JPS59102902A - Production of chlorinated copolymer - Google Patents
Production of chlorinated copolymerInfo
- Publication number
- JPS59102902A JPS59102902A JP21205383A JP21205383A JPS59102902A JP S59102902 A JPS59102902 A JP S59102902A JP 21205383 A JP21205383 A JP 21205383A JP 21205383 A JP21205383 A JP 21205383A JP S59102902 A JPS59102902 A JP S59102902A
- Authority
- JP
- Japan
- Prior art keywords
- methylpentene
- copolymer
- chlorinated
- give
- olefin
- 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
Links
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は塩素化α−オレフィン・4−メチルペンテン−
1共重合体の製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention provides chlorinated α-olefin 4-methylpentene-
The present invention relates to a method for producing a copolymer.
本出願人は先に260℃、5 Kyにお(プるメルトイ
ンデックスが8〜70g/10n+in (ASTM
D1238−65T)である結晶性のポリ−4−メチル
ペンテン−1を溶液状態で塩素含有m50重量%以上に
均一塩素化してなる塩素化ポリ4−メチルペンテン−1
であることを特徴とする塩素化重合体の製造方法(特願
昭54−153909号)及びコーチング組成物(分割
出願:特願昭57−211684) 、更にはメルトイ
ンデックス(条件:温度260℃、圧力5に9/cm
)が8〜70g/10m1n (ASTMD1238−
65T)である結晶性ポリ4−メチルペンテン−1を塩
素化度50〜70重1%の範囲で塩素化した塩素化ポリ
4−メチルペンテン−1を塩素化ポリオレフィン樹脂1
00重量部に対して少なくとも5重聞部以上併用したこ
とを特徴とする耐熱性コーチング組成物(特願昭55−
037997号)を開発したが、本発明はこれの拡張に
係わる塩素化共重合体の製造方法を提供したものである
。The present applicant previously tested the product at 260°C and 5 Ky (with a melt index of 8 to 70 g/10n+in (ASTM
Chlorinated poly-4-methylpentene-1 obtained by uniformly chlorinating crystalline poly-4-methylpentene-1 (D1238-65T) in a solution state to a chlorine content of 50% by weight or more.
A method for producing a chlorinated polymer (Japanese Patent Application No. 54-153909), a coating composition (divisional application: Japanese Patent Application No. 57-211684), and a melt index (conditions: temperature 260°C, Pressure 5 to 9/cm
) is 8~70g/10m1n (ASTMD1238-
Chlorinated poly(4-methylpentene-1) obtained by chlorinating crystalline poly(4-methylpentene-1), which is
A heat-resistant coating composition characterized in that it is used in combination with at least 5 parts per 00 parts by weight (Japanese Patent Application No. 1973-
No. 037997), and the present invention provides a method for producing a chlorinated copolymer that is an extension of this method.
特願昭54−153909号において出願人は結晶性の
ポリ4−メチルペンテン−1を溶液状態において塩素含
有量50重量%以上に均一塩素化することににり従来公
知の塩素化ポリマーと比較して、その熱安定性と熱軟化
性に関して格段にすぐれた物質を冑 lこ。In Japanese Patent Application No. 54-153909, the applicant uniformly chlorinated crystalline poly-4-methylpentene-1 in a solution state to a chlorine content of 50% by weight or more, and compared it with conventionally known chlorinated polymers. Therefore, we have created a material that has significantly superior thermal stability and thermal softening properties.
出願人は更に、4−メチルペンテン−1を主たる七ツマ
−とし、その他のαオレフイン類一種以上をモノマーと
じて、デーグラ−ナツタ系触媒による立体規則性重合に
よって生成させたところの共重合イホ類の塩素化を検問
したところ、共重合しているその曲のα−オレフィンモ
ノマーの吊が20モル%以内では、その溶液法均−塩素
化物の諸性状がはず結晶性のボモボリ4−メヂルペンテ
ンー1の溶液法均−塩素化物に匹敵゛りると言う予期U
ざる結果を見出して本発明をなすに至った。The applicant has further disclosed copolymerized iphos produced by stereoregular polymerization using a Daegler-Natsuta catalyst using 4-methylpentene-1 as the main heptamer and one or more other α-olefins as monomers. When the chlorination of the copolymerized α-olefin monomer was within 20 mol%, the properties of the solution-method chlorinated product were found to be that of crystalline Vomoboly 4-methylpentene-1. Solution method - expected to be comparable to chlorinated products
The present invention was realized based on these results.
出願人はづでに塩素化ポリ4−メタルペンテン−1を、
他のより軟化温度の低い塩素化ポリα−オレフィン類(
ジオレフィンを含む)と配合づることにJ:りその配合
物が予想外の熱軟化抵抗性と熱変色抵抗性を示づことを
見出しているが(特願昭55−037997号)、これ
笠の場合は当然のことながら得られる配合物の性状は純
品のJn素化ポリ4−メチルペンテン−1のそれには1
歩も2歩も劣るものであった。しかるに共重合体の塩素
化物においては共重合しているその他の1種以上のα−
オレフィンの合計量が20モル%以内のものでは、得ら
れる塩素化共重合体の性状は塩素化小モボリ4−メチル
ペンテン−1重合体のそれにくらべ実質上遜色なく、そ
の上これら共重合体は四塩化炭素への溶解性にすぐれて
いるので、溶液法均−塩素化物を冑ることがその沸点以
下でさえ容易に実施出来て経済上極めて有利であるとい
う利点もある。The applicant has already prepared chlorinated poly-4-metalpentene-1,
Other chlorinated polyα-olefins with lower softening temperatures (
J: found that a blend of riso (including diolefin) showed unexpected heat softening resistance and heat discoloration resistance (Japanese Patent Application No. 55-037997); Naturally, in the case of
He was inferior by a step or two. However, in the case of chlorinated copolymers, one or more other copolymerized α-
When the total amount of olefins is within 20 mol%, the properties of the resulting chlorinated copolymers are substantially comparable to those of chlorinated small 4-methylpentene-1 polymers; Since it has excellent solubility in carbon tetrachloride, it also has the advantage that it can easily dissolve chlorinated compounds in a solution method even below its boiling point, which is extremely advantageous economically.
得られた塩素化物は前記の特願昭54−153909号
および「接着剤組成物」 (特願昭55−128104
号)等に記載の発明と同様に、その熱分解抵抗性と高い
熱軟化湿度、良好な耐候性を生かして、単独或いは各種
仙物質と配合して、耐熱性インキ、OPニス、塗料等の
コーチング組成物として有用であり、またゴム系接着剤
と配合して、その接着強度と耐熱クリープ性が向上した
接着剤組成物を製することかできた。The obtained chlorinated product is used in the above-mentioned Japanese Patent Application No. 54-153909 and "Adhesive Composition" (Japanese Patent Application No. 128104-1982).
Similar to the invention described in No. 1, etc., by taking advantage of its thermal decomposition resistance, high heat softening humidity, and good weather resistance, it can be used alone or in combination with various substances to produce heat-resistant inks, OP varnishes, paints, etc. It was possible to produce an adhesive composition that is useful as a coating composition and has improved adhesive strength and heat creep resistance by blending with a rubber adhesive.
更に本発明の塩素化共重合体は前記の特願昭55−03
7997号に記載されているが如き、その他の塩素化ポ
リオレフィン類との(7f用に際しても、塩素化ホモポ
リ4−メチルペンテン−1とはゞ同等の成果を示づ。Furthermore, the chlorinated copolymer of the present invention is disclosed in the above-mentioned Japanese Patent Application No. 55-03.
Even when used for 7f, chlorinated homopoly-4-methylpentene-1 shows comparable results with other chlorinated polyolefins such as those described in No. 7997.
共重合するα−オレフィンの例としてはエチレン、プロ
ピレン等の短鎖モノマーの場合も、オクタアセンの如き
長jf1モノマーの場合も共に本発明品の特色をそなえ
ていることが実験的に確かめられている。As examples of α-olefins to be copolymerized, it has been experimentally confirmed that both short chain monomers such as ethylene and propylene and long jf1 monomers such as octaacene have the characteristics of the product of the present invention. .
以下に本発明を実施例に基づき説明覆る。The present invention will be explained below based on examples.
実施例1
4−メチルペンテン−195mo1%とデセン−15m
o1%をチーグラーナツタ系触媒による立体規則性重合
によって生成させた、ヌル1〜インデツクスが8g/1
0m1n (ASTMD1238−65T)の1−デ
セン・4−メチルペンテン−1の共重合物を200gと
り5ぶの四塩化炭素を加え、常圧下にa3いて四塩化炭
素の沸点(78°C)で十分に溶解した後、エアーパー
ジした後、光を照剣しつ)ガス状の塩素を反応器底部か
ら吹ぎ込んで常圧下(温度78°C)で塩素化を行なっ
た。Example 1 4-methylpentene-195mol% and decene-15m
O1% was produced by stereoregular polymerization using a Ziegler-Natsuta catalyst, and the null 1 to index was 8 g/1.
Take 200g of 1-decene/4-methylpentene-1 copolymer of 0mln (ASTMD1238-65T), add 5 parts of carbon tetrachloride, and heat at the boiling point of carbon tetrachloride (78°C) under normal pressure. After dissolving in the reactor, gaseous chlorine was blown into the reactor from the bottom after air purging and chlorination was carried out under normal pressure (temperature 78° C.).
この際の塩素化所要時間は12時間を要したが、特願昭
54−15909号のうちメルトインデックスが同値で
あるホモポリマーの塩素化所要時間、15時間に比べ短
時間で塩素化が行なわれた。The time required for chlorination in this case was 12 hours, but the chlorination was completed in a shorter time than the 15 hours required for chlorination of a homopolymer with the same melt index as described in Japanese Patent Application No. 54-15909. Ta.
実施例2
4−メチルペンテン−194mo1%とヘキサデセン−
13mo1%とオクタデセン−13mo1%をチーグラ
ーナツタ系触媒による立体規則性重合によって生成させ
た、ヌル1〜インデツクスが70’J / iomin
(A S TM D 1238−65T )の4−メ
チルペンテン・ヘキザデ′セン・オクタデセン共重合物
を200gとり5(の四塩化炭素を加え、常圧下におい
て四塩化炭素の沸点(78℃)で十分に)a解した後、
エアーパージした後、光を照r1」シっ)カス状の塩素
を反応器底部から吹き込んで常圧下(温度78℃)で塩
素化を行なった。Example 2 4-methylpentene-194mol1% and hexadecene-
13 mo1% and octadecene-13 mo1% were produced by stereoregular polymerization using a Ziegler-Natsuta catalyst, and the null 1 to index was 70'J/iomin.
Take 200 g of 4-methylpentene/hexade'cene/octadecene copolymer (A STM D 1238-65T), add carbon tetrachloride of 5 (5), and heat the solution at the boiling point of carbon tetrachloride (78°C) under normal pressure. ) a After understanding,
After air purging, chlorine in the form of scum was blown into the reactor from the bottom of the reactor under a light beam and chlorination was carried out under normal pressure (temperature 78° C.).
この際の」n素化所要時間は6時間を要したが、特願昭
54−15909号のうちメルトインデックスが同値で
あるホモポリマーの塩素化所要時間、8時間に比べ短時
間で塩素化が行なわれた。In this case, the time required for chlorination was 6 hours, but the chlorination was completed in a shorter time than the 8 hours required for chlorination of a homopolymer with the same melt index in Japanese Patent Application No. 54-15909. It was done.
実施例1及び2において特2願昭54−153909号
の場合、四塩化炭素の沸点以下におけるホモポリマーの
溶解は困難(長0.″i間を要1−)で均−jM素化を
保証−4るため、かつ経済的実用性からは加圧下、Th
J1点以上での溶解と、少なくとも塩素化の初期では加
圧下での塩素化が好ましかった。In Examples 1 and 2, in the case of Japanese Patent Application No. 54-153909, it is difficult to dissolve the homopolymer below the boiling point of carbon tetrachloride (length 0.''i is required 1-), and homogeneous -jM reduction is guaranteed. -4, and from the viewpoint of economical practicality, Th
Dissolution at the J1 point or higher and chlorination under pressure were preferred at least at the initial stage of chlorination.
しかし、本発明の場合はコポリマーの大部分は四塩化炭
素の沸点く常圧)においても容易に溶解し、また反応の
初期からあえて加圧下で塩素化を行なわなくとも均−j
福素化が実施できた。However, in the case of the present invention, most of the copolymer is easily dissolved even at normal pressure (at the boiling point of carbon tetrachloride), and the copolymer can be uniformly dissolved without chlorination under pressure from the initial stage of the reaction.
Fukusoification was implemented.
各種のポリ4−メチルペンテン−1系ポリマーの塩素化
を実施例1及び2と同様の方法で行ないその性状を表−
1に示した。Various poly-4-methylpentene-1-based polymers were chlorinated in the same manner as in Examples 1 and 2, and their properties are shown in the table below.
Shown in 1.
表−1かられかるように本発明物質は実買上、特願昭5
4−153909号物質に遜色のない性状を右している
。As can be seen from Table 1, the substance of the present invention is commercially available and patent application filed in 1973.
It has properties comparable to those of substance No. 4-153909.
比較例どしてヌル1−インデックスが8g/10m1n
AS TMD−1238−65T ) rアロホーE
ホ!J 4−メヂルベンテン−1の塩素化物を示した。Comparative example: Null 1-index is 8g/10m1n
AS TMD-1238-65T) r Aloho E
Ho! J shows a chlorinated product of 4-methylbentene-1.
表−にあける各種測定方法の説明
軟化温度:融点測定装置により測定
熱変色性=180℃、30分後の加熱変色インキ ;イ
ンキ而にコート原紙を置き各温度に耐熱性 設定した
ヒートシールバーを当てプレスした後、30分以上放冷
、これを剥がしたときの紙むけ状態で判定した。Explanation of various measurement methods in the table Softening temperature: Measured by melting point measuring device Thermochromic property = 180℃, discoloration ink heated after 30 minutes; Place coated base paper on the ink and heat seal bar set at each temperature. After pressing, it was left to cool for 30 minutes or more, and the paper was judged by the peeled state when it was peeled off.
◎・・・・・・紙むけなし O・・・・・・5%以下
△・・・・・・30%以下 ×・・・・・・50%
以上OPニス:市販の塩素化パラフィン(トヨバラA鉛
筆硬度 −40:東洋ソーダ(株)製)を20重量部配
合したOPニスを調製しフィルム
化した後鉛筆硬度を測定。◎・・・No paper peeling O・・・・・・5% or less △・・・30% or less ×・・・・・・50%
OP varnish: An OP varnish containing 20 parts by weight of commercially available chlorinated paraffin (Toyobara A pencil hardness -40: manufactured by Toyo Soda Co., Ltd.) was prepared, formed into a film, and then its pencil hardness was measured.
Claims (1)
つチーグラーナツタ系触媒による立体規則性重合によっ
て生成した4−メチルペンテン−1とその他のα−オレ
フィンモノマーとの共重合体を、溶液状態で塩素含有0
50重量%以上に均一塩素化してなる塩素化α−オレフ
ィン・4−メチルペンテン−1共重合体である′ことを
特徴とする塩素化共重合体の製造方法A copolymer of 4-methylpentene-1 and other α-olefin monomers produced by stereoregular polymerization with 4-methylpentene-1 as the main constituent monomer using a Ziegler-Natsuta catalyst is prepared in a solution state with zero chlorine content.
A method for producing a chlorinated copolymer, which is a chlorinated α-olefin/4-methylpentene-1 copolymer obtained by uniformly chlorinating 50% by weight or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21205383A JPS5942003B2 (en) | 1983-11-11 | 1983-11-11 | Method for producing chlorinated copolymer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21205383A JPS5942003B2 (en) | 1983-11-11 | 1983-11-11 | Method for producing chlorinated copolymer |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13956980A Division JPS5921346B2 (en) | 1980-10-06 | 1980-10-06 | Compositions using chlorinated copolymers |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59102902A true JPS59102902A (en) | 1984-06-14 |
| JPS5942003B2 JPS5942003B2 (en) | 1984-10-12 |
Family
ID=16616079
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21205383A Expired JPS5942003B2 (en) | 1983-11-11 | 1983-11-11 | Method for producing chlorinated copolymer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5942003B2 (en) |
-
1983
- 1983-11-11 JP JP21205383A patent/JPS5942003B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5942003B2 (en) | 1984-10-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP3333214B2 (en) | LLDPE blends with ethylene-norbornene copolymers for resins with improved toughness and processability for film production | |
| JP3386186B2 (en) | Concentrate suitable for the production of functionalized polyolefins and a method of functionalization using this concentrate | |
| JP4291512B2 (en) | Use of block chlorinated polyolefins as impact modifier compatibilizers for PVC or CPVC and methods for their production | |
| US3577365A (en) | Novel blends of chlorinated carboxyl group containing polymers and ethylene-vinyl acetate copolymers | |
| BRPI0619788A2 (en) | processes for preparing a reaction product, reaction product containing funiconised polypropylene, hot melt polymer solution, polypropylene film, molded article of manufacture and hot melt adhesive | |
| US4312964A (en) | Polyolefin resin composition | |
| US3256365A (en) | Composition comprising polyethylene and oxidation products of polyethylene and articles thereof | |
| PT690891E (en) | POLYMERIC COMPOSITIONS BASED ON HIGHLY PROCESSABLE LLDPE | |
| WO1992002668A1 (en) | Solution of ultra-high molecular weight polyethylene | |
| JPS61501782A (en) | Modification of LLDPE by peroxide treatment | |
| DE102007007793A1 (en) | Process for producing a thermoplastic resin composition | |
| JPS6215092B2 (en) | ||
| DE69513864T2 (en) | Use of polyketone / HDPE mixtures | |
| JPS59102902A (en) | Production of chlorinated copolymer | |
| US20060217490A1 (en) | Polyethylene compositions having improved printability | |
| JPH0113486B2 (en) | ||
| JPS5921346B2 (en) | Compositions using chlorinated copolymers | |
| US3356638A (en) | Oxychloropolyethylene coating | |
| US5310809A (en) | Arylcyclobutene grafted polyolefins | |
| US20080103260A1 (en) | Polyethylene compositions having improved printability | |
| JPH026513A (en) | Modified polyolefin polymer | |
| JPH0344090B2 (en) | ||
| US5116896A (en) | Photo-degradable heat resistant resin composition | |
| JPS58120608A (en) | Manufacturing method of modified polyolefin | |
| JPS596241A (en) | Extrusion-coating resin composition |