JPS5823844A - Polyvinyl chloride composition - Google Patents

Polyvinyl chloride composition

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Publication number
JPS5823844A
JPS5823844A JP13861681A JP13861681A JPS5823844A JP S5823844 A JPS5823844 A JP S5823844A JP 13861681 A JP13861681 A JP 13861681A JP 13861681 A JP13861681 A JP 13861681A JP S5823844 A JPS5823844 A JP S5823844A
Authority
JP
Japan
Prior art keywords
ethylene
copolymer
chlorinated
rubber
weight
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP13861681A
Other languages
Japanese (ja)
Other versions
JPH021181B2 (en
Inventor
Tetsuo Tojo
哲夫 東條
Akira Matsuda
松田 昭
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Petrochemical Industries Ltd
Original Assignee
Mitsui Petrochemical Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from US06/289,821 external-priority patent/US4433105A/en
Application filed by Mitsui Petrochemical Industries Ltd filed Critical Mitsui Petrochemical Industries Ltd
Publication of JPS5823844A publication Critical patent/JPS5823844A/en
Publication of JPH021181B2 publication Critical patent/JPH021181B2/ja
Granted legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:The titled semirigid or nonrigid composition having extremely improved plasticity, low-temperature impact resistance, and flexibility, obtained by blending chlorinated ethylene.1-butene copolymer rubber, etc. with polyvinyl chloride. CONSTITUTION:100pts.wt. polyvinyl chloride is blended with 30-200pts.wt. chlorinated rubber with a chlorine content of 5-50wt% obtained by chlorinating ethylene.1-butene copolymer rubber having a molar ratio of ethylene to 1-butene of (85/15)-(95/5) or ethylene.1-bitene.5-ethylidene-2-norbornene copolymer rubber having a molar ratio of ethylene to 1-butene of (85/15)-(95/5). The addition of 1-20pts.wt. ethylene.alpha-olefin copolymer rubber having a molar ratio of ethylene to alpha-olefin of (95/5)-(20/80) and/or ethylene.alpha-olefin.polyene (preferably nonconjugate polyene) terpolymer rubber to the polyvinyl chloride improves further low-temperature impact strength.

Description

【発明の詳細な説明】 本発明はIり塩化ビニル組成物に関し、更に評しくは、
−り塩化ビニルの可塑性愛着しく改良しかつぼり塩化ビ
ニルの低温における針術撃性及び条軟性會着しく改良し
た−り塩化ビニル組成−に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a polyvinyl chloride composition, and more particularly,
The present invention relates to a polyvinyl chloride composition which has improved the plasticity of vinyl chloride, and has also improved the low-temperature needle percussion properties and flexibility of vinyl chloride.

Iり塩化ビニルは代表的なプラスチ、りの一つで参り、
フィルム、シート、ノダイグ、レゾ−1紙加工品、押出
物、型物、繊維などの形状に成形され、極めて多岐多様
表応用用途に使用畜れている。
Polyvinyl chloride is one of the representative plastics.
It is formed into shapes such as films, sheets, paper products, reso-1 paper products, extrusions, molds, fibers, etc., and is used for a wide variety of table applications.

しかしこのIり塩化ビニルは可塑性の不足、低温時の性
質、脣に耐衡撃性に劣るなどO劣性が69、このため種
々の可履剤ある−は改質剤を配合・して使用されている
のが現状である。ζOような4す塩化r=ルの改質剤と
しては、従来からDOP (ジオクチルフタレート) 
 DBP(ジツチルフタレート)などの7#ル酸エステ
、A/@中tcp<トvクレゾルホ、X7.−))など
のシン駿エステル類が知られているが、これらの液体可
塑剤は移行性や浸出性があり、また加熱により減量する
とiう欠陥1有して−るため、これらの欠陥を是正する
良めニトリルゴムや塩素化4リエチレンなどのポリマー
會可塑剤としてブレンドすることが行なわれている。
However, this polyvinyl chloride has poor plasticity, poor properties at low temperatures, and low impact resistance,69 and for this reason, various lubricants are mixed with modifiers and used. The current situation is that DOP (dioctyl phthalate) has traditionally been used as a modifier for tetrachloride such as ζO.
7# acid esthetics such as DBP (dittylphthalate), A/@Nakatcp, X7. Shinshun esters such as -)) are known, but these liquid plasticizers have migration and leaching properties, and also have defects in that they lose weight when heated. Blending with polymers such as nitrile rubber and chlorinated tetraethylene as plasticizers has been practiced.

しかしニトリルゴムや塩素化Iリエチレンなどを配合し
九11!ツ塩化Cエルは回層性は改良されるが、低■で
の耐衝撃性中低11における柔軟性の改jLK対して癲
%/%tだ不十分であった。
However, by blending nitrile rubber and chlorinated I-lyethylene, 911! C.L. chloride improved the layering properties, but the impact resistance at low (1) and the flexibility at (medium and low) 11 were improved by %/%t.

本発明者ら社、かかる従来の−り塩化fxル組成物O欠
点!改良すべく鋭意研究を進めた結果、−リ塩化ビ=#
に4を定の塩素化が五を配合することによ〕、−リ塩化
1fxルO可履性が著しく教員されるだけでなくニトリ
ルが人中塩素化/Vエチレンに此べ、低−におけ1耐衝
撃性と柔軟性が着しく改jLされることを見出し、本発
明管するに至り良・ すなわち、本発明に従えば、 弾) Iり塩化ビニ1しと。
The present inventors have found that such conventional chlorinated fxle compositions have no drawbacks! As a result of intensive research to improve -PVC=#
By adding 4 to 4 and 5 to 5], not only is the chlorinated 1fxle O wearability significantly improved, but also the nitrile is reduced to chlorinated/V ethylene. It has been found that the impact resistance and flexibility of PVC can be improved in a suitable manner, leading to the present invention.That is, according to the present invention, the impact resistance and flexibility of polyvinyl chloride can be improved.

(b)  (llエチレンと1−2テンの4に比が約8
5/1 !1〜95Aの範囲にあるエチレンと1−)P
テンとの共重合体ゴムもしくはop)エチレンと1−1
テンのモル比が約85/15〜95/’)の範囲にある
エチレンと1−1テンと5−エチリデン−2−ノルがル
ネンとO共重合体ゴム【塩素化して得られる塩業含有量
約5〜50重量−の少なくとも一″1IiO塩素化tム とから成るIり塩化ビニル組成物が提供される。
(b) (The ratio of 1-2 ethylene to 4 is about 8
5/1! Ethylene and 1-)P ranging from 1 to 95A
Copolymer rubber with ten or op) ethylene and 1-1
Ethylene, 1-1 thene, 5-ethylidene-2-nor, runene and O copolymer rubber in which the molar ratio of ten is in the range of about 85/15 to 95/') [salt content obtained by chlorination] A polyvinyl chloride composition is provided comprising about 5 to 50% by weight of at least 1" 1IiO chlorinated tm.

本発明に従えば、更に、 (a)  −り塩化ビニルと、 (b)  (1)エチレンと1−ラテンのモル比が約1
45〜95A (D範囲にあるエチレンと1−1テンと
O共重合体ゴムもしくは(11)エチレンと1−1テン
のモル比が約85/15〜9!S15 O範囲にあるエ
チレンと1−1テンとS−エチリデン−2−ノルがルネ
ンとの共重合体tAt−塩素化して得られゐ塩素含有量
的S〜50重量−の少なくとも一種の塩素化ゴムと、 (・)  (1)エチレンとα−オレフィンとの共重合
体tム又a/、lび0i)エチレンとα−オレフィンと
4リエンとの共重合体tふ1〜20重量部からなるiり
塩化虻エル組成物が提供される。
According to the invention, the molar ratio of (a) -vinyl chloride and (b) (1) ethylene to 1-Latin is about 1.
45-95A (Ethylene, 1-1 tene and O copolymer rubber in the D range or (11) ethylene and 1-1 tene molar ratio of about 85/15 to 9! S15 O copolymer rubber or (11) ethylene and 1-1 tene in the range D At least one chlorinated rubber having a chlorine content of S ~ 50% by weight obtained by chlorinating a copolymer of 1-ten and S-ethylidene-2-nor with runene, tAt, and (.) (1) Ethylene. A copolymer of ethylene, an α-olefin and a olefin, and a copolymer of ethylene, an α-olefin and a 4-ethylene chloride composition comprising 1 to 20 parts by weight is provided. be done.

本11mKシーて4り塩化ビニルに配合される塩素化/
 A O原料となる塩素化されるべきエチレン・l−1
テン共重合体fム又はエチレン・1−2テン・5−エチ
リデンノルIルネン共重合体fふ中Oエチレンと1−1
テンとのモル比は、約85/15〜9574.好’* 
L < ハ87/13〜94’6 O範囲ニナければな
らず、このような毫ル比Oζ0共重合体/AQ塩素化物
をぼり塩化ビニルに配合したもOO戚形物#i岡じモル
比をとるエチレンとプロピレンとt共重合体成分とする
二元又は三元共重合体fAO塩素化wをぼり塩化ビニル
に配合したものOR形愉と比較して、1り塩化ビニルに
約50重量部以上大量に配合したと龜III#に、すな
わち半硬質又は軟質OSV塩化ビニル組成物tII供し
ようとしたときに%に、強に及び柔軟性に優れる。又こ
の二元又は三元共重合体ゴムのエチレンと1−1テンの
モル比において、1−1テン単位が約154d4y−以
上では、塩素化ゴムt−4り塩化ビニルに配合したもの
の成形物は強度の点で劣り、咳塩化f五に1F、tて公
知のエチレンとプロピレンを共単量体成分とする二元又
は三元共重合体ゴムの塩素化−を用%/にたときと変る
処がない。
Chlorination added to vinyl chloride in this book 11mK/
Ethylene/l-1 to be chlorinated as A O raw material
Tene copolymer f or ethylene/1-2 tene/5-ethylidenenor I rune copolymer f with ethylene and 1-1
The molar ratio with ten is approximately 85/15 to 9574. Good'*
L <HA87/13~94'6 O range must be nina, and even if such a mole ratio Oζ0 copolymer/AQ chlorinated product is blended with vinyl chloride, the OO relative product #i Oka same molar ratio A binary or ternary copolymer containing ethylene, propylene, and t-copolymer component fAO chlorinated w and blended with vinyl chloride. If the above amount is blended, it will be very strong and have excellent flexibility when it is intended to be used as a semi-rigid or soft OSV vinyl chloride composition. In addition, if the molar ratio of ethylene to 1-1 ten in this binary or ternary copolymer rubber is about 154 d4y- or more in 1-1 ten units, molded products of chlorinated rubber T-4 blended with vinyl chloride is inferior in strength, and when compared to chlorinated f5 and 1F, when compared to the chlorination of a known binary or ternary copolymer rubber containing ethylene and propylene as comonomer components. There's nothing to change.

一方、エチレン単位が約95モル1&を越えると自は成
形物の耐衝撃性が劣る欠点が生じる。
On the other hand, if the ethylene unit exceeds about 95 moles, the molded product will have a disadvantage of poor impact resistance.

エチレン・1−1テン・非共役ジエン三元共重合体を1
料として用−る場合にお埴て、非共役ジエン共単量体成
分として5−エチリデン−2−ノルールネンの代りに、
ジシクロペンタジェン管用いたエチレン・l−1テン・
ゾシクロペン#ジエン共重合体fAを用いゐと、その塩
素化物itrル量が多(4す塩化ビニルに配合しても均
一に配合することができなiので成形物0**撃性及び
彊[#低h*一方、rs−エチリデン−2−ノルールネ
ンはその少′&%Aeル生成量の点からみて好重しh非
共役ジエンである。
1 ethylene/1-1 tenene/nonconjugated diene terpolymer
In place of 5-ethylidene-2-norurunene as a non-conjugated diene comonomer component when used as a material,
Ethylene, l-1 ten, using dicyclopentadiene tube
When zocyclopene/diene copolymer fA is used, the amount of chlorinated compounds is large (it cannot be uniformly blended even when blended with vinyl chloride), so molded products have low impact resistance and #Low h* On the other hand, rs-ethylidene-2-norurunene is a preferable non-conjugated diene in view of its small amount of Ael produced.

塩素化が五の原料に用いられるエチレン・l−1テン−
5−エテリデンノルールネン共重合体fム中の3−エチ
リデンノルがルネン成分の含量は璽り素価表示で約30
以下であることが推奨され為、錬成分量がTo壇り大で
あると咳成分は高価故経済的てな−0 本発明において用iるMAR化r A O原料となるエ
チレン・l−1テン共重合体又祉エチレン・l−1テン
・5−エチリデン−2−ノルがルネン共重合体fムは、
約S〜100.好鵞しくは約lO〜800ムーニー粘[
(ML   100℃)のもの1+4、 が用−られることがant、い、五−二−粘度が低すぎ
ると塩素化ゴムの強![を低下させ、一方高すぎると塩
素化ゴム0Ill!融流動性が低下し、成形性、加工!
1を墨化盲せ、塩化ビニルとブレンドしたと自に均一!
1が損われるようになる・ かかゐ共重合体/ A O塩素化は、例えば共重合体r
Aを粉砕して細粒化し、こO細粒を水性けん滴状■にし
て約70〜90CのiI厘で分子状塩素と接触させる方
法、四塩化炭素、テトラクロルエチレンのような塩素に
対して安定な溶媒中に共重合体ゴムを溶解し、均一な溶
液状態として分子状塩素と接触させる方法、あるいはN
−クロルアセトアミド、N−クロルサクシイミド、l、
3−ジタールー5.5−ゾメテルヒダントインのような
塩素化合−管ロールやバンバリーミキサ−危どで共重合
体ゴム中に均一に#り込み、塩素管遊腸する温[K加熱
する方法などによって行われ、特に水性けん濁状態でO
塩素化が好ましい、これは、共重合体ゴム中のエチレン
と1−1テンと(D4ル比が前記規定され良範囲内KT
oり、又共重合体f A O結晶指数が25以上である
丸め常温ての機械粉砕による細粒化が可能であって、低
摩に塩素化し得る水性けん濁液に分子状塩素を吹込む方
法が採用できるからである。なお、ここで−う結晶指数
は、低密&、#リエチレンミラソンM−9(三井−リケ
建カル製低密屓Iリエチレン、A8TM−D−1238
法によるメ々トインjyクス(190℃)1.5、A8
TM−D−1505法による密[9,9!1)0示差熱
分析を行い、20℃〜120℃の範IP8KToる吸熱
面積’1looとし、これに対する共重合体がムの吸熱
面積の割合で定義されるものである。この懸濁塩素化に
用iる細粒は10メッシ、 (Tyl@r No、)通
過であることが望ましい、これよp細粒が大きくなると
塩素化に要する時間がかかp工業的に好宜しくなく、鵞
た均一な塩素化が困難とな夛、rル発生等0rIJII
が生じるなどO欠点があゐ、そして、ζOll濁塩素化
O場合、界面活性剤管使用して塩素化反応系を安定化し
て実施することが推奨される。
Ethylene l-1ten- used as raw material for chlorination
The content of 3-ethylidenenor runene component in the 5-ethylidenenor runene copolymer is approximately 30 in raw material value.
Since it is recommended that the content of ethylene/l-1, which is the raw material for MAR conversion used in the present invention, is A copolymer of ethylene/l-1ten/5-ethylidene-2-nor is a runene copolymer,
Approximately S~100. Approximately 10 to 800 Mooney viscosity [
(ML 100°C) 1+4, is not used, 5-2- If the viscosity is too low, the strength of chlorinated rubber! On the other hand, if it is too high, chlorinated rubber 0Ill! Melt flowability decreases, moldability and processing!
When 1 is blackened and blended with vinyl chloride, it becomes uniform!
1 becomes impaired.
A method of crushing A into fine particles, making the fine particles into aqueous droplets, and contacting them with molecular chlorine at about 70 to 90 C, for chlorine such as carbon tetrachloride and tetrachlorethylene. A method in which the copolymer rubber is dissolved in a stable solvent and brought into contact with molecular chlorine as a homogeneous solution, or
-Chloracetamide, N-chlorsuccinimide, l,
Chlorinated compounds such as 3-ditar-5.5-someterhydantoin are uniformly incorporated into the copolymer rubber using a tube roll or Banbury mixer, and the temperature at which the chlorine enters the tube [K heating method, etc.] O
Chlorination is preferred, since the ethylene and 1-1 tenene in the copolymer rubber (D4 ratio is within the range specified above).
Also, a copolymer f A with an O crystal index of 25 or more can be made into fine particles by mechanical pulverization at room temperature, and molecular chlorine is blown into an aqueous suspension that can be chlorinated with low friction. This is because the method can be adopted. In addition, the crystalline index here is low-density &#lyeethylene Milason M-9 (Mitsui-Rike Kencal low-density polyethylene, A8TM-D-1238
Method of measurement (190℃) 1.5, A8
A dense [9,9!1)0 differential thermal analysis was performed using the TM-D-1505 method, and the endothermic area in the range of 20°C to 120°C was set as 1looo, and the ratio of the endothermic area of the copolymer to this was defined. The fine particles used for this suspension chlorination are preferably 10 mesh, (Tyl@r No.) passing through.If the fine particles are larger than this, the time required for chlorination will be longer and it is not suitable for industrial use. This is not good, and it is difficult to chlorinate uniformly.
If there are disadvantages such as the occurrence of chlorination, and ζOll cloudy chlorination, it is recommended to use a surfactant tube to stabilize the chlorination reaction system.

塩素化のli&は、分子状塩素その他の塩素化剤の使用
量、反応時間、反応槁度碌どt適宜選択するζ七によp
、調節することができる。また、分子状塩素管使用して
塩素化する場合には、党の照射によ)塩素化反応速度を
大幅に増大し得るのも、従来の知見の如くである。
The li& of chlorination depends on the amount of molecular chlorine or other chlorinating agent used, reaction time, reaction strength, etc. selected as appropriate.
, can be adjusted. Furthermore, when chlorinating using a molecular chlorine tube, it is known that the chlorination reaction rate can be greatly increased (by irradiation).

塩素化反応llは、次のようにして処、Illれる。The chlorination reaction is carried out as follows.

水性妙ん濁状謙ての塩素化の場合、塩素化ゴムは水洗を
行なうζ七によ1分子状塩素を除き、乾燥させる。#!
液状態での塩素化の場合には、反応溶at過剰のメタノ
ール表との塩素化ゴムの貧溶媒中に投入し、沈澱物を口
遇し、この溶媒で洗浄して乾燥させる。
In the case of aqueous chlorination, monomolecular chlorine is removed from the chlorinated rubber by washing with water, and the rubber is dried. #!
In the case of chlorination in a liquid state, the reaction solution is poured into a poor solvent of chlorinated rubber along with an excess of methanol, and the precipitate is washed with this solvent and dried.

このようにして得られる塩素化ゴムは、共重合体中約5
〜50重量%、好ましくは約5〜35重量−の塩素含有
量と約20〜150、好オしくけ約30〜80のムーニ
ー粘Wl(ML1+4.100℃)を有していなければ
なら碌い、塩素含有量およびムーニー粘質がToオク高
いと、塩素化ゴムの溶融流動性が低下し、成形性、加工
性を悪化させ、−り塩化ビニル樹脂とブレンドしたとき
の均一性が損われ得られる成形物の衝撃強rjlが充分
でない。
The chlorinated rubber thus obtained has approximately 5%
It should have a chlorine content of ~50% by weight, preferably about 5-35% by weight, and a Mooney viscosity Wl (ML1+4.100°C) of about 20-150, preferably about 30-80. If the chlorine content and Mooney viscosity are too high, the melt fluidity of the chlorinated rubber will decrease, the moldability and processability will deteriorate, and the uniformity when blended with polyvinyl chloride resin may be impaired. The impact strength rjl of the molded product is not sufficient.

一方、これ以下の塩素含有量では4り塩化(=ルと混合
して得られる成形物の耐衝撃性が充分でない謙たToま
シムーニー粘fが低いと同様に成形物の耐衝撃性が低下
する。
On the other hand, if the chlorine content is lower than this, the impact resistance of the molded product obtained by mixing it with tetrachloride will not be sufficient.If the viscosity is low, the impact resistance of the molded product will decrease as well. do.

本発明に従りて、fり塩化ビニルに塩素化ゴ五會配合す
る方法は、従来二トリルプムや塩素化−リエチレン[−
jす塩化ビニルにブレンドする任意の方法tそOtオ採
用できる。特に1本発明において使用する塩素ゴムは粒
状化しやすく、10メ、シ&(テyl@r No、)以
下に、4H’C10メツシ。
According to the present invention, the method of blending chlorinated rubber with fluorinated vinyl chloride is conventionally performed using nitrile pum or chlorinated polyethylene [-
Any method of blending with vinyl chloride can be employed. In particular, the chlorine rubber used in the present invention is easily granulated and has a particle size of 4H'C10 or less.

〜lOOメッシ、O粒径に細粒化した場合、従来の塩素
化エチレン−プロピレン共重合体ゴムや塩素化エチレン
−プロピレン−非共役ゾエン共重合体/Aを細粒化し九
場合に比べ積載時の10.キング−IIX1kく、優れ
た貯蔵安定性を示すので、押出機中中へンシエルミキナ
ー中で4す塩化ビニルとIVンrする際極めて有利であ
る。
~1OO mesh, when the particles are refined to O particle size, the loading time is lower than when conventional chlorinated ethylene-propylene copolymer rubber or chlorinated ethylene-propylene-nonconjugated zoene copolymer/A is refined to a particle size of 9. 10. King-IIX 1k exhibits excellent storage stability, making it extremely advantageous when reacting with 4-vinyl chloride in a Henschelmikiner in an extruder.

Iす塩化C二kK対する本発明の塩素化ゴムの配合比率
は、その用途(軟質又は中硬質)によっても異なるが、
一般的にはぼり塩化ビニル100重量IIK対し、塩素
化ゴム3〜2σO重量部、好重しくは約5〜lOO重量
部であることが望まし−6 塩素化IムO配合量があtり少ない場合には、19塩化
ビニルに耐衝撃性を付与することができなiので好まし
くなく、逆にあ14)多く配合しても一す塩化gニルの
改質効果の増加【期待出来ず無駄なので好ましくない。
The blending ratio of the chlorinated rubber of the present invention to Isu C chloride varies depending on its use (soft or medium hard), but
Generally, it is desirable that the amount of chlorinated rubber is 3 to 2σO parts by weight, preferably about 5 to 1OO parts by weight, per 100 weight parts of vinyl chloride IIK. If it is less, it is not preferable because impact resistance cannot be imparted to 19-vinyl chloride, and conversely, even if it is added in a large amount, the modification effect of 1-g-vinyl chloride will increase [unexpected and wasteful]. So I don't like it.

本発tlAK従えば、iた、上記塩素化ゴムに加えて、
更に%’A成分として、(1)エチレンとα−オレフィ
ンとの共重合体ゴム又は/及び(11)エチレンとα−
オレフィンとIジエンとO共重合体ゴムt。
According to the present invention, in addition to the above chlorinated rubber,
Furthermore, as the %A component, (1) copolymer rubber of ethylene and α-olefin or/and (11) ethylene and α-olefin
Olefin, I diene and O copolymer rubber t.

好オしくはI9#1化ビニル100重量部に対して1〜
20重量部通常の方法によp配合することによって4り
塩化ビニルの低温の耐衝撃強rjILを大幅に敏善する
ことができる。
Preferably 1 to 100 parts by weight of vinyl I9#1
By adding 20 parts by weight of p in a conventional manner, the low-temperature impact strength rjIL of polyvinyl tetrachloride can be greatly improved.

上記α−オレフィンの具体例としては、プロピレン、l
−1テン 1−−4ンテン、4−メチル−1−ペンテン
、1−ヘキセン、1−オクテン、l−デセンなどを例示
できる。
Specific examples of the above α-olefin include propylene, l
Examples include -1-tene, 1--4-tene, 4-methyl-1-pentene, 1-hexene, 1-octene, and l-decene.

又Iジエンとしては非共役4リエンが好壕しく、具体的
には、1,4−へキサジエン、l、6−オタタジエン、
2−メチル−1,5−へキサジエン、6−メチル−1,
5−へ!タジエン、7−メチル−1,6=オクタゾエン
の如き″鎖状非共役ジエン、ジターへキサジエン、ジシ
クロインタジエン、メチルテトラヒドロインデン、5−
ビニルノルIルネン、5−エチリデン−2−ノルールネ
ン、5−メチレン−2−ノルールネン、5−イソゾロビ
リデン−2−ノルールネン、6−りnルメチル−5−イ
ソ!口(ニル−2−ノルールネンの如1環状非共役ジエ
ン、2.3−ジイソプロピリデン−5−ラルーpy4ン
、2−エチリデン−3−イソ7”!−ビリデンー5−/
ル一ルネン、2−7”胃ベニルー2,2−ノル#ルナジ
エン、!、3.7−オクタトリエン、1.4.9−デカ
トリエンO如暑トリエンなどが代表的な例として示され
、41に1.4−へキサジエン、ジシクロペンタジェン
、6−エチリデン−2−ノルールネンなどが好ましい。
In addition, non-conjugated 4-lienes are preferable as the I diene, and specifically, 1,4-hexadiene, l,6-otatadiene,
2-methyl-1,5-hexadiene, 6-methyl-1,
Go to 5-! tadiene, linear non-conjugated dienes such as 7-methyl-1,6-octazoene, diterhexadiene, dicyclointadiene, methyltetrahydroindene, 5-
Vinylnorrunene, 5-ethylidene-2-norrunene, 5-methylene-2-norrunene, 5-isozolobylidene-2-norrunene, 6-rinmethyl-5-iso! (1-cyclic non-conjugated diene such as nyl-2-norurunene, 2,3-diisopropylidene-5-ralupylene, 2-ethylidene-3-iso7''!-pylidene-5-/
Typical examples include lunene, 2-7'' gastric benylene, 2,2-nor#lunadiene, !, 3,7-octatriene, 1,4,9-decatriene, and 41. 1.4-hexadiene, dicyclopentadiene, 6-ethylidene-2-norurunene and the like are preferred.

従りて使用し得る第3成分としてO共重合体ゴムは各種
あるがこれらt−混合し1用い得ることは勿論である。
Therefore, there are various O copolymer rubbers that can be used as the third component, and it goes without saying that a t-mix of these rubbers can be used.

工業的にはエチレン・プロピレン二元共重合体がム、エ
チレン・l−1テン二元共重合体!ム、エチレン・プロ
ピレン1−)シクロインタジエン三元共重合体ゴム、エ
チレン・プロピレン・5−エチリデン−2−ノルールネ
ンゴム共重合体fム、エチレン・l−1テン・ジシクw
−4ンタジエン共重合体イム、エチレン・1−1テン・
5−エテリfンー2−ノルIルネン三元共重合体rAな
どの使用が推奨される。
Industrially, ethylene/propylene binary copolymer is used, and ethylene/1-1 tenium binary copolymer is used! ethylene/propylene 1-) cyclointadiene terpolymer rubber, ethylene/propylene/5-ethylidene-2-norurunene rubber copolymer f, ethylene/l-1tene/disic w
-4-ntadiene copolymer im, ethylene, 1-1 ten,
The use of 5-ether-2-nor-I runene terpolymer rA is recommended.

これら共重合体がムのエチレンとα−オレフィンのモル
比は通常的9515〜20AOの範囲であること又ムー
ニー粘凝(ML、+4.100℃ )#i約20〜15
0であることが推奨される。又/ 17工ン成分が共重
合している共重合体がムにあってはlつ素価表示で約3
0以下のも00使用が好j L n aζO様な共重合
体ゴムの併用効果は前記塩素イヒゴムをIり塩化ビニル
100重量部に対して約3〜50重量部と少量配合する
とき、すなわち耐衝撃性に優れた硬質ぼり塩化ビニルを
提供しようと意図するときに著しく発現し、低温に於い
ても秀いでた耐衝撃性1有する硬質Iり塩化ビニル成形
物が得られることになる。
The molar ratio of ethylene to α-olefin in these copolymers is typically in the range of 9515 to 20 AO, and Mooney coagulation (ML, +4.100°C) #I is about 20 to 15
It is recommended that it be 0. Also, if there is a copolymer in which 17 components are copolymerized, the base price is about 3
It is preferable to use a copolymer rubber of 0 or less. When the intention is to provide hard vinyl chloride with excellent impact resistance, this effect is remarkable, and a hard vinyl chloride molded product having excellent impact resistance 1 even at low temperatures can be obtained.

なシ、4り塩化ビニルへの配合にあたって、この第3成
分表予め前記塩素化fふとロール押出機等を用φて均一
に混合しておくと極めて良好な結果が得られる。この第
3成分の法加量力11p多−とむしろ耐衝撃性が低下す
る場合がある。
However, when blending into tetravinyl chloride, very good results can be obtained if the third component table is uniformly mixed in advance using the chlorinated foot roll extruder or the like. If the third component has a modulus of force 11p, the impact resistance may actually decrease.

本発明の組成物からは射撃性に優れた硬質/ IJ塩化
ビニルの成形物(/す塩化ビニル100重量部に対して
約3〜50重量部の塩素化ゴム、更には約1〜20重量
部のエチレン、α−オレフィン、場合によりては4リ工
ン成分からシる共重合体ゴムを配合したと暑)が得られ
、又装置及び柔軟性に優れた半硬質又は軟質−り塩化ビ
ニル成形物(Iす塩化11#工ル100重量部に対して
50重量部以上の塩素化rAl配合したとき)が得られ
、従来の−り塩化ビニル樹脂の用途に良好に使用される
From the composition of the present invention, molded hard/IJ vinyl chloride with excellent shooting properties (about 3 to 50 parts by weight of chlorinated rubber per 100 parts by weight of vinyl chloride, and further about 1 to 20 parts by weight) By blending copolymer rubber made from ethylene, α-olefin, and in some cases 4-recycle components, it is possible to obtain semi-rigid or flexible polyvinyl chloride molding with excellent equipment and flexibility. A product (when 50 parts by weight or more of chlorinated rAl is blended with 100 parts by weight of 11# chloride) is obtained, and can be used satisfactorily for conventional polyvinyl chloride resin applications.

以下に実施例及び比較例¥tあげて本発明を更に^体的
に説明するが、本発明の範囲【これらの実施例に限定す
るもので危いこと1j1451でもない。
The present invention will be described in more detail below with reference to Examples and Comparative Examples, but the scope of the present invention is not limited to these Examples.

jllI1表に示した性状會有するエチレン・l−ブテ
ン・5−エチリデン−2−ノルぎルネン共重合体fAl
、ターがしル(ターが工業製)で20メッシ、 (’l
’yl@r No・)の金網を通過する大きさに常温で
機械粉砕した。粉砕して得られた共重合体ゴム粉1g2
009. xノ豐ン750(ノニオン系乳化剤I第一工
業製薬製品)0.111および水2jの混合物を、攪拌
機および温度針を備えた内容積3ノのガラス製容器に仕
込み、加熱した。系の温度が80℃に達したら、外側よ
り20W昼光色螢光灯を照射しながら、塩素ガスt2.
1’/分の割合で前記混合物のけん濁液中に導入し、8
0〜83℃の瀉縦で第1表に示した時間だけ塩素化反応
を継続し友。その後口遇し、60℃の温水2ノ【用い1
時間の洗浄を3回くり返し、更K1回冷水で洗浄して5
0℃で減圧下に乾燥させ、20メツシ。
Ethylene/l-butene/5-ethylidene-2-norgyrunene copolymer fAl having the properties shown in Table 1
, 20 meshes with targashiru (made by targa industry), ('l
It was mechanically crushed at room temperature to a size that could pass through a wire mesh. 1g2 of copolymer rubber powder obtained by pulverization
009. A mixture of 0.111 of X-NO-FUIN 750 (Nonionic Emulsifier I Daiichi Kogyo Seiyaku Products) and 2J of water was charged into a glass container with an internal volume of 3 mm equipped with a stirrer and a temperature needle, and heated. When the temperature of the system reaches 80°C, chlorine gas t2.
into the suspension of the mixture at a rate of 1'/min,
The chlorination reaction was continued for the time shown in Table 1 at a temperature of 0 to 83°C. After that, we met and had two baths of 60℃ warm water.
Repeat washing for 3 times, then wash once with cold water for 5 hours.
Dry under reduced pressure at 0°C for 20 mesh.

の金網を通過するサイズの粒径の塩素化ゴムを得た。こ
の塩素化ゴム中の塩素含有量を、−ンぺ燃焼法で測定し
、第1!!に示し良、tた、これら塩素化ゴムのグル分
率を、次のようKして測定し良。
A chlorinated rubber having a particle size that could pass through a wire mesh was obtained. The chlorine content in this chlorinated rubber was measured using the -npe combustion method. ! The glue fraction of these chlorinated rubbers was measured as follows.

100メッシ、の金網でスクリーンバスケットを作p、
この中に約0.21の塩素化ゴム【0.lダ単位迄精秤
して入れ、沸騰p−キシレン30〇−中に1時間放置し
、スクリーンバスケット中に残りた不溶物t50℃、減
圧下で3時間乾燥し、Wi−に放冷後0. I M9単
位迄精秤し、不溶分の割合trグル分率して示した・ 未加硫塩素化ゴムの資性till定するため、塩素化ゴ
ムを150℃のホ、トゲレスで6分間予熱し、100 
kll/alの加圧下で4分間プレス、続いて25c、
lo Ok$/aF 4D加圧下でコールドグレスして
厚さ2■のプレスシートに作製し、このシー)Kついて
JI8 K−6301の方法に準拠して、破断点応力お
よび伸びの値を測定した。結果を第111K示す。
Make a screen basket with 100 mesh wire mesh,
In this, about 0.21 chlorinated rubber 0. Precisely weigh it to the nearest 1.5 kg, leave it in boiling p-xylene for 1 hour, dry the insoluble matter remaining in the screen basket at 50°C for 3 hours under reduced pressure, and leave it to cool to 0. .. Weighed accurately to the nearest 9 units, and expressed the insoluble content as the glue fraction. To determine the properties of unvulcanized chlorinated rubber, the chlorinated rubber was preheated at 150°C for 6 minutes without splinters. , 100
Press for 4 minutes under pressure of kll/al, followed by 25c,
lo Ok$/aF A press sheet with a thickness of 2 cm was produced by cold glazing under 4D pressure, and the stress at break and elongation values of this sheet were measured in accordance with the method of JI8 K-6301. . The results are shown in the 111th K.

合成例3 第1!IK示し穴性状管有する粉末状(20メッシ、ス
クリーン通過)のエチレン・1−2テン共重合体fJ−
に’:)Vhて、合成例1及び2と同じ方法で塩素化¥
t59分間行埴、20メッシ、の金網【通過するサイ、
leO塩素化fAl得た。この塩素化ゴム中の塩素含有
量を、−ンペ燃焼法で測定したところ、重量で21−の
値が得られた。この塩素化fAKついて物性181足し
、結果を馬1表にした・ 実施例1(IIIす塩化ビニル硬質用途)合成fllで
得られた20メッシ、 (Tyl@r No−)の金網
を通過するサイズの粉末状の塩素化ジム10重量部と粉
末状の4す塩化ビニル(商品名ゼp103ΣP1日本ゼ
オン製)100重量部と有機Cd −Ba −Zm系塩
化ビニル用安定剤(商品名Ll[1Z−80絣化学製)
1.5重量部、Cd −Zn系安定剤(商品名LCZ−
101化学製)0.化学量部及びステアリン酸カルシウ
ム(和光純系製)1.0重量部管50℃でヘンシェルZ
キナー中で混合し、更にζO混合物を表−湯度130〜
140℃の8インチロールで5分間混練した。この混線
物を次の条件でプレス成形し、厚さ2鱈のプレスシート
(但し落鍾衝撃強度試験用はl■シート)を作製し各種
測定に供した。その測定結果tl1211K示す。
Synthesis example 3 1st! Powdered (20 mesh, screen passed) ethylene/1-2 tenene copolymer fJ- with IK and hole properties
ni':) Vh, chlorination using the same method as Synthesis Examples 1 and 2
T59 minutes Yukihana, 20 Messi, wire mesh [Rice passing through,
leO chlorinated fAl was obtained. When the chlorine content in this chlorinated rubber was measured by the combustion method, a weight value of 21 was obtained. The physical properties of this chlorinated fAK were added to 181, and the results were summarized in Table 1. Example 1 (III Vinyl chloride hard application) 20 mesh obtained from synthetic fll, size to pass through the wire mesh of (Tyl@r No-) 10 parts by weight of powdered gym chloride, 100 parts by weight of powdered tetravinyl chloride (product name: Zep103ΣP1 manufactured by Nippon Zeon), and an organic Cd-Ba-Zm stabilizer for vinyl chloride (product name: Ll[1Z- 80 Kasuri Kagaku)
1.5 parts by weight, Cd-Zn stabilizer (trade name LCZ-
101 Chemical) 0. Henschel Z at 50°C in a stoichiometric part and 1.0 part by weight of calcium stearate (manufactured by Wako Junkei)
Mix in a water heater and add the ζO mixture to a boiling temperature of 130~
The mixture was kneaded for 5 minutes using an 8-inch roll at 140°C. This mixed wire was press-molded under the following conditions to produce a press sheet with a thickness of 2 mm (1 sheet for the hammer impact strength test) and used for various measurements. The measurement result tl1211K is shown.

(fレス成形条件) IIIす塩化ビニル混線物t170℃で3分間予熱し、
次に170℃で2分間100ゆ7512の加圧下で熱プ
レスを行%A、続iて20℃で5分間、100hya、
i o加圧下で冷却プレスを行う。
(f-less molding conditions) III. Vinyl chloride mixed material t Preheat at 170°C for 3 minutes,
Next, heat press at 170℃ for 2 minutes under a pressure of 100yen7512%A, then at 20℃ for 5 minutes at 100hya,
io Perform a cold press under pressure.

j!施何例 2施例Iにおいて合成f11で得危塩素化エチレン・1
−:j’テン・5−工fすf”ノー2−ノルールネンゴ
ム合体プムの代pに、合成例2で得た塩素化エチレン・
l−ブテン共重合体ゴム【用iた以外は、実施例1と全
く同様にしてI9塩化ビニル組成物tllllL7”レ
ス成型した。測定結果を第2表に示す。
j! Example 2 In Example I, synthesis f11 yields hazardous chlorinated ethylene 1
-:j'Ten・5-Fsf''No2-Norrunene Rubber Combined Plum P, the chlorinated ethylene obtained in Synthesis Example 2
The vinyl chloride composition I9 was molded in exactly the same manner as in Example 1 except that the l-butene copolymer rubber was used. The measurement results are shown in Table 2.

比較例1 実施IPvIにおいて、合成例1で得え塩素化ゴムの代
pに合成例2の塩素化前の未来性エチレン1−2テン共
重合体を用いた以外#i実施例1と全く同様にしてぼり
塩化ビニル組成物tllll L、プレス成層した。測
定結果【第2表に示す。
Comparative Example 1 In IPvI, #i is exactly the same as Example 1 except that the futuristic ethylene 1-2 tenene copolymer before chlorination of Synthesis Example 2 was used instead of the chlorinated rubber obtained in Synthesis Example 1. The fresh vinyl chloride composition tllll L was press laminated. Measurement results [shown in Table 2].

比較例2 冥施fillにお−て、合成例1で得大塩素化ゴムO代
りに塩素化ぼりエチレン(商品名エラスレン301 A
昭和電工M)を用iえ以外は実施例1と全く同様にして
Iり塩化ビニル組成**uJlシ、/レス成型した。測
定結果t−票2表に示す。
Comparative Example 2 Chlorinated ethylene (trade name Elasrene 301 A) was used in place of the large chlorinated rubber O obtained in Synthesis Example 1.
Molding was carried out in exactly the same manner as in Example 1 except that Showa Denko M) was used, except that the polyvinyl chloride composition was molded. The measurement results are shown in Table 2.

実施9$3(1)J塩化ビニル半硬質用途)合成f13
で得た20メ、シm (Tyl@r No、)の金網を
通過するサイズの粉末状の塩素化ゴム100重量部と粉
末状のポリ塩化ビニル(商品名ゼオン103EP  日
本ゼオン製)100重量部と有機Cd −IIs −Z
11系塩化ビニル用安定剤(商品名IJilZ−80J
fp化学all)15重量部、Cd −Zn系安定剤(
商品名LCZ−10堺化学製)0.5重量部及びステア
リン酸カルシウム(和光純系製)1.0重量部【へフシ
エルミキサー中で混合し、更にこの混合物tII面11
11F130〜140℃の8インチμ−ルで5分間混練
した。この混線物を次の条件でプレス成形し各種測定に
供した。その測定結果を第3RK示す。
Implementation 9 $3 (1) J Vinyl chloride semi-rigid use) Synthesis f13
100 parts by weight of powdered chlorinated rubber of a size that can pass through a wire mesh of 20 mm (Tyl@r No.) obtained in step 1 and 100 parts by weight of powdered polyvinyl chloride (trade name: Zeon 103EP, manufactured by Nippon Zeon). and organic Cd-IIs-Z
11 series vinyl chloride stabilizer (trade name IJilZ-80J
fp chemical all) 15 parts by weight, Cd-Zn stabilizer (
0.5 parts by weight of calcium stearate (product name LCZ-10 manufactured by Sakai Chemical) and 1.0 parts by weight of calcium stearate (manufactured by Wako Junkei Co., Ltd.)
The mixture was kneaded for 5 minutes using an 8-inch micrometer of 11F at 130-140°C. This mixed wire was press-molded under the following conditions and subjected to various measurements. The measurement results are shown in the third RK.

(プレス成形条件) 4り塩化ビニル混練物【170℃で3分間予熱し、次に
170℃で2分間、1ookIy112テ熱フレスを行
いその後20℃で5分間、100 kg/am’で冷却
プレスを行う。
(Press molding conditions) Quadrivinyl chloride kneaded material [Preheated at 170°C for 3 minutes, then heat pressed at 170°C for 2 minutes, then cooled at 20°C for 5 minutes at 100 kg/am'. conduct.

比較例3 実施f13にお−て合成例3で得た塩素化ゴムの代pK
、塩素化ポリエチレン(商品名MR104大阪曹這11
)を用いた以外は、実施例3と全く同様にして半硬質−
リ塩化ビニル組成物tlI製しプレス成層してその資性
を測定したell定結果を第3表に示す。
Comparative Example 3 The pK of the chlorinated rubber obtained in Synthesis Example 3 in Example f13
, chlorinated polyethylene (product name MR104 Osaka Soho 11
) was used in the same manner as in Example 3, except that semi-rigid
Table 3 shows the ELL determination results obtained by making a polyvinyl chloride composition tlI, press layering it, and measuring its properties.

比較例4 実施f13において合成例3で得た塩素化ゴム100重
量部の代fiK%ジオクチル7タレー■和光純JIII
調)40重量Wt用%Aた以外は、実施例3六全く同様
にして半硬質fり塩化ビニル組成物を調製し、プレス成
層して、その物性を測定した。
Comparative Example 4 100 parts by weight of chlorinated rubber obtained in Synthesis Example 3 in Example f13 fiK% dioctyl 7 tala ■ Wako Pure JIII
A semi-rigid polyvinyl chloride composition was prepared in exactly the same manner as in Example 36, except that the composition was 40% A for weight Wt, and then press laminated and its physical properties were measured.

測定結果1富3表に示す。The measurement results are shown in Table 1 and 3.

以下余白 実施例4〜6及び比較例5 第4表に示した各種共重合体fAQ混合−1O重量l1
t8インチロール【用−て表面装置80℃で5分間混練
した。ζO混練fゴムG重量St。
The following margins are Examples 4 to 6 and Comparative Example 5 Various copolymers fAQ mixture shown in Table 4-1O weight l1
The mixture was kneaded using a T8-inch roll at 80°C for 5 minutes. ζO kneading f rubber G weight St.

II*状0IIIす塩化ビニル(商品名 ヤオン103
1P日本ゼオン製)100重量部、有機C纏−Ba −
Z+a系塩化11”xル用安定化剤(商品名IJIZ 
−80、堺化学鵬)1.5重量部、Cd −Km系安定
剤(商品名LCD−10,徘化学製)O,S重量部及び
ステアリン酸カルシウム(和光綿I&製)1.01量部
とll!EIIl1gtso〜140C01インチ曹−
ルで5分間混練しえ。
II* Form 0III Vinyl chloride (Product name: Yaon 103
1P Nippon Zeon) 100 parts by weight, organic C-Ba-
Stabilizer for Z+a-based chloride 11”xle (product name: IJIZ)
-80, Sakai Chemical Co., Ltd.) 1.5 parts by weight, Cd-Km stabilizer (trade name LCD-10, manufactured by Waki Kagaku) O, S parts by weight, and calcium stearate (Wako Cotton I & Co., Ltd.) 1.01 parts by weight. ll! EIIl1gtso~140C01 inch carbon-
Knead for 5 minutes.

ζO混混練管実施例1と同様にしてプレスし、各種−*
**定した。結果を第4表に示す。
The ζO kneading tube was pressed in the same manner as in Example 1, and various -*
**Determined. The results are shown in Table 4.

以下余白 昏 手続補正書(自発) 昭和56年lθ月13日 特許庁長官 島1)春樹殿 1、事件の表示 昭和56年 特許願第138616号 2、発明の名称 ポリ塩化ビニル組成物 3、補正をする者 事件との関係 特許出願人 名称(58B)三井石油化学工業株式会社4、代理人 住所 東京都港区虎ノ門−丁目8番10号静光虎ノ門ビ
ル 5、補正の対象 明細書の「発明の詳細な説明」の欄 6、補正の内容 1)明細書第21頁第2表、ポリ塩化ビニル組成物物性
の欄の「サンシャインウェザロタ−ター500時間照射
後」を「サンシャインウェザロタ−ター5’00時間照
射1(25℃)jに補正する。
The following is a blank procedural amendment (spontaneous) dated January 13, 1980 Director General of the Japan Patent Office Shima 1) Haruki-dono 1, Indication of the case 1982 Patent Application No. 138616 2, Title of invention Polyvinyl chloride composition 3, Amendment Relationship with the case of a person who does Column 6, "Detailed explanation of the Sunshine Weather rotor" column 6, contents of correction 1) Table 2, page 21 of the specification, "After 500 hours of irradiation with Sunshine Weather rotor" in the column of physical properties of polyvinyl chloride composition. Corrected to 5'00 hour irradiation 1 (25°C)j.

2)同第21頁jl!2表、ポリ塩化ビニル組成物物性
の欄の「落鍾衝撃強度」をr落鍾衝撃強度(−20℃)
」に補正する。
2) Same page 21 jl! Table 2, "Drop impact strength" in the column of physical properties of polyvinyl chloride compositions r Drop impact strength (-20°C)
”.

以上that's all

Claims (1)

【特許請求の範囲】 l (a)  Iす塩化ビニルと、 (b)  (i)エチレンと1−1テンOモル比が約8
5/1 m〜9!に150範囲にあるエチレンと1−7
”テンとO共重合体fムもしくは(11)エチレンと1
−f゛テン毫ル比が約85/15〜95Aの範囲にある
エチレンと1−yテンと5−エチリデン−2−ノルール
ネンとO共重合体/ A を塩素化して得られる塩素含
有量的5〜50重量襲゛の少なくと4一種の塩素化がム
とから成るぼり塩化ビニル組成物。 L  (a)  Iす塩化ビニルと、 (b)  (1)エチレンと1−2テンO毫ル比が約a
s/1S 〜ms/ISom囲ElるエテL/7と1−
ffンとO共重合体fムもしくは(11)エチレンと1
−2f ンQ4に比が約86/is 〜9615の範1
1にあるエチレンと1−1テンとS−エチリデン−2−
ノルlルネンとO共重合体fAl塩素化して得られる塩
累含有量約5〜50重量襲の少シくとも一種の塩素化が
ムと、 (e)  (1)エチレンとα−オレフィンとの共重合
体fム及び/又Fi(ii>エチレンとα−オレフィン
とfリエンとの共重合体fム とからなるIす塩化ビニル組成物。
[Scope of Claims] l (a) vinyl chloride; (b) (i) ethylene and a 1-1 ten-O molar ratio of about 8;
5/1 m~9! Ethylene in the 150 range and 1-7
"Tene and O copolymer fm or (11) ethylene and 1
-5 in terms of chlorine content obtained by chlorinating ethylene, 1-ytene, 5-ethylidene-2-norrunene and O copolymer/A with a tenyl ratio in the range of about 85/15 to 95A. A vinyl chloride composition comprising at least four types of chlorinated rubber having a weight of ~50% by weight. L (a) Vinyl chloride, (b) (1) Ethylene and 1-2O2 O2 ratio is approximately a
s/1S ~ms/ISom range L/7 and 1-
ff and O copolymer f or (11) ethylene and 1
-2f Q4 has a ratio of approximately 86/is to 9615 range 1
Ethylene, 1-1 thene and S-ethylidene-2- in 1
(e) (1) At least one type of chlorination with a cumulative salt content of about 5 to 50% by weight obtained by chlorinating norl-runene and O copolymer fAl; (e) (1) ethylene and α-olefin; A vinyl chloride composition comprising a copolymer f and/or Fi (ii> copolymer f of ethylene, α-olefin, and f-riene).
JP13861681A 1981-08-04 1981-09-04 Polyvinyl chloride composition Granted JPS5823844A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US289821 1981-08-04
US06/289,821 US4433105A (en) 1980-10-16 1981-08-04 Chlorinated rubber and polyvinyl chloride composition containing the same

Publications (2)

Publication Number Publication Date
JPS5823844A true JPS5823844A (en) 1983-02-12
JPH021181B2 JPH021181B2 (en) 1990-01-10

Family

ID=23113250

Family Applications (3)

Application Number Title Priority Date Filing Date
JP13606581A Granted JPS5823802A (en) 1981-08-04 1981-09-01 Chlorinated rubber
JP13861681A Granted JPS5823844A (en) 1981-08-04 1981-09-04 Polyvinyl chloride composition
JP5636889A Pending JPH01272602A (en) 1981-08-04 1989-03-10 Chlorinated rubber

Family Applications Before (1)

Application Number Title Priority Date Filing Date
JP13606581A Granted JPS5823802A (en) 1981-08-04 1981-09-01 Chlorinated rubber

Family Applications After (1)

Application Number Title Priority Date Filing Date
JP5636889A Pending JPH01272602A (en) 1981-08-04 1989-03-10 Chlorinated rubber

Country Status (1)

Country Link
JP (3) JPS5823802A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61185553A (en) * 1985-02-13 1986-08-19 Sumitomo Chem Co Ltd Thermoplastic elastomer composition

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5823802A (en) * 1981-08-04 1983-02-12 Mitsui Petrochem Ind Ltd Chlorinated rubber
JPS601501U (en) * 1983-06-17 1985-01-08 住友電気工業株式会社 Small cemented carbide roll

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5823802A (en) * 1981-08-04 1983-02-12 Mitsui Petrochem Ind Ltd Chlorinated rubber

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61185553A (en) * 1985-02-13 1986-08-19 Sumitomo Chem Co Ltd Thermoplastic elastomer composition
JPH0588268B2 (en) * 1985-02-13 1993-12-21 Sumitomo Chemical Co

Also Published As

Publication number Publication date
JPH021181B2 (en) 1990-01-10
JPS5823802A (en) 1983-02-12
JPH01272602A (en) 1989-10-31
JPH0142284B2 (en) 1989-09-12

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