JPH0581620B2 - - Google Patents
Info
- Publication number
- JPH0581620B2 JPH0581620B2 JP59020146A JP2014684A JPH0581620B2 JP H0581620 B2 JPH0581620 B2 JP H0581620B2 JP 59020146 A JP59020146 A JP 59020146A JP 2014684 A JP2014684 A JP 2014684A JP H0581620 B2 JPH0581620 B2 JP H0581620B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- vinyl chloride
- pvc
- polymer
- parts
- 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 - Fee Related
Links
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 14
- 229920000642 polymer Polymers 0.000 claims description 14
- 229920000578 graft copolymer Polymers 0.000 claims description 11
- 238000006116 polymerization reaction Methods 0.000 claims description 10
- 239000004698 Polyethylene Substances 0.000 claims description 5
- -1 polyethylene Polymers 0.000 claims description 5
- 229920000573 polyethylene Polymers 0.000 claims description 5
- 125000005397 methacrylic acid ester group Chemical group 0.000 claims description 3
- 239000011342 resin composition Substances 0.000 claims description 3
- PZWQOGNTADJZGH-SNAWJCMRSA-N (2e)-2-methylpenta-2,4-dienoic acid Chemical compound OC(=O)C(/C)=C/C=C PZWQOGNTADJZGH-SNAWJCMRSA-N 0.000 claims 1
- 229920003067 (meth)acrylic acid ester copolymer Polymers 0.000 claims 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical group CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims 1
- 238000000034 method Methods 0.000 description 20
- 238000012545 processing Methods 0.000 description 12
- 229920001577 copolymer Polymers 0.000 description 11
- 229920001971 elastomer Polymers 0.000 description 8
- 239000000806 elastomer Substances 0.000 description 8
- 239000000178 monomer Substances 0.000 description 6
- 229920000098 polyolefin Polymers 0.000 description 6
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 4
- 239000005977 Ethylene Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 230000000379 polymerizing effect Effects 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000004566 building material Substances 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 230000003014 reinforcing effect Effects 0.000 description 3
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 2
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 2
- QYKIQEUNHZKYBP-UHFFFAOYSA-N Vinyl ether Chemical compound C=COC=C QYKIQEUNHZKYBP-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- GMSCBRSQMRDRCD-UHFFFAOYSA-N dodecyl 2-methylprop-2-enoate Chemical compound CCCCCCCCCCCCOC(=O)C(C)=C GMSCBRSQMRDRCD-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000009477 glass transition Effects 0.000 description 2
- 229920001519 homopolymer Polymers 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000003607 modifier Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 229920001567 vinyl ester resin Polymers 0.000 description 2
- 230000000007 visual effect Effects 0.000 description 2
- JHPBZFOKBAGZBL-UHFFFAOYSA-N (3-hydroxy-2,2,4-trimethylpentyl) 2-methylprop-2-enoate Chemical compound CC(C)C(O)C(C)(C)COC(=O)C(C)=C JHPBZFOKBAGZBL-UHFFFAOYSA-N 0.000 description 1
- 229920002818 (Hydroxyethyl)methacrylate Polymers 0.000 description 1
- WDQMWEYDKDCEHT-UHFFFAOYSA-N 2-ethylhexyl 2-methylprop-2-enoate Chemical compound CCCCC(CC)COC(=O)C(C)=C WDQMWEYDKDCEHT-UHFFFAOYSA-N 0.000 description 1
- GNSFRPWPOGYVLO-UHFFFAOYSA-N 3-hydroxypropyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCCO GNSFRPWPOGYVLO-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001252 acrylic acid derivatives Chemical class 0.000 description 1
- XECAHXYUAAWDEL-UHFFFAOYSA-N acrylonitrile butadiene styrene Chemical compound C=CC=C.C=CC#N.C=CC1=CC=CC=C1 XECAHXYUAAWDEL-UHFFFAOYSA-N 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 description 1
- 150000008360 acrylonitriles Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229920005549 butyl rubber Polymers 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- GTBGXKPAKVYEKJ-UHFFFAOYSA-N decyl 2-methylprop-2-enoate Chemical compound CCCCCCCCCCOC(=O)C(C)=C GTBGXKPAKVYEKJ-UHFFFAOYSA-N 0.000 description 1
- 229920005558 epichlorohydrin rubber Polymers 0.000 description 1
- SUPCQIBBMFXVTL-UHFFFAOYSA-N ethyl 2-methylprop-2-enoate Chemical compound CCOC(=O)C(C)=C SUPCQIBBMFXVTL-UHFFFAOYSA-N 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 229920006226 ethylene-acrylic acid Polymers 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000007970 homogeneous dispersion Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 125000005395 methacrylic acid group Chemical group 0.000 description 1
- 150000005673 monoalkenes Chemical class 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- NZIDBRBFGPQCRY-UHFFFAOYSA-N octyl 2-methylprop-2-enoate Chemical compound CCCCCCCCOC(=O)C(C)=C NZIDBRBFGPQCRY-UHFFFAOYSA-N 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000012744 reinforcing agent Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 239000006097 ultraviolet radiation absorber Substances 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
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Description
本発明は、耐候性、低温耐衝撃性、耐熱変形性
および熱安定性が優れ、かつ広い加工条件が採用
可能である塩化ビニル系樹脂組成物に関するもの
である。
塩化ビニル系重合体(以下PVCということが
ある)は、優れた物理的性質、難燃性、耐薬品
性、耐候性に加えて、その経済性ゆえに建材や車
輌等に大量に使用されている。これらの用途の中
には、屋外で長期にわたつて使用されるものも多
く、高度の耐衝撃性と耐候性を兼ね備える事が要
求される製品が少なくない。
これまで、PVCの耐衝撃強度及び耐候性を改
良する方法としては次の(1)〜(4)の方法が知られて
いる。すなわち(1)エチレン−ビニルエステル共重
合体(EVA)、エチレン−アクリル酸エステル共
重合体(EEA)、塩素化ポリオレフイン(CPE)
等のエラストマーを1種以上PVCと混合する方
法(2)EVA、EEA、CPE、エチレン−プロピレン
共重合体(EPR)、エチレン−プロピレン−非共
役ジエン共重合体(EPT)、ブチルゴムもしくは
その塩素化物(IIR)、エピクロルヒドリンゴム
(CHR)、(メタ)アクリル酸エステルを主体とす
る共重合体(AR)又はポリオレフイン(PE)等
のようなガラス転移点が−20℃以下の重合体の存
在下に塩化ビニルを重合して得た重合物を使用す
る方法、(3)EVA、EEA、EPR、EPT、IIR、
CHR、CPE、AR、PE等の存在下に塩化ビニル
を重合して得た重合物をPVCに混合する方法、
(4)EVA、EEA、EPT、EPR、IIR、CPE、AR、
PE等の存在下に(メタ)アクリル酸エステル、
芳香族ビニル化合物、シアン化ビニル化合物の中
から選ばれる1種以上の重合性単量体を重合して
得た重合物とPVCを混合する方法が知られてい
る。
ところが、これらの従来の方法は実際の加工上
や使用上において多くの問題点を有しており、必
らずしも使用者にとつて満足な水準にないのが現
状である。
すなわち、(1)の方法ではPVCの耐衝撃性を向
上させるためにエラストマーとしてPVCと半相
溶となる様なものが使用されるので、通常の混練
条件下では分散が不充分で補強効果が現われない
ことが多い。一方、エラストマーとしてPVCと
相溶性の高いタイプのものを用いることは可能で
あるが、この場合には耐衝撃強度の発現が小さく
なるばかりでなく、製品の硬度が低下してしま
う。またこの方法によると、混合物の軟化温度の
低下が大きいため製品の使用温度を低く制限せざ
るを得なくなる。また、EVAを使う例では衝撃
強度の改良効果が小さく、CPEを使う例では耐
候安定性に乏しい。なお両者の併用で耐候安定性
と衝撃強度は改良できるが、軟化温度の低下は避
けられない。
(2)の方法で得られたものは、エラストマーの一
部がPVCと化学的に結合しており、重合体が
PVCとエラストマーの均一分散体となつている
ため、高い衝撃値を有する製品が容易に得られる
有利さがあり、また重合体中のエラストマー比率
も小さくできるうえ、軟化温度の低下も小さく、
耐候性に優れている。しかしながら、この重合体
は加工時間が少し長くなつたり、加温温度が少し
上つただけで急激に衝撃強度が低下してしまうと
いう加工幅の狭さが問題となつている。またこの
重合体を、通常のPVCと同様の各種配合剤と混
合しやすい粉体として得るには、重合に際してエ
ラストマーを塩化ビニルに溶解するか、あるいは
微粉化する必要があり、重合操作が煩雑になる。
(3)の方法によれば、(2)の方法による以上に経済
的にPVCとエラストマーとの優れた分散性を達
成することが可能である。しかし、この方法もま
た加工幅の狭さが最大の問題点として残つてい
る。
(4)の方法によれば、得られた混合物は加工幅が
広いので、高い衝撃強度の製品を安定して製造す
ることができ、また、軟化温度の低下も少ない
が、衝撃強度の耐候安定性は必ずしも充分でな
い。また切り欠き形状の種類により衝撃強度が大
幅に変化することもこの方法の問題点である。
本発明者は以上の如き、従来の耐候性、耐衝撃
性樹脂製品を得るための方法について鋭意検討
し、本質的に優れた耐候性を有する(3)の方法にお
ける加工幅の狭さを改良する方法について研究を
行つた結果、特定のグラフト重合体を用いると広
い加工条件下に安定して成形することが可能であ
つて、しかもそれにより低温耐衝撃性、耐候性が
良好で、軟化温度の高い製品を与えることのでき
るPVC組成物が得られることを見い出し、本発
明を完成するに至つた。
すなわち本発明は、メタクリル酸エステルの含
有量が5〜75重量%であるエチレン−メタクリル
酸エステル共重合体(以下EMAということがあ
る)(A)及びポリエチレン(B)の存在下に塩化ビニル
又は塩化ビニルを主体とする単量体混合物を重合
して得られるものであつて、(A)及び(B)がそれぞれ
15重量%より多く、かつ(A)及び(B)の合計量が85重
量%以下であるグラフト重合体5〜60重量部と
PVC100重量部とからなることを特徴とする硬質
樹脂組成物を提供するものである。
本発明におけるグラフト重合体に使用される
EMA中のメタクリル酸エステルの含有量は5〜
75重量%のものである。メタクリル酸エステルの
含有量が5重量%未満のものはグラフト重合体と
PVCとの相溶性が乏しく、75重量%を越えると
ガラス転移温度が高すぎて、耐衝撃強度の発現が
不充分である。EMA中のメタクリル酸エステル
の例としては、メチルメタクリレート、エチルメ
タクリレート、ブチルメタクリレート、ヒドロキ
シエチルメタクリレート、ヒドロキシプロピルメ
タクリレート、2−エチルヘキシルメタクリレー
ト、オクチルメタクリレート、デシルメタクリレ
ート、ドデシルメタクリレート、ラウリルメタク
リレート等が挙げられるが、耐熱変形性及び入手
容易性の点でメチルメタクリレートが好ましい。
これらのメタクリル酸エステルと共に第3成分と
して一酸化炭素、ビニルエーテル、エチレン以外
のオレフイン等を共重合させたものを用いてもよ
い。なお、この共重合体のメルトインデツクス
(ASTM D−1238)は0.1〜300g/10min、好ま
しくは1〜150g/10minである。
またポリエチレン(B)としては、高圧、中圧また
は低圧法で製造されたエチレンの単独重合体、エ
チレンと他の単量体10重量%以下との共重合体、
あるいはこれらのポリエチレンの15重量%未満の
塩素化物や金属イオン配向物を挙げることがで
き、メルトインデツクス値として0.01〜50g/
10min程度のものが使用可能である。
かかるポリエチレン(B)は、エチレン単量体を重
合缶に仕込むことによりグラフト重合体を製造す
る過程で生成させてもよい。
(A)及び(B)の存在下で重合される塩化ビニルとと
もに、通常の共重合性単量体を所望に応じて塩化
ビニルとの混合物中30重量%までの範囲で用いる
ことができる。その例としては、モノオレフイ
ン、ビニルエーテル、(メタ)アクリレート、ビ
ニルエステル、不飽和酸、不飽和ニトリル、芳香
族ビニル等が挙げられる。
本発明のグラフト重合体はその中のエチレン−
メタクリル酸エステル共重合体(A)及びポリエチレ
ン(B)の含有量がそれぞれ少なくとも15%より多く
なる様に、かつ、(A)と(B)との合計量が85重量%以
下となるように製造される。(A)の量が15重量%以
下であると、耐衝撃助剤としても補強効果が小さ
く、(B)の量が15重量%以下であると、高衝撃値を
与える加工条件の幅が狭くなる。また、(A)と(B)と
の合計量が85重量%を越えると、塩化ビニルと化
学的に結合していない(A)および(B)の比率が増え、
補強効果が少なくなるばかりか、組成物の軟化点
の低下が著しくなつて本発明の目的を達成するこ
とができない。
なお、グラフト重合体の製造は通常の手法によ
りなされる。重合系に供される(A)及び(B)の形状は
特に限定されず、ペレツト、シート、ベール、粉
末、水性分散液等のいずれでもよい。ただし、(A)
は、特定組成のもの以外は塩化ビニルへの溶解が
困難であつたり、溶解液の粘度が高く、操業が困
難になつたりすることが多いので、グラフト重合
体をPVCと混合しやすい粉末状で得るためには、
(A)および(B)は粉末又は水性分散液として重合系に
供するのが好ましい。
この、グラフト重合体は、PVC100重量部に対
し5〜60重量部、好ましくは10〜50重量部の範囲
で用いられる。5重量部未満では、衝撃強度の改
良効果が小さくて実用的ではなく、60重量部を越
えると組成物の軟化温度の低下が大きくなる。
本発明において用いられるPVCとしては通常
の建材や硬質製品に用いられるものであれば特に
制限はないが、通常は塩化ビニルの単独重合体も
しくは塩化ビニル80重量%以上と、これと共重合
可能な単量体20重量%以下との共重合体又はこれ
らの塩素化物であつて、JIS K 6721の方法で測
定される平均重合度が400〜1500程度のものが用
いられる。平均重合度が400未満では加工性は優
れるが、耐衝撃性が低くなり、1500より大きい
と、加工性が悪い。
本発明の組成物は、必要に応じて、可塑剤、安
定剤、紫外線吸収剤、酸化防止剤、滑剤、顔料、
充填剤、補強剤等の通常のPVC用配合剤及び
EVA、EEA、CPE、EPR、EPT、IIR、CHR、
AR、ポリオレフイン、これらの重合体への塩化
ビニルのグラフト重合体、アクリロニトリル−ブ
タジエン−スチレン共重合体、メタクリル酸−ブ
タジエン−スチレン共重合体などの通常のPVC
用高分子改質剤を含有することができる。この高
分子改質剤はPVC100重量部当たり通常は30重量
部までの範囲で用いることができる。この組成物
の成形は通常の方法で行うことができるが、この
際加工条件を広く選択することが可能である。ま
た、得られた成形品は優れた耐候性、耐衝撃性及
び耐熱変形性を発揮するので建材、車輌、農水産
資材等の一般の硬質製品として有用性が高い。
次に本発明を実施例により説明する。なお、
%、部数は重量基準である。
実施例
第1表に示す重合用原料(単位g)にステンレ
ス製オートクレーブに仕込み、50℃にて、12時間
重合させた後、重合体を回収し、乾燥した。次い
で生成重合体を適当に粉砕するかあるいはそのま
ま18メツシユのふるいにかけてふるい下のグラフ
ト重合体を得た。
次に第2表に示す配合成分を表示の重合割合で
ミルロールを用いて170℃で3分間(混合条件
a),180℃で10分間(混合条件b)又は170℃で
6分間(混合条件c)混合して1mm厚のシート状
とし、これを3層重ねて180℃で5分間プレスす
ることによつて3mm厚の試料シートを作成した。
この試料の衝撃強さ(JISK−7111)、軟化温度
(JISK−6745の柔軟温度試験法に準ずる)、耐候
性(衝撃強さの高いもの及び軟化温度の高いもの
についてウエザロメーター(ブラツクパネル温度
63℃、1000時間)により衝撃強さ(JISK−
7111)、色調変化(目視)、チヨーキングの有無
(目視)〕を測定した。結果を第2表に示す。
第2表より、本発明の組成物は、加工条件を変
えても耐衝撃製、耐候性及び耐熱変形性等の優れ
た成形品を与えることがわかる。それに対して、
例えば実験番号5,8比較組成物は、加工条件に
よつて物性のバランスがくずれることがあるの
で、加工条件を広く採用することがむづかしい。
The present invention relates to a vinyl chloride resin composition that has excellent weather resistance, low-temperature impact resistance, heat deformation resistance, and thermal stability, and can be used under a wide range of processing conditions. Vinyl chloride polymers (hereinafter sometimes referred to as PVC) are used in large quantities in building materials, vehicles, etc. due to their excellent physical properties, flame retardance, chemical resistance, and weather resistance, as well as their economic efficiency. . Many of these products are used outdoors for long periods of time, and many products require a high degree of impact resistance and weather resistance. Up to now, the following methods (1) to (4) have been known as methods for improving the impact strength and weather resistance of PVC. Namely (1) ethylene-vinyl ester copolymer (EVA), ethylene-acrylic acid ester copolymer (EEA), chlorinated polyolefin (CPE)
Method of mixing one or more elastomers such as PVC with PVC (2) EVA, EEA, CPE, ethylene-propylene copolymer (EPR), ethylene-propylene-nonconjugated diene copolymer (EPT), butyl rubber or its chlorinated product (IIR), epichlorohydrin rubber (CHR), (meth)acrylic acid ester-based copolymer (AR), or polyolefin (PE) in the presence of a polymer with a glass transition point of -20°C or lower. A method using a polymer obtained by polymerizing vinyl chloride, (3) EVA, EEA, EPR, EPT, IIR,
A method of mixing a polymer obtained by polymerizing vinyl chloride in the presence of CHR, CPE, AR, PE, etc. with PVC,
(4) EVA, EEA, EPT, EPR, IIR, CPE, AR,
(meth)acrylic acid ester in the presence of PE etc.
A method is known in which PVC is mixed with a polymer obtained by polymerizing one or more polymerizable monomers selected from aromatic vinyl compounds and vinyl cyanide compounds. However, these conventional methods have many problems in actual processing and use, and the current situation is that they are not necessarily at a level that satisfies users. In other words, in method (1), in order to improve the impact resistance of PVC, an elastomer that is semi-compatible with PVC is used, so under normal kneading conditions, dispersion is insufficient and the reinforcing effect is poor. Often does not appear. On the other hand, it is possible to use a type of elastomer that is highly compatible with PVC, but in this case, not only will the impact resistance strength be reduced, but the hardness of the product will also be reduced. Furthermore, according to this method, the softening temperature of the mixture is significantly lowered, so that it is necessary to limit the use temperature of the product to a low level. In addition, examples using EVA have a small impact strength improvement effect, and examples using CPE have poor weather resistance stability. Although weather resistance stability and impact strength can be improved by using both in combination, a decrease in the softening temperature is unavoidable. In the product obtained by method (2), part of the elastomer is chemically bonded to PVC, and the polymer is
Because it is a homogeneous dispersion of PVC and elastomer, it has the advantage that products with high impact values can be easily obtained, and the ratio of elastomer in the polymer can also be reduced, and the softening temperature decreases little.
Excellent weather resistance. However, this polymer has the problem of a narrow processing range in which the impact strength suddenly decreases even if the processing time becomes slightly longer or the heating temperature rises slightly. In addition, in order to obtain this polymer as a powder that is easy to mix with various compounding agents similar to ordinary PVC, it is necessary to dissolve the elastomer in vinyl chloride or to make it into a fine powder during polymerization, which makes the polymerization operation complicated. Become. According to method (3), it is possible to achieve excellent dispersibility of PVC and elastomer more economically than method (2). However, the biggest problem with this method remains that the processing width is narrow. According to method (4), the resulting mixture can be processed over a wide range of processes, so products with high impact strength can be stably manufactured, and the softening temperature decreases little, but the impact strength is stable against weathering. Gender is not always enough. Another problem with this method is that the impact strength varies greatly depending on the type of notch shape. The present inventor has conducted extensive studies on the conventional methods for obtaining weather-resistant and impact-resistant resin products as described above, and has improved the narrow processing width of method (3), which inherently has excellent weather resistance. As a result of research on methods for molding, we found that using a specific graft polymer allows stable molding under a wide range of processing conditions, and also provides good low-temperature impact resistance, weather resistance, and a low softening temperature. The present inventors have discovered that a PVC composition can be obtained that can provide products with high levels of carbon dioxide, and have completed the present invention. That is, the present invention provides vinyl chloride or It is obtained by polymerizing a monomer mixture mainly composed of vinyl chloride, and (A) and (B) are each
5 to 60 parts by weight of a graft polymer of more than 15% by weight and the total amount of (A) and (B) not more than 85% by weight;
The present invention provides a hard resin composition comprising 100 parts by weight of PVC. Used in the graft polymer in the present invention
The content of methacrylic ester in EMA is 5~
75% by weight. If the content of methacrylic acid ester is less than 5% by weight, it is considered a graft polymer.
It has poor compatibility with PVC, and if it exceeds 75% by weight, the glass transition temperature is too high and the impact strength is insufficient. Examples of methacrylic acid esters in EMA include methyl methacrylate, ethyl methacrylate, butyl methacrylate, hydroxyethyl methacrylate, hydroxypropyl methacrylate, 2-ethylhexyl methacrylate, octyl methacrylate, decyl methacrylate, dodecyl methacrylate, lauryl methacrylate, etc. Methyl methacrylate is preferred in terms of heat deformation resistance and easy availability.
A copolymer of carbon monoxide, vinyl ether, olefin other than ethylene, etc. may be used as a third component together with these methacrylic esters. The melt index (ASTM D-1238) of this copolymer is 0.1 to 300 g/10 min, preferably 1 to 150 g/10 min. In addition, polyethylene (B) includes ethylene homopolymers produced by high-pressure, medium-pressure, or low-pressure methods, copolymers of ethylene with 10% by weight or less of other monomers,
Alternatively, less than 15% by weight of these polyethylenes can be chlorinated products or oriented metal ions, and the melt index value is 0.01 to 50g/
Approximately 10 min can be used. Such polyethylene (B) may be produced in the process of producing a graft polymer by charging ethylene monomer into a polymerization can. With the vinyl chloride polymerized in the presence of (A) and (B), conventional copolymerizable monomers can be used, if desired, in amounts up to 30% by weight in the mixture with the vinyl chloride. Examples include monoolefins, vinyl ethers, (meth)acrylates, vinyl esters, unsaturated acids, unsaturated nitriles, aromatic vinyls, and the like. The graft polymer of the present invention has ethylene-
The content of methacrylic acid ester copolymer (A) and polyethylene (B) is at least 15% each, and the total amount of (A) and (B) is 85% by weight or less. Manufactured. If the amount of (A) is less than 15% by weight, the reinforcing effect as an impact resistance aid will be small, and if the amount of (B) is less than 15% by weight, the range of processing conditions that can provide high impact values will be narrow. Become. Furthermore, when the total amount of (A) and (B) exceeds 85% by weight, the proportion of (A) and (B) that are not chemically bonded to vinyl chloride increases,
Not only will the reinforcing effect be reduced, but the softening point of the composition will be significantly lowered, making it impossible to achieve the object of the present invention. Incidentally, the graft polymer is produced by a conventional method. The shapes of (A) and (B) to be subjected to the polymerization system are not particularly limited, and may be pellets, sheets, veils, powders, aqueous dispersions, or the like. However, (A)
It is difficult to dissolve in vinyl chloride unless it has a specific composition, and the viscosity of the solution is often high, making operation difficult. In order to get
(A) and (B) are preferably applied to the polymerization system as a powder or an aqueous dispersion. This graft polymer is used in an amount of 5 to 60 parts by weight, preferably 10 to 50 parts by weight, based on 100 parts by weight of PVC. If it is less than 5 parts by weight, the effect of improving impact strength is small and is not practical, and if it exceeds 60 parts by weight, the softening temperature of the composition will be significantly lowered. The PVC used in the present invention is not particularly limited as long as it is used for ordinary building materials and hard products, but it is usually a homopolymer of vinyl chloride or a copolymer with 80% by weight or more of vinyl chloride. A copolymer with 20% by weight or less of a monomer or a chlorinated product thereof having an average degree of polymerization of about 400 to 1500 as measured by the method of JIS K 6721 is used. If the average degree of polymerization is less than 400, the processability is excellent, but the impact resistance is low, and if it is greater than 1500, the processability is poor. The composition of the present invention may optionally contain a plasticizer, a stabilizer, an ultraviolet absorber, an antioxidant, a lubricant, a pigment,
Regular PVC compounding agents such as fillers and reinforcing agents and
EVA, EEA, CPE, EPR, EPT, IIR, CHR,
Conventional PVC such as AR, polyolefins, graft polymers of vinyl chloride onto these polymers, acrylonitrile-butadiene-styrene copolymers, methacrylic acid-butadiene-styrene copolymers
may contain a polymeric modifier for use. This polymer modifier can be used in an amount of usually up to 30 parts by weight per 100 parts by weight of PVC. Molding of this composition can be carried out in a conventional manner, and the processing conditions can be selected from a wide range. In addition, the obtained molded product exhibits excellent weather resistance, impact resistance, and heat deformation resistance, so it is highly useful as general hard products such as building materials, vehicles, agricultural and fishery materials, etc. Next, the present invention will be explained by examples. In addition,
% and parts are based on weight. Example The raw materials for polymerization shown in Table 1 (unit: g) were charged into a stainless steel autoclave and polymerized at 50° C. for 12 hours, and then the polymer was collected and dried. Next, the resulting polymer was appropriately pulverized or directly passed through an 18-mesh sieve to obtain a graft polymer under the sieve. Next, mix the ingredients shown in Table 2 at the indicated polymerization ratio using a mill roll at 170°C for 3 minutes (mixing condition a), 180°C for 10 minutes (mixing condition b), or 170°C for 6 minutes (mixing condition c). ) A sample sheet with a thickness of 3 mm was prepared by mixing to form a sheet with a thickness of 1 mm, stacking three layers and pressing at 180° C. for 5 minutes. The impact strength (JISK-7111), softening temperature (according to the JISK-6745 Softening Temperature Test Method), and weather resistance (high impact strength and high softening temperature) were measured using a weatherometer (black panel temperature).
Impact strength (JISK-
7111), color tone change (visual observation), and presence or absence of yoking (visual observation)]. The results are shown in Table 2. Table 2 shows that the composition of the present invention provides molded products with excellent impact resistance, weather resistance, heat deformation resistance, etc. even when processing conditions are changed. On the other hand,
For example, for the comparative compositions of Experiment Nos. 5 and 8, the physical properties may be unbalanced depending on the processing conditions, so it is difficult to widely adopt the processing conditions.
【表】【table】
Claims (1)
%であるエチレン−メタクリル酸エステル共重合
体(A)及びポリエチレン(B)の存在下に塩化ビニル又
は塩化ビニルを主体とする単量体混合物を重合し
て得られるものであつて、(A)及び(B)がそれぞれ15
重量%より多く、かつ(A)及び(B)の合計量が85重量
%以下であるグラフト重合体5〜60重量部と塩化
ビニル系重合体100重量部とからなることを特徴
とする塩化ビニル系樹脂組成物。1 Polymerization of vinyl chloride or a monomer mixture mainly composed of vinyl chloride in the presence of an ethylene-methacrylic acid ester copolymer (A) and polyethylene (B) with a methacrylic acid ester content of 5 to 75% by weight. (A) and (B) are each 15
Vinyl chloride comprising 5 to 60 parts by weight of a graft polymer in which the total amount of (A) and (B) is greater than 85% by weight and 100 parts by weight of a vinyl chloride polymer. based resin composition.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2014684A JPS60163954A (en) | 1984-02-07 | 1984-02-07 | Vinyl chloride resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2014684A JPS60163954A (en) | 1984-02-07 | 1984-02-07 | Vinyl chloride resin composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60163954A JPS60163954A (en) | 1985-08-26 |
JPH0581620B2 true JPH0581620B2 (en) | 1993-11-15 |
Family
ID=12019009
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2014684A Granted JPS60163954A (en) | 1984-02-07 | 1984-02-07 | Vinyl chloride resin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60163954A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0337580A (en) * | 1989-07-04 | 1991-02-18 | Toshiba Corp | Detection of partial discharge of three-phase transformer winding |
-
1984
- 1984-02-07 JP JP2014684A patent/JPS60163954A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0337580A (en) * | 1989-07-04 | 1991-02-18 | Toshiba Corp | Detection of partial discharge of three-phase transformer winding |
Also Published As
Publication number | Publication date |
---|---|
JPS60163954A (en) | 1985-08-26 |
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