JPS61225218A - Block copolymer - Google Patents

Block copolymer

Info

Publication number
JPS61225218A
JPS61225218A JP60067726A JP6772685A JPS61225218A JP S61225218 A JPS61225218 A JP S61225218A JP 60067726 A JP60067726 A JP 60067726A JP 6772685 A JP6772685 A JP 6772685A JP S61225218 A JPS61225218 A JP S61225218A
Authority
JP
Japan
Prior art keywords
polysulfone
pps
polymer
measured
block copolymer
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
JP60067726A
Other languages
Japanese (ja)
Other versions
JPH0629319B2 (en
Inventor
Toheiji Kawabata
川端 十平次
Toshinori Sugie
杉江 敏典
Fumihiro Furuhata
古畑 文弘
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.)
DIC Corp
Original Assignee
Dainippon Ink and Chemicals Co 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
Application filed by Dainippon Ink and Chemicals Co Ltd filed Critical Dainippon Ink and Chemicals Co Ltd
Priority to JP60067726A priority Critical patent/JPH0629319B2/en
Priority to US06/845,455 priority patent/US4678831A/en
Publication of JPS61225218A publication Critical patent/JPS61225218A/en
Publication of JPH0629319B2 publication Critical patent/JPH0629319B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:A block copolymer improved in impact resistance and flexibility, prepared by chemically bonding a polysulfone as a soft segment to a polyphenylene sulfide. CONSTITUTION:A halogen-substituted aromatic compound (e.g., p-dichloro benzene) is polymerized with Na2S in an amide or sulfone solvent (e.g., sulfolane) to obtain a polyphenylene sulfide containing at least 70mol% structural units of formula I. This polyphenylene sulfide is graft-copolymerized with a polysulfone of one of formulas II-IV, etc. (wherein n>=10) having a reduced viscosity (as measured in 0.2g/100ml chloroform solution at 25 deg.C) of 0.05-1.0 in an organic polar solvent (e.g., formamide) to obtain a block copolymer having a relative viscosity [eta] (as measured in a 0.4g/100ml alpha-chloronaphthalene solu tion at 206 deg.C and calculated according to the equation of formula V) of 0.03-1.0.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、/リフェニレンスルフィド(以後PPSと略
す)部分と4リサルホン部分とからなるブロック共重合
体に関する。さらに詳しくは、ppsKソフトセグメン
トとしてポリサルホンを化学的に結合せしめて表る耐衝
撃性、柔軟性などの靭性にかかる機械的性質が改善され
たブロック樹脂に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a block copolymer comprising a /rifhenylene sulfide (hereinafter abbreviated as PPS) moiety and a 4-resulfone moiety. More specifically, the present invention relates to a block resin with improved mechanical properties related to toughness such as impact resistance and flexibility, which is produced by chemically bonding polysulfone as a ppsK soft segment.

(従来の技術および問題点) PPSはナイロン、ポリカー♂ネート、ポリブチレンテ
レフタレート、ポリアセタール等のエンジニアリングプ
ラスチックに比較し、卓越した耐熱性、耐薬品性、剛性
を有する高性能エンジニアリンググラスチックとして注
目されている。しかしながら、この樹脂は上記のエンジ
ニアリングプラスチックに比較して靭性に乏しく、脆弱
であるという重大な欠点を有している。近年、従来の熱
架橋型PPSと異なる直鎖状PPSが開発されつつある
が、その場合でも結晶化状態では耐衝撃性および伸び等
の靭性に乏しい。
(Conventional technology and problems) PPS has attracted attention as a high-performance engineering plastic that has excellent heat resistance, chemical resistance, and rigidity compared to engineering plastics such as nylon, polycarbonate, polybutylene terephthalate, and polyacetal. There is. However, this resin has serious drawbacks in that it has poor toughness and is brittle compared to the above-mentioned engineering plastics. In recent years, linear PPS, which is different from conventional thermally crosslinked PPS, is being developed, but even in this case, it is poor in impact resistance and toughness such as elongation in a crystallized state.

従来1、pps耐衝撃性を改善するためガラス繊維等の
充てん剤を配合することが行なわれているが、十分でな
いために1例えば成形収縮歪によるクラック発生の防止
には効果がない。
Conventionally, fillers such as glass fibers have been added to improve pps impact resistance, but this is insufficient and is therefore ineffective in preventing cracks caused by, for example, molding shrinkage distortion.

一方、柔軟性ポリマーとのポリマーブレンドは有力な方
法であるが、柔軟でかつ耐熱性、耐薬品性に優れるポリ
マーが少ないことやPPSとの相溶性が不十分なため1
曲げ強さ等の機械的強度の低下、成形品の表面状態の劣
化等の問題点を有し、未だppsの特徴を損なわず、耐
衝撃性、柔軟性が改善されたPPSを得るに到っていな
い。
On the other hand, polymer blending with a flexible polymer is an effective method, but there are few polymers that are flexible and have excellent heat resistance and chemical resistance, and the compatibility with PPS is insufficient.
It has problems such as a decrease in mechanical strength such as bending strength and deterioration of the surface condition of molded products, and it has not yet been possible to obtain PPS with improved impact resistance and flexibility without impairing the characteristics of PPS. Not yet.

(問題点を解決するための手段) 本発明者らは、上記の如き状況に鑑み、耐衝撃性等の機
械的性質が改善され、かつブレンド相溶性に優れたpp
s樹脂を得るべく鋭意検討した結果、末端反応性基をも
つppsとポリサルホンの共重合反応を行なわせ、両者
を化学的に結合させて得られるブロック樹脂が有効であ
ることを見出し1本発明に到達したものである。
(Means for Solving the Problems) In view of the above-mentioned circumstances, the present inventors have developed a ppm with improved mechanical properties such as impact resistance and excellent blend compatibility.
As a result of intensive studies to obtain S resin, it was discovered that a block resin obtained by carrying out a copolymerization reaction of pps having a terminal reactive group and polysulfone and chemically bonding the two was effective. 1. The present invention has been made. It has been reached.

即ち、本発明はpps部分とポリサルホン部分とからな
り、対数粘度〔η〕(ここで、〔η〕は0.41/10
0−の溶液なるポリマー濃度においてα−クロルナフタ
レン中206℃で測定し、下式〔η) = tn (相
対粘度)/ポリマー濃度に従い算出した値である。)が
0.03〜1.0の範囲であるブロック共重合体を提供
するものである。
That is, the present invention consists of a pps part and a polysulfone part, and has a logarithmic viscosity [η] (here, [η] is 0.41/10
The value was measured at 206° C. in α-chlornaphthalene at a polymer concentration of 0−1 solution, and calculated according to the following formula: [η) = tn (relative viscosity)/polymer concentration. ) is in the range of 0.03 to 1.0.

本発明のブロック共重合体を構成するpps部分ルチ以
上含むものが好ましく、その量が70モルチ未満ではす
ぐれた特性のブロック共重合体は得難い。また、そのP
PSの対数粘度〔η〕(ここで〔η〕は0.41!/1
00−の溶液なるポリマー濃度において、α−クロルナ
フタレン中206℃で測定し、下式〔η) =−tn 
(相対粘度〕/ポリマー濃度に従い算出した値である。
It is preferable that the block copolymer of the present invention contains more than 100% of the pps mole, and if the amount is less than 700%, it is difficult to obtain a block copolymer with excellent properties. Also, that P
Logarithmic viscosity of PS [η] (here [η] is 0.41!/1
Measured at 206°C in α-chlornaphthalene at a polymer concentration of 00- solution, and the following formula [η) = -tn
This is a value calculated according to (relative viscosity)/polymer concentration.

)が0.03〜0.80の範囲であるのが好ましい。) is preferably in the range of 0.03 to 0.80.

この/ IJママ−重合方法としては、ハロゲン置換芳
香族化合物、例えばp−ジクロルベンゼンを硫黄と炭酸
ソーダの存在下で重合させる方法、極性溶媒中で硫化ナ
トリウムあるいは水硫化ナトリウムと水酸化ナトリウム
又は硫化水素と水酸化ナトリウムあるいはナトリウムア
ミノアルカノエートの存在下で重合させる方法、p−ク
ロルチオフェノールの自己縮合などがあげられるが、N
−メチルピロリドン、ジメチルアセトアミドなどのアミ
ド系溶媒やスルホラン等のスルホン系溶媒中で硫化ナト
リウムとp−ジクロルベンゼンを反応させる方法が適当
である。この際に重合度を調節するためにカルボン酸や
スルホン酸のアルカリ金属塩を添加したり、水酸化アル
カリを添加することは好ましい方法である。共重合成分
として、30ヒフ工ニ#結合((■H原ΣS−)、置換
フェニルニトロ基、フェニル基、アルコキシ基、カルビ
ン酸基またはカルボン酸の金属塩基を示す)、3官マー
の結晶性に大きく影響しない範囲でかまわないが、好ま
しくは共重合成分は10モルチ以下がよい。特に3官能
性以上のフェニル、ビフェニル。
This/IJ polymerization method includes polymerizing a halogen-substituted aromatic compound, such as p-dichlorobenzene, in the presence of sulfur and sodium carbonate, or polymerizing sodium sulfide or sodium hydrosulfide and sodium hydroxide or Methods include polymerization in the presence of hydrogen sulfide and sodium hydroxide or sodium aminoalkanoate, self-condensation of p-chlorothiophenol, etc.
- A method in which sodium sulfide and p-dichlorobenzene are reacted in an amide solvent such as methylpyrrolidone or dimethylacetamide or a sulfone solvent such as sulfolane is suitable. At this time, in order to adjust the degree of polymerization, it is a preferable method to add an alkali metal salt of carboxylic acid or sulfonic acid, or to add alkali hydroxide. As a copolymerization component, 30 Hifonic di# bond ((■H original ΣS-), substituted phenyl nitro group, phenyl group, alkoxy group, carbic acid group or metal base of carboxylic acid), trifunctional mer crystallinity The amount of the copolymerized component is preferably 10 mol or less, although it may be within a range that does not significantly affect the amount. Especially phenyl and biphenyl having trifunctionality or more.

ナフチルスルフィド結合などを共重合に選ぶ場合は3モ
ルチ以下、さらに好ましくは1モルチ以下がよい。
When a naphthyl sulfide bond or the like is selected for copolymerization, the amount is preferably 3 molar or less, more preferably 1 molar or less.

かかるPPSの具体的な製造法としては1例えば(1)
ハロゲン置換芳香族化合物と硫化アルカリとによる製法
(米国特許第2513188号、特公昭44−2767
1号および特公昭45−3368号参照)。
A specific method for producing such PPS is 1, for example (1).
Production method using halogen-substituted aromatic compound and alkali sulfide (U.S. Patent No. 2513188, Japanese Patent Publication No. 44-2767)
(See No. 1 and Special Publication No. 45-3368).

(2)チオフェノール類のアルカリ触媒又は銅塩等の共
存下における縮合反応による製法(米国特許第3274
165号および英国特許第1160660号参照) 、
 (3)芳香族化合物を塩化硫黄とのルイス酸触媒共存
下に於ける縮合反応による製法(特公昭46−2725
5号およびベルギー特許第29437号参照)等が挙げ
られる。
(2) Production method by condensation reaction of thiophenols in the coexistence of an alkali catalyst or copper salt (US Patent No. 3274)
165 and British Patent No. 1160660),
(3) Production method by condensation reaction of aromatic compounds with sulfur chloride in the coexistence of a Lewis acid catalyst (Japanese Patent Publication No. 46-2725
No. 5 and Belgian Patent No. 29437).

本発明におけるブロック共重合体は、例えばポリサルホ
ンの末端基とPPSの末端基とを反応せしめることによ
って得られるため1例えば、ポリサルホンの末端基がク
ロルフェニル基(構造式:C2−@S)である場合PP
Sの末端基をナトリウムスルフィド基(構造式: Na
p−)の如き反応性基にしておく必要がある。かかるp
psを得る方法として、予め重合反応時にモノマーの硫
化す) IJウム成分の量をp−ジクロルベンゼン成分
に対し1〜20モルチ過剰の状態で反応させる方法、あ
るいは、ポリサルホンとの共重合反応時に第3成分とし
て硫化ナトリウム等の結合剤を添加する方法等が挙げら
れる。
The block copolymer in the present invention can be obtained by, for example, reacting the terminal group of polysulfone with the terminal group of PPS. Case PP
The terminal group of S is a sodium sulfide group (structural formula: Na
It is necessary to use a reactive group such as p-). It takes p
As a method for obtaining ps, there is a method in which the monomer is sulfurized in advance during the polymerization reaction, and the amount of the IJium component is 1 to 20 molar excess relative to the p-dichlorobenzene component. Examples include a method of adding a binder such as sodium sulfide as the third component.

一方1本発明のブロック共重合体を構成するポリサルホ
ン部分はアリーレン単位がエーテル及びスルホン結合と
共に、無秩序に、または秩序正しく位置するポリアリー
レン化合物として定義され。
On the other hand, the polysulfone moiety constituting the block copolymer of the present invention is defined as a polyarylene compound in which arylene units are positioned randomly or orderly together with ether and sulfone bonds.

例えば次の■〜[相]の構造式(式中のnは10以上の
整数を表わす)からなるものが挙げられるが、好適には
■または■の構造を有するものが望ましい。
For example, those having the following structural formulas (1) to (phase) (n in the formula represents an integer of 10 or more) may be mentioned, but those having the structure (1) or (2) are preferable.

■(soKト(漉0□QCH2C\ ■ 缶)0M2QOて>so2℃許 ■ 壬0(叉へ7J)、、B02α ぜ・G“o−G(X @        c    o    so□上記ポ
リサルホン部分の還元粘度ηsp/C(ここで、ηll
p/cは0.2 !i/100−の溶液なるポリマー濃
度において、クロロホルム中25℃で測定し、下式 ’l s p/c = (相対粘度−1)/ポリマー濃
度に従い算出した値である。)は0.05〜1.0の範
囲のものが好ましい。この4リマーの重合方法としては
、例えばジクロルジフェニルスルホント2゜2−ビス(
4−ヒドロキシフェニル)−プロパンのナトリウム塩を
反応させる方法(特公昭42−7799号)などが挙げ
られる。
■(soKto(filter 0□QCH2C\ ■Can)0M2QOte>so2℃allow■ 壬0(叉he7J),,B02α ze・G"o-G(X @ c o so□Reduced viscosity of the above polysulfone part ηsp/C (where ηll
p/c is 0.2! The value was measured at 25°C in chloroform at a polymer concentration of a solution of i/100-, and was calculated according to the following formula: 'l sp/c = (relative viscosity-1)/polymer concentration. ) is preferably in the range of 0.05 to 1.0. As a method for polymerizing this 4-limer, for example, dichlorodiphenylsulfont 2゜2-bis(
Examples include a method of reacting sodium salt of (4-hydroxyphenyl)-propane (Japanese Patent Publication No. 7799/1983).

本発明の20ツク共重合体をIリサルホンの末端基とp
psの末端基とを反応せしめて合成する場合、予めポリ
サルもン合成時にジクロルジフェニルスルホン成分の量
をビス(4−ヒドロキシフェニル)−プロノ臂ン成分の
量に対し1〜20モルチ過剰の状態で反応させる方法、
あるいはppsとの共重合反応時に第3成分としてジク
ロルジフェニルスルホン等の結合剤を添加する方法等を
用いるのが好ましい。
The terminal group of I resulfone and p
When synthesizing by reacting with the terminal group of ps, the amount of dichlorodiphenyl sulfone component is adjusted in advance to be in excess of 1 to 20 moles relative to the amount of bis(4-hydroxyphenyl)-pronobenzene component during polysulfone synthesis. How to react with
Alternatively, it is preferable to use a method in which a binder such as dichlorodiphenyl sulfone is added as a third component during the copolymerization reaction with pps.

また、共重合反応する際、PPSとポリサルホンの末端
反応性基の数を同じにすることは収率よくプロ、り共重
合体が得られ最も好ましい。一方、いずれか一方の成分
の末端基数が過剰の場合、反応終了後、未反応のホそポ
リマー成分のみを分別あるいは抽出除去することにより
てプロ、り共重合体のみを回収することができる。
Furthermore, during the copolymerization reaction, it is most preferable to make the number of terminal reactive groups of PPS and polysulfone the same, since a pro- and poly-copolymer can be obtained in good yield. On the other hand, if the number of terminal groups of either component is excessive, only the pro-copolymer can be recovered by fractionating or extracting only the unreacted photo-polymer component after the reaction is completed.

共重合反応において使用される溶媒は、その温度および
圧力において実質的1c!状である有機極性溶媒が好ま
しい。具体的には、ホルムアミP。
The solvent used in the copolymerization reaction has a substantially 1c! Preferred are organic polar solvents that are Specifically, formami-P.

アセトアミド、N−メチルホルムアミド、N、N−ジメ
チルホルムアミド、N、N−ジメチルアセトアミド、2
−ピロリドン、N−メチル−2−ピロリドン、N−エチ
ル−2−ピロリドン、ε、−カプロラクタム、N−メチ
ル−6−カプロラクタム、ヘキサメチルホスホルアミド
、テトラメチル尿素、1.3−ジメチル−2−インダシ
リジノン等のアミド、尿素およびラクタム類;スルホラ
ン、ジメチルスルホラン等のスルホン類;ベンゾニトリ
ル等のニトリル類;メチルフェニルケトン尋のケトン類
等およびこれらの混合物を挙げることができる。
Acetamide, N-methylformamide, N,N-dimethylformamide, N,N-dimethylacetamide, 2
-pyrrolidone, N-methyl-2-pyrrolidone, N-ethyl-2-pyrrolidone, ε, -caprolactam, N-methyl-6-caprolactam, hexamethylphosphoramide, tetramethylurea, 1,3-dimethyl-2- Amides such as indasilidinone, urea and lactams; sulfones such as sulfolane and dimethylsulfolane; nitrites such as benzonitrile; ketones such as methylphenylketone; and mixtures thereof.

これらの溶媒のうちでは、アミド類、ラクタム類アルい
はスルホン類等の非プロトン性有機標性溶媒を使用する
ことが特に好ましい。有機極性溶媒の使用量はポリマー
成分の量に対する重量比で2〜20の範囲で、好ましく
゛は3〜10の範囲である。
Among these solvents, it is particularly preferable to use aprotic organic solvents such as amides, lactams, or sulfones. The amount of the organic polar solvent used is in the range of 2 to 20, preferably 3 to 10, in weight ratio to the amount of the polymer component.

プロ、り化反応による共重合反応生成物が化学的に結合
したPPSとポリサルホンとのプロ、り共重合体である
ことは、得られたポリマーをポリサルホンの良溶媒であ
るN−メチルピロリドンやクロロホルムでくり返し抽出
した後のポリマーケーキ中に含まれるポリサルホンの量
が低減しないことで確かめられる。一方、共重合反応生
成物中に未反応のppsが含まれるかどうかは、該生成
物をα−クロルナフタレンに混ぜ、210℃に溶解せし
め、160℃に冷却した時K PPSが沈殿してくるか
否かで確認できる。
The fact that the copolymerization reaction product resulting from the pro- and polysulfone reaction is a pro- and polysulfone copolymer of chemically bonded PPS and polysulfone means that the resulting polymer can be used in N-methylpyrrolidone or chloroform, which is a good solvent for polysulfone. This is confirmed by the fact that the amount of polysulfone contained in the polymer cake does not decrease after repeated extractions. On the other hand, whether unreacted pps is contained in the copolymerization reaction product can be determined by mixing the product with α-chlornaphthalene, dissolving it at 210°C, and cooling it to 160°C. K PPS precipitates. You can check whether it is or not.

本発明のブロック共重合体はIリフェニレンオキサイド
、Iリアリレート、Iリアミド、?リツチレンテレフタ
レート、ポリエーテルエーテルケトン、ポリイミド等の
熱可塑性樹脂、ノがラック型エポキシ樹脂等のエポキシ
樹脂、ポリエチレン、ポリエチレン等のポリオレフィン
類、マレイン酸変性ポリプロピレン等のα−オレフィン
共重合体、あるいはナイロ11/f!リエーテルIリア
ミドエラストマー尋の熱可塑性エラストマーとの組成物
に適用することができる。さらに1ガラス繊維、炭素繊
維等の繊維状強化材、あるいはメルク、マイカ、炭酸カ
ルシウム等の無機充填剤を併用したコンノぐクンドに適
用することもできる。
The block copolymer of the present invention includes I-riphenylene oxide, I-realylate, I-lyamide, ? Thermoplastic resins such as littylene terephthalate, polyetheretherketone, polyimide, epoxy resins such as Nogalac type epoxy resin, polyolefins such as polyethylene, polyethylene, α-olefin copolymers such as maleic acid-modified polypropylene, or nylon. 11/f! Liether I lyamide elastomer can be applied to compositions with thermoplastic elastomers. Furthermore, it is also possible to apply the present invention to a container using a fibrous reinforcing material such as glass fiber or carbon fiber, or an inorganic filler such as Merck, mica, or calcium carbonate.

而して、本発明のブロック共重合体は電気・電子部品等
のPPS従来品の主要な用途である射出成形品あるいは
圧縮成形品用途のみならず、繊維、シート、フィルム、
チューブ等の押出成形品用、プロー成形品用、トランス
ファー成形品用等に用いることができる。
Therefore, the block copolymer of the present invention can be used not only for injection molded products or compression molded products, which are the main uses of conventional PPS products such as electrical and electronic parts, but also for fibers, sheets, films,
It can be used for extrusion molded products such as tubes, blow molded products, transfer molded products, etc.

(発明の効果) 本発明のプロ、り共重合体は、PPSおよびこれと相溶
性の悪いポリサルホンの単なるブレンドによる組成物と
異なり、PPSとポリサルホンのポリマー鎖がブロック
共重合したものであるため、曲げ強度、耐衝撃性等の機
械的性質に優れ、しかも228%ポリスルホン等との相
溶性に優れたものである。
(Effects of the Invention) The pro-copolymer of the present invention differs from a composition that is simply a blend of PPS and polysulfone, which has poor compatibility, because it is a block copolymer of polymer chains of PPS and polysulfone. It has excellent mechanical properties such as bending strength and impact resistance, and is also excellent in compatibility with 228% polysulfone and the like.

(実施例) 次に、本発明を実施例にょシ具体的に説明するが、本発
明はこれらに限定されるものではない。
(Example) Next, the present invention will be specifically explained using Examples, but the present invention is not limited to these.

実施例1.比較例1 まず、末端クロルフェニル基型ポリサルホンを以下のよ
うにして合成した。51ガラスフラスコにビス(4−ヒ
ドロキシフェニル)−プロパン(以下、ビスフェノール
Aと略す) 343 #(1,50モル)とジメチルス
ルホキシド10100Oとモノクロルベンゼン2000
rLt1に仕込み、60〜80℃に熱し、系を窒素で置
換した。次いで、5Otsカセインーダ水溶液2411
(3,0モル)を激しく攪拌しながら10分間で滴下し
た。系はクロルベンゼン相とジメチルスルホキシドに溶
解したビスフェノールAのニナ) IJウム塩の水溶液
相に分離した。次いで、反応混合物を窒素で置換しなが
ら還流させ、共沸によシ水を追い出しクロルベンゼンを
系内に戻し友。内温は120℃から140℃まで上昇し
、系内の水は殆んど留去され、ビスフェノールAのニナ
トリウム塩は沈澱物として析出した。系内の温度を15
5〜160℃に上げることにより、クロルベンゼンを蒸
留し、析出物を再溶解させた。次に、乾燥した4、4′
−ジクロルジフェニルスルホン448g(1,56モル
)の50チクロルベンゼン溶液を110℃に保ちながら
10分かけて加えた。その際、系内は150〜160℃
GC:ry)ロールシタ。ジクロルジフェニルスルホン
を添加終了後、160℃で3時間反応させた後、こはく
色の粘稠なポリマー溶液を得た。この溶液を冷却し、1
000−のクロルベンゼンで希釈し副生食塩t−濾過に
よシ除去した後、ポリマー溶液の5倍量のメタノール中
に注入しポリマーを沈澱させた。得られた白色沈澱をク
ロロホルムに溶解し、水洗した後、再度クロロホルムと
メタノールで再沈澱し、その沈澱物f:130℃で減圧
乾燥して白色のポリサルホン633Iを得た(収率96
.0%)。
Example 1. Comparative Example 1 First, a terminal chlorphenyl group type polysulfone was synthesized as follows. 51 In a glass flask, add bis(4-hydroxyphenyl)-propane (hereinafter abbreviated as bisphenol A) 343 # (1,50 mol), 10,100 O of dimethyl sulfoxide, and 2,000 O of monochlorobenzene.
rLt1, heated to 60-80°C, and purged the system with nitrogen. Then, 5Ots caseinida aqueous solution 2411
(3.0 mol) was added dropwise over 10 minutes with vigorous stirring. The system was separated into a chlorobenzene phase and an aqueous solution phase of the Nina)IJium salt of bisphenol A dissolved in dimethyl sulfoxide. Next, the reaction mixture is refluxed while purging with nitrogen, water is removed by azeotropy, and chlorobenzene is returned to the system. The internal temperature rose from 120°C to 140°C, most of the water in the system was distilled off, and the disodium salt of bisphenol A was precipitated. The temperature in the system is 15
By increasing the temperature from 5 to 160°C, chlorobenzene was distilled and the precipitate was redissolved. Next, dry 4,4'
- A solution of 448 g (1.56 mol) of dichlorodiphenyl sulfone in 50 cyclobenzene was added over 10 minutes while maintaining the temperature at 110°C. At that time, the temperature inside the system is 150 to 160℃.
GC:ry) Roll sita. After the addition of dichlordiphenyl sulfone was completed, the reaction was carried out at 160° C. for 3 hours, and an amber viscous polymer solution was obtained. Cool this solution and
After diluting with 000-chlorobenzene and removing by-product sodium chloride by t-filtration, the polymer was poured into methanol in an amount 5 times the amount of the polymer solution to precipitate the polymer. The obtained white precipitate was dissolved in chloroform, washed with water, reprecipitated again with chloroform and methanol, and the precipitate f: dried under reduced pressure at 130°C to obtain white polysulfone 633I (yield: 96
.. 0%).

このポリマーの還元粘度η、、/C(ポリ、−5iO,
2,9/100a/、クロロホルム中25℃で測定し、
η8p/C=比粘度/ポリマー濃度の式に従い算出しし
た値)は0.34であった。
The reduced viscosity of this polymer is η, /C (poly, -5iO,
2,9/100a/, measured at 25°C in chloroform,
The value calculated according to the formula η8p/C=specific viscosity/polymer concentration) was 0.34.

次に、末端ナトリウムスルフィド基型ppst以下のよ
うにして合成した。101オートクレーブにN−メチル
ピロリドン350011と硫化ナトリウム2.7水塩1
153.9 (8,80モル)および水酸化ナトリウム
4.0,9(0,10モル)を仕込み、窒素雰囲気下、
200℃まで約2時間かけて攪拌しながら昇温して25
0dの水を留出させた。反応系を150℃に冷却した後
、p−ジクロルベンゼン117611(8,0モル)、
N−メチルピロリドン800Iiを加え、230℃で1
時間、次いで260℃で2時間反応させた。1合終了時
の内圧は7.1に9/cm”であった。反応容器を冷却
後、内容物の一部をサンプリングしテ別した後、固形分
を熱水で3回煮沸洗浄し、さらにアセトンで2回洗浄し
た後120℃で乾燥して淡灰褐色粉末状PPSポリマー
を得た(収率的94%)。ポリマーの対数粘度〔η〕(
ポリマー濃度0.4g/100mt、α−クロルナフタ
レン中206℃で測定し、〔η) = An (相対粘
度)/ポリマー濃度に従い算出した値)は0.1牛であ
りた。
Next, terminal sodium sulfide group type ppst was synthesized as follows. 101 In an autoclave, add 350011 N-methylpyrrolidone and 11 sodium sulfide 2.7 hydrate.
153.9 (8.80 mol) and sodium hydroxide 4.0.9 (0.10 mol), under nitrogen atmosphere,
Raise the temperature to 200°C while stirring for about 2 hours.
0 d of water was distilled off. After cooling the reaction system to 150°C, p-dichlorobenzene 117611 (8.0 mol),
Add N-methylpyrrolidone 800Ii and heat at 230℃ for 1
The reaction was then carried out at 260° C. for 2 hours. The internal pressure at the end of 1 cup was 7.1 to 9/cm''. After cooling the reaction vessel, a part of the contents was sampled and separated, and the solid content was boiled and washed three times with hot water. Furthermore, it was washed twice with acetone and then dried at 120°C to obtain a pale gray-brown powdery PPS polymer (yield: 94%). Logarithmic viscosity of the polymer [η] (
Measured at 206° C. in α-chlornaphthalene at a polymer concentration of 0.4 g/100 mt, [η) = An (value calculated according to relative viscosity)/polymer concentration) was 0.1 cow.

引続き、上記のPPS重合混合物2360#と前述のポ
リサルホン30011およびN−メチルピロリドン13
00.9を加え、貸素ノージ後密封し230℃まで昇温
し、この温度で2時間反応させた。反応容器を冷却後、
内容物をF別し、固形分’iN−メチルピロリドンで2
回洗浄した後熱水で3回煮沸洗浄した。得られたケーキ
を120℃で5時間乾燥して5281の灰褐色粉末状ポ
リマーを得た。
Subsequently, the above PPS polymerization mixture 2360# and the above polysulfone 30011 and N-methylpyrrolidone 13 were added.
00.9 was added, the mixture was sealed, the temperature was raised to 230°C, and the reaction was carried out at this temperature for 2 hours. After cooling the reaction vessel,
Separate the contents and reduce the solid content by 2 with N-methylpyrrolidone.
After washing twice, it was boiled and washed three times with hot water. The resulting cake was dried at 120° C. for 5 hours to obtain 5281 gray-brown powdery polymer.

このポリマーの〔η〕は0.27であった。また、赤外
線吸収スペクトルを測定したところ、当該PPSとポリ
サルホンの吸収以外のピークは観察されず、かつ139
0cIn および1240cm  に見られる特性吸収
の強度からポリサルホンを定量したところ、ポリマー中
49.6重量%含まれてい友。同時に、ポリマーの元素
分析を行ない、イオウを定量したところ18.52%の
値を示し、ポリマー中にポリサルホンが49.6重i1
含まれていることを確認した。
[η] of this polymer was 0.27. In addition, when the infrared absorption spectrum was measured, no peaks other than the absorption of the PPS and polysulfone were observed, and 139
Polysulfone was quantified from the intensity of the characteristic absorption seen at 0 cIn and 1240 cm, and was found to contain 49.6% by weight in the polymer. At the same time, elemental analysis of the polymer was carried out, and the sulfur content was determined to be 18.52%.
Confirmed that it is included.

さらK、上記ポリマーの溶媒抽出実験を行なった。即ち
、ポリサルホンの良溶媒であるクロロホルムを上記ポリ
マー10gに対し200.9用い、ソックスレー抽出を
2時間行なったが、ポリスルホンは全く溶出せず、かつ
抽出実験後回収した上記4リマーの赤外線吸収スペクト
ルの測定よシポリサルホンの含量は49.6重量%であ
った。同時に、前記ポリサルホンを49.6重量%含む
PPSブレンド物についても同様の抽出実験を行なった
Furthermore, K. conducted a solvent extraction experiment on the above polymer. That is, Soxhlet extraction was performed for 2 hours using chloroform, a good solvent for polysulfone, for 10 g of the polymer for 2 hours, but no polysulfone was eluted. The content of cypolysulfone was determined to be 49.6% by weight. At the same time, a similar extraction experiment was conducted on the PPS blend containing 49.6% by weight of polysulfone.

PPSブレンド物からは完全にポリサルホンが溶出した
The polysulfone was completely eluted from the PPS blend.

一方、上記ポリマー、及び前記ポリサルホンを49.6
重量%含むPPSブレンド物についてα−クロルナフタ
レン中での分別沈澱実験を行なりた。
On the other hand, the above polymer and the above polysulfone were 49.6
Fractional precipitation experiments in α-chlornaphthalene were performed on PPS blends containing % by weight.

各々のサンプル21をα−クロルナフタレン100縦と
混ぜ、210℃で溶解させt後、徐々に冷却し九ところ
160℃においてブレンド物中のPPSは全量沈澱した
のに対し、上記ポリマーの溶液からはPPSの沈澱は析
出せず、上記ポリマー中にPPSホモポリマーが含まれ
ていな−ことを示した。
Each sample 21 was mixed with 100% α-chlornaphthalene, dissolved at 210°C, and then gradually cooled. At 160°C, all of the PPS in the blend precipitated, whereas the PPS from the solution of the polymer No PPS precipitate was observed, indicating that the above polymer did not contain PPS homopolymer.

これらの結果から、本実施例の共重合反応生成物がPP
Sとポリサルホンが化学的に結合したブロック共重合体
であることを確認し友。
From these results, it is clear that the copolymerization reaction product of this example is PP.
It was confirmed that S and polysulfone are chemically bonded to form a block copolymer.

本実施例で得られた共重合体1260℃で5時間熱処理
した後、30mの2軸押量機を用いて加熱混練しペレッ
ト化した。このペレットを330℃で射出成形しテスト
ピースを作成した。ASTM D−1238(315℃
、5に9荷重)の方法にてメルトフロー・インデックス
(MI値と略す)、ASTM D−790の方法にて曲
げ強度、ASTMD−256の方法にてアイゾツト衝撃
強度を測定した。
The copolymer obtained in this example was heat-treated at 1260° C. for 5 hours, and then heated and kneaded using a 30 m twin-screw presser to form pellets. This pellet was injection molded at 330°C to prepare a test piece. ASTM D-1238 (315℃
The melt flow index (abbreviated as MI value) was measured by the method of , 5 to 9 loads), the bending strength was measured by the method of ASTM D-790, and the Izot impact strength was measured by the method of ASTM D-256.

また、外観相溶性は肉眼にて観察し、成形品の剥離状態
はテストピース破断面に接着テープを付着させた抜取シ
除く方法で剥離試験を行った後の状態を肉眼にて観察し
た。
In addition, appearance compatibility was observed with the naked eye, and the peeling state of the molded product was visually observed after a peel test was conducted using a sampling method in which an adhesive tape was attached to the fractured surface of the test piece.

比較例1においては、本実施例で合成したポリサルホン
とPPS重合反応後前述の処理によりて得られ72 p
ps粉末とを用い、ポリサルホン含量が49.6重tS
になるように混合したものを上記の方法に従い、テスト
ピースを作成し物性を測定し次。
In Comparative Example 1, 72 p was obtained by the above-mentioned treatment after the polymerization reaction of the polysulfone synthesized in this example and PPS.
Using PS powder, the polysulfone content is 49.6 weight tS.
Following the above method, a test piece was prepared and the physical properties were measured.

さらに、比較例2において、本実施例と同様の方法で得
られたPPS粉末単独の場合についても同様のテストピ
ースを作成し物性を測定した。
Furthermore, in Comparative Example 2, a similar test piece was prepared using only PPS powder obtained by the same method as in this example, and the physical properties were measured.

結果を表−1に示す。共重合体の場合はpps単独ある
いは混合物に比べ、そのMI値が著しく低下しており、
ブロック共重合による溶融粘度の増大を示している。外
観および成形品剥離状態から共重合体は両者の分散性が
良く、ミクロ相分離を引き起こしていると推察される。
The results are shown in Table-1. In the case of copolymers, the MI value is significantly lower than that of pps alone or as a mixture.
This shows an increase in melt viscosity due to block copolymerization. It is inferred from the appearance and peeling state of the molded product that the copolymer has good dispersibility between the two, causing microphase separation.

また1曲げ強度、衝撃強度ともに、混合物に比べ著しく
向上しており、本共重合体は耐衝撃性の改良された樹脂
であることを示している。
Furthermore, both the bending strength and the impact strength were significantly improved compared to the mixture, indicating that this copolymer is a resin with improved impact resistance.

実施例2.比較例3 硫化ナトリウムと共に安息香酸ナトリウム1152.9
 (8,0モル)を添加した以外は実施例1と同様の方
法で末端す) IJウムスルフィド基型PPS 重合混
合物を合成した。一部サンプリングし、〔η〕を測定し
たところ0.30であった。
Example 2. Comparative Example 3 Sodium benzoate with sodium sulfide 1152.9
An IJ umsulfide group type PPS polymerization mixture was synthesized in the same manner as in Example 1, except that (8.0 mol) was added. When some samples were taken and [η] was measured, it was 0.30.

この重合混合物の一部3710gと、実施例1と同様の
方法で合成した末端クロルフェニル基型ポリサルホン(
ηsp/C=0.35)210 #およびN−メチルピ
ロリドン8009を混ぜ、雪素ノトフ後密封し230℃
まで昇温し、この温度で2時間反応させた。実施例1と
同様に処理し、489.Fの灰褐色粉末状4リマーを得
た。このポリマーの対数粘度〔η〕は0.36であった
。また、赤外線吸収スペクトルを測定したところ、ポリ
サルホンが30.4重量%含まれていた。実施例1で記
述したクロロホルム抽出実験およびα−クロルナフタレ
ンによる分別沈殿実験を行なった結果、ppsおよびポ
リサルホンのホモポリマーは殆んど回収されなかったこ
とから1本実施例で得られたポリマーの殆んどがブロッ
ク共重合体であることを確認した。
A portion of 3710 g of this polymerization mixture and a terminal chlorphenyl group type polysulfone synthesized in the same manner as in Example 1 (
ηsp/C=0.35) 210# and N-methylpyrrolidone 8009 were mixed, sealed after snow removal, and heated at 230°C.
The temperature was raised to 100.degree. C., and the reaction was continued at this temperature for 2 hours. Processed in the same manner as in Example 1, yielding 489. A gray-brown powdery 4rimer of F was obtained. The logarithmic viscosity [η] of this polymer was 0.36. Further, when an infrared absorption spectrum was measured, it was found that 30.4% by weight of polysulfone was contained. As a result of conducting the chloroform extraction experiment and the fractional precipitation experiment using α-chlornaphthalene as described in Example 1, almost no homopolymer of pps and polysulfone was recovered. It was confirmed that most of the polymers were block copolymers.

上記共重合体をペレット化および射出成形してテストピ
ースを作成した。又、比較例3として。
A test piece was prepared by pelletizing and injection molding the above copolymer. Also, as Comparative Example 3.

本実施例で合成したポリサルホンとPPS粉末をポリサ
ルホン含量が30.4重量%になるように混合したもの
を用い、物性を測定した。
The physical properties were measured using a mixture of the polysulfone synthesized in this example and PPS powder so that the polysulfone content was 30.4% by weight.

結果を表−2に示す。実施例1と同様、この共重合体は
混合物と比較し、衝撃強度および曲げ強度が著しく向上
しており、耐衝撃性の改良された樹脂である。
The results are shown in Table-2. Similar to Example 1, this copolymer has significantly improved impact strength and bending strength compared to the mixture, and is a resin with improved impact resistance.

Claims (1)

【特許請求の範囲】 ポリフェニレンスルフィド部分とポリサルホン部分とか
らなり、対数粘度〔η〕(ここで、〔η〕は0.4g/
100mlの溶液なるポリマー濃度においてα−クロル
ナフタレン中206℃で測定し、下式〔η〕=ln(相
対粘度)/ポリマー濃度 に従い算出した値である。)が0.03〜1.0の範囲
であるブロック共重合体。
[Claims] Consists of a polyphenylene sulfide part and a polysulfone part, and has a logarithmic viscosity [η] (here, [η] is 0.4 g/
The value was measured at 206° C. in α-chlornaphthalene at a polymer concentration of 100 ml of solution, and calculated according to the following formula [η]=ln (relative viscosity)/polymer concentration. ) is in the range of 0.03 to 1.0.
JP60067726A 1985-03-30 1985-03-30 Block copolymer Expired - Lifetime JPH0629319B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP60067726A JPH0629319B2 (en) 1985-03-30 1985-03-30 Block copolymer
US06/845,455 US4678831A (en) 1985-03-30 1986-03-28 Block copolymers and resin compositions

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60067726A JPH0629319B2 (en) 1985-03-30 1985-03-30 Block copolymer

Publications (2)

Publication Number Publication Date
JPS61225218A true JPS61225218A (en) 1986-10-07
JPH0629319B2 JPH0629319B2 (en) 1994-04-20

Family

ID=13353250

Family Applications (1)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0268765A2 (en) * 1986-11-20 1988-06-01 Dainippon Ink And Chemicals, Inc. Resin comprising a polyphenylene sulfide/polyphenylene sulfone block copolymer, process for preparing the copolymer and molded article
EP0275991A2 (en) * 1987-01-20 1988-07-27 Dainippon Ink And Chemicals, Inc. Thermoplastic resin composition
US4946912A (en) * 1985-11-13 1990-08-07 Dainippon Ink And Chemicals, Inc. Block copolymer and compositions
US5064937A (en) * 1989-03-27 1991-11-12 Eastman Kodak Company Copoly(phenylene sulfide)
US5258489A (en) * 1993-03-05 1993-11-02 Eastman Chemical Company Fluorinated poly(arylene sulfide)(arylene disulfide)
WO2014136448A1 (en) 2013-03-06 2014-09-12 東レ株式会社 Block copolymer and production method for same

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4946912A (en) * 1985-11-13 1990-08-07 Dainippon Ink And Chemicals, Inc. Block copolymer and compositions
EP0268765A2 (en) * 1986-11-20 1988-06-01 Dainippon Ink And Chemicals, Inc. Resin comprising a polyphenylene sulfide/polyphenylene sulfone block copolymer, process for preparing the copolymer and molded article
EP0275991A2 (en) * 1987-01-20 1988-07-27 Dainippon Ink And Chemicals, Inc. Thermoplastic resin composition
US5064937A (en) * 1989-03-27 1991-11-12 Eastman Kodak Company Copoly(phenylene sulfide)
US5258489A (en) * 1993-03-05 1993-11-02 Eastman Chemical Company Fluorinated poly(arylene sulfide)(arylene disulfide)
WO2014136448A1 (en) 2013-03-06 2014-09-12 東レ株式会社 Block copolymer and production method for same
CN105008427A (en) * 2013-03-06 2015-10-28 东丽株式会社 Block copolymer and production method for same
EP2966107A4 (en) * 2013-03-06 2016-08-17 Toray Industries Block copolymer and production method for same
JPWO2014136448A1 (en) * 2013-03-06 2017-02-09 東レ株式会社 Block copolymer and method for producing the same
US9718928B2 (en) 2013-03-06 2017-08-01 Toray Industries, Inc. Block copolymer and production method of the same

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