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JPH0132857B2 - - Google Patents
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JPH0132857B2 - - Google Patents

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Publication number
JPH0132857B2
JPH0132857B2 JP56135508A JP13550881A JPH0132857B2 JP H0132857 B2 JPH0132857 B2 JP H0132857B2 JP 56135508 A JP56135508 A JP 56135508A JP 13550881 A JP13550881 A JP 13550881A JP H0132857 B2 JPH0132857 B2 JP H0132857B2
Authority
JP
Japan
Prior art keywords
block copolymer
compound
block
weight
styrene
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
Application number
JP56135508A
Other languages
Japanese (ja)
Other versions
JPS5837044A (en
Inventor
Katsuhiko Yamamoto
Tatsuo Isoko
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.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo KK
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
Application filed by Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP13550881A priority Critical patent/JPS5837044A/en
Publication of JPS5837044A publication Critical patent/JPS5837044A/en
Publication of JPH0132857B2 publication Critical patent/JPH0132857B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はスチレン化合物と共役ジエン化合物と
のブロツク共重合樹脂、さらに詳しくは重量平均
分子鎖長(以下、平均分子鎖長と略す)及びスチ
レン化合物と共役ジエン化合物との比が異る2種
のスチレン化合物と共役ジエン化合物とのブロツ
ク共合体(以下SBブロツク共重合体という)を
主成分とする透明性、耐衝撃性及び熱安定性にす
ぐれたブロツク共重合樹脂に関する。 従来からSBブロツク共重合樹脂は透明性、耐
衝撃性にすぐれ、射出、押出などの成形法によつ
て成形され、種々の分野で広く用いられている。 通常、SBブロツク共重合樹脂は非極性溶媒中
で有機リチウム化合物の存在下、50重量%以上の
スチレン化合物と共役ジエン化合物とを重合させ
る手段などによつて製造されているが、これらの
手段によつて得られたSBブロツク共重合樹脂は
成形時の熱安定性、及び耐衝撃性が充分でなく、
これら物性の向上が要望されていた。 このようなSBブロツク共重体樹脂の透明性を
維持しつつ、その耐衝撃性を向上させる方法とし
ては、例えばSBブロツク共重合樹脂を製造する
際に共役ジエン化合物量を増加し、SBブロツク
共重合体中の共役ジエン化合物比を増加させる方
法などがある。しかしこの方法によつて得られた
SBブロツク共重合体は成形加工の段階において、
共役ジエン化合物が熱的に不安定となり、ゲル化
現象を起し、熱安定性が低いという問題があつ
た。 本発明者らはこれらのSBブロツク共重合体の
透明性を維持しながら、熱安定性と耐衝撃性を改
良することについて鋭意研究を行つた結果、SB
ブロツク共重合体中の共役ジエン化合物の含有量
を20%以下に押えれば熱安定性は改良されるがこ
れだけでは充分でなく、これに更に共役ジエン化
合物の含有量が前記のものよりも多く、しかもよ
り低分子量のSBブロツク共重合体を配合すれば、
耐衝撃性も改良され、従来のSBブロツク共重合
体の問題点を解決することができるという知見を
得て本発明を完成するに至つた。 すなわち、本発明は平均分子鎖長が600〜1400
Å、スチレン化合物比が50〜70重量%に制御され
たブロツク共重合体(A)と平均分子鎖長が3600〜
6000Å、スチレン化合物比が80〜95重量%に制御
されたブロツク共重合体(B)とを(A)/(B)が重量比で
1以下になるように混合した樹脂である。 本発明においてはスチレン化合物とはスチレン
の他α−メチルスチレン、ビニルトルエン、tert
−ブチルスチレン等のビニル芳香族化合物及びそ
の置換体を含む。また、共役ジエン化合物として
はブタジエン、クロロプレン、イソプレン等が挙
げられる。 ブロツク共重合体(A)のスチレン化合物の含有量
が50重量%以下になると(A)及び(B)の混合物の透明
性が著しく低下し、70重量%を越えると耐衝撃性
を向上させることができない。一方、ブロツク共
重合体(B)のスチレン化合物含有量が80重量%以下
では熱安定性が低下し、95重量%を越えると透明
性が著しく低下する。 また、ブロツク共重合体(A)の平均分子鎖長が
600Å以下では(A)、(B)混合物の耐衝撃性が低下し、
1400Å以上では熱安定性が低下する。一方、ブロ
ツク共重合体(B)の平均分子鎖長が3600Å以下では
衝撃強度が改良されず、6000Åを越えると成形加
工が困難となる。 なお、ブロツク共重合体(A)及び(B)の平均分子鎖
長の調節は重合開始剤の有機リチウム化合物の使
用量を調節する一般的方法によつて達成される。 平均分子鎖長はゲル・パーミエーシヨン・クロ
マトグラフイー(以下GPCという)により測定
した。これを具体的に説明すると、Waters社製
の単分散ポリスチレンのGPCにより、そのピー
クカウント数と単分散ポリスチレンの分子鎖長と
の検量線を作成し、上記サンプルのGPCのパタ
ーンのピークカウント数に対応する分子鎖長を検
量線から読みとる方法によつて決められる。 ブロツク共重合体(A)と(B)を混合するにあたつて
は(A)/(B)の重量比が1以下がよく、好ましくは
0.8以下である。1を越えると(A)、(B)混合物、す
なわち、SBブロツク共重合体の透明性が低下し、
又剛性も低下し著しく軟質化するので好ましくな
い。 本発明に係るブロツク共重合体は、構造的には
一般構造式、(A−B)o又は(A−B)o−A(Aは
スチレン化合物重合体のブロツクを、Bは共役ジ
エン重合体のブロツクを、nは正の整数を表わ
す)で表わされる線型ブロツク共重合体、あるい
はUSP−3639517に記載された一般構造式
The present invention relates to a block copolymer resin of a styrene compound and a conjugated diene compound, and more specifically, two kinds of block copolymer resins having different weight average molecular chain lengths (hereinafter referred to as average molecular chain lengths) and ratios of styrene compounds and conjugated diene compounds. This invention relates to a block copolymer resin having excellent transparency, impact resistance, and thermal stability, the main component of which is a block copolymer of a styrene compound and a conjugated diene compound (hereinafter referred to as SB block copolymer). Conventionally, SB block copolymer resins have excellent transparency and impact resistance, are molded by molding methods such as injection and extrusion, and are widely used in various fields. Normally, SB block copolymer resins are produced by polymerizing 50% by weight or more of a styrene compound and a conjugated diene compound in the presence of an organolithium compound in a nonpolar solvent. The resulting SB block copolymer resin had insufficient thermal stability and impact resistance during molding.
Improvements in these physical properties have been desired. One way to improve the impact resistance of such SB block copolymer resins while maintaining their transparency is to increase the amount of conjugated diene compound when producing SB block copolymer resins. There are methods of increasing the ratio of conjugated diene compounds during coalescence. However, obtained by this method
During the molding process, the SB block copolymer
There was a problem that the conjugated diene compound became thermally unstable and caused a gelation phenomenon, resulting in low thermal stability. The present inventors conducted extensive research on improving the thermal stability and impact resistance of these SB block copolymers while maintaining their transparency.
If the content of the conjugated diene compound in the block copolymer is kept below 20%, the thermal stability will be improved, but this alone is not sufficient; , and if a lower molecular weight SB block copolymer is added,
The present invention was completed based on the knowledge that the impact resistance was improved and the problems of conventional SB block copolymers could be solved. That is, the present invention has an average molecular chain length of 600 to 1400.
Å, block copolymer (A) with a styrene compound ratio controlled to 50-70% by weight and an average molecular chain length of 3600-
6000 Å, and a block copolymer (B) with a styrene compound ratio controlled to 80 to 95% by weight, is mixed so that the weight ratio of (A)/(B) is 1 or less. In the present invention, styrene compounds include styrene, α-methylstyrene, vinyltoluene, tert
-Includes vinyl aromatic compounds such as butylstyrene and substituted products thereof. Moreover, butadiene, chloroprene, isoprene, etc. are mentioned as a conjugated diene compound. If the content of the styrene compound in the block copolymer (A) is less than 50% by weight, the transparency of the mixture of (A) and (B) will decrease significantly, and if it exceeds 70% by weight, the impact resistance will be improved. I can't. On the other hand, if the styrene compound content of the block copolymer (B) is less than 80% by weight, the thermal stability will be reduced, and if it exceeds 95% by weight, the transparency will be significantly reduced. In addition, the average molecular chain length of the block copolymer (A) is
Below 600Å, the impact resistance of the mixtures (A) and (B) decreases,
At 1400 Å or more, thermal stability decreases. On the other hand, if the average molecular chain length of the block copolymer (B) is less than 3,600 Å, the impact strength will not be improved, and if it exceeds 6,000 Å, molding becomes difficult. The average molecular chain length of the block copolymers (A) and (B) can be adjusted by a general method of adjusting the amount of the organolithium compound used as a polymerization initiator. The average molecular chain length was measured by gel permeation chromatography (hereinafter referred to as GPC). To explain this specifically, we created a calibration curve between the peak count number and the molecular chain length of monodisperse polystyrene using GPC of monodisperse polystyrene manufactured by Waters, and calculated the peak count number of the GPC pattern of the above sample. It is determined by the method of reading the corresponding molecular chain length from the calibration curve. When mixing block copolymers (A) and (B), the weight ratio of (A)/(B) is preferably 1 or less, preferably
It is 0.8 or less. When it exceeds 1, the transparency of the mixture of (A) and (B), that is, the SB block copolymer, decreases,
In addition, the rigidity decreases and the material becomes extremely soft, which is not preferable. The block copolymer according to the present invention has a general structural formula (A-B) o or (A-B) o -A (A is a block of a styrene compound polymer, and B is a conjugated diene polymer). (n represents a positive integer) or the general structural formula described in USP-3639517.

【式】又は[Formula] or

【式】で表わされる星型 ブロツク共重合体であり、またブロツクの構造と
しては完全にブロツク構造あるいは特開昭48−
48546に見られる如く、ブロツクAとブロツクB
の遷移部にABランダム共重合体部分を含有し
た、いわゆるテーパーブロツク構造のいずれでも
良いが、特にテーパーブロツク構造のものが有利
である。 これらのブロツク共重合体は一般的に、非極性
溶媒中で、有機リチウム化合物を開始剤として、
脱水精製されたスチレン化合物および共役ジエン
を共重合させることによつて得られるが、重合手
法の相違により、上記の各種構造の重合体を得る
ことができる。 非極性溶媒としてはペンタン、ヘキサン、ヘプ
タン等の脂肪族炭化水素、シクロヘキサン、メチ
ルシクロヘキサン、シクロペンタン等の脂環式炭
化水素、ベンゼン、トルエン、キシレン等の芳香
族炭化水素であり、また、開始剤として使用され
る有機リチウム化合物としては、n−ブチルリチ
ウム、sec−ブチルリチウム等のアルキルリチウ
ム、ブタジエンオリゴマ−ジリチウム、α−メチ
ルスチレンテトラマ−ジリチウム等が用いられる
が、特にsec−ブチルリチウムが有効である。 まず、本発明で最も好ましいとされるテーパー
ブロツク構造をもつ重合体は、オートクレーブに
脱水された非極性溶媒と、開始剤として所定量の
有機リチウム化合物を入れ、次いで、脱水精製し
た所定量のスチレン化合物を添加してスチレン化
合物のブロツクを形成させ、次いで、残りのスチ
レン化合物と共役ジエンを同時に添加することに
より、共役ジエンとスチレン化合物のテーパー構
造をもつたブロツクを連結させることによつて製
造される。 又、完全ブロツク構造をもつた重合体は、例え
ば上記の製造法に於いて、スチレン化合物と共役
ジエンを同時に添加せずにまず共役ジエンのみを
重合させ、引続き、スチレン化合物のみを重合さ
せることによつて得ることができる。 更に星型のブロツク構造をもつ重合体は、まず
スチレン化合物のブロツク、引続き、共役ジエン
のブロツクを形成させたあと、多官能性のカツプ
リング剤(例えばCHBr3、SiCl4など)を添加し、
反応させることによつて製造することができる。 このように限定された範囲にあるブロツク共重
合体(A)及び(B)の混合及び溶媒除去の方法とその順
序はどのように行なつても良いが、各重合体の重
合液を均一混合した後溶媒除去を行なう方式が最
も好ましい。このようにして得られたブロツク共
重合体樹脂組成物は、射出成形により各種成形品
に加工されたり、押出成形によつてシートあるい
はフイルムに加工される。また耐衝撃性及び熱安
定性が著しく改良されたものであるのでポリスチ
レンの衝撃性改良剤として、更には熱的環境の厳
しい高温高速成形等の分野にも利用することがで
きる。 以下実施例を挙げて本発明を具体的に説明す
る。 実施例 1 100のオートクレーブに脱水精製したベンゼ
ン80を仕込み、これにsec−ブチルリチウム440
mmolを添加し、温度40℃に保持した。次に重合
反応の第1段階用スチレンモノマー(以下SM−
1と略記する)を4.4Kg投入し重合を完結させた。
次に重合反応の第2段階用のブタジエン(以下
Bd−2と略記する)及びスチレンモノマー(以
下SM−2と略記する)をそれぞれ9Kg、6.6Kg混
合した状態で一括投入し、重合を完結させた。そ
の後重合液に少量のアルコールを添加し、重合を
停止させブロツク共重合体(A)の重合液を得た。こ
の試料を共重合体(A−1)とした。共重合体
(A−1)はA−B/Aの構造(Aはスチレンの
ブロツク、Bはブタジエンのブロツク、B/Aは
両ブロツクの境界がテーパー構造であることを示
す)を有する。 更にsec−ブチルリチウム110mmol、SM−1
を6.8Kg、Bd−2を3Kg、SM−2を10.2Kgとした
以外はブロツク共重合体(A)の製法と同様にしてブ
ロツク共重合体(B)の重合液を得、この試料を共重
合体(B−1)とした。共重合体(B−1)は共
重合体(A−1)と同様のポリマー構造を有す
る。 共重合体(A−1)の重合液50と共重合体
(B−1)の重合液100を混合撹拌した後、スチ
ームストリツピングを行い混合物をクラム状に折
出させ、熱風乾燥機で乾燥した。次いでこの乾燥
クラムに対し2・6−ジ−tertブチル−4−メチ
ルフエノール0.5重量部、トリスノニルフエニル
フオスフアイト0.3重量部、ステアリン酸0.2重量
部を添加して後、押出機にてペレツトとした。こ
のペレツトの物性を測定し、その結果を表1に示
した。 実施例2、3及び比較例1〜4 SM−1、Bd−2、SM−2及び開始剤を表1
に示す割合で使用した以外は実施例1と同様にし
てブロツク共重合体(A)を得、これを共重合体(A
−2)及び(A−3)とした。 別にSM−1、Bd−2、SM−2及び開始剤を
表1に示す割合で使用した以外は実施例1と同様
にしてブロツク共重合体(A)を得、これを(A−
4)ないし(A−7)とした。 (A−2)及び(A−3)を実施例2、3と
し、(A−4)ないし(A−7)を順次比較例1
ないし4とし、ブロツク共重合体(B−1)と表
1に示す割合に混合し、実施例1と同様にしてペ
レツトを作り、その物性を測定し、表1に示し
た。 なお、以下の表中、物性の測定は下記の方法に
よつた。 曇度…射出成形機を用い、200℃で2mm厚のプレ
ートを成形し、これをASTM−D−1003の方
法により測定した。 落錘強度…射出成形機を用い200℃で3mm厚、4
cm×4cmのプレートを成形し、20℃の雰囲気に
おいて、先端のRが5m/mφの錘を重量及び
高さを変えて落下させ、破壊の起らない最高の
高さを求め重量×高さで表示した。 熱安定性…射出成形機を用い、250℃で3mm厚の
プレートを連続成形し、1シヨツト目と20シヨ
ツト目の表面光沢を測定し、光沢の低下差(△
G)を測定した。
It is a star-shaped block copolymer represented by the formula [Formula], and the block structure is completely block structure or
As seen in 48546, block A and block B
It may have any so-called tapered block structure containing an AB random copolymer portion in the transition region, but a tapered block structure is particularly advantageous. These block copolymers are generally prepared by using an organolithium compound as an initiator in a non-polar solvent.
Although it can be obtained by copolymerizing a dehydrated and purified styrene compound and a conjugated diene, polymers with various structures described above can be obtained by using different polymerization techniques. Examples of nonpolar solvents include aliphatic hydrocarbons such as pentane, hexane, and heptane, alicyclic hydrocarbons such as cyclohexane, methylcyclohexane, and cyclopentane, and aromatic hydrocarbons such as benzene, toluene, and xylene. Examples of organic lithium compounds used as organic lithium compounds include alkyllithiums such as n-butyllithium and sec-butyllithium, butadiene oligomer dilithium, α-methylstyrene tetramer dilithium, etc., but sec-butyllithium is particularly effective. It is. First, a polymer with a tapered block structure, which is considered to be the most preferable in the present invention, is prepared by adding a dehydrated nonpolar solvent and a predetermined amount of an organic lithium compound as an initiator to an autoclave, and then adding a predetermined amount of dehydrated styrene. It is produced by adding a compound to form a block of a styrene compound, and then simultaneously adding the remaining styrene compound and a conjugated diene to connect the tapered block of the conjugated diene and the styrene compound. Ru. Furthermore, a polymer having a completely block structure can be obtained by, for example, using the above production method, by first polymerizing only the conjugated diene without adding the styrene compound and the conjugated diene at the same time, and then polymerizing only the styrene compound. You can get it by twisting it. Furthermore, a polymer with a star-shaped block structure can be obtained by first forming a styrene compound block, then a conjugated diene block, and then adding a polyfunctional coupling agent (for example, CHBr 3 , SiCl 4 , etc.).
It can be produced by reaction. Although the method and order of mixing the block copolymers (A) and (B) within a limited range and removing the solvent may be carried out in any manner, it is important to uniformly mix the polymer solution of each polymer. The most preferred method is to remove the solvent after the reaction. The block copolymer resin composition thus obtained is processed into various molded products by injection molding, or into sheets or films by extrusion molding. In addition, since the impact resistance and thermal stability are significantly improved, it can be used as an impact modifier for polystyrene, and also in fields such as high-temperature, high-speed molding in harsh thermal environments. The present invention will be specifically explained below with reference to Examples. Example 1 Dehydrated and purified benzene 80 was placed in a 100 autoclave, and sec-butyl lithium 440 was added to it.
mmol was added and the temperature was kept at 40°C. Next, the styrene monomer for the first stage of the polymerization reaction (hereinafter referred to as SM-
1) was added to complete the polymerization.
Butadiene for the second stage of the polymerization reaction (hereinafter referred to as
Bd-2) and styrene monomer (hereinafter abbreviated as SM-2) were added at once in a mixed state of 9 kg and 6.6 kg, respectively, to complete the polymerization. Thereafter, a small amount of alcohol was added to the polymerization solution to stop the polymerization, and a polymerization solution of block copolymer (A) was obtained. This sample was designated as copolymer (A-1). The copolymer (A-1) has a structure AB/A (A is a styrene block, B is a butadiene block, and B/A indicates that the boundary between both blocks is a tapered structure). Furthermore, 110 mmol of sec-butyllithium, SM-1
A polymerization solution of block copolymer (B) was obtained in the same manner as the production method of block copolymer (A) except that Bd-2 was 6.8 kg, Bd-2 was 3 kg, and SM-2 was 10.2 kg. It was referred to as a polymer (B-1). Copolymer (B-1) has the same polymer structure as copolymer (A-1). After mixing and stirring 50% of the polymerization solution of copolymer (A-1) and 100% of the polymerization solution of copolymer (B-1), the mixture was separated into crumbs by steam stripping and dried in a hot air dryer. Dry. Next, 0.5 parts by weight of 2,6-di-tert-butyl-4-methylphenol, 0.3 parts by weight of trisnonyl phenyl phosphorite, and 0.2 parts by weight of stearic acid were added to the dried crumbs, and then pelletized using an extruder. did. The physical properties of this pellet were measured and the results are shown in Table 1. Examples 2, 3 and Comparative Examples 1 to 4 SM-1, Bd-2, SM-2 and initiators are shown in Table 1.
A block copolymer (A) was obtained in the same manner as in Example 1 except that the proportions shown in
-2) and (A-3). Separately, a block copolymer (A) was obtained in the same manner as in Example 1, except that SM-1, Bd-2, SM-2 and the initiator were used in the proportions shown in Table 1.
4) to (A-7). (A-2) and (A-3) are Examples 2 and 3, and (A-4) to (A-7) are sequentially Comparative Example 1.
to 4 were mixed with the block copolymer (B-1) in the proportions shown in Table 1, pellets were prepared in the same manner as in Example 1, and their physical properties were measured and shown in Table 1. In addition, in the table below, the physical properties were measured by the following methods. Haze: A 2 mm thick plate was molded at 200° C. using an injection molding machine and measured according to the method of ASTM-D-1003. Falling weight strength: 3mm thick at 200℃ using an injection molding machine, 4
A cm x 4 cm plate is formed, and in an atmosphere of 20°C, a weight with a radius of 5 m/mφ at the tip is dropped at different weights and heights, and the highest height without breakage is determined by weight x height. It was displayed in Thermal stability...Using an injection molding machine, plates with a thickness of 3 mm were continuously molded at 250℃, and the surface gloss of the 1st and 20th shots was measured, and the difference in gloss reduction (△
G) was measured.

【表】 実施例4、5及び比較例5〜8 SM−1、Bd−2、SM−2及び開始剤を表2
に示る割合で使用した以外は実施例1と同様にし
てブロツク共重合体(B)を得、これを共重合体(B
−2)及び(B−3)とした。 別にSM−1、Bd−2、SM−2及び開始剤を
表2に示す割合で使用した以外は実施例1と同様
にしてブロツク共重合体(B)を得、これを(B−
4)ないし(B−7)とした。 (B−2)、(B−3)をそれぞれ実施例4、5
とし、(B−4)ないし(B−7)を順次比較例
5ないし8とし、ブロツク共重合体(A−1)と
表2に示す割合に混合し、実施例1と同様にして
ペレツトを作りその物性を測定し、表2に示し
た。 実施例6及び比較例9 ブロツク共重合体(A−1)の重合液量30と
ブロツク共重合体(B−1)の重合液量90とを
混合した以外は実施例1と同様にしてペレツトを
作りその物性を測定し、実施例6として表2に示
した。 別にブロツク共重合体(A−1)の重合液量90
とブロツク共重合体(B−1)の重合液量60
とを混合した以外は実施例1と同様にしてペレツ
トを作り、その物性を測定し、比較例9として表
2に示した。 実施例 7 実施例1の重合装置に於いて、脱水精製したベ
ンゼン80を仕込み、これに開始剤としてsec−
ブチルリチウムを120mmol添加し、次いで、精
製したスチレンモノマーを8.5Kg投入して、40℃
にて重合を完結させた。次いでブタジエンを3Kg
投入し、60℃で1時間反応させたのち、残りのス
チレンモノマー8.5Kgを添加し、重合させた。得
られた重合液に少量のアンコールを添加して重合
を停止させ、完全ブロツク構造をもつブロツク共
重合体(B)を得た。 この重合液を(A−1)の重合液と表2に示す
割合に混合し、実施例1と同様にしてペレツトを
作りその物性を測定し、表2に示した。 実施例 8 実施例1の装置に於いて、脱水精製したベンゼ
ン80を仕込み、これに開始剤としてsec−ブチ
ルリチウム360mmolを添加し、次いで、精製し
たスチレンモノマーを17Kg投入して、重合させた
のち、ブタジエンを3Kg添加し、60℃で1時間反
応させた。次いで、100mmolの四塩化ケイ素を
含むベンゼン溶液500ccを添加し、60℃で1時間
撹拌したのち、少量のアルコールを添加し、重合
を停止させて、星型ブロツク構造をもつ共重合体
(B)を得た。 この重合液を重合液(A−1)と表2に示す割
合に混合し、実施例1と同様にしてペレツトを作
り、その物性を測定し表2に示した。
[Table] Examples 4, 5 and Comparative Examples 5 to 8 SM-1, Bd-2, SM-2 and initiators are shown in Table 2.
A block copolymer (B) was obtained in the same manner as in Example 1 except that the proportions shown in
-2) and (B-3). Separately, a block copolymer (B) was obtained in the same manner as in Example 1, except that SM-1, Bd-2, SM-2 and the initiator were used in the proportions shown in Table 2.
4) to (B-7). (B-2) and (B-3) in Examples 4 and 5, respectively
(B-4) to (B-7) were sequentially used as Comparative Examples 5 to 8, mixed with the block copolymer (A-1) in the proportions shown in Table 2, and pelletized in the same manner as in Example 1. The physical properties were measured and shown in Table 2. Example 6 and Comparative Example 9 Pellets were prepared in the same manner as in Example 1, except that 30% of the polymerization liquid of block copolymer (A-1) and 90% of polymerization liquid of block copolymer (B-1) were mixed. was prepared, its physical properties were measured, and the results are shown in Table 2 as Example 6. Separately, the amount of polymerization liquid of block copolymer (A-1) is 90
Polymerization liquid volume of block copolymer (B-1) and block copolymer (B-1) 60
Pellets were made in the same manner as in Example 1 except that the following were mixed, and the physical properties of the pellets were measured and shown in Table 2 as Comparative Example 9. Example 7 In the polymerization apparatus of Example 1, dehydrated and purified benzene 80 was charged, and sec-80 was added as an initiator.
Added 120 mmol of butyllithium, then added 8.5 kg of purified styrene monomer, and heated to 40°C.
Polymerization was completed at . Then 3Kg of butadiene
After reacting at 60°C for 1 hour, the remaining styrene monomer (8.5 kg) was added and polymerized. A small amount of encore was added to the obtained polymerization solution to stop the polymerization, and a block copolymer (B) having a complete block structure was obtained. This polymerization solution was mixed with the polymerization solution of (A-1) in the proportions shown in Table 2, pellets were prepared in the same manner as in Example 1, and the physical properties of the pellets were measured and are shown in Table 2. Example 8 In the apparatus of Example 1, dehydrated and purified benzene 80 was charged, 360 mmol of sec-butyllithium was added as an initiator, and then 17 kg of purified styrene monomer was charged and polymerized. , 3 kg of butadiene was added, and the mixture was reacted at 60°C for 1 hour. Next, 500 cc of a benzene solution containing 100 mmol of silicon tetrachloride was added, and after stirring at 60°C for 1 hour, a small amount of alcohol was added to stop the polymerization, resulting in a copolymer with a star-shaped block structure.
I got (B). This polymerization solution was mixed with polymerization solution (A-1) in the proportions shown in Table 2, pellets were prepared in the same manner as in Example 1, and the physical properties of the pellets were measured and shown in Table 2.

【表】【table】

Claims (1)

【特許請求の範囲】 1 (A) 重量平均分子鎖長が600〜1400Å、スチ
レン化合物が50〜70重量%であるスチレン化合
物と共役ジエン化合物のブロツク共重合体;
と、 (B) 重量平均分子鎖長が3600〜6000Å、スチレン
化合物が80〜95重量%であるスチレン化合物と
共役ジエン化合物とのブロツク共重合体; とを主成分とし、その(A)/(B)の重量比が1以下で
あるスチレン化合物と共役ジエン化合物とのブロ
ツク共重合樹脂。
[Scope of Claims] 1 (A) A block copolymer of a styrene compound and a conjugated diene compound having a weight average molecular chain length of 600 to 1400 Å and a styrene compound content of 50 to 70% by weight;
and (B) a block copolymer of a styrene compound and a conjugated diene compound with a weight average molecular chain length of 3600 to 6000 Å and a styrene compound content of 80 to 95% by weight; A block copolymer resin of a styrene compound and a conjugated diene compound in which the weight ratio of B) is 1 or less.
JP13550881A 1981-08-31 1981-08-31 Block copolymer resin Granted JPS5837044A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13550881A JPS5837044A (en) 1981-08-31 1981-08-31 Block copolymer resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13550881A JPS5837044A (en) 1981-08-31 1981-08-31 Block copolymer resin

Publications (2)

Publication Number Publication Date
JPS5837044A JPS5837044A (en) 1983-03-04
JPH0132857B2 true JPH0132857B2 (en) 1989-07-10

Family

ID=15153393

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13550881A Granted JPS5837044A (en) 1981-08-31 1981-08-31 Block copolymer resin

Country Status (1)

Country Link
JP (1) JPS5837044A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59187048A (en) * 1983-03-10 1984-10-24 Nippon Steel Chem Co Ltd thermoplastic resin composition
JPH0692519B2 (en) * 1985-05-01 1994-11-16 旭化成工業株式会社 Sheet composition
JPS62197409A (en) * 1986-02-24 1987-09-01 Asahi Chem Ind Co Ltd Block copolymer and composition containing same
JPS62197410A (en) * 1986-02-24 1987-09-01 Asahi Chem Ind Co Ltd Block copolymer resin and composition containing same
JPS63268766A (en) * 1987-04-28 1988-11-07 Asahi Chem Ind Co Ltd Bituminous composition

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51130454A (en) * 1975-05-08 1976-11-12 Asahi Chem Ind Co Ltd Transparent styrene resin compositions havingi good shock resistance
JPS5213572A (en) * 1975-07-22 1977-02-01 Asahi Chemical Ind Transparent shock resisting sheets
US4048255A (en) * 1975-08-26 1977-09-13 Abbott Laboratories Blend of thermoelastic polymers with block radial polymers used as pharmaceutical sealing and resealing materials
JPS5851208B2 (en) * 1976-08-27 1983-11-15 大和製衡株式会社 electromagnetic balance device

Also Published As

Publication number Publication date
JPS5837044A (en) 1983-03-04

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