JPS63152620A - Molded article of crosslinked polymer, production thereof and combination of reactive solution - Google Patents
Molded article of crosslinked polymer, production thereof and combination of reactive solutionInfo
- Publication number
- JPS63152620A JPS63152620A JP1594187A JP1594187A JPS63152620A JP S63152620 A JPS63152620 A JP S63152620A JP 1594187 A JP1594187 A JP 1594187A JP 1594187 A JP1594187 A JP 1594187A JP S63152620 A JPS63152620 A JP S63152620A
- Authority
- JP
- Japan
- Prior art keywords
- metasense
- solution
- mol
- catalyst system
- polymerization
- 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
- 229920006037 cross link polymer Polymers 0.000 title claims description 12
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000000203 mixture Substances 0.000 claims abstract description 24
- 239000003054 catalyst Substances 0.000 claims abstract description 22
- 239000000178 monomer Substances 0.000 claims abstract description 21
- 125000004093 cyano group Chemical group *C#N 0.000 claims abstract description 20
- 239000002685 polymerization catalyst Substances 0.000 claims abstract description 16
- HECLRDQVFMWTQS-RGOKHQFPSA-N 1755-01-7 Chemical compound C1[C@H]2[C@@H]3CC=C[C@@H]3[C@@H]1C=C2 HECLRDQVFMWTQS-RGOKHQFPSA-N 0.000 claims abstract description 14
- 150000001924 cycloalkanes Chemical class 0.000 claims abstract description 3
- 238000000034 method Methods 0.000 claims description 18
- -1 cyclic olefin compound Chemical class 0.000 claims description 16
- 150000002848 norbornenes Chemical class 0.000 claims description 15
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 9
- 150000001925 cycloalkenes Chemical class 0.000 claims description 8
- 239000002994 raw material Substances 0.000 claims description 6
- 230000000379 polymerizing effect Effects 0.000 claims description 4
- 239000012190 activator Substances 0.000 claims description 3
- PMJHHCWVYXUKFD-SNAWJCMRSA-N (E)-1,3-pentadiene Chemical compound C\C=C\C=C PMJHHCWVYXUKFD-SNAWJCMRSA-N 0.000 claims description 2
- 150000001335 aliphatic alkanes Chemical class 0.000 claims 1
- 230000009257 reactivity Effects 0.000 claims 1
- 238000006116 polymerization reaction Methods 0.000 abstract description 23
- 229920000642 polymer Polymers 0.000 abstract description 13
- 150000001875 compounds Chemical class 0.000 abstract description 8
- BMAXQTDMWYDIJX-UHFFFAOYSA-N bicyclo[2.2.1]hept-2-ene-5-carbonitrile Chemical compound C1C2C(C#N)CC1C=C2 BMAXQTDMWYDIJX-UHFFFAOYSA-N 0.000 abstract description 7
- 150000003658 tungsten compounds Chemical class 0.000 abstract description 7
- 125000003518 norbornenyl group Chemical class C12(C=CC(CC1)C2)* 0.000 abstract description 4
- 230000003213 activating effect Effects 0.000 abstract 2
- 239000000243 solution Substances 0.000 description 51
- 239000000306 component Substances 0.000 description 21
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 12
- 239000007788 liquid Substances 0.000 description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 9
- 238000002156 mixing Methods 0.000 description 8
- 238000000465 moulding Methods 0.000 description 8
- 239000000654 additive Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 229910052721 tungsten Inorganic materials 0.000 description 6
- 239000010937 tungsten Substances 0.000 description 6
- 239000013543 active substance Substances 0.000 description 5
- 229920001971 elastomer Polymers 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 5
- YRKCREAYFQTBPV-UHFFFAOYSA-N acetylacetone Chemical compound CC(=O)CC(C)=O YRKCREAYFQTBPV-UHFFFAOYSA-N 0.000 description 4
- 239000003963 antioxidant agent Substances 0.000 description 4
- 239000000945 filler Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 3
- 239000002879 Lewis base Substances 0.000 description 3
- 239000004480 active ingredient Substances 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- JFDZBHWFFUWGJE-UHFFFAOYSA-N benzonitrile Chemical compound N#CC1=CC=CC=C1 JFDZBHWFFUWGJE-UHFFFAOYSA-N 0.000 description 3
- YNLAOSYQHBDIKW-UHFFFAOYSA-M diethylaluminium chloride Chemical compound CC[Al](Cl)CC YNLAOSYQHBDIKW-UHFFFAOYSA-M 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 239000000806 elastomer Substances 0.000 description 3
- 150000007527 lewis bases Chemical class 0.000 description 3
- JFNLZVQOOSMTJK-KNVOCYPGSA-N norbornene Chemical compound C1[C@@H]2CC[C@H]1C=C2 JFNLZVQOOSMTJK-KNVOCYPGSA-N 0.000 description 3
- 238000010107 reaction injection moulding Methods 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- KPGXUAIFQMJJFB-UHFFFAOYSA-H tungsten hexachloride Chemical compound Cl[W](Cl)(Cl)(Cl)(Cl)Cl KPGXUAIFQMJJFB-UHFFFAOYSA-H 0.000 description 3
- KYPOHTVBFVELTG-OWOJBTEDSA-N (e)-but-2-enedinitrile Chemical compound N#C\C=C\C#N KYPOHTVBFVELTG-OWOJBTEDSA-N 0.000 description 2
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- IGFHQQFPSIBGKE-UHFFFAOYSA-N Nonylphenol Natural products CCCCCCCCCC1=CC=C(O)C=C1 IGFHQQFPSIBGKE-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 125000005234 alkyl aluminium group Chemical group 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 230000003078 antioxidant effect Effects 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 238000010538 cationic polymerization reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 230000000977 initiatory effect Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Chemical compound CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 description 2
- JMANVNJQNLATNU-UHFFFAOYSA-N oxalonitrile Chemical compound N#CC#N JMANVNJQNLATNU-UHFFFAOYSA-N 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 229910052702 rhenium Inorganic materials 0.000 description 2
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 2
- 239000005060 rubber Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- 229910052715 tantalum Inorganic materials 0.000 description 2
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 2
- LFXVBWRMVZPLFK-UHFFFAOYSA-N trioctylalumane Chemical compound CCCCCCCC[Al](CCCCCCCC)CCCCCCCC LFXVBWRMVZPLFK-UHFFFAOYSA-N 0.000 description 2
- JXPDNDHCMMOJPC-UHFFFAOYSA-N 2-hydroxybutanedinitrile Chemical compound N#CC(O)CC#N JXPDNDHCMMOJPC-UHFFFAOYSA-N 0.000 description 1
- VSKJLJHPAFKHBX-UHFFFAOYSA-N 2-methylbuta-1,3-diene;styrene Chemical compound CC(=C)C=C.C=CC1=CC=CC=C1.C=CC1=CC=CC=C1 VSKJLJHPAFKHBX-UHFFFAOYSA-N 0.000 description 1
- YOIUGOIMAYHZFY-UHFFFAOYSA-N 5-(2-methylpropyl)bicyclo[2.2.1]hept-2-ene Chemical compound C1C2C(CC(C)C)CC1C=C2 YOIUGOIMAYHZFY-UHFFFAOYSA-N 0.000 description 1
- INYHZQLKOKTDAI-UHFFFAOYSA-N 5-ethenylbicyclo[2.2.1]hept-2-ene Chemical compound C1C2C(C=C)CC1C=C2 INYHZQLKOKTDAI-UHFFFAOYSA-N 0.000 description 1
- OJOWICOBYCXEKR-UHFFFAOYSA-N 5-ethylidenebicyclo[2.2.1]hept-2-ene Chemical compound C1C2C(=CC)CC1C=C2 OJOWICOBYCXEKR-UHFFFAOYSA-N 0.000 description 1
- PGNNHYNYFLXKDZ-UHFFFAOYSA-N 5-phenylbicyclo[2.2.1]hept-2-ene Chemical compound C1=CC2CC1CC2C1=CC=CC=C1 PGNNHYNYFLXKDZ-UHFFFAOYSA-N 0.000 description 1
- WDJHALXBUFZDSR-UHFFFAOYSA-N Acetoacetic acid Natural products CC(=O)CC(O)=O WDJHALXBUFZDSR-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- UTGQNNCQYDRXCH-UHFFFAOYSA-N N,N'-diphenyl-1,4-phenylenediamine Chemical compound C=1C=C(NC=2C=CC=CC=2)C=CC=1NC1=CC=CC=C1 UTGQNNCQYDRXCH-UHFFFAOYSA-N 0.000 description 1
- 229920000459 Nitrile rubber Polymers 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- DJNPQHBMESQZIP-UHFFFAOYSA-N bicyclo[2.2.1]hept-5-ene-2,3-dicarbonitrile Chemical compound C1C2C=CC1C(C#N)C2C#N DJNPQHBMESQZIP-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- FACXGONDLDSNOE-UHFFFAOYSA-N buta-1,3-diene;styrene Chemical compound C=CC=C.C=CC1=CC=CC=C1.C=CC1=CC=CC=C1 FACXGONDLDSNOE-UHFFFAOYSA-N 0.000 description 1
- 229920005549 butyl rubber Polymers 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 150000001728 carbonyl compounds Chemical class 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- BWKCCRPHMILRGD-UHFFFAOYSA-N chloro hypochlorite;tungsten Chemical compound [W].ClOCl BWKCCRPHMILRGD-UHFFFAOYSA-N 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 239000013256 coordination polymer Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- NOSWQDCFTDHNCM-UHFFFAOYSA-N cyclopenta-1,3-diene;1-methylcyclopenta-1,3-diene Chemical compound C1C=CC=C1.CC1=CC=CC1 NOSWQDCFTDHNCM-UHFFFAOYSA-N 0.000 description 1
- DIBHLCJAJIKHGB-UHFFFAOYSA-N dec-5-ene Chemical compound [CH2]CCCC=CCCCC DIBHLCJAJIKHGB-UHFFFAOYSA-N 0.000 description 1
- 239000000539 dimer Substances 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- UAIZDWNSWGTKFZ-UHFFFAOYSA-L ethylaluminum(2+);dichloride Chemical compound CC[Al](Cl)Cl UAIZDWNSWGTKFZ-UHFFFAOYSA-L 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000012442 inert solvent Substances 0.000 description 1
- AGQPHHBPENBBIO-UHFFFAOYSA-M iodo(dioctyl)alumane Chemical compound [I-].CCCCCCCC[Al+]CCCCCCCC AGQPHHBPENBBIO-UHFFFAOYSA-M 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000004611 light stabiliser Substances 0.000 description 1
- 230000000873 masking effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000012533 medium component Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 125000000325 methylidene group Chemical group [H]C([H])=* 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 239000006082 mold release agent Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 150000002902 organometallic compounds Chemical class 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- NFHFRUOZVGFOOS-UHFFFAOYSA-N palladium;triphenylphosphane Chemical compound [Pd].C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 NFHFRUOZVGFOOS-UHFFFAOYSA-N 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 229920001195 polyisoprene Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910000077 silane Inorganic materials 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 230000003381 solubilizing effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229920000468 styrene butadiene styrene block copolymer Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- AFCAKJKUYFLYFK-UHFFFAOYSA-N tetrabutyltin Chemical compound CCCC[Sn](CCCC)(CCCC)CCCC AFCAKJKUYFLYFK-UHFFFAOYSA-N 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 239000010456 wollastonite Substances 0.000 description 1
- 229910052882 wollastonite Inorganic materials 0.000 description 1
Landscapes
- Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)
Abstract
Description
【発明の詳細な説明】
a、産業上の利用分野
本発明は、シクロペンタジェン系重合体の改良された新
規重合体成型物、その製造方法及びそのための反応性溶
液の組合せに関する。更に詳しくは、ジシクロペンタジ
ェンを含有する単量体をメタセンス重合触媒を用いてバ
ルク重合せしめて、得られた架橋重合体成型物、その製
造方法及びそのために使用される反応性溶液の組合せに
関する。DETAILED DESCRIPTION OF THE INVENTION a. Field of Industrial Application The present invention relates to an improved new polymer molded product of a cyclopentadiene polymer, a method for producing the same, and a combination of reactive solutions therefor. More specifically, it relates to a crosslinked polymer molded product obtained by bulk polymerizing monomers containing dicyclopentadiene using a metasense polymerization catalyst, a method for producing the same, and a combination of reactive solutions used therefor. .
b、従来技術
ジシクロペンタジェン(以下” D CP”と略称する
ことがある)は、ナフサクラッキングによってエチレン
等を製造する際のC5留分の主成分の1つであるシクロ
ペンタジェンが熱力学的により安定な二量体の形で得ら
れるものであって、豊富な石油化学原料と云える。b. Prior art Dicyclopentadiene (hereinafter sometimes abbreviated as "D CP") is a thermodynamically produced cyclopentadiene, which is one of the main components of the C5 fraction used to produce ethylene etc. by naphtha cracking. It can be obtained in the form of a dimer, which is more stable than before, and can be said to be an abundant petrochemical raw material.
従来よりDCPは熱ラジカル重合やカチオン重合させて
石油樹脂等を得る原料として用いられてきた。しかし最
近DCPの環中の2つの二重合結合をオレフィンメタセ
ンス重合触媒系によって開巻重合せしめ、DCPから一
挙に架橋重合体の成形体を得る技術が開発されたく例え
ば特開昭58−129013号公報参照)。この技術は
、反応成形法によって、前記豊富な石油化学原料から一
段で大型の成型品が容易に得られること、及びその成型
品は剛性と耐衝撃性のバランスのよい優れた物性を有し
ている点で工業的に価値がある。DCP has conventionally been used as a raw material for obtaining petroleum resins and the like through thermal radical polymerization or cationic polymerization. However, recently, a technique has been developed in which two double bonds in the ring of DCP are subjected to open-roll polymerization using an olefin metasense polymerization catalyst system to obtain a molded body of a crosslinked polymer from DCP at once. reference). This technology uses the reaction molding method to easily obtain large molded products in one step from the aforementioned abundant petrochemical raw materials, and the molded products have excellent physical properties with a good balance of rigidity and impact resistance. It has industrial value in that it is
ところで、上記反応成形法において用いられるメタセン
ス触媒系は、一般にタングステン、レニウム、タンタル
などの遷移金属塩触媒とそれを活性化するためのアルミ
ニウム、スズなどの有機全屈化合物の組合せによって触
媒系として活性が発現される。上記方法はこの点を利用
して、前記触媒成分と活性剤成分の両成分を、別々に分
けられたDCP中に混合した状態では重合は開始されな
いが、両者を急激に混合することによって、メタセンス
重合が開示され、反応成形が進行し成形物が一挙に得ら
れるように工夫されている。By the way, the metasense catalyst system used in the above reaction molding method is generally activated as a catalyst system by a combination of a transition metal salt catalyst such as tungsten, rhenium, or tantalum, and an organic total bending compound such as aluminum or tin to activate it. is expressed. The above method takes advantage of this point, and polymerization does not start when both the catalyst component and the activator component are mixed in separately separated DCP, but by rapidly mixing them, the metasensitivity Polymerization is disclosed, reaction molding proceeds and molded products are obtained all at once.
かかるメタセンス触媒系は、上記の両成分とも、非常に
反応性に冨んでおり、上述した如き反応射出成型法をと
るにしても、両成分混合後の反応速度が早過ぎるため、
充分型中に流し込まないうちにゲル化が開始されて良好
な成型物が得られない場合が出ることが判った。In such a metasense catalyst system, both of the above components are highly reactive, and even if the reaction injection molding method described above is used, the reaction rate after mixing the two components is too fast.
It has been found that gelation may begin before the mixture is sufficiently poured into the mold, making it impossible to obtain a good molded product.
更に用途によっては、反応射出成型よりも、一旦両液を
混合したプレミックスの状態である程度時間をおいた後
、型に流入加熱硬化させる方が、装置が簡単になり有利
な場合が多いことも判ってきた。Furthermore, depending on the application, it may be more advantageous to mix the two liquids in a premix state for a certain period of time, then pour it into the mold and heat it to harden, as the equipment is simpler, rather than reaction injection molding. I've come to understand.
かかるメタセンス重合触媒の活性度の調節はルイスペー
ス系の化合物を添加することによっておこない得ること
は知られている。しかしながら、充分に活性化度を調節
するためにかかるルイスペースを添加するとそれが重合
体中に残存し、重合体の性質を損ったり、揮発成分を発
生したりの不都合が生じる問題があった。そこで、本発
明者は、かかる不都合を克服する方法について鋭意研究
の結果本発明に到達したものである。It is known that the activity of such a metasense polymerization catalyst can be controlled by adding a Lewis space compound. However, when Lewis space is added to sufficiently adjust the degree of activation, it remains in the polymer, causing problems such as impairing the properties of the polymer and generating volatile components. . Therefore, the present inventor has arrived at the present invention as a result of intensive research into a method for overcoming such disadvantages.
C3発明の構成
即ち、本発明者は、かかるルイスペースをメタセンス重
合性を有するモノマー中に含有させ一緒に重合させると
、低分子量のルイスペースが残留することがなくなり上
記の不都合はなくなり、しかも、かがる共重合したルイ
スペース基が重合体に有用な性質を与えることが出来れ
ば一挙両得になるはずであると考え、かかるルイスペー
ス基含有モノマーについて、研究の結果ルイスペースと
として、シアノ基を1〜2個含有するノルボルネン誘導
体が、上記目的に極めて適していることを見出し1qて
、本発明を完成したものである。The structure of the C3 invention, that is, the present inventor has discovered that when such Lewis space is contained in a monomer having metasense polymerizability and polymerized together, low molecular weight Lewis space does not remain, and the above-mentioned disadvantages are eliminated. We believe that it would be a win-win situation if the copolymerized Lewis space group could impart useful properties to the polymer, and as a result of research on such Lewis space group-containing monomers, we found that the cyano group was used as Lewis space. The present invention was completed by discovering that a norbornene derivative containing 1 to 2 is extremely suitable for the above purpose.
すなわち、本発明は下記(1)〜(3)の発明を包含す
る。That is, the present invention includes the following inventions (1) to (3).
1、 ジシクロペンタジェンを少なくとも30モル%含
有するメタセンス重合性シクロアルケン類過半モル〜9
9.5モル%を含み残余が分子中にペンダントシアノ基
を1〜2個有するノルボルネン誘導体の少なくとも1種
より実質的になる単量体混合物を、メタセンス重合触媒
系の存在下重合せしめることによって得られた架橋重合
体成型物。1. Majority of metasense polymerizable cycloalkenes containing at least 30 mol% of dicyclopentadiene - 9
A monomer mixture containing 9.5 mol % and the remainder consisting essentially of at least one norbornene derivative having 1 to 2 pendant cyano groups in the molecule is polymerized in the presence of a metasense polymerization catalyst system. A cross-linked polymer molded product.
2. ジシロンペンタジエンを含有するメタセンス重合
性環状オレフィン化合物を、メタセンス重合触媒系の存
在下重合せしめて架橋重合体成型物を得る方法において
、原料単量体としてジシクロペンタジェンを少なくとも
30モル%含有するメタセンス重合性シクロアルカン類
過半モル〜99.5モル%を含み、残余が分子中にペン
ダントシアノ基を1〜2@有するノルボルネン誘導体の
少なくとも1種より実質的になる単量体混合物を使用す
ることを特徴とする架橋重合体成型物の製造方法。2. A method for obtaining a crosslinked polymer molded product by polymerizing a metasense polymerizable cyclic olefin compound containing disilone pentadiene in the presence of a metasense polymerization catalyst system, the method comprising at least 30 mol% of dicyclopentadiene as a raw material monomer. Use a monomer mixture containing the majority of metasense polymerizable cycloalkanes to 99.5 mol%, with the remainder consisting essentially of at least one norbornene derivative having 1 to 2 pendant cyano groups in the molecule. A method for producing a crosslinked polymer molded article, characterized by:
3、(ω メタセンス重合触媒系の触媒を含むメタセン
ス重合性環状オレフィンの反応性溶液(溶液A)、
山) メタセンス重合触媒系の活性化剤を含むメタセン
ス重合性環状オレフィンの反応性溶液(溶液B)、
より少なくともなる反応性溶液の組合せにおいて、前記
溶液A及び溶液B中のメタセンス重合性環状オレフィン
は、両方を合せた組成が、ジシクロペンタジェンを少な
くとも30モル%含有するメタセンス重合性ジクロフル
カン類過半モル〜99.5モル%を含み残余が分子中に
ペンダントシアノ基を1〜2個有するノルボルネン誘導
体の少なくとも1種より実質的になる単量体混合物であ
ることを特徴とする反応性溶液の組合せ。3. (ω A reactive solution of a metasense polymerizable cyclic olefin containing a catalyst of a metasense polymerization catalyst system (solution A), mountain) A reactive solution of a metasense polymerizable cyclic olefin containing an activator of a metasense polymerization catalyst system (solution B) ), the metasense polymerizable cyclic olefins in solution A and solution B are metasense polymerizable dichloroflucanes whose combined composition contains at least 30 mol% of dicyclopentadiene. A reactive solution characterized in that it is a monomer mixture comprising a majority of 99.5 mol % and the remainder consisting essentially of at least one norbornene derivative having 1 to 2 pendant cyano groups in the molecule. combination.
本発明で用いられるDCPは高度に精製されたものが好
ましい。本発明で用いられるDCPは、一般にDCP純
度95%以上さらに好ましくは97%以上であってしか
も不純物は、メタセンス触媒系の活性を阻害しないもの
であることは当然であるが、メタセンス重合性を有する
ものであることが好ましい。メタセンス重合を阻害する
アルコール類、カルボン酸類、カルボニル化合物類とな
どの極性化合物の含有量は出来るだけ少ないことが好ま
しい。The DCP used in the present invention is preferably highly purified. The DCP used in the present invention generally has a DCP purity of 95% or more, more preferably 97% or more, and impurities do not inhibit the activity of the metasense catalyst system, and have metasense polymerizability. Preferably. The content of polar compounds such as alcohols, carboxylic acids, and carbonyl compounds that inhibit metasense polymerization is preferably as small as possible.
DCPとともに少量成分として用いられるメタセンス重
合性シクロアルケン類としては一般にメタセンス重合性
シクロアルケン基を1〜2個含有するものが用いられる
。特にノルボルネン型の結合を有するものが好ましい。As the metasense polymerizable cycloalkenes used as a minor component together with DCP, those containing 1 to 2 metasense polymerizable cycloalkenes are generally used. Particularly preferred are those having norbornene type bonds.
特に炭化水素系のものが好ましく、具体例としては、シ
クロペンタジェン−メチルシクロペンタジェン共二吊体
、5−エチリデンノルボルネン、5−ビニルノルボルネ
ン、5−フェニルノルボルネン、5−イソブチルノルボ
ルネン、1,4,5.8−ジメタノ−1,4,4a 、
5゜8.8a−へキサヒドロナフタレン、トリシクロ[
5,2,1,0]デカ−5−エン、トリシクロペンタジ
ェン、1,4,5.8−ジメタノ−1,4,4a、5,
6,7,8゜8a−オクタヒドムナフタレン、6−ニチ
リデンー1.4,5.8−ジメタノ−1,4,4a、5
,6,8.8a−へブタヒドロナフタレンなどをあげる
ことができる。ペテロ原子を含有するシクロアルケン類
についてもノルボルネン基含有のものが好ましく、5−
メトキシカルボニル−ノルボルネン
ルボニルメチルノルボルネン、ヘキサメチレン−ごスー
ナディクィミドなどをあげることができる。Hydrocarbons are particularly preferred, and specific examples include cyclopentadiene-methylcyclopentadiene, 5-ethylidenenorbornene, 5-vinylnorbornene, 5-phenylnorbornene, 5-isobutylnorbornene, 1,4 , 5.8-dimethano-1,4,4a,
5゜8.8a-hexahydronaphthalene, tricyclo[
5,2,1,0]dec-5-ene, tricyclopentadiene, 1,4,5.8-dimethano-1,4,4a,5,
6,7,8゜8a-octahydomnaphthalene, 6-nitylidene-1,4,5,8-dimethano-1,4,4a,5
, 6,8.8a-hebutahydronaphthalene and the like. Regarding the cycloalkenes containing a petero atom, those containing a norbornene group are also preferable, and 5-
Examples include methoxycarbonyl-norbornenerubonylmethylnorbornene, hexamethylene-sunadiquimide, and the like.
本発明で用いられるペンダントシアノ基を1〜2個有す
るノルボルネン誘導体とは、下記式で表わされるノルボ
ルネン構造単位を少なくとも一つ有するものを包含する
。The norbornene derivatives having one or two pendant cyano groups used in the present invention include those having at least one norbornene structural unit represented by the following formula.
(但し式中原子価は他の原子を介して環を形成してもよ
い。)
従って、ビシクロ構造のノルボルネン環以外にトリシク
ロ体やテトラシクロ、例えば1,4,5.8−ジメタノ
−1.4,4a,5,6,7,8,8a−オクタヒドロ
ナ他の原子を介して環を形成してもよい) 、1.4
−メタン−1.4.4a,5,6, 7,8.8a−オ
クタヒドロナフかかる多環オレフィンに、ペンダントシ
アノ基を1〜2個有する化合物を本発明の七ツマ−とし
て使用することができるが、一般に50℃以下で液状を
呈するものが好ましい。(However, the valence in the formula may form a ring via another atom.) Therefore, in addition to the norbornene ring of the bicyclo structure, tricyclo and tetracyclo, for example, 1,4,5.8-dimethano-1.4 , 4a,5,6,7,8,8a-octahydrona may form a ring via other atoms), 1.4
-Methane-1.4.4a,5,6,7,8.8a-Octahydronaf A compound having 1 to 2 pendant cyano groups in the polycyclic olefin can be used as the 7mer of the present invention. Generally, those exhibiting a liquid state at 50° C. or lower are preferred.
具体例として、例えば下記のものを挙げることができる
。Specific examples include the following.
5−シアノ−ノルボルネン
5−シアノ−5−メチルノルボルネン
5.6−ジアツーノルボルネン
6−ジアツー1.4,5,8.−ジメタノ−1,4,4
a、5,6゜7.8.8a−オクタヒドロナフタレン6
.7−ジシアノ−1,4,5,8−ジメタノ−1,4,
4a。5-cyano-norbornene 5-cyano-5-methylnorbornene 5.6-diatu norbornene 6-diatu 1.4,5,8. -dimethano-1,4,4
a, 5,6°7.8.8a-octahydronaphthalene 6
.. 7-dicyano-1,4,5,8-dimethano-1,4,
4a.
5.6,7,8.8a−オクタヒドロナフタレン6−ジ
アツー 1,4−メタノ−1,4,4a、5,6,7,
8.8a−オクタヒドロナフタレン
かかるシアノ基含有ノルボルネン誘導体類は、シクロペ
ンタジェン(反応器にはシクロペンタジェン、ジシクロ
ペンタジェンいずれの形でも使用することができる)S
1アクリロニトリル、マロニトリル、フマロニトリル、
5−シアノノルボルネン、5,6−ジシアツノルボルネ
ン、シアネジクロヘキセンなどとのD 1els −A
1der反応によって極めて収率よく得ることができ
る。当然のことながらかかるシアノ基含有ノルボルネン
誘導体類は、使用に当って充分に精製しておくことが必
要である。5.6,7,8.8a-Octahydronaphthalene 6-diatu 1,4-methano-1,4,4a,5,6,7,
8.8a-Octahydronaphthalene Such cyano group-containing norbornene derivatives are cyclopentadiene (which can be used in the reactor in the form of either cyclopentadiene or dicyclopentadiene) S
1 Acrylonitrile, malonitrile, fumaronitrile,
D 1els-A with 5-cyanonorbornene, 5,6-dicyanonorbornene, cyanedichlorohexene, etc.
It can be obtained in extremely high yield by a 1der reaction. Naturally, such cyano group-containing norbornene derivatives need to be sufficiently purified before use.
本発明におけるメタセンス重合性シクOアルケン類中の
DCPの使用割合については、少なくとも30モル%必
要であるが、好ましくは50モル%以上である。The proportion of DCP used in the metasense polymerizable cycloalkenes in the present invention is required to be at least 30 mol%, but preferably 50 mol% or more.
一方かかるシクロアルケン類とシアノ基含有ノルボルネ
ン誘導体との使用割合については、成型方法によって好
ましい範囲が異なる。前’rfLした如く、反応射出成
型法で架橋成型体を得ようとする場合には、溶液A、溶
液Bの混合後、重合開始までの時間は、型中に液が流れ
込むに充分な時間があればよい訳で従ってシアノ基含有
ノルボルネン誘導体による調節作用は小さくてよく、従
って、0.5〜25モル%の範囲が好ましい。一方、プ
レミックス状態を経る成型法ではプレミックス状態での
安定性がある程度以上必要であり従って、30モル%〜
45モル%の範囲が好ましい。On the other hand, the preferred range of the ratio of the cycloalkenes to the cyano group-containing norbornene derivative varies depending on the molding method. As mentioned above, when trying to obtain a crosslinked molded product by reaction injection molding, the time from mixing solution A and solution B until the start of polymerization is sufficient for the liquid to flow into the mold. Therefore, the regulating effect of the cyano group-containing norbornene derivative may be small, and therefore, the range of 0.5 to 25 mol % is preferable. On the other hand, in the molding method that goes through a premix state, stability in the premix state is required to a certain extent, and therefore, 30 mol% to
A range of 45 mol% is preferred.
なお、これらの七ツマー混合物の組成は溶液Aと溶液B
とにおいて、必ずしも同じである必要はなく、目的によ
って適宜調整して用いることが出来、両方あわせたもの
が上記の如き範囲にあればよいことになる。The composition of these seven-mer mixtures is solution A and solution B.
They do not necessarily have to be the same, and can be appropriately adjusted and used depending on the purpose, and it is sufficient that the combination of both falls within the above range.
シアン基含有ノルボルネン類の共重合効果としては、前
述の重合開始時間の調整作用以外に、シアノ基は極性が
高いため得られた架橋重合体の極性もだかくなり、分子
間力が大きくなるので二次転移点を低下させることが少
なく、かつ耐薬品性等も改良出来る場合もある。また、
モノマー状態においても高極性のため、常温で固体で炭
化水素系シクロアルケン類に溶解しないような他の単量
体や添加剤もよく溶解しつる利点を有する。The copolymerization effect of cyanogen-containing norbornenes is that in addition to the above-mentioned effect of adjusting the polymerization initiation time, the polarity of the crosslinked polymer obtained is also increased because the cyano group is highly polar, which increases the intermolecular force. In some cases, the secondary transition point is less likely to be lowered, and chemical resistance can also be improved. Also,
Since it is highly polar even in the monomer state, it has the advantage of being able to easily dissolve other monomers and additives that are solid at room temperature and do not dissolve in hydrocarbon cycloalkenes.
前述した成形方式におけるメタセンス重合触媒系におけ
る触媒成分としてはタングステン、レニウム、タンタル
等のハライドなどの塩類が用いられるが、特にタングス
テン化合物が好ましい。かかるタングステン化合物とし
ては、タングステンハライド、タングステンオキシハラ
イドなどが好ましくより具体的には、タングステンへキ
サクロライド、タングステンオキシクロライドなとが好
ましい。かかるタングステン化合物は、直接ジシクロペ
ンタジェンに添加すると、直ちにカチオン重合を開始す
ることが判っており好ましくない。Salts such as halides such as tungsten, rhenium, and tantalum are used as catalyst components in the metasense polymerization catalyst system in the above-described molding method, and tungsten compounds are particularly preferred. As such a tungsten compound, tungsten halide, tungsten oxyhalide, etc. are preferable, and more specifically, tungsten hexachloride, tungsten oxychloride, etc. are preferable. It is known that when such a tungsten compound is directly added to dicyclopentadiene, cationic polymerization starts immediately, which is not preferable.
従ってかかるタングステン化合物は不活性溶媒例えばベ
ンゼン、トルエン、クロロベンゼン等に予め懸濁し、少
量のアルコール系化合物またはフェノール系化合物を添
加することによって可溶化させて使用するのが好ましい
。Therefore, it is preferable to use such a tungsten compound by first suspending it in an inert solvent such as benzene, toluene, chlorobenzene, etc., and solubilizing it by adding a small amount of an alcoholic compound or a phenolic compound.
さらに、上述した如き、好ましくない重合を予防するた
めにタンクズテン化合物1モルに対し、約1〜5モルの
ルイス塩基又はキレート化剤を添加することが好ましい
。かかる添加剤としてはアセチルアセトン、アセト酢酸
アルキルエステル類。Furthermore, in order to prevent undesirable polymerization as described above, it is preferable to add about 1 to 5 moles of a Lewis base or a chelating agent per mole of the tankzusten compound. Such additives include acetylacetone and acetoacetic acid alkyl esters.
テトラヒドロフラン、ベンゾニトリルなどをあげること
ができる。本発明で用いられるシアノ基含有ノルボルネ
ン類は、前述の如く、そのものがルイス塩基であり、上
記の如き化合物を特に加えなくてもその作用を有してい
る場合が多い。Examples include tetrahydrofuran and benzonitrile. As mentioned above, the cyano group-containing norbornenes used in the present invention are Lewis bases themselves, and often have this effect even without the addition of any of the above compounds.
かくして、主触媒成分を含むモノマー溶液(溶液A)は
、実用上充分な安定性を有することになる。Thus, the monomer solution (solution A) containing the main catalyst component has sufficient stability for practical use.
一方メタセンス重合触媒系における活性他剤成分は、周
期律表第1〜第■族の金属のアルキル化物を中心とする
有機金属化合物、特にテトラアルキルスズ、アルキルア
ルミニウム化合物、アルキルアルモニウムハライド化合
物が好ましく、具体的には、塩化ジエチルアルミニウム
、ジ塩化エチルアルミニウム、トリオクチルアルミニウ
ム、テトラブチル錫などをあげることができる。これら
活性他剤成分としての有機金属化合物を、混合単量体に
溶解することにより、もう一方の溶液(溶液Bに相当す
る)が形成される。On the other hand, the active component in the metasense polymerization catalyst system is preferably an organometallic compound centered on alkylated metals of Groups 1 to Ⅰ of the Periodic Table, particularly tetraalkyltin, alkylaluminum compounds, and alkylalmonium halide compounds. Specifically, diethylaluminum chloride, ethylaluminum dichloride, trioctylaluminum, tetrabutyltin, etc. can be mentioned. The other solution (corresponding to solution B) is formed by dissolving the organometallic compound as the active ingredient in the mixed monomer.
本発明においては、基本的に前記溶液A及び溶液Bを混
合することによって、架橋重合体成形物を得ることがで
きるが、反応速度については、シアノ基含有ノルボルネ
ン類が調節作用を有しているめ安定した条件で硬化する
ことが出来るが、さらに重合速度を調整したい場合には
他のルイス塩基を添加することも出来る。In the present invention, a crosslinked polymer molded article can basically be obtained by mixing the solutions A and B, but the cyano group-containing norbornenes have a regulating effect on the reaction rate. Therefore, it can be cured under stable conditions, but if it is desired to further adjust the polymerization rate, other Lewis bases can be added.
メタセンス集合触媒系の使用量は例えば触媒成分として
タングステン化合物を用いる場合は、上記混合単量体に
対するタングステン化合物の比率は、モル基準で、約1
000対1〜約15000対1、好ましくは2000対
1の付近でありまた、活性他剤成分はアルキルアルミニ
ウム類を用いる場合には、上記DCP混合単量体に対す
るアルミニウム化合物の比率は、モル基準で約100対
1〜約2000対1、好ましくは約200対1〜約50
0対1の付近が用いられる。更に上述の如き、マスク剤
や調節剤については、実験によって上記触媒系の使用量
に応じて、適宜、調節して用いることが出来る。For example, when a tungsten compound is used as a catalyst component, the ratio of the tungsten compound to the above-mentioned mixed monomers is about 1 on a molar basis.
000:1 to about 15,000:1, preferably around 2,000:1, and when an alkylaluminum is used as the active agent component, the ratio of the aluminum compound to the DCP mixed monomer is on a molar basis. about 100:1 to about 2000:1, preferably about 200:1 to about 50
A value around 0:1 is used. Further, as described above, the masking agent and the regulating agent can be appropriately adjusted and used depending on the amount of the catalyst system to be used through experiments.
本発明による架1!重合体成形物には、実用に当って、
その特性を改良または維持するために、各種添加剤を配
合することができる。かかる添加剤としては、充填剤、
顔料、酸化防止剤、光安定剤。Rack 1 according to the present invention! In practical use, polymer molded products have
Various additives can be added to improve or maintain its properties. Such additives include fillers,
Pigments, antioxidants, light stabilizers.
高分子改良剤などがある。このような添加剤は、本発明
の架橋重合体が成形されて後は添加することが不可能で
あるから、添加する場合には予め前記した原料溶液に添
加しておく必要がある。Examples include polymer modifiers. Such additives cannot be added after the crosslinked polymer of the present invention has been molded, so if they are added, they must be added to the above-mentioned raw material solution in advance.
その最も容易な方法としては、前記溶液Aおよび溶液B
のいずれか又は両方に前もって添加しておく方法をあげ
ることが出来るが、その場合、その液中の反応性の強い
触媒成分や、活性他剤成分と実用上さしつかえある程度
に、は反応せず、かつ重合を阻害しないものでなくては
、ならない。どうしても、その反応がさけえないが共存
しても、重合は実質的に阻害しないものの場合は、単量
体と混合して、第三液を調整し、重合直前に、混合使用
することも出来る。また、固体の充填剤の場合であって
、両成分が混合されて、重合反応を開始する直前あるい
は重合をしながら、その空隙を充分にうずめ得る形状の
ものについては、成型用モールド中に、充填しておくこ
とも、可能である。The easiest method is to use the solution A and solution B.
One method is to add it to either or both of them in advance, but in that case, it will not react with the highly reactive catalyst components or other active agent components in the liquid to a practical extent. In addition, it must not inhibit polymerization. If the reaction cannot be avoided, but coexistence does not substantially inhibit polymerization, it can be mixed with the monomer to prepare a third liquid and mixed and used immediately before polymerization. . In the case of a solid filler, in the case of a filler in a shape that can sufficiently fill the voids immediately before starting the polymerization reaction or during polymerization when both components are mixed, in the mold for forming, It is also possible to fill it.
添加剤としての補強材又は充填剤は、曲げモジュラスを
向上するのに効果がある。かかるものとしてはガラス繊
維、雲母、カーボンブラック、ウオラストナイト等をあ
げることが出来る。これらを、いわゆるシランガブラー
などによって表面処理したものも好適に使用できる。Reinforcements or fillers as additives are effective in improving the flexural modulus. Examples of such materials include glass fiber, mica, carbon black, and wollastonite. Those surface-treated with so-called silane gobbler can also be suitably used.
また、本発明の架1重合体成形物は、酸化防止剤を添加
しておくことが好ましく、そのためフェノール系又はア
ミン系の酸化防止剤を予め溶液中に加えてかくことが望
ましい。これら酸化防止剤の具体例としては、2.6−
t−ブチル−P−クレゾール、N、N’ −ジフェニ
ル−P−フェニレンジアミン、テトラキス[メチレン(
3,5−ジーを一ブチルー4−ヒドロキシシンナメート
)]メタンなどがあげられる。Further, it is preferable to add an antioxidant to the cross-monopolymer molded article of the present invention, and therefore it is desirable to add a phenolic or amine antioxidant to the solution in advance. Specific examples of these antioxidants include 2.6-
t-Butyl-P-cresol, N,N'-diphenyl-P-phenylenediamine, tetrakis[methylene(
Examples include 3,5-di-butyl-4-hydroxycinnamate)]methane.
また、本発明による重合体成形物は、他の重合体を1f
fi体溶液状態の時に添加しておくことが出来る。かが
る重合体添加剤としてはエラストマーの添加が成形物の
耐衝撃性を強めること及び溶液の粘度を調節(る上で効
果がある。かかる目的に用いられるエラストマーとして
は、スチレン−ブタジェン−スチレントリブロックゴム
、スチレン−イソプレン−スチレントリブロックゴム、
ポリブタジェン、ポリイソプレン、ブチルゴム、エチレ
ンブロビレンージエンターボリマー、ニトリルゴムなど
広範なエラストマーをあげることが出来る。Moreover, the polymer molded article according to the present invention contains 1f of other polymers.
It can be added when the fi body is in a solution state. As a bending polymer additive, the addition of an elastomer is effective in increasing the impact resistance of the molded product and controlling the viscosity of the solution. Elastomers used for this purpose include styrene-butadiene-styrene. Triblock rubber, styrene-isoprene-styrene triblock rubber,
A wide range of elastomers can be mentioned, including polybutadiene, polyisoprene, butyl rubber, ethylene brobylene-dienter polymer, and nitrile rubber.
本発明の重合体成形物は、前記した如く、重合と成形と
を同時に行うことによって製造される。The polymer molded article of the present invention is produced by simultaneously performing polymerization and molding, as described above.
かかる成型法としては前述の如く、触媒系とモノマー混
合物を前ちって、混合したプレミックスを型の中に流入
せしめるレジンインジェクション方式、触媒系を2つに
分けた溶液Δと溶液Bをヘッド部で衝突混合せしめてそ
のまま型に流し込むRIM方式をとることが出来る。い
ずれの場合も異型(モールド)への注入圧力は比較的低
圧であることができ、従って安価な鋳型を使用すること
が可能である。As mentioned above, such molding methods include the resin injection method, in which the catalyst system and monomer mixture are prepared in advance and the mixed premix is flowed into the mold, and the catalyst system is divided into two parts, solution Δ and solution B, into the head part. It is possible to use the RIM method, in which the mixture is mixed by collision and then poured directly into a mold. In either case, the injection pressure into the mold can be relatively low, so it is possible to use inexpensive molds.
また、型内の重合反応が開始されど反応熱によって型内
の温度は急速に上昇し、短時間に重合反応が終了する。Furthermore, although the polymerization reaction inside the mold is started, the temperature inside the mold rapidly rises due to the reaction heat, and the polymerization reaction ends in a short time.
ポリウレタン−RIMの場合と異なり、モールドから離
脱は容易であり、特別の離形剤を必要としない場合が多
い。Unlike polyurethane-RIMs, they are easily released from molds and often do not require special mold release agents.
成形物は、表面に酸化層が出来ることかつシアノ基の穫
性によってエポキシやポリウレタ等の一般に使用される
塗料への付着性は、良好である。The molded product has good adhesion to commonly used paints such as epoxy and polyurethane due to the formation of an oxidized layer on the surface and the removability of the cyano group.
かくして得られた成形物は、自動車等を含めた各種運m
閤器の部材、電気、電子線型のハウジングなど、大型の
成型物を中心に広範な用途に使用出来る。The molded product thus obtained can be used in various vehicles including automobiles.
It can be used in a wide range of applications, mainly large molded items, such as parts for pottery tools, housings for electrical and electronic wire types, etc.
以下に実施例を掲げて本発明を詳述する。なお実施例は
説明のためであって、それに限定されるものではない。The present invention will be described in detail with reference to Examples below. Note that the examples are for illustrative purposes only, and are not limited thereto.
実施例1〜6.比較例
市販のDCPを減圧下、窒素気流中で蒸溜精製し、凝固
点33.4℃をしめず精製ジクロペンタジェンを得た。Examples 1-6. Comparative Example Commercially available DCP was purified by distillation under reduced pressure in a nitrogen stream to obtain purified diclopentadiene without lowering its freezing point to 33.4°C.
ガスクロマトグラフによる純度測定では99%以上の純
度をしめした。Purity measurement using a gas chromatograph showed a purity of 99% or more.
一方市販のジシクロペンタジェンを熱wiI!!させ、
シフペンタジェンを(q、これにアクリロニトリルを反
応せしめる方法によって、5−シアノノルボルネンを合
成した。蒸溜精製し、ガスクロマトグラフによる純度測
定では同様に99%以上の純度をしめした。On the other hand, heat the commercially available dicyclopentadiene! ! let me,
5-Cyanonorbornene was synthesized by reacting schifpentadiene (q) with acrylonitrile. It was purified by distillation, and the purity measurement by gas chromatography similarly showed a purity of 99% or more.
[M媒成分溶液の調整1
六塩化タングステン20gを乾燥トルエン70dに窒素
気流中下で添IIOL、、次いでノニルフェノール21
g及びトルエン16dよりなる溶液を添加して0.5M
のタングステン含有触媒溶液を調整し、この溶液に対し
、窒素ガスを一晩パージして、六塩化タングステンとノ
ニルフェノールとの反応によって精製された塩化水素ガ
スを除去して、重合用触媒とした。[Preparation of M medium component solution 1 20 g of tungsten hexachloride was added to 70 d of dry toluene under a nitrogen stream IIOL, then nonylphenol 21
g and 16 d of toluene to make 0.5 M
A tungsten-containing catalyst solution was prepared, and this solution was purged with nitrogen gas overnight to remove the hydrogen chloride gas purified by the reaction between tungsten hexachloride and nonylphenol, thereby obtaining a polymerization catalyst.
かかる溶液10d、アセチルアセトン1.Ome混合単
酊体500dを混合し、タングステン含m 0.001
M溶液A溶液製した。10d of such solution, acetylacetone 1. Mix 500d of Ome mixed monomer, containing tungsten m 0.001
M solution A solution was prepared.
[活性他剤成分溶液の調製1
ジエチルアルミニウムクロライド0.189混合単Φ体
500dを混合してアルミニウム分として、0.003
Mの溶液Bを調製した。[Preparation of active ingredient solution 1 500d of diethyl aluminum chloride 0.189 mixed single Φ body was mixed to give an aluminum content of 0.003
Solution B of M was prepared.
かかる溶液中の混合単量体のDCPと5−シアノノルボ
ルネンの使用モル比は以下通りであった。The molar ratio of the mixed monomers DCP and 5-cyanonorbornene in this solution was as follows.
かかる上記の溶液を触媒成分溶液(溶液A)10d、活
性他剤成分溶液(溶液B ) 10mを所定の温度とし
た後充分、窒素でおきかえたシリンジ内に取り出した。After bringing the above-mentioned solution to a predetermined temperature, 10 d of the catalyst component solution (solution A) and 10 m of the active agent component solution (solution B) were taken out into a syringe which was sufficiently replaced with nitrogen.
かかるシリンジから液を一定速度で両方を同時に撹拌器
つきガラスフラスコ内急速撹拌下に押し出し急速混合し
た後、撹拌器をあげ熱電対を挿入し、液のシリンジから
の注入が終った時点から 100℃に到達した時間を測
定した。Both liquids were simultaneously extruded from the syringe at a constant speed into a glass flask equipped with a stirrer under rapid stirring, and after rapid mixing, the stirrer was raised, a thermocouple was inserted, and the temperature was 100°C from the time the liquid was injected from the syringe. The time it took to reach was measured.
さらに、固化した架橋樹脂を取・り出し切片を切り出し
TMA法−針浸入モードで、軟化点及び膨潤率を測定し
た。結果を下記表にまとめて示した。Furthermore, the solidified crosslinked resin was taken out, a section was cut out, and the softening point and swelling rate were measured using the TMA method - needle penetration mode. The results are summarized in the table below.
5−シアノノルボルネンの共重合によって混合時から重
合が充分起って温度が100℃に達するまでの時間が伸
び、重合開始が調節出来ているのが判る。It can be seen that the copolymerization of 5-cyanonorbornene lengthens the time from the time of mixing until polymerization sufficiently occurs and the temperature reaches 100°C, indicating that the initiation of polymerization can be controlled.
実施例3.4の組成の液については、液をA。For the liquid having the composition of Example 3.4, use liquid A.
B各々シリンジ内にとり出し、それを機械的に一定速度
で押し出しノズル内に導き、そこで衝突混合して型内に
流し込める超小型RIMiにかけて成型した所褐色の丈
夫な板状物が成型出来た。Each of B was taken out into a syringe, mechanically introduced at a constant speed into an extrusion nozzle, and molded by an ultra-compact RIMi that could be mixed by collision and poured into a mold.A brown, durable plate-like product was molded.
次いで、実施例4,5の組成の液を5蛇づつとって、窒
素気流下で撹拌し、プレミックスを作成しこれを60℃
に保持した型内に流し込んだ所、同様に丈夫な褐色の板
を得た。Next, 5 portions each of the liquids having the compositions of Examples 4 and 5 were taken and stirred under a nitrogen stream to create a premix, which was heated at 60°C.
When the mixture was poured into a mold held at a temperature, a similarly strong brown plate was obtained.
実施例7−8
フマロニトリルとシクロペンタジェンをジエチルエーテ
ル中で反応せしめ、精製した5、6−ジシアツノルボル
ネン(DCN)を再結晶精製して融点98〜99℃のも
のを得た。Example 7-8 Fumaronitrile and cyclopentadiene were reacted in diethyl ether, and purified 5,6-dicyazunorbornene (DCN) was purified by recrystallization to obtain a product with a melting point of 98 to 99°C.
単層体の組成を次表の如くかえる伯は、実施例1と同様
にして触媒成分溶液(溶液A)と活性他剤成分溶液(溶
液B)を調製した。かかる溶液A。A catalyst component solution (solution A) and an active agent component solution (solution B) were prepared in the same manner as in Example 1, with the composition of the monolayer body being changed as shown in the following table. Such solution A.
Bを実施例1と同様にして樹脂成型物を得たがその際の
混合時温度2重合時間を下記表に併記した。A resin molded product was obtained using B in the same manner as in Example 1, and the mixing temperature and polymerization time are also listed in the table below.
同表から重合時間が長くなりシアノ基による遅延効果が
現われているのが判る。From the same table, it can be seen that as the polymerization time becomes longer, the retardation effect due to the cyano group appears.
実施例9−16
5−シアノノルボルネンと市販のジシクロペンタジェン
を熱解離させて得たシクロペンタジェンとを常法によっ
て反応せしめさらに蒸溜精製する事により6−ジアツー
1.4,5.8−ジメタノ−1,4゜4a、5,6,7
,8.8a−オクタヒドロナフタレン(CDMON)を
合成した。ガスクロマトグラフによる純度測定でき99
%以上の純度を示した。Example 9-16 5-cyanonorbornene and cyclopentadiene obtained by thermally dissociating commercially available dicyclopentadiene were reacted in a conventional manner and further purified by distillation to produce 6-dia2-1.4,5.8- Dimethano-1,4゜4a,5,6,7
,8.8a-octahydronaphthalene (CDMON) was synthesized. Purity can be measured by gas chromatography 99
% or more purity.
単母体の組成を次表の如くかえ、かつ活性他剤成分のジ
エチルアルミニウムクロライドを等モル濃度のトリオク
チルアルミニウムとジオクチルアルミニウムアイオダイ
ドのモル比で85:15の混合物を用いる以外は、実施
例1と同様にして下記表に示すような組成の触媒成分溶
液(溶液A)と活性他剤成分溶液(溶液B)を調製した
。Example 1 except that the composition of the single matrix was changed as shown in the table below, and the active ingredient diethylaluminum chloride was a mixture of equimolar concentrations of trioctylaluminum and dioctylaluminum iodide in a molar ratio of 85:15. In the same manner as above, a catalyst component solution (solution A) and an active agent component solution (solution B) having the compositions shown in the table below were prepared.
かかる溶液A、Bを実施例1と同様にして、フラスコ内
に硬化樹脂成型物を得た。実施例1と同様にして、混合
時温度1重合時間及び成型物からサンプルを切り出して
TMAによる軟化点測定。These solutions A and B were treated in the same manner as in Example 1 to obtain a cured resin molded product in a flask. In the same manner as in Example 1, the temperature during mixing was 1 polymerization time, and the sample was cut out from the molded product and the softening point was measured by TMA.
膨潤率の測定をおこなった結果を下記表に示した。The results of measuring the swelling ratio are shown in the table below.
対応する5−シアノノルボルネンを用いた場合に比較し
て軟化点が向上している事がわかる。It can be seen that the softening point is improved compared to when the corresponding 5-cyanonorbornene is used.
次いで、実施例4と同様に実施例11−14の場合の各
々の溶液A、Bから5dづつとり、窒素気流中に撹拌し
プレミックスを作成しこれを90℃保持した型内に注入
し、同様に褐色の硬化成型物を(qた。Next, in the same manner as in Example 4, 5 d of each solution A and B in Examples 11-14 were taken and stirred in a nitrogen stream to create a premix, which was poured into a mold maintained at 90°C. Similarly, a brown cured molded product was prepared (q).
実施例9.10.15.16の組成の液については、実
施例3と同様に液をA、B各々シリンジ内に取り出し、
それを機械的に一定速度で押し出しノズル内に導き、そ
こで衝突混合した型内に流し込める超小型RIM機にか
けて成型した所、褐色の丈夫な板状物が成型出来た。Regarding the liquid having the composition of Example 9.10.15.16, take out the liquid into each syringe of A and B in the same manner as in Example 3,
It was mechanically guided at a constant speed into an extrusion nozzle, where it was molded using an ultra-compact RIM machine that allowed it to be poured into a mold where it was collided and mixed, resulting in a brown, durable plate.
Claims (1)
するメタセンス重合性シクロアルケン類過半モル〜99
.5モル%を含み残余が分子中にペンダントシアノ基を
1〜2個有するノルボルネン誘導体の少なくとも1種よ
り実質的になる単量体混合物を、メタセンス重合触媒系
の存在下重合せしめることによって得られた架橋重合体
成型物。 2、ジシロンペンタジエンを含有するメタセンス重合性
環状オレフィン化合物を、メタセンス重合触媒系の存在
下重合せしめて架橋重合体成型物を得る方法において、
原料単1体としてジシクロペンタジエンを少なくとも3
0モル%含有するメタセンス重合性シクロアルカン類過
半モル〜99.5モル%を含み、残余が分子中にペンダ
ントシアノ基を1〜2個有するノルボルネン誘導体の少
なくとも1種より実質的になる単量体混合物を使用する
ことを特徴とする架橋重合体成型物の製造方法。 3、(a)メタセンス重合触媒系の触媒を含むメタセン
ス重合性環状オレフィンの反応性溶液 (溶液A)、 (b)メタセンス重合触媒系の活性化剤を含むメタセン
ス重合性環状オレフィンの反応性 溶液(溶液B)、 より少なくともなる反応性溶液の組合せにおいて、前記
溶液A及び溶液B中のメタセンス重合性環状オレフィン
は、両方を合せた組成が、ジシクロペンタジエンを少な
くとも30モル%含有するメタセンス重合性シクロアル
カン類過半モル〜99.5モル%を含み残余が分子中に
ペンダントシアノ基を1〜2個有するノルボルネン誘導
体の少なくとも1種より実質的になる単量体混合物であ
ることを特徴とする反応性溶液の組合せ。[Scope of Claims] 1. Metasense polymerizable cycloalkenes containing at least 30 mol % of dicyclopentadiene with a majority of 99 to 99 mol %
.. obtained by polymerizing a monomer mixture containing 5 mol % and the remainder consisting essentially of at least one norbornene derivative having 1 to 2 pendant cyano groups in the molecule in the presence of a metasense polymerization catalyst system. Cross-linked polymer molded product. 2. A method for obtaining a crosslinked polymer molded product by polymerizing a metasense polymerizable cyclic olefin compound containing disilone pentadiene in the presence of a metasense polymerization catalyst system,
At least 3 dicyclopentadiene as a single raw material
A monomer containing a majority of metasense polymerizable cycloalkanes containing 0 mol% to 99.5 mol%, with the remainder consisting essentially of at least one norbornene derivative having 1 to 2 pendant cyano groups in the molecule. A method for producing a crosslinked polymer molded article, the method comprising using a mixture. 3. (a) A reactive solution of a metasense polymerizable cyclic olefin containing a catalyst of a metasense polymerization catalyst system (solution A), (b) A reactive solution of a metasense polymerizable cyclic olefin containing an activator of a metasense polymerization catalyst system ( Solution B), wherein the metasense polymerizable cyclic olefin in solution A and solution B is a metasense polymerizable cycloolefin whose combined composition contains at least 30 mol% dicyclopentadiene. Reactivity characterized by being a monomer mixture containing a majority of alkanes to 99.5 mol % and the remainder consisting essentially of at least one norbornene derivative having 1 to 2 pendant cyano groups in the molecule. Combination of solutions.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61-183469 | 1986-08-06 | ||
JP18346986 | 1986-08-06 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63152620A true JPS63152620A (en) | 1988-06-25 |
JPH0739472B2 JPH0739472B2 (en) | 1995-05-01 |
Family
ID=16136337
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62015941A Expired - Lifetime JPH0739472B2 (en) | 1986-08-06 | 1987-01-28 | Method for producing crosslinked polymer molding |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0739472B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0229423A (en) * | 1988-07-19 | 1990-01-31 | Nippon Zeon Co Ltd | Manufacture of colored norbornene polymer |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5272780A (en) * | 1975-12-16 | 1977-06-17 | Showa Denko Kk | Laminated |
-
1987
- 1987-01-28 JP JP62015941A patent/JPH0739472B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5272780A (en) * | 1975-12-16 | 1977-06-17 | Showa Denko Kk | Laminated |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0229423A (en) * | 1988-07-19 | 1990-01-31 | Nippon Zeon Co Ltd | Manufacture of colored norbornene polymer |
Also Published As
Publication number | Publication date |
---|---|
JPH0739472B2 (en) | 1995-05-01 |
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