂組成物である。
本発明において()成分の塩化ビニル系重合
体は少なくとも80重量%が塩化ビニル成分であ
り、この99.9〜70重量部に対し、()成分の添
加量は0.1〜30重量部である。0.1部以下では効果
が発現せず、又30部を越えると塩化ビニル樹脂本
来の特徴が損なわれる。
本発明における()成分の特徴は、相溶性が
悪く、流動性の良好なスチレンとアクリル酸エス
テルとの共重合体(B)成分の内側と外側にメチルメ
タクリレート系重合体である(A)、(C)成分を配置す
る、いわゆるサンドイツチ構造をとらせることに
ある。このサンドイツチ構造は少なくとも60重量
%がメチルメタクリレートで、かつηsp/Cが2
以上の重合体または共重合体である(A)成分を含む
ラテツクスの存在下に、スチレン30〜70重量%と
アクリル酸エステル70〜30重量%との混合物であ
る(B)成分の原料5〜55重量部を(B)成分のηsp/C
が1以上になるような条件で重合し、更に(A)及び
(B)成分を含有するラテツクスの存在下に、メチル
メタクリレートを少なくとも80重量%含む単量体
または単量体混合物である(C)成分の原料5〜25重
量部を(C)成分のηsp/Cが2以上になるような条
件で重合する三段重合法を適用することにより得
られる。
(A)〜(C)成分の各重合体のηsp/Cは、各成分を
単独で重合した時の値であり、連鎖移動剤、重合
条件等で任意に調整可能である。各重合体(A)〜(C)
成分のηsp/Cの求め方は以下の通りである。
あらかじめ、各成分単独で規定の乳化剤、触
媒、重合温度で重合し、連鎖移動剤量を変量とし
て、ηsp/Cの検量線を得る。三段重合物を重合
する際に重合条件を検量線を得た条件と同じに
し、添加した連鎖移動剤量に対するηsp/Cを検
量線より読み取り、その値を各成分のηsp/Cと
した。
このサンドイツチ構造を形成するためには、二
段目以降の存在下重合におて、乳化剤の添加を出
来るだけせずに重量を行い、実質的に(B)成分、(C)
成分単独のポリマーの形成を押えねばならない。
流動性が小さく比較的やわらかい高分子量のメチ
ルメタクリレート系成分を核とし、その周囲に流
動性が良好な(B)成分を重合させることによつて得
た組成物を塩化ビニル樹脂に配合した本組成物
は、塩化ビニル樹脂のゲル化速度を早め、成形品
の高温引張り伸度、二次加工性に優れた効果を発
揮するのみでなく流動性の良好な(B)成分と(C)成分
として含まれる、塩化ビニルと相溶性の良好なメ
チルメタクリレート系成分との相剰効果によつて
ブレンド中にブロツクを形成せず、器壁への付着
もなく、軟質配合での分散性が向上し、未ゲル化
物の発生等の難問を解消出来、その上透明性も損
わないという驚くべき効果をも有する。なお(B)成
分をηsp/C1未満となるような条件で重合する
と、これらの効果が損われる。
本発明の組成物は、従来のメチルメタクリレー
トを主成分とする重合体を添加した塩化ビニル樹
脂組成物に見られるような成形時のトルク(混練
抵抗)の増大、ブレンド中のブロツクの形成、成
形物中への未ゲル化物の残存などの欠点を改善し
た組成物である。
本発明の組成物における第()成分100重量
部中の(A)成分は45重量部を超え〜70重量部が適当
で有り、好ましくは45重量部を超え60重量部であ
る。70重量部をこえるとブレンド中にブロツクを
形成し、トルクが増大し、45重量部以下では軟質
分散性が損われて来る。ηsp/Cは2以上である
ことが必要で、2未満ではポリメチルメタクリレ
ートの加工性に及ぼす効果が認められず、また(B)
成分との相剰効果も小さくなつて軟質ポリ塩化ビ
ニルに対する分散性も低下してくる。(A)成分はポ
リメチルメタクリレートもしくは少なくとも60重
量%以上がメチルメタクリレートである共重合体
であるが、メチルメタクリレートの重合体の相手
モノマーには別に制限はなく、最終組成物の使用
目的に応じて適当な単量体を用いることが出来、
例えば芳香族ビニル、不飽和ニトリル、ビニルエ
ステル、メタクリル酸エステルまたはアクリル酸
エステル等のうちの1種または2種以上が40%以
下の範囲で用いられる。使用量が40%をこえると
組成物の塩化ビニル樹脂に対する相溶性が低下す
るので好ましくない。
更に(A)成分中にジビニルベンゼン、アリルメタ
クリレート等の多官能性単量体を用いることも可
能であるが、この場合は使用量1%以下が好まし
い。
第()成分100重量部中の(B)成分は5重量部
〜50重量部未満、好ましくは20〜30重量部であ
る。5重量部以下では軟質分散性が損われ、50重
量部以上ではゲル化が非常に遅くなる。(B)成分の
大きな特徴は、スチレンとアクリル酸エステルを
共重合することであり、スチレンを必須成分とし
て使用することとηsp/Cが1以上になるような
条件で重合することとによつて、軟質分散性の向
上、耐ブロツク性の改良に優れた効果が見られ
る。(B)成分を構成するスチレンは30〜70重量%、
アクリル酸エステルは70〜30重量%であり、アク
リル酸エステルが70%以上では最終生成物のゲル
化が極端に遅くなつてしまうために、表面特性が
悪くなる。アクリル酸エステルとしては、例えば
エチルアクリレート、n−ブチルアクリレート、
イソブチルアクリレート、2エチルヘキシルアク
リレート等が使用出来るが、特にn−ブチルアク
リレートが好ましく、他のアクリル酸エステルと
の共重合も可能である。(B)成分中のスチレンとア
クリル酸エステルはランダム共重合の形をとらせ
ることが必要であり、スチレンとアクリル酸エス
テルを逐次グラフト重合させてはならない。何故
なら生成物の中に例えばブチルアクリレート等の
結合がブロツク的に存在すると最終生成物を塩化
ビニル系樹脂に混合した組成物は全くその透明性
を失うことになる。
第()成分100重量部中の(C)成分は5〜25重
量部、好ましくは15重量部前後である。5重量部
以下では優れた耐ブロツク性、軟質分散性と二次
加工性を充分に発揮出来ない。また25重量部以上
でも軟質分散不良を起し、未ゲル化物の発生が多
い。二次加工性の観点から(C)成分はηsp/Cが少
なくとも2以上になるような条件で重合されてい
ることが必要である。
三段重合物を合成する際は乳化重合で行われ、
それに用いる乳化剤は通常知られているものが使
用出来、又重合開始剤としては、水溶性、油溶性
およびレドツクス系のものが用いられる。重合体
のηsp/Cは連鎖移動剤、重合温度等の一般的方
法にて任意に調節される。三段重合物()を塩
化ビニル系樹脂()と混合する方法は一般に行
われる方法に従い制限はない。得られた塩化ビニ
ル樹脂組成物には、必要に応じ安定剤、滑剤、耐
衝撃強化剤、可塑剤、着色剤、充填剤等を含有さ
せることもできる。
下記実施例中、部は重量部をあらわす。
実施例 1〜3
撹拌機および還流冷却器つき反応容器に蒸留水
280部、ジオクチルスルフオコハク酸ソーダ1.5
部、過硫酸アンモニウム0.2部と表−1の(A)成分
の混合物を仕込み、容器内を窒素にて置換したの
ち、撹拌下で反応容器を65℃に昇温し、2時間加
熱撹拌する。つづいて(B)成分の混合物を1時間に
わたつて添加し、添加終了後2時間継続撹拌し
た。しかる後に(C)成分の混合物を1時間かかつて
添加し、更に2時間継続撹拌し重合を終了した。
The present invention relates to vinyl chloride resin compositions having good processing and physical properties. Polyvinyl chloride is widely used due to its excellent physical and chemical properties, but the processing temperature is close to the thermal decomposition temperature, making the molding area narrow and the gelation rate slow. I have the above problem. Although it is well known that the addition of plasticizers solves some of these drawbacks, it also leads to a decrease in the mechanical properties of other molded parts with problems such as plasticizer volatilization, and cured polyvinyl chloride. It is far from a complete solution to the applications of It improves productivity by slowing down the gelation rate of the resin during the molding process of vinyl chloride resin and reducing the adhesion to the metal surface of the molding machine.
In addition, vinyl chloride resin is used to smooth the surface of molded products, give them a gloss that does not change even after long-term continuous molding, and enable deep drawing of molded products. A number of copolymers that are compatible with these materials have been investigated as processing aids, with great success in some applications.
The main ones currently used on the market are copolymers whose main component is methyl methacrylate. These have a great effect of accelerating the gelation rate and greatly improve the secondary processability, especially by increasing the tensile elongation at high temperatures. (also called "Fish eye"). In particular, when it is blended with soft vinyl chloride resin, it exhibits almost no compatibility and is scattered as countless ungelled substances, which significantly reduces the commercial value.In this sense, it cannot be applied to the soft field. It is extremely difficult. A composition that solves the above problems all at once, that is, maintains the transparency of vinyl chloride resin,
A processing aid that improves elongation at high temperatures and secondary processability such as deep drawing, and also provides excellent dispersibility and processing properties not only for hard vinyl chloride resins but also for soft vinyl chloride resins. has been devised, but from the viewpoint of improving productivity and saving energy, when processing vinyl chloride resin, it is necessary to have good dispersibility for vinyl chloride, quick gelation, and in the blending process before processing. There has been a growing demand for no torque to be applied during kneading in Henschel mixers and the like. Furthermore, due to the difference in compatibility of vinyl chloride and processing aids with plasticizers, there is a phenomenon of fusion of processing aids during blending, and the resulting generation of ungelled materials during film sheet processing, especially when using soft vinyl chloride resin. There is a need to greatly improve dispersibility, and the above compositions have their limitations, and depending on the formulation, processing aids may adhere to the vessel walls during blending, so we cannot fully meet market demands. The situation cannot be said to be satisfactory. The inventors of the present invention have conducted a wide range of studies while taking the above points into consideration, and have found that while having the excellent processing properties shown by the polymethyl methacrylate system, it also has excellent soft dispersibility, and has a high gelation rate. However, with the aim of quickly obtaining a composition that does not adhere to or fuse to the vessel wall during blending, the present invention was arrived at after repeated studies. The present invention provides () a vinyl chloride polymer or copolymer in which at least 80% by weight is a vinyl chloride component;
99.9 to 70 parts by weight and () (A) at least 60% by weight
is methyl methacrylate, and the reduced viscosity (ηsp/C) measured at 25°C of a solution of 0.1 g of the polymer in 100 ml of chloroform is 2 or more, exceeding 45 parts by weight. (B) Mixture 5 consisting of 30 to 70% by weight of styrene and 70 to 30% by weight of acrylic ester in the presence of 70 parts by weight.
Parts by weight to less than 50 parts by weight are polymerized under conditions such that ηsp/C of component (B) is 1 or more, and in the presence of the obtained polymer containing both components (A) and (B), ( C) Add 5 to 25 parts by weight of a monomer or monomer mixture containing at least 80% by weight of methyl methacrylate so that the ηsp/C of component (C) is 2.
A three-stage polymer obtained by polymerizing under the above conditions (the sum of components (A), (B), and (C) is 100 parts by weight) 0.1 to 30
This is a novel vinyl chloride-based resin composition having good processability and physical properties. In the present invention, at least 80% by weight of the vinyl chloride polymer as component () is a vinyl chloride component, and the amount of component () added is 0.1 to 30 parts by weight relative to 99.9 to 70 parts by weight. If it is less than 0.1 part, no effect will be exhibited, and if it exceeds 30 parts, the original characteristics of vinyl chloride resin will be impaired. The characteristics of component () in the present invention are a copolymer of styrene and acrylic acid ester with poor compatibility and good fluidity, and (B) a methyl methacrylate polymer on the inside and outside of the component (A). (C) Components are arranged in a so-called Sandermanch structure. This Sanderch structure has at least 60% by weight methyl methacrylate and ηsp/C of 2.
In the presence of latex containing component (A), which is the above polymer or copolymer, raw materials for component (B), which is a mixture of 30 to 70% by weight of styrene and 70 to 30% by weight of acrylic ester, are 55 parts by weight of component (B) ηsp/C
Polymerizes under conditions such that 1 or more, and further (A) and
In the presence of a latex containing component (B), 5 to 25 parts by weight of the raw material for component (C), which is a monomer or monomer mixture containing at least 80% by weight of methyl methacrylate, is added to the It is obtained by applying a three-stage polymerization method in which polymerization is performed under conditions such that C becomes 2 or more. The ηsp/C of each polymer of components (A) to (C) is the value when each component is polymerized alone, and can be arbitrarily adjusted by changing the chain transfer agent, polymerization conditions, etc. Each polymer (A) to (C)
The method for determining the component ηsp/C is as follows. In advance, each component is polymerized alone using a specified emulsifier, catalyst, and polymerization temperature, and a calibration curve of ηsp/C is obtained using the amount of chain transfer agent as a variable. When polymerizing the three-stage polymer, the polymerization conditions were the same as those for obtaining the calibration curve, and the ηsp/C with respect to the amount of chain transfer agent added was read from the calibration curve, and the value was taken as the ηsp/C of each component. In order to form this sandwich structure, it is necessary to carry out the polymerization in the presence of the second and subsequent stages without adding an emulsifier as much as possible, so that component (B), component (C)
Formation of polymers of individual components must be suppressed.
This composition has a relatively soft high molecular weight methyl methacrylate component with low fluidity as a core, and a composition obtained by polymerizing component (B) with good fluidity around the core, which is blended with vinyl chloride resin. As components (B) and (C), they not only accelerate the gelation rate of vinyl chloride resin and have excellent effects on the high-temperature tensile elongation and secondary processability of molded products, but also have good fluidity. Due to the mutual effect of the vinyl chloride and methyl methacrylate components that are included, it does not form blocks during blending, does not adhere to the vessel wall, and improves dispersibility in soft blends. It has the surprising effect of being able to solve difficult problems such as the generation of ungelled substances, and also not impairing transparency. Note that if component (B) is polymerized under conditions such that ηsp/C1 is less than this, these effects will be impaired. The composition of the present invention has the advantage of increasing the torque (kneading resistance) during molding, forming blocks during blending, and preventing molding, which is seen in conventional vinyl chloride resin compositions containing a polymer containing methyl methacrylate as a main component. This is a composition that has improved the drawbacks such as residual ungelled substances in the product. The amount of component (A) in 100 parts by weight of component () in the composition of the present invention is suitably more than 45 parts by weight to 70 parts by weight, preferably more than 45 parts by weight to 60 parts by weight. If it exceeds 70 parts by weight, blocks will be formed during blending and torque will increase, and if it is less than 45 parts by weight, soft dispersibility will be impaired. ηsp/C needs to be 2 or more; if it is less than 2, no effect on the processability of polymethyl methacrylate is observed, and (B)
The mutual effect with the other components also decreases, and the dispersibility in soft polyvinyl chloride also decreases. Component (A) is polymethyl methacrylate or a copolymer in which at least 60% by weight is methyl methacrylate, but there are no particular restrictions on the partner monomer of the methyl methacrylate polymer, and it may vary depending on the intended use of the final composition. Appropriate monomers can be used,
For example, one or more of aromatic vinyl, unsaturated nitriles, vinyl esters, methacrylic esters, acrylic esters, etc. are used in an amount of 40% or less. If the amount used exceeds 40%, the compatibility of the composition with the vinyl chloride resin decreases, which is not preferable. Furthermore, it is also possible to use polyfunctional monomers such as divinylbenzene and allyl methacrylate in component (A), but in this case, the amount used is preferably 1% or less. The amount of component (B) in 100 parts by weight of component () is 5 parts by weight to less than 50 parts by weight, preferably 20 to 30 parts by weight. If the amount is less than 5 parts by weight, soft dispersibility will be impaired, and if it is more than 50 parts by weight, gelation will be extremely slow. The major feature of component (B) is that it copolymerizes styrene and acrylic ester, and by using styrene as an essential component and polymerizing under conditions such that ηsp/C is 1 or more. Excellent effects are seen in improving soft dispersibility and blocking resistance. The styrene that constitutes component (B) is 30 to 70% by weight,
The acrylic ester content is 70 to 30% by weight, and if the acrylic ester content is 70% or more, the gelation of the final product will be extremely slow, resulting in poor surface properties. Examples of acrylic esters include ethyl acrylate, n-butyl acrylate,
Isobutyl acrylate, 2-ethylhexyl acrylate, etc. can be used, but n-butyl acrylate is particularly preferred, and copolymerization with other acrylic esters is also possible. Styrene and acrylic ester in component (B) must be copolymerized randomly, and styrene and acrylic ester must not be graft-polymerized sequentially. This is because, if a block of bonds such as butyl acrylate is present in the product, the composition obtained by mixing the final product with the vinyl chloride resin will completely lose its transparency. The amount of component (C) in 100 parts by weight of component () is 5 to 25 parts by weight, preferably around 15 parts by weight. If the amount is less than 5 parts by weight, excellent block resistance, soft dispersibility and secondary processability cannot be fully exhibited. Moreover, if it exceeds 25 parts by weight, poor soft dispersion occurs, and ungelled substances are often generated. From the viewpoint of secondary processability, component (C) must be polymerized under conditions such that ηsp/C is at least 2 or more. When synthesizing three-stage polymers, emulsion polymerization is used.
As the emulsifier used therein, commonly known emulsifiers can be used, and as the polymerization initiator, water-soluble, oil-soluble and redox-based ones can be used. The ηsp/C of the polymer can be arbitrarily adjusted by using a chain transfer agent, polymerization temperature, etc. in a conventional manner. The method of mixing the three-stage polymer () with the vinyl chloride resin () is not limited and may be any commonly used method. The obtained vinyl chloride resin composition can also contain stabilizers, lubricants, impact-strengthening agents, plasticizers, colorants, fillers, etc., if necessary. In the following examples, parts represent parts by weight. Examples 1-3 Distilled water in a reaction vessel with stirrer and reflux condenser
280 parts, dioctyl sulfosuccinate sodium 1.5
1 part, ammonium persulfate (0.2 parts) and a mixture of component (A) in Table 1. After purging the inside of the container with nitrogen, the temperature of the reaction container was raised to 65° C. with stirring, and the mixture was heated and stirred for 2 hours. Subsequently, the mixture of component (B) was added over 1 hour, and after the addition was completed, stirring was continued for 2 hours. Thereafter, the mixture of component (C) was added for one hour or so, and stirring was continued for an additional two hours to complete the polymerization.
【表】
得られたエマルジヨンは冷却後、塩化アルミニ
ウムを用いて塩析し、過、洗浄、乾燥して各試
料を得た。
上記各試料の3部をポリ塩化ビニル(平均重合
度715)100部、ジブチル錫マレート2.0部、エポ
キシ系安定化助剤1.5部、滑剤0.5部と共にヘンシ
エルミキサーにて混合し、内温120℃にてブレン
ドを終了し、ゲル化特性、光沢、高温引張り試験
に供した。又この配合物に更にジオクチルフタレ
ート(DOP)40部を加え、軟質分散性、器壁へ
の付着の試験に供した。
上記の塩化ビニル系樹脂組成物の加工性の測定
結果を表−2にまとめて示した。[Table] After cooling, the obtained emulsion was salted out using aluminum chloride, filtered, washed, and dried to obtain each sample. Three parts of each of the above samples were mixed in a Henschel mixer with 100 parts of polyvinyl chloride (average degree of polymerization 715), 2.0 parts of dibutyltin malate, 1.5 parts of an epoxy stabilizing agent, and 0.5 parts of a lubricant, and the internal temperature was 120°C. Blending was completed at , and subjected to gelation properties, gloss, and high temperature tensile tests. Furthermore, 40 parts of dioctyl phthalate (DOP) was added to this mixture, and the mixture was tested for soft dispersibility and adhesion to the vessel wall. The processability measurement results of the above vinyl chloride resin composition are summarized in Table 2.
【表】【table】
【表】
実施例 4〜5
撹拌機および還流冷却機つき反応容器に蒸留水
280部、ジオクチルスルフオコハク酸ソーダ1.5
部、過硫酸アンモニウム0.2部と表−3の(A)成分
の混合物を仕込み、容器内を窒素にて置換したの
ち、撹拌下で反応容器を65℃に昇温し、2時間加
熱撹拌する。つづいて(B)成分の混合物を1時間に
わたつて添加し、添加終了後2時間継続撹拌し
た。しかる後に(C)成分の混合物を1時間かかつて
添加し、更に2時間継続撹拌し重合を終了した。[Table] Examples 4-5 Distilled water in a reaction vessel equipped with a stirrer and reflux condenser
280 parts, dioctyl sulfosuccinate sodium 1.5
1 part, ammonium persulfate 0.2 part and a mixture of component (A) in Table 3 were charged, and after purging the inside of the container with nitrogen, the temperature of the reaction container was raised to 65° C. with stirring, and the mixture was heated and stirred for 2 hours. Subsequently, the mixture of component (B) was added over 1 hour, and after the addition was completed, stirring was continued for 2 hours. Thereafter, a mixture of component (C) was added for one hour or so, and stirring was continued for another two hours to complete the polymerization.
【表】
上記の組成で得られたエマルジヨンは冷却後塩
化アルミニウムを用いて塩析し、過、洗浄、乾
燥して各試料を得た。
上記各試料の3部をポリ塩化ビニル(平均重合
度715)100部、ジブチル錫マレート2.0部、エポ
キシ系安定化助剤1.5部、滑剤0.5部と共にヘンシ
エルミキサーにて混合し、内温120℃にてブレン
ドを終了し、ゲル化特性、光沢、高温引張り試験
に供した。又この配合物にDOP40部を加え、軟
質分散性、器壁への付着性の試験に供した。
上記の塩化ビニル系樹脂組成物の加工性の測定
結果を表−4にまとめて示した。[Table] After cooling, the emulsion obtained with the above composition was salted out using aluminum chloride, filtered, washed and dried to obtain each sample. Three parts of each of the above samples were mixed in a Henschel mixer with 100 parts of polyvinyl chloride (average degree of polymerization 715), 2.0 parts of dibutyltin malate, 1.5 parts of an epoxy stabilizing agent, and 0.5 parts of a lubricant, and the internal temperature was 120°C. Blending was completed at , and subjected to gelation properties, gloss, and high temperature tensile tests. Additionally, 40 parts of DOP was added to this mixture and subjected to tests for soft dispersibility and adhesion to vessel walls. The processability measurement results of the above vinyl chloride resin composition are summarized in Table 4.
【表】
表−2および表−4より(A)成分、(B)成分、(C)成
分の組成割合、ηsp/Cなどが本発明の範囲外で
ある場合には優れた加工性を有する組成物が得ら
れないことが明らかである。[Table] From Tables 2 and 4, when the composition ratio of component (A), component (B), and component (C), ηsp/C, etc. are outside the scope of the present invention, it has excellent processability. It is clear that no composition is obtained.
Claims (1)
である塩化ビニル系重合体または共重合体99.9
〜70重量部と ()(A) 少なくとも60重量%がメチルメタクリレ
ートであり、100mlのクロロホルム中に0.1g
の重合体を溶解した溶液について25℃で測定
した還元粘度(ηsp/C)が2以上である重
合体又は共重合体45重量部を超え〜70重量部
の存在下に、 (B) スチレン30〜70重量%とアクリル酸エステ
ル70〜30重量%とから成る混合物5重量部〜
50重量部未満を(B)成分のηsp/Cが1以上に
あるような条件で重合し、得られた(A)、(B)両
成分を含む重合体の存在下に、 (C) メチルメタクリレートを少なくとも80重量
%を含む単量体または単量体混合物5〜25重
量部を(C)成分のηsp/Cが2以上になるよう
な条件で重合((A)、(B)、(C)成分の和は100重
量部)して得られる三段重合物0.1〜30重量
部 とから成る良好な加工性と物理特性とを有する塩
化ビニル系樹脂組成物。[Scope of Claims] 1 () A vinyl chloride polymer or copolymer 99.9 in which at least 80% by weight is a vinyl chloride component
~70 parts by weight and ()(A) at least 60% by weight methyl methacrylate, 0.1 g in 100 ml chloroform
(B) Styrene 30 in the presence of more than 45 parts by weight to 70 parts by weight of a polymer or copolymer having a reduced viscosity (ηsp/C) of 2 or more measured at 25°C for a solution containing a polymer of (B) 5 parts by weight of a mixture consisting of ~70% by weight and 70-30% by weight of an acrylic ester ~
(C) Methyl in the presence of a polymer containing both components (A) and (B) obtained by polymerizing less than 50 parts by weight of component (B) under conditions such that ηsp/C is 1 or more. Polymerization ((A), (B), ( A vinyl chloride resin composition having good processability and physical properties, comprising 0.1 to 30 parts by weight of a three-stage polymer obtained by C) (total of component C) is 100 parts by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9829980A JPS5723645A (en) | 1980-07-18 | 1980-07-18 | Vinyl chloride resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9829980A JPS5723645A (en) | 1980-07-18 | 1980-07-18 | Vinyl chloride resin composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5723645A JPS5723645A (en) | 1982-02-06 |
JPS6354017B2 true JPS6354017B2 (en) | 1988-10-26 |
Family
ID=14216033
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9829980A Granted JPS5723645A (en) | 1980-07-18 | 1980-07-18 | Vinyl chloride resin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5723645A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0573669U (en) * | 1992-03-09 | 1993-10-08 | サンデン株式会社 | Position information display device |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0611831B2 (en) * | 1984-12-03 | 1994-02-16 | 三菱レイヨン株式会社 | Vinyl chloride resin composition |
JPH064744B2 (en) * | 1984-12-03 | 1994-01-19 | 三菱レイヨン株式会社 | Vinyl chloride resin composition |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS509653A (en) * | 1973-05-28 | 1975-01-31 |
-
1980
- 1980-07-18 JP JP9829980A patent/JPS5723645A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS509653A (en) * | 1973-05-28 | 1975-01-31 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0573669U (en) * | 1992-03-09 | 1993-10-08 | サンデン株式会社 | Position information display device |
Also Published As
Publication number | Publication date |
---|---|
JPS5723645A (en) | 1982-02-06 |
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