JPH02229809A - Improved polybutadiene rubber - Google Patents
Improved polybutadiene rubberInfo
- Publication number
- JPH02229809A JPH02229809A JP5013589A JP5013589A JPH02229809A JP H02229809 A JPH02229809 A JP H02229809A JP 5013589 A JP5013589 A JP 5013589A JP 5013589 A JP5013589 A JP 5013589A JP H02229809 A JPH02229809 A JP H02229809A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- polybutadiene
- rubber
- impact
- lithium
- 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
- 229920002857 polybutadiene Polymers 0.000 title description 26
- 239000003054 catalyst Substances 0.000 claims abstract description 17
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical group C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 claims abstract description 15
- 229920000642 polymer Polymers 0.000 claims abstract description 12
- 150000001451 organic peroxides Chemical class 0.000 claims abstract description 10
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 8
- 229910052744 lithium Inorganic materials 0.000 claims abstract description 7
- 229920002554 vinyl polymer Polymers 0.000 claims abstract description 7
- 125000001979 organolithium group Chemical group 0.000 claims description 7
- 238000012545 processing Methods 0.000 claims description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 abstract description 23
- 229920005989 resin Polymers 0.000 abstract description 19
- 239000011347 resin Substances 0.000 abstract description 19
- 238000000034 method Methods 0.000 abstract description 17
- 229920001971 elastomer Polymers 0.000 abstract description 16
- 239000005060 rubber Substances 0.000 abstract description 10
- 150000001491 aromatic compounds Chemical class 0.000 abstract description 4
- 239000007795 chemical reaction product Substances 0.000 abstract description 4
- 229920006216 polyvinyl aromatic Polymers 0.000 abstract description 4
- 238000010528 free radical solution polymerization reaction Methods 0.000 abstract description 3
- 239000003607 modifier Substances 0.000 abstract description 3
- 230000000379 polymerizing effect Effects 0.000 abstract description 3
- 150000002642 lithium compounds Chemical class 0.000 abstract description 2
- 239000011243 crosslinked material Substances 0.000 abstract 1
- DWAWYEUJUWLESO-UHFFFAOYSA-N trichloromethylsilane Chemical compound [SiH3]C(Cl)(Cl)Cl DWAWYEUJUWLESO-UHFFFAOYSA-N 0.000 abstract 1
- 239000005062 Polybutadiene Substances 0.000 description 21
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 17
- 229920001890 Novodur Polymers 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 10
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 8
- 239000000047 product Substances 0.000 description 8
- 239000000243 solution Substances 0.000 description 8
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 6
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 6
- 238000006116 polymerization reaction Methods 0.000 description 6
- 238000005259 measurement Methods 0.000 description 5
- 229920005990 polystyrene resin Polymers 0.000 description 5
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 4
- MZRVEZGGRBJDDB-UHFFFAOYSA-N N-Butyllithium Chemical compound [Li]CCCC MZRVEZGGRBJDDB-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 4
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 3
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 3
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 3
- 239000010931 gold Substances 0.000 description 3
- 229910052737 gold Inorganic materials 0.000 description 3
- 238000004898 kneading Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 150000002900 organolithium compounds Chemical class 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- KVNYFPKFSJIPBJ-UHFFFAOYSA-N 1,2-diethylbenzene Chemical compound CCC1=CC=CC=C1CC KVNYFPKFSJIPBJ-UHFFFAOYSA-N 0.000 description 2
- VXEGSRKPIUDPQT-UHFFFAOYSA-N 4-[4-(4-methoxyphenyl)piperazin-1-yl]aniline Chemical compound C1=CC(OC)=CC=C1N1CCN(C=2C=CC(N)=CC=2)CC1 VXEGSRKPIUDPQT-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000000748 compression moulding Methods 0.000 description 2
- LJSQFQKUNVCTIA-UHFFFAOYSA-N diethyl sulfide Chemical compound CCSCC LJSQFQKUNVCTIA-UHFFFAOYSA-N 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000005049 silicon tetrachloride Substances 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- FWFAJEYKHANIJP-UHFFFAOYSA-N 1,3,5-tris(ethenyl)naphthalene Chemical compound C1=CC=C(C=C)C2=CC(C=C)=CC(C=C)=C21 FWFAJEYKHANIJP-UHFFFAOYSA-N 0.000 description 1
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical compound C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- OIFBSDVPJOWBCH-UHFFFAOYSA-N Diethyl carbonate Chemical compound CCOC(=O)OCC OIFBSDVPJOWBCH-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- LXXUYORAHKLDLS-UHFFFAOYSA-N [Li]C1CCC([Li])C(CC)C1 Chemical compound [Li]C1CCC([Li])C(CC)C1 LXXUYORAHKLDLS-UHFFFAOYSA-N 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- MPMBRWOOISTHJV-UHFFFAOYSA-N but-1-enylbenzene Chemical compound CCC=CC1=CC=CC=C1 MPMBRWOOISTHJV-UHFFFAOYSA-N 0.000 description 1
- 150000004650 carbonic acid diesters Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- -1 divinyl aromatic compounds Chemical class 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 150000002366 halogen compounds Chemical class 0.000 description 1
- GNOIPBMMFNIUFM-UHFFFAOYSA-N hexamethylphosphoric triamide Chemical compound CN(C)P(=O)(N(C)C)N(C)C GNOIPBMMFNIUFM-UHFFFAOYSA-N 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- WTTUTKBXMMXKBQ-UHFFFAOYSA-N lithium;stilbene Chemical compound C=1C=CC=CC=1C([Li])C([Li])C1=CC=CC=C1 WTTUTKBXMMXKBQ-UHFFFAOYSA-N 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- DAZXVJBJRMWXJP-UHFFFAOYSA-N n,n-dimethylethylamine Chemical compound CCN(C)C DAZXVJBJRMWXJP-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- SSDSCDGVMJFTEQ-UHFFFAOYSA-N octadecyl 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CCCCCCCCCCCCCCCCCCOC(=O)CCC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 SSDSCDGVMJFTEQ-UHFFFAOYSA-N 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 239000004926 polymethyl methacrylate Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 230000002940 repellent Effects 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 150000004756 silanes Chemical class 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
- 150000003606 tin compounds Chemical class 0.000 description 1
- HPGGPRDJHPYFRM-UHFFFAOYSA-J tin(iv) chloride Chemical compound Cl[Sn](Cl)(Cl)Cl HPGGPRDJHPYFRM-UHFFFAOYSA-J 0.000 description 1
- 239000012745 toughening agent Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- IMFACGCPASFAPR-UHFFFAOYSA-N tributylamine Chemical compound CCCCN(CCCC)CCCC IMFACGCPASFAPR-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Graft Or Block Polymers (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、新規なポリブタジエンに関し、特にスチレン
系樹脂やポリメチルメタクリレート樹脂〔従来の技術〕
近年、ゴム変性されたスチレン系樹脂、即ち耐衝撃性ス
チレン系樹脂は、その製法技術の進歩と共に、樹脂の用
途が家庭電気機器のハウジングやその部品、事務機器の
部品、日用雑貨品及び玩具などの各種用途に広がってき
ている.このような背景により、最近は耐衝撃性スチレ
ン系樹脂に対して、より優れた各種物性が要求されるよ
うになり、なかでも耐衝撃性と剛性、さらに光沢といっ
た外観性をもバランスさせる高度なものとなっている.
周知のように、耐衝撃性の向上はゴム状重合体の金量を
増加させることより可能となるが、ゴム状重合体を増加
させたスチレン系樹脂は、耐衝撃性が向上する反面、剛
性が著しく低下し、光沢も低下する。一方、剛性や光沢
の向上は、ゴム状重合体の含脊■を低下させるか、ある
いは樹脂中に分散するゴム状重合体の粒子を微細化させ
ることにより可能となるが、反面耐i11撃性の低下が
著しい。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a new polybutadiene, particularly styrenic resins and polymethyl methacrylate resins [Prior Art] In recent years, rubber-modified styrenic resins, that is, impact-resistant With advances in manufacturing technology, the use of polystyrene-based resins has expanded to include housings and parts for household electrical equipment, parts for office equipment, daily necessities, and toys. Against this background, impact-resistant styrenic resins have recently been required to have various superior physical properties, and in particular, advanced styrene resins that balance impact resistance, rigidity, and appearance such as gloss are required. It has become a thing. As is well known, impact resistance can be improved by increasing the amount of gold in the rubbery polymer, but styrenic resins with increased rubbery polymer have improved impact resistance, but have lower rigidity. is significantly reduced, and the gloss is also reduced. On the other hand, improvements in rigidity and gloss can be achieved by reducing the spine content of the rubbery polymer or by making the particles of the rubbery polymer dispersed in the resin finer. There is a significant decrease in
さらに、近年、耐衝撃性スチレン系樹脂は、ABS樹脂
(アクリロニトリル・プタジエン・スチレン樹脂)の用
途分野への進出が注目されているが、最大の問題点は、
耐衝讐性スチレン系樹脂の光沢が劣ることである.
そこで最近では、光沢を改良するためゴム粒子径を、例
えば1、7μ以下と小さくコントロールする方法が採用
されているが、衝撃強度が劣り実用に耐え難いというの
が現状である.
このように、耐衝撃性と光沢、さらに剛性は相反する特
性であるため、高い光沢と剛性を維持し、しかも優れた
耐衝撃性を有するスチレン系樹脂を得ることは困難であ
る.
従来、耐衝撃性スチレン系樹脂を改良する方法として、
溶液粘度の特定化(特開昭5 8−4 9 34号公報
)、溶液粘度とムーニー粘度の関係の特定化(特開昭5
3−44188号公報)、分子量分布の特定化(特開昭
54−15912号公報)、溶液粘度と有機過酸化物架
橋体における引張弾性率、膨潤度の関係の特定化(特開
昭6 0−2 5 0021号公報)などの方法が提案
されている.〔発明が解決しようとしている課題〕
然しなから、これらの方法においては、光沢と耐街窄性
と剛性の3者のバランスを向上させることについては、
必ずしも満足しうるものではない.また、特開昭60−
250021号公報において、低引張弾性率を有する特
定のゴム状重合体を強靭化剤として用いることにより、
耐衝撃性と剛性がともに優れている耐衝撃性スチレン系
樹脂が得られることが述べられている.
〔課題を解決するための手段〕
そこで、本発明者らは、耐衝撃性と剛性、さらに光沢の
バランスに優れた耐衝撃性スチレン系樹脂を得るための
ゴム状重合体の開発をすべく、特に、ゴム状重合体の弾
性率の低いゴムについて研究を重ねた.その結果、ゴム
状重合体の弾性率が従来のゴムより大幅に低い碩域にお
いて、衝撃強度と閘性に優れ、かつ光沢の良好な樹脂が
得られることを発見した.
すなわち本発明は;
例えば、有機リチウム化合物の存在下に溶液重合して得
られたポリプタジエンであって、(aH,2−ビニル結
合金量が10〜40重量%で、かつ
(b)ムーニー粘度(ML..,)が30〜80で、(
C)25℃で測定した5重撥%スチレン溶液粘度(S
V)が20〜60センチポイズ(cps)の範囲であり
、
(d)後述の特定の条件で架橋させた該ポリプタジエン
の有II通酸化物架橋物における、後述の特定の条件下
で測定する弾性率(E)が10〜18kg/ cd以下
で
あることを特徴とする、スチレン系樹脂の改良に好適な
ゴム重合体である.
本発明のポリブタジエンは、市販の有機リチウム系触媒
によるポリブタジエンと比較して、弾性率が極めて低い
ことが特徴であり、該ポリブタジエンの重合技術におい
ても工夫が必要である.以下、本発明をさらに詳細に説
明する.本発明の特定のポリブタジエンは、特定の有機
リチウム化合物触媒を用いて、,溶液重合することによ
り得ることができる.
特定の有機リチウム化合物触媒としては、例えば、特開
昭57−40513号公報に示される様に、1,2−ジ
リチオ−1.2−ジフェニルエタン、1,4−ジリチオ
−2〜エチルシクロヘキサンの如き多官能性有機リチウ
ムと有機モノリチウムとの混合物、或いは有機七ノリ,
チウムとポリビニル芳香族化合物(例えばジビニルベン
ゼン)の2者を含む反応生成物等がある.
本発明のポリブタジエンは、1,2−ビニル結合金量が
10〜40重量%であり、好ましくはlO〜25重量%
である.この範囲外であれば、耐衝撃性スチレン系樹脂
に用いた場合、得られる樹脂の耐衝撃性が不十分となる
.
このような特定のミクロ構造を有するポリブタジエンを
製造する方法は、上記構造になるような方法であれば従
来公知のいかなる方法であってもよいが、具体的な方法
として、例えば重合系にジメチルエーテル、ジエチルエ
ーテル、テトラヒド口フラン等のエーテル類;ジメチル
サルファイド、ジエチルサルファイド等のチオエーテル
類;ジメチルエチルアミン、トリエチルアミン等のアミ
ン類などの極性化合物を添加して重合を行う方法が挙げ
られる.
このビニル結合は、分子饋中に均一にあっても、特公昭
48−875号公報に示されるように分子額に沿って漸
減的に変化するようなものでも、あるいはブロック的に
結合していてもよく、全体として10〜40重量%含ま
れていればよい.本発明のポリブタジエンは1.2−ビ
ニル結合金量が10〜40重置%であるが、これに伴い
、シスー1,4一結合金量は20〜40重量%、トラン
ス−1.4一結合金量は30〜60重量%となる.
本発明のポリブタジエンゴムは、ムーニー粘度(ML.
..)は30〜80であり、25℃で測定した5重景%
スチレン溶液粘度(SV)は、20〜60センチポイズ
(cps)であることが必要である.ムーニー粘度30
未満では、耐衝撃性ボリスチレン系樹脂に用いた場合に
、得られる樹脂の耐衝撃性が劣り、80より高い場合に
外観特性が劣る.また、5重量%スチレン溶液粘度が2
0cps未満では、耐衝撃性ボリスチレン系樹脂に用い
た場合に、得られる樹脂の耐衝撃性が劣り、60cps
より高い場合には、剛性と外観特性とが低下する.
さらに、本発明でポリブタジエンの有機過酸化物架橋体
における弾性率は、lO〜18kg/cdであることを
要する.弾性率がIOkg/d未満あるいは、18kg
/cjより高い場合には、耐衝撃性ボリスチレン系樹脂
に用いた時、いずれも得られる樹脂の耐衝撃性が劣る.
次に、本発明で用いるポリブタジエンの特性の測定方法
について述べる.
■ムーニー粘度は、ML1.4 (100℃)である
.
■5重量%スチレン溶液粘度はキヤノンフェンスヶ型粘
度計を用いて25℃で測定した.■1,2−ビニル結合
金量は、赤外分光光度計を用いてモレロ法(La c
himica EL’ industria,41
,758 (1959)による〕で測定した.
■本発明でいう弾性率とは、特定の条件で架橋、調製し
た有機過酸化物架橋物を粘弾性測定装置を用いて、特定
の条件で測定した動的弾性率をいう.以下にその具体的
な条件について述べる;l)まず、有機過酸化物による
架橋物の調製は、以下の方法で行う.
ポリブタジエンゴム55gと有機過酸化物のジクミルバ
ーオキサイド0.055g(ゴム100重量部に対して
0. 1重量部)を下記の装置に混練する.
混練装置:■東洋精機製作所製
ラボブラストミル(型式LPM−2500−200)混
練条件:■予備混合(サンプル投入);50℃、10回
転、30秒、
■混練;50℃、50回転、2分間、
この混練物を160″Cの温度で2o0kg/cjの圧
力下、18分間圧縮成形して、有機過酸化物架橋物のシ
ートを得る.
2)次いで、この有機過酸化物架橋物のシート成形品よ
り試験片をカットして、粘弾性測定装置により動的弾性
率を測定する.
(測定条件)
■測定機種:■岩本製作所製VESF−111型、■測
定法 :伸長変形(初期荷重一定)、■測定周波数:1
00Hz,
■初期荷重: 200g、
■加振振幅:3ooμ、
■測定温度;25℃、
■サンプル寸法: (幅)5■×(厚さ)2ffll×
(長さ)30■、
本発明のポリブタジエンゴムは、前述したように、従来
の一般的なゴムに比べて有機過酸化物架橋物の弾性率が
低い.このようなポリブタジエンを製造するためには、
何らかの工夫が必要である.具体的な方法としては、例
えば、少なくとも有機リチウム化合物とポリビニル芳香
族化合物とを含む反応生成物を触媒として、ブタジエン
単量体を重合し、重合が実質的に完了した後、生成した
末端リチウム活性重合体を多官能性処理剤で結合させる
などの方法がある.
しかも、ブタジエン単量体を重合させる場合に、バッジ
式で行い、かつその上、触媒とブタジエンとをそれぞれ
分割添加して、反応させる方法が好ましい.
ここでいうポリビニル芳香族化合物とは、例えばジビニ
ルベンゼン、1.2.4−トIJビニルベンゼン、1.
3−ジビニルナフタレン、1,3.5−トリビニルナフ
タレン、2.4−ジビニルビフェニル、3.5.4−ト
リビニルビフェニルなどであり、特にジビニルベンゼン
が好ましい.このジビニルベンゼンには、o−、m −
% p−の異性体があるが、これらの異性体混合物のジ
ビニルベンゼンを用いても十分に効果が発運される。Furthermore, in recent years, impact-resistant styrene-based resins have been attracting attention for their advancement into the application field of ABS resins (acrylonitrile-ptadiene-styrene resins), but the biggest problem is that
The problem is that the impact-resistant styrene resin has poor gloss. Recently, a method has been adopted to control the rubber particle size to a value of 1.7 μm or less in order to improve gloss, but the current situation is that the impact strength is poor and it is difficult to put it into practical use. In this way, since impact resistance, gloss, and rigidity are contradictory properties, it is difficult to obtain a styrenic resin that maintains high gloss and rigidity and also has excellent impact resistance. Conventionally, as a method to improve impact-resistant styrenic resin,
Specification of solution viscosity (Japanese Unexamined Patent Publication No. 5 8-4 9 34), Specification of the relationship between solution viscosity and Mooney viscosity (Japanese Patent Application Laid-open No. 5
3-44188), specification of molecular weight distribution (JP-A-54-15912), specification of the relationship between solution viscosity, tensile modulus and degree of swelling in organic peroxide cross-linked products (JP-A 1987-15912), -250021) and other methods have been proposed. [Problem to be solved by the invention] However, in these methods, it is difficult to improve the balance of gloss, road narrowing resistance, and rigidity.
This is not necessarily satisfactory. Also, JP-A-60-
In JP 250021, by using a specific rubbery polymer having a low tensile modulus as a toughening agent,
It is stated that impact-resistant styrenic resins with excellent impact resistance and rigidity can be obtained. [Means for Solving the Problems] Therefore, the present inventors aimed to develop a rubber-like polymer to obtain an impact-resistant styrenic resin with an excellent balance of impact resistance, rigidity, and gloss. In particular, we conducted extensive research on rubber-like polymers with low elastic modulus. As a result, they discovered that a resin with excellent impact strength and locking properties as well as good gloss can be obtained in the range where the elastic modulus of the rubbery polymer is significantly lower than that of conventional rubber. That is, the present invention provides; For example, a polyptadiene obtained by solution polymerization in the presence of an organolithium compound, which has an aH,2-vinyl bond amount of 10 to 40% by weight, and (b) a Mooney viscosity of ( ML..,) is 30-80, (
C) Viscosity of 5-layer repellent % styrene solution measured at 25°C (S
V) is in the range of 20 to 60 centipoise (cps), and (d) an elastic modulus measured under the specific conditions described below in the cross-linked polyptadiene per oxide crosslinked under the specific conditions described below. A rubber polymer suitable for improving styrene resins, characterized in that (E) is 10 to 18 kg/cd or less. The polybutadiene of the present invention is characterized by an extremely low modulus of elasticity compared to commercially available polybutadiene prepared using organolithium catalysts, and the polymerization technology for the polybutadiene requires some ingenuity. The present invention will be explained in more detail below. The specific polybutadiene of the present invention can be obtained by solution polymerization using a specific organolithium compound catalyst. Specific organolithium compound catalysts include, for example, 1,2-dilithio-1,2-diphenylethane and 1,4-dilithio-2-ethylcyclohexane, as shown in JP-A-57-40513. A mixture of a polyfunctional organolithium and an organic monolithium, or an organic seven-layer mixture,
There are reaction products containing both lithium and polyvinyl aromatic compounds (eg divinylbenzene). The polybutadiene of the present invention has a 1,2-vinyl bond amount of 10 to 40% by weight, preferably 10 to 25% by weight.
It is. If it is outside this range, the resulting resin will have insufficient impact resistance when used in an impact-resistant styrenic resin. The method for producing polybutadiene having such a specific microstructure may be any conventionally known method as long as it produces the above structure, but as a specific method, for example, dimethyl ether, dimethyl ether, Examples of polymerization methods include adding polar compounds such as ethers such as diethyl ether and tetrahydrofuran; thioethers such as dimethyl sulfide and diethyl sulfide; and amines such as dimethylethylamine and triethylamine. These vinyl bonds may exist uniformly in the molecule, or they may change gradually along the molecular length as shown in Japanese Patent Publication No. 48-875, or they may be bonded in blocks. It is sufficient that the total content is 10 to 40% by weight. In the polybutadiene of the present invention, the amount of 1,2-vinyl bond gold is 10 to 40% by weight. The amount of gold is 30-60% by weight. The polybutadiene rubber of the present invention has a Mooney viscosity (ML.
.. .. ) is 30-80, and the 5-fold view% measured at 25℃
The styrene solution viscosity (SV) needs to be between 20 and 60 centipoise (cps). Mooney viscosity 30
If it is less than 80, the resulting resin will have poor impact resistance when used in an impact-resistant polystyrene resin, and if it is higher than 80, the appearance characteristics will be poor. In addition, the viscosity of 5% by weight styrene solution is 2
If it is less than 0 cps, the resulting resin will have poor impact resistance when used in impact resistant polystyrene resin, and if it is less than 60 cps.
If it is higher, the stiffness and appearance properties will be reduced. Furthermore, in the present invention, the elastic modulus of the organic peroxide crosslinked polybutadiene is required to be 10 to 18 kg/cd. Elastic modulus is less than IO kg/d or 18 kg
If it is higher than /cj, the resulting resin will have poor impact resistance when used in impact resistant polystyrene resins. Next, a method for measuring the properties of polybutadiene used in the present invention will be described. ■Mooney viscosity is ML1.4 (100°C). ■The viscosity of the 5% by weight styrene solution was measured at 25°C using a Canon fence type viscometer. ■The amount of 1,2-vinyl bond is measured using the Morello method (La c
himica EL' industry, 41
, 758 (1959)]. ■The elastic modulus as used in the present invention refers to the dynamic elastic modulus measured under specific conditions using a viscoelasticity measuring device for an organic peroxide crosslinked product that has been crosslinked and prepared under specific conditions. The specific conditions are described below; l) First, the preparation of a crosslinked product using an organic peroxide is carried out by the following method. 55 g of polybutadiene rubber and 0.055 g of dicumyl peroxide (0.1 part by weight per 100 parts by weight of rubber), an organic peroxide, are kneaded in the following apparatus. Kneading equipment: ■ Labo blast mill manufactured by Toyo Seiki Seisakusho (model LPM-2500-200) Kneading conditions: ■ Pre-mixing (sample input): 50°C, 10 rotations, 30 seconds, ■ Kneading: 50°C, 50 rotations, 2 minutes , This kneaded material is compression molded at a temperature of 160''C under a pressure of 200 kg/cj for 18 minutes to obtain a sheet of the organic peroxide crosslinked product. 2) Next, a sheet of this organic peroxide crosslinked product is formed. Cut a test piece from the product and measure the dynamic elastic modulus using a viscoelasticity measuring device. (Measurement conditions) ■Measurement model: ■VESF-111 model manufactured by Iwamoto Seisakusho ■Measurement method: Elongation deformation (constant initial load) , ■Measurement frequency: 1
00Hz, ■Initial load: 200g, ■Excitation amplitude: 3ooμ, ■Measurement temperature: 25℃, ■Sample dimensions: (width) 5■ (thickness) 2ffll×
(Length) 30 cm. As mentioned above, the polybutadiene rubber of the present invention has a lower elastic modulus of the organic peroxide crosslinked product than conventional general rubber. In order to produce such polybutadiene,
Some kind of ingenuity is required. As a specific method, for example, a butadiene monomer is polymerized using a reaction product containing at least an organic lithium compound and a polyvinyl aromatic compound as a catalyst, and after the polymerization is substantially completed, the generated terminal lithium activity is There are methods such as bonding polymers with polyfunctional processing agents. Furthermore, when polymerizing the butadiene monomer, it is preferable to perform the polymerization in a batch method, and to add the catalyst and butadiene in portions to react. The polyvinyl aromatic compounds mentioned here include, for example, divinylbenzene, 1.2.4-toIJ vinylbenzene, 1.
Examples include 3-divinylnaphthalene, 1,3.5-trivinylnaphthalene, 2.4-divinylbiphenyl, 3.5.4-trivinylbiphenyl, and divinylbenzene is particularly preferred. This divinylbenzene has o-, m-
% p- isomers, and divinylbenzene, which is a mixture of these isomers, can be used with sufficient effect.
一方、多官能性処理剤としては、例えばトリクロロメチ
ルシラン、ジメチルジクロロシラン、シリコンテトラク
ロライドなどのシラン化合物[J,po1ym,sci
,^−1.3.93(1965) ) ,炭酸ジエチル
などの炭酸ジエステル類(特公昭54−8716号公報
)、ジビニルベンゼンなどのジビニル芳香族化合物(特
開昭51−34290号公報)、四塩化炭素などのハロ
ゲン化合物、テトラクロ口スズのようなスズ化合物など
、公知のものを使用することができる.これらはそれぞ
れ単独で用いてもよいし、2種以上組み合わせて用いて
も良い, さらに、トリエチルアミン、トリn−ブチル
アミン、ヘキサメチルホスホルアミド、ジエチルエーテ
ル、テトラヒド口フランなどの極性物質を重合系に添加
しても良い.
本発明のポリプタジエンは有機リチウム系触媒でブタジ
エン単量体を重合し、得られる末端リチウム活性重合体
を多官能性処理剤で結合させているが、結合されて生成
した重合体成分の金量は、全重合体中の2031量%以
上であることが好ましく、50〜95重量%であること
がより好ましい.この結合重合体成分量は、多官能性処
理剤と有機リチウム系触媒の量比によって調整される.
このようにして得られたポリブタジエンの分子量分布に
ついては、GPC (ゲル・パーミエーシッンク口マト
グラフイー)で測定した重量平均分子1(’nw)と数
平均分子量(Mn)(7)比(MW/n)は通常2.2
〜4.2の範囲にあり、ポリモーダルな形状となる。On the other hand, examples of polyfunctional treatment agents include silane compounds [J, polyym, sci
, ^-1.3.93 (1965) ), carbonic acid diesters such as diethyl carbonate (Japanese Patent Publication No. 54-8716), divinyl aromatic compounds such as divinylbenzene (Japanese Patent Application Laid-Open No. 51-34290), Known compounds such as halogen compounds such as carbon chloride and tin compounds such as tetrachlorotin can be used. Each of these may be used alone or in combination of two or more. Furthermore, polar substances such as triethylamine, tri-n-butylamine, hexamethylphosphoramide, diethyl ether, and tetrahydrofuran may be added to the polymerization system. May be added. The polyptadiene of the present invention is produced by polymerizing butadiene monomers using an organolithium-based catalyst, and bonding the resulting terminal lithium-activated polymer with a polyfunctional treatment agent. , preferably 2031% by weight or more, more preferably 50 to 95% by weight, based on the total polymer. The amount of this bonded polymer component is adjusted by the ratio of the polyfunctional treatment agent to the organolithium catalyst.
Regarding the molecular weight distribution of the polybutadiene obtained in this way, the ratio (MW /n) is usually 2.2
~4.2, resulting in a polymodal shape.
本発明で用いるポリブタジエンの製造例としては、オー
トクレープ中にシクロヘキサンを仕込み、テトラヒド口
フランをシクロヘキサンに対し50pp一〜4000p
p−添加する.次に、ブタジエンモノマー総使用量の3
0〜70%を加えて、60〜80℃に昇温後、別にn−
ブチルリチウムとブタジエンモノマーとジビニルベンゼ
ンとから調製した反応生成触媒の総使用量(n−ブチル
リチウム換算量としてブタジエンモノマーの使用量lO
O部に対して0.25〜0.60部)のIθ〜50%を
添加して反応を開始する.モノマーの反応が終了後、さ
らに残りのモノマー(ブタジエンモノマー総使用量の7
0〜30%)と残りの触媒(総使用触媒の90〜50%
)を添加して反応を続行する.
この反応終了後、多官能性処理剤として、四塩化ケイ素
を0.05〜0.15部添加、カップリング処理したう
えで、安定剤を添加し、溶削を分離し、目的のポリプタ
ジエンを得る.
〔実施例〕
以下に若干の実施例を示し、本発明の具体的実施態様を
示すが、これは本発明の趣旨をより具体的に説明するた
めのものであって、本発明を限定するものではない.
実施例l
次に示す方法により、表−1の仕込み量及び、条件で、
ポリブタジエンを得た.
内容積lOlのオートクレープを洗浄乾燥し、窒素置換
後、予め精製、乾燥したシクロヘキサンとテトラヒド口
フランとを加え、次に、乾燥した初期プタジエンモノマ
ーを加えた.次いで、この溶液を反応開始温度まで昇温
し、初期触媒を加え.。As an example of producing polybutadiene used in the present invention, cyclohexane is charged in an autoclave, and tetrahydrofuran is added at a concentration of 50 pp to 4000 pp to cyclohexane.
p-Add. Next, 3 of the total amount of butadiene monomer used
After adding 0-70% of n-
Total amount of reaction product catalyst prepared from butyllithium, butadiene monomer, and divinylbenzene (amount of butadiene monomer used as n-butyllithium equivalent)
The reaction is started by adding 50% of Iθ (0.25-0.60 parts based on parts O). After the monomer reaction is completed, add the remaining monomer (7 of the total amount of butadiene monomer used)
0-30%) and the remaining catalyst (90-50% of the total catalyst used)
) to continue the reaction. After this reaction is complete, add 0.05 to 0.15 parts of silicon tetrachloride as a polyfunctional treatment agent, perform a coupling treatment, add a stabilizer, separate the cuttings, and obtain the desired polyptadiene. .. [Examples] Some examples are shown below to show specific embodiments of the present invention, but these are intended to explain the gist of the present invention more specifically, and are not intended to limit the present invention. isn't it. Example 1 By the method shown below, with the amount of preparation and conditions shown in Table-1,
Polybutadiene was obtained. After washing and drying an autoclave with an internal volume of 100 liters and purging it with nitrogen, previously purified and dried cyclohexane and tetrahydrofuran were added, and then the dried initial putadiene monomer was added. Next, this solution was heated to the reaction starting temperature, and an initial catalyst was added. .
反応を開始した.反応終了後、引き続いて、添加触媒と
添加ブタジエンモノマー等を加え、反応を再開し、.反
応終了後、四塩化ケイ素を加えて、20分間反応した。The reaction started. After the reaction is completed, the added catalyst, added butadiene monomer, etc. are added, and the reaction is restarted. After the reaction was completed, silicon tetrachloride was added and reacted for 20 minutes.
反応終了後、得られたボリマー溶液に安定剤として2,
6−ジーt−4−メチルフェノール(BHT)をボリマ
ーtoO重flLaBに対し0.5重量部加え、溶媒を
2本ロールで加熱除去した.
以下、実施例1と同様の手法にて、表−1に示した条件
で実施例1〜6及び比較例1〜6のポリブタジエンを得
た.
このポリブタジエンの製造に用いた有機リチウム基質触
媒の調製方法を表一八に示す.表一八
有機リチウム基質触媒A,B,Cは、夫々表一Aの調製
比、条件で反応・調製した.
ジビニルベンゼンは、商業的に手に入るジビニルベンゼ
ンを用いた.この製品は、57%のジビニルベンゼン異
性体を含有する混合物で、その残部はエチルビニルベン
ゼン、ジエチルベンゼンであった.
実施例1〜6および比較例1〜6で得た、夫々のポリブ
タジエンを用いて、以下に述べる塊状重合法により耐衝
撃性スチレン系樹脂を得た.ポリブタジエン28〜42
g,スチレン672〜6 5 8 g,ミネラルオイル
14g、安定剤(イルガノックス1076)2.1gを
それぞれの割合で均一に溶解させた.
これを攪拌装置付Ilセバラブルフラスコに移し、12
0゜Cで3時間、135゜Cで2時間、150℃で2時
間、170℃で2時間重合させた.さらに230℃で3
0分間加熱後、未反応物を減圧除去した後、得られた重
合体を押出機でベレット化した.
■アイゾット街輩強度は、圧縮成形によって作成された
厚さ3.2111の試験片を用いて、JISK−7 1
1 0に従って測定した.■光沢は、ASTM D
−638に従い、射出成形したダンベル試験片を用いて
、ASTM D−523に従い、ゲート部とエンドゲ
ート部の光沢度(入射角601)を測定し、平均した.
■曲げ弾性率は、圧縮成形によって作成した厚さ3.2
−の試験片を用いて、ASTM D−790に従って
測定した.
得られた結果を、参考実施例1〜6、参考比較例1〜6
に示す.
参考実施例1〜6の結果から明らかなように、本発明の
ポリブタジエンを用いて耐衝撃性ボリスチレン樹脂を重
合した場合に、光沢、剛性が優れ、同時に耐衝撃性の改
良された樹脂が得られることが分かった.
これに対して、参考比較例1〜6の結果から明らかなよ
うに、本発明以外のポリブタジエンを用いて、耐衝撃性
ポリスチレン樹脂を得た場合には、光沢、耐衝撃性のい
ずれかの特性が劣る.〔発明の効果]
本発明のポリブタジエンは、スチレン系樹脂の製造に用
いた場合、スチレン系樹脂の外観、剛性を損なうことな
く、耐衝撃性を改良できる.また、アクリル樹脂の耐衝
撃性の改良にも用いられる.さらに、従来、タイヤ用に
使われていたゴムの代わりに、本発明のポリプタジエン
を用いれば、加工性と耐屈曲性能を向上出来る.以上の
様に、本発明のポリブタジエンは、樹脂の改質剤として
優れ、またタイヤ用ゴムとしても優れた効果を発揮する
.After the reaction, 2,
0.5 parts by weight of 6-di-t-4-methylphenol (BHT) was added to the polymer toO heavy flLaB, and the solvent was removed by heating with two rolls. Polybutadiene of Examples 1 to 6 and Comparative Examples 1 to 6 was obtained in the same manner as in Example 1 under the conditions shown in Table 1. Table 18 shows the method for preparing the organolithium substrate catalyst used to produce this polybutadiene. Table 18 Organolithium substrate catalysts A, B, and C were reacted and prepared using the preparation ratios and conditions shown in Table 1A, respectively. Commercially available divinylbenzene was used. This product was a mixture containing 57% divinylbenzene isomers, the balance being ethylvinylbenzene and diethylbenzene. Using the respective polybutadienes obtained in Examples 1 to 6 and Comparative Examples 1 to 6, impact-resistant styrenic resins were obtained by the bulk polymerization method described below. Polybutadiene 28-42
g, 672 to 658 g of styrene, 14 g of mineral oil, and 2.1 g of a stabilizer (Irganox 1076) were uniformly dissolved in their respective ratios. Transfer this to an Il separable flask equipped with a stirrer, and
Polymerization was carried out at 0°C for 3 hours, at 135°C for 2 hours, at 150°C for 2 hours, and at 170°C for 2 hours. Further at 230℃ 3
After heating for 0 minutes, unreacted materials were removed under reduced pressure, and the resulting polymer was pelletized using an extruder. ■Izod street strength is measured using JISK-7 1 test piece made by compression molding with a thickness of 3.2111.
Measured according to 10. ■Gloss is ASTM D
-638, using a dumbbell test piece injection molded, the glossiness (incidence angle 601) of the gate part and end gate part was measured in accordance with ASTM D-523 and averaged.
■The bending elastic modulus is 3.2 for the thickness created by compression molding.
- Measurement was performed according to ASTM D-790 using a test piece. The obtained results are shown in Reference Examples 1 to 6 and Reference Comparative Examples 1 to 6.
It is shown in As is clear from the results of Reference Examples 1 to 6, when impact-resistant polystyrene resin is polymerized using the polybutadiene of the present invention, a resin with excellent gloss and rigidity and at the same time improved impact resistance can be obtained. I found out that. On the other hand, as is clear from the results of Reference Comparative Examples 1 to 6, when impact-resistant polystyrene resin is obtained using polybutadiene other than the present invention, either the gloss or impact resistance properties is inferior. [Effects of the Invention] When the polybutadiene of the present invention is used in the production of styrenic resins, it can improve impact resistance without impairing the appearance and rigidity of the styrene resins. It is also used to improve the impact resistance of acrylic resins. Furthermore, if the polyptadiene of the present invention is used in place of the rubber conventionally used for tires, processability and bending resistance can be improved. As described above, the polybutadiene of the present invention is excellent as a modifier for resins and also exhibits excellent effects as a rubber for tires.
Claims (1)
2−ビニル結合金量が10〜40重量%、 (d)その有機過酸化物架橋物における弾性率が10〜
18kg/cm^2、であり、 有機リチウム系触媒でブタジエン単量体を重合し、得ら
れる末端リチウム活性重合体を多官能性処理剤で結合さ
せていることを特徴とする、ポリブタジエン重合体。[Scope of Claims] (a) Mooney viscosity is 30 to 80, (b) solution viscosity is 20 to 60 centipoise, (c) 1,
2-vinyl bond amount is 10 to 40% by weight; (d) the elastic modulus of the organic peroxide crosslinked product is 10 to 40% by weight;
18 kg/cm^2, and is characterized in that a butadiene monomer is polymerized with an organolithium catalyst, and the obtained terminal lithium active polymer is bonded with a polyfunctional processing agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1050135A JP2847521B2 (en) | 1989-03-03 | 1989-03-03 | Improved polybutadiene rubber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1050135A JP2847521B2 (en) | 1989-03-03 | 1989-03-03 | Improved polybutadiene rubber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02229809A true JPH02229809A (en) | 1990-09-12 |
| JP2847521B2 JP2847521B2 (en) | 1999-01-20 |
Family
ID=12850703
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1050135A Expired - Fee Related JP2847521B2 (en) | 1989-03-03 | 1989-03-03 | Improved polybutadiene rubber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2847521B2 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010131646A1 (en) | 2009-05-11 | 2010-11-18 | 日本ゼオン株式会社 | Method for producing radial conjugated diene polymer |
| JP2011068828A (en) * | 2009-09-28 | 2011-04-07 | Asahi Kasei Chemicals Corp | Modified conjugated diene-based copolymer, modified conjugated diene-based copolymer composition, rubber composition, and method for producing modified conjugated diene-based copolymer |
| JP2011219701A (en) * | 2010-04-14 | 2011-11-04 | Asahi Kasei Chemicals Corp | Modified conjugated diene polymer, method for producing the same, modified conjugated diene polymer composition, and tire |
| JP5520829B2 (en) * | 2008-10-14 | 2014-06-11 | 旭化成ケミカルズ株式会社 | Modified conjugated diene polymer, production method thereof, modified conjugated diene polymer composition, and tire |
| CN104231119A (en) * | 2013-06-24 | 2014-12-24 | 中国石油化工股份有限公司 | Preparation method of long-chain branched cis-rich polybutadiene |
| US11974745B2 (en) | 2006-05-19 | 2024-05-07 | Cilag Gmbh International | Electrically self-powered surgical instrument with cryptographic identification of interchangeable part |
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|---|---|---|---|---|
| JPS5575413A (en) * | 1978-12-05 | 1980-06-06 | Nippon Erasutomaa Kk | Preraration of high rubber content impact resistant polystyrene |
| JPS59217712A (en) * | 1983-05-26 | 1984-12-07 | Nippon Erasutomaa Kk | Impact-resistant styrene resin |
| JPS61148213A (en) * | 1984-12-21 | 1986-07-05 | Asahi Chem Ind Co Ltd | Impact-resistant polystyrene based resin and production thereof |
| JPS6372711A (en) * | 1986-09-17 | 1988-04-02 | Nippon Erasutomaa Kk | Rubber-modified styrene resin |
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| JP5520829B2 (en) * | 2008-10-14 | 2014-06-11 | 旭化成ケミカルズ株式会社 | Modified conjugated diene polymer, production method thereof, modified conjugated diene polymer composition, and tire |
| JP2014122359A (en) * | 2008-10-14 | 2014-07-03 | Asahi Kasei Chemicals Corp | Modified conjugated diene polymer, method for producing the same, modified conjugated diene polymer composition, and tire |
| US8946339B2 (en) | 2008-10-14 | 2015-02-03 | Asahi Kasei Chemicals Corporation | Modified conjugated diene-based polymer, method for producing the same, modified conjugated diene-based polymer composition, and tire |
| WO2010131646A1 (en) | 2009-05-11 | 2010-11-18 | 日本ゼオン株式会社 | Method for producing radial conjugated diene polymer |
| US8993675B2 (en) | 2009-05-11 | 2015-03-31 | Zeon Corporation | Method of production of radial conjugated diene polymer |
| JP2011068828A (en) * | 2009-09-28 | 2011-04-07 | Asahi Kasei Chemicals Corp | Modified conjugated diene-based copolymer, modified conjugated diene-based copolymer composition, rubber composition, and method for producing modified conjugated diene-based copolymer |
| JP2011219701A (en) * | 2010-04-14 | 2011-11-04 | Asahi Kasei Chemicals Corp | Modified conjugated diene polymer, method for producing the same, modified conjugated diene polymer composition, and tire |
| CN104231119A (en) * | 2013-06-24 | 2014-12-24 | 中国石油化工股份有限公司 | Preparation method of long-chain branched cis-rich polybutadiene |
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|---|---|
| JP2847521B2 (en) | 1999-01-20 |
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