CN1116320C - Catalyst for syndiotatic phenylethylene polymerization - Google Patents
Catalyst for syndiotatic phenylethylene polymerization Download PDFInfo
- Publication number
- CN1116320C CN1116320C CN 00127437 CN00127437A CN1116320C CN 1116320 C CN1116320 C CN 1116320C CN 00127437 CN00127437 CN 00127437 CN 00127437 A CN00127437 A CN 00127437A CN 1116320 C CN1116320 C CN 1116320C
- Authority
- CN
- China
- Prior art keywords
- mol
- styrene
- polystyrene
- hour
- 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.)
- Expired - Fee Related
Links
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical group C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 title claims abstract description 70
- 238000006116 polymerization reaction Methods 0.000 title claims abstract description 26
- 239000003054 catalyst Substances 0.000 title abstract description 15
- 125000000217 alkyl group Chemical group 0.000 claims abstract description 4
- 125000003454 indenyl group Chemical group C1(C=CC2=CC=CC=C12)* 0.000 claims abstract description 4
- YBYIRNPNPLQARY-UHFFFAOYSA-N 1H-indene Natural products C1=CC=C2CC=CC2=C1 YBYIRNPNPLQARY-UHFFFAOYSA-N 0.000 claims abstract description 3
- CPOFMOWDMVWCLF-UHFFFAOYSA-N methyl(oxo)alumane Chemical compound C[Al]=O CPOFMOWDMVWCLF-UHFFFAOYSA-N 0.000 claims description 15
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 239000000470 constituent Substances 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 abstract description 30
- 229920010524 Syndiotactic polystyrene Polymers 0.000 abstract description 21
- -1 titanocene compound Chemical class 0.000 abstract description 5
- 239000002685 polymerization catalyst Substances 0.000 abstract description 2
- 238000009776 industrial production Methods 0.000 abstract 1
- 229910052751 metal Inorganic materials 0.000 abstract 1
- 239000002184 metal Substances 0.000 abstract 1
- 150000003609 titanium compounds Chemical class 0.000 abstract 1
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 105
- 239000004793 Polystyrene Substances 0.000 description 51
- 239000000243 solution Substances 0.000 description 41
- 229920002223 polystyrene Polymers 0.000 description 28
- 239000010936 titanium Substances 0.000 description 28
- 239000003708 ampul Substances 0.000 description 22
- 150000001875 compounds Chemical class 0.000 description 20
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 18
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 18
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 12
- LVVOITZLMNPGOL-UHFFFAOYSA-N 2-methyloxaluminane;toluene Chemical compound C[Al]1CCCCO1.CC1=CC=CC=C1 LVVOITZLMNPGOL-UHFFFAOYSA-N 0.000 description 10
- MZRVEZGGRBJDDB-UHFFFAOYSA-N N-Butyllithium Chemical compound [Li]CCCC MZRVEZGGRBJDDB-UHFFFAOYSA-N 0.000 description 10
- 229920000642 polymer Polymers 0.000 description 10
- 229940126062 Compound A Drugs 0.000 description 7
- NLDMNSXOCDLTTB-UHFFFAOYSA-N Heterophylliin A Natural products O1C2COC(=O)C3=CC(O)=C(O)C(O)=C3C3=C(O)C(O)=C(O)C=C3C(=O)OC2C(OC(=O)C=2C=C(O)C(O)=C(O)C=2)C(O)C1OC(=O)C1=CC(O)=C(O)C(O)=C1 NLDMNSXOCDLTTB-UHFFFAOYSA-N 0.000 description 7
- 125000005233 alkylalcohol group Chemical group 0.000 description 7
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- 229910052786 argon Inorganic materials 0.000 description 6
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 229910003002 lithium salt Inorganic materials 0.000 description 4
- 159000000002 lithium salts Chemical class 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- 229910052719 titanium Inorganic materials 0.000 description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 150000001793 charged compounds Chemical class 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000000921 elemental analysis Methods 0.000 description 3
- 238000002329 infrared spectrum Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000001819 mass spectrum Methods 0.000 description 3
- 239000012266 salt solution Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- IRAWLGHJHQBREM-UHFFFAOYSA-N 4-methyl-1h-indene Chemical compound CC1=CC=CC2=C1C=CC2 IRAWLGHJHQBREM-UHFFFAOYSA-N 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- LVTJOONKWUXEFR-FZRMHRINSA-N protoneodioscin Natural products O(C[C@@H](CC[C@]1(O)[C@H](C)[C@@H]2[C@]3(C)[C@H]([C@H]4[C@@H]([C@]5(C)C(=CC4)C[C@@H](O[C@@H]4[C@H](O[C@H]6[C@@H](O)[C@@H](O)[C@@H](O)[C@H](C)O6)[C@@H](O)[C@H](O[C@H]6[C@@H](O)[C@@H](O)[C@@H](O)[C@H](C)O6)[C@H](CO)O4)CC5)CC3)C[C@@H]2O1)C)[C@H]1[C@H](O)[C@H](O)[C@H](O)[C@@H](CO)O1 LVTJOONKWUXEFR-FZRMHRINSA-N 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- BGJSXRVXTHVRSN-UHFFFAOYSA-N 1,3,5-trioxane Chemical compound C1OCOCO1 BGJSXRVXTHVRSN-UHFFFAOYSA-N 0.000 description 1
- ZWELHCJHLNGACT-UHFFFAOYSA-N 1H-indene titanium Chemical class [Ti].C1C=CC2=CC=CC=C12 ZWELHCJHLNGACT-UHFFFAOYSA-N 0.000 description 1
- SFJSPHKDURKWNV-UHFFFAOYSA-N 4-ethyl-1h-indene Chemical compound CCC1=CC=CC2=C1C=CC2 SFJSPHKDURKWNV-UHFFFAOYSA-N 0.000 description 1
- YLHSETDFVAXPRB-UHFFFAOYSA-N 5-methyl-1h-indene Chemical compound CC1=CC=C2CC=CC2=C1 YLHSETDFVAXPRB-UHFFFAOYSA-N 0.000 description 1
- SFPQWMKUAVIGIX-UHFFFAOYSA-N C1=CC=C2C([Ti])C=CC2=C1 Chemical compound C1=CC=C2C([Ti])C=CC2=C1 SFPQWMKUAVIGIX-UHFFFAOYSA-N 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 150000001555 benzenes Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000002178 crystalline material Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 239000012968 metallocene catalyst Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- GRVDJDISBSALJP-UHFFFAOYSA-N methyloxidanyl Chemical group [O]C GRVDJDISBSALJP-UHFFFAOYSA-N 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- VMGAPWLDMVPYIA-HIDZBRGKSA-N n'-amino-n-iminomethanimidamide Chemical compound N\N=C\N=N VMGAPWLDMVPYIA-HIDZBRGKSA-N 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- BOLDJAUMGUJJKM-LSDHHAIUSA-N renifolin D Natural products CC(=C)[C@@H]1Cc2c(O)c(O)ccc2[C@H]1CC(=O)c3ccc(O)cc3O BOLDJAUMGUJJKM-LSDHHAIUSA-N 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- YONPGGFAJWQGJC-UHFFFAOYSA-K titanium(iii) chloride Chemical compound Cl[Ti](Cl)Cl YONPGGFAJWQGJC-UHFFFAOYSA-K 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
- 150000003755 zirconium compounds Chemical class 0.000 description 1
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Abstract
本发明涉及一种苯乙烯间规聚合的催化剂,主要解决以往文献中存在茂钛化合物制成的催化剂用于苯乙烯聚合过程时,催化活性低,获得的间规聚苯乙烯含量不高的问题。本发明通过采用结构式为IndTiCl2(OR)的茚基金属钛化合物与烷基铝氧烷组成苯乙烯间规聚合催化剂的技术方案,其中Ind为茚基,较好地解决了该问题,可用于苯乙烯间规聚合的工业生产中。The invention relates to a catalyst for the syndiotactic polymerization of styrene, which mainly solves the problems of low catalytic activity and low content of syndiotactic polystyrene obtained when the catalyst made of titanocene compound is used in the styrene polymerization process in previous literatures . The present invention solves this problem well by adopting the technical scheme of forming a styrene syndiotactic polymerization catalyst with an indenyl metal titanium compound having a structural formula of IndTiCl 2 (OR) and an alkyl aluminoxane, wherein Ind is an indenyl group, and can be used for In the industrial production of syndiotactic polymerization of styrene.
Description
技术领域technical field
本发明涉及一种苯乙烯间规聚合的催化剂。The invention relates to a catalyst for syndiotactic polymerization of styrene.
背景技术Background technique
通过自由基聚合得到的聚苯乙烯(Polystyrene,PS)是一种无规聚合物,质硬,透明,刚性,电绝缘性,价格低廉,容易染色,已成为当今五大通用塑料之一,被广泛应用于包装,建筑,医药,电子,汽车,日用品等行业。但由于结构的无规性导致其易碎,不耐热,不耐化学腐蚀。Polystyrene (Polystyrene, PS) obtained by free radical polymerization is a random polymer with hard quality, transparency, rigidity, electrical insulation, low price and easy dyeing. It has become one of the five general-purpose plastics today and is widely used. Used in packaging, construction, medicine, electronics, automobiles, daily necessities and other industries. However, due to the randomness of the structure, it is fragile, not heat-resistant, and not resistant to chemical corrosion.
欧洲专利EP210615中介绍了一种高立体规整性的聚苯乙烯,其中苯环取代按间规结构排列。这种结晶性材料不再具有无规聚合物的缺点,几乎不溶于任何有机溶剂,且具有高的熔点(250~280℃),耐热、耐化学腐蚀,其性能可与聚酯、聚酰胺等相媲美。European patent EP210615 introduced a polystyrene with high stereoregularity, in which the substitution of benzene rings is arranged in a syndiotactic structure. This crystalline material no longer has the disadvantages of random polymers, is almost insoluble in any organic solvent, and has a high melting point (250-280 ° C), heat resistance, chemical corrosion resistance, and its performance can be compared with polyester, polyamide and so on.
通常用于苯乙烯间规聚合的催化体系由两部分组成,即过渡金属有机化合物,尤其是Ti,Zr的化合物,以及以甲基铝氧烷(MAO)和B(C6F5)3为代表的助催化剂。The catalytic system usually used for the syndiotactic polymerization of styrene consists of two parts, that is, transition metal organic compounds, especially Ti, Zr compounds, and methylaluminoxane (MAO) and B(C 6 F 5 ) 3 as Representative cocatalyst.
文献中常见的催化剂包括钛的各种卤化物,四烷氧基化合物(甲氧基、乙氧基、丙氧基、异丙氧基等),茂金属化合物(一茂三氯钛,一茂三烷基钛,一茂三烷氧基钛,以及取代茂的各种化合物),四烃基钛以及相应的锆化合物。Common catalysts in the literature include various halides of titanium, tetraalkoxy compounds (methoxyl, ethoxyl, propoxyl, isopropoxyl, etc.), metallocene compounds (titanium trichloride, trioxane Titanium, a trialkoxytitanium, and a variety of compounds substituted), titanium tetrahydrocarbyl and the corresponding zirconium compounds.
茂金属催化剂自五十年代以来,一直是催化烯烃聚合的研究热点,80年代初Kaminsky助催化剂甲基铝氧烷的发现更是推动烯烃的催化聚合进入新的研究高潮,其中半夹心化合物与甲基铝氧烷等组成的催化体系对苯乙烯类单体的催化聚合具有显著的间规定向性和高的催化活性。此后,涉及各种半夹心结构化合物的专利相继出现。Since the 1950s, metallocene catalysts have been a research hotspot in catalyzing olefin polymerization. In the early 1980s, the discovery of Kaminsky cocatalyst methylaluminoxane promoted the catalytic polymerization of olefins into a new research climax. Among them, semi-sandwich compounds and formazan The catalytic system composed of aluminoxane and the like has remarkable syndiotropic and high catalytic activity for the catalytic polymerization of styrene monomers. Since then, patents involving various semi-sandwich compounds have appeared one after another.
欧洲专利EP0796875(1997年)(Process for the preparation of crystalline vinylaromaticpolymers with a predominant syndiotactic structure)公开了结构式如下所示的一类茚钛催化剂:典型化合物为Ind’TiCl3,European Patent EP0796875 (1997) (Process for the preparation of crystalline vinylomatic polymers with a dominant syndiotactic structure) discloses a class of indene-titanium catalysts with the following structural formula: Typical compound is Ind'TiCl 3 ,
Ind’Ti(OR1)3,Ind’Ti(R2)3,(Ind’=4-甲基茚,4-乙基茚,5-甲基茚,Ind'Ti(OR 1 ) 3 , Ind'Ti(R 2 ) 3 , (Ind'=4-methylindene, 4-ethylindene, 5-methylindene,
5-苯基茚,4,5-二甲基茚,4,5-二乙基茚;
R1=Me,Et,Pr,Bu,Ph;R2=Me,Et,iBu,Bz)R 1 =Me, Et, Pr, Bu, Ph; R 2 =Me, Et, iBu , Bz)
其实施例中,该类催化剂的催化活性达到2.5×106克PS/(摩尔Ti·摩尔S·小时),所得聚苯乙烯的间规度达到99.4%。但三烷氧基类,三烷基类的催化剂没有报道实施情况。根据文献,该种类型的化合物的合成是通过三氯一茚钛的化合物与相应的醇在三乙胺存在下反应得到,原料醇与生成的产物的极性相似,易与产物相混,难以进行分离提纯。In the examples, the catalytic activity of this type of catalyst reaches 2.5×10 6 g PS/(mole Ti·mole S·hour), and the syndiotacticity of the obtained polystyrene reaches 99.4%. However, the implementation of trialkoxy and trialkyl catalysts has not been reported. According to the literature, the synthesis of this type of compound is obtained by reacting the compound of trichloroindene titanium with the corresponding alcohol in the presence of triethylamine. The polarity of the raw material alcohol is similar to that of the product, so it is easy to mix with the product and difficult to obtain. Carry out separation and purification.
发明内容Contents of the invention
本发明的目的是为了克服以往文献中介绍的茂金属化合物制成的催化剂用于苯乙烯间规聚合过程时,存在催化效果不高的缺点,提供一种新的苯乙烯间规聚合的催化剂。该催化剂用于苯乙烯间规聚合过程时,具有催化活性高,催化效果好,获得的间规聚苯乙烯含量高,所得聚合物熔点高的特点。The object of the present invention is to provide a new catalyst for the syndiotactic polymerization of styrene in order to overcome the shortcoming that the catalyst made of metallocene compounds introduced in the previous literature has a low catalytic effect when used in the styrene syndiotactic polymerization process. When the catalyst is used in the syndiotactic polymerization process of styrene, it has the characteristics of high catalytic activity, good catalytic effect, high content of syndiotactic polystyrene obtained, and high melting point of the obtained polymer.
本发明的目的是通过以下的技术方案来实现的:一种苯乙烯间规聚合的催化剂包括以下活性组份:The purpose of the present invention is achieved by the following technical solutions: a catalyst for syndiotactic polymerization of styrene comprises the following active components:
a)IndTiCl2(OR);a) IndTiCl 2 (OR);
b)烷基铝氧烷;b) alkylaluminoxanes;
其中:Ind为茚基;Wherein: Ind is indenyl;
R为3~6个碳原子的直链、支链或环状结构的烷基;R is an alkyl group with a straight chain, branched chain or cyclic structure of 3 to 6 carbon atoms;
以摩尔比计,烷基铝氧烷/IndTiCl2(OR)为300~4100。In terms of molar ratio, alkylaluminoxane/IndTiCl 2 (OR) is 300-4100.
上述技术方案中,烷基铝氧烷的优选方案为甲基铝氧烷,以摩尔比计,烷基铝氧烷/IndTiCl2(OR)的优选范围为300~2100。In the above technical solutions, the preferred solution of alkylaluminoxane is methylaluminoxane, and the preferred range of alkylaluminoxane/IndTiCl 2 (OR) is 300-2100 in terms of molar ratio.
本发明催化剂的制备用一般混合即可。The catalyst of the present invention can be prepared by general mixing.
本发明由于采用一种新型的茚基钛化合物与烷基铝氧烷组成催化剂,它是一高效的苯乙烯类单体间规聚合催化剂。用于苯乙烯间规聚合时,催化剂的活性最高可达1.39×107克PS/摩尔Ti·摩尔S·小时,催化所得聚苯乙烯的间规重量含量最高达到99.6%,聚合物熔点为273~277℃,取得了较好的效果。The invention adopts a novel indenyl titanium compound and an alkyl aluminoxane to form a catalyst, which is a high-efficiency syndiotactic polymerization catalyst for styrene monomers. When used in the syndiotactic polymerization of styrene, the activity of the catalyst can reach up to 1.39×10 7 g PS/mole Ti·mol S·hour, the syndiotactic weight content of the polystyrene obtained by catalysis can reach up to 99.6%, and the melting point of the polymer is 273 ~277°C, good results have been achieved.
具体实施方式Detailed ways
下面通过实施例对本发明作进一步的阐述:【实施例1】The present invention will be further elaborated below by embodiment: 【Embodiment 1】
聚合反应在一烘烤充氩三次的安培瓶中进行。2毫升苯乙烯,3.4毫升甲苯,6.6毫升浓度1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.05毫升的0.05摩尔/升化合物IndTiCl2(OMe)的甲苯溶液依次注射入安培瓶中,放置于预先恒温至50℃的油浴中聚合1小时。用以重量百分比计为10%HCl的乙醇终止聚合反应,经过滤、洗涤处理后,所得聚合物于80℃下真空干燥24小时至恒重,得0.1616克聚苯乙烯,催化活性为3.72×106克PS/(摩尔Ti·摩尔S·小时)。在丁酮中回流2小时,除去无规聚苯乙烯,测得间规聚苯乙烯重量含量为99.3%,所得聚合物熔点为277℃。【实施例2】Polymerizations were carried out in a baked argon-filled ampule three times. 2 milliliters of styrene, 3.4 milliliters of toluene, 6.6 milliliters of methylalumoxane toluene solution with a concentration of 1.53 mol/liter, and 0.05 milliliters of 0.05 mol/liter compound IndTiCl 2 (OMe) in toluene were injected into the ampoule successively, and placed Polymerize for 1 hour in an oil bath whose temperature was previously adjusted to 50°C. Terminate the polymerization reaction with ethanol that is 10% HCl in terms of weight percentage. After filtering and washing, the resulting polymer is vacuum-dried at 80° C. for 24 hours to constant weight to obtain 0.1616 grams of polystyrene. The catalytic activity is 3.72×10 6 g PS/(mole Ti·mole S·hour). Reflux in methyl ethyl ketone for 2 hours to remove atactic polystyrene, the measured weight content of syndiotactic polystyrene is 99.3%, and the melting point of the obtained polymer is 277°C. [Example 2]
2毫升苯乙烯,3.4毫升甲苯,6.6毫升浓度1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升化合物IndTiCl2(OMe)的甲苯溶液依次注射入安培瓶中,其中Me为甲基,放置于预先恒温至50℃的油浴中聚合1小时,得0.1955克聚苯乙烯,催化活性为2.25×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为95.8%。【实施例3】2 milliliters of styrene, 3.4 milliliters of toluene, 6.6 milliliters of 1.53 mol/liter methylaluminoxane toluene solution, and 0.1 milliliter of 0.05 mol/liter compound IndTiCl 2 (OMe) in toluene were injected into the ampoule successively, wherein Me is a methyl group, placed in an oil bath with a constant temperature at 50°C and polymerized for 1 hour to obtain 0.1955 g of polystyrene, with a catalytic activity of 2.25×10 6 g PS/(mole Ti·mol S·hour). The weight content of tactic polystyrene is 95.8%. [Example 3]
11毫升苯乙烯,0.5毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.05毫升的0.05摩尔/升化合物IndTiCl2(OMe)的甲苯溶液依次注射入安培瓶中,放置于预先恒温至50℃的油浴中聚合0.5小时,得1.5709克聚苯乙烯,催化活性为1.31×107克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为90.1%。【比较例1】11 ml of styrene, 0.5 ml of methylaluminoxane toluene solution with a concentration of 1.53 mol/L, and 0.05 ml of toluene solution of 0.05 mol/L compound IndTiCl 2 (OMe) were injected into the ampoule in sequence, and placed in a pre-constant temperature Polymerize in an oil bath at 50°C for 0.5 hours to obtain 1.5709 grams of polystyrene, with a catalytic activity of 1.31× 107 grams of PS/(mole Ti mole S hour), and the measured syndiotactic polystyrene weight content is 90.1% . [Comparative Example 1]
11毫升苯乙烯,0.5毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.05毫升的0.05摩尔/升IndTiCl3的甲苯溶液依次注射入安培瓶中,放置于预先恒温至50℃的油浴中聚合0.5小时,得1.0996克聚苯乙烯,催化活性为9.19×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为86.4%。【实施例4】11 ml of styrene, 0.5 ml of methylalumoxane toluene solution with a concentration of 1.53 mol/L, and 0.05 ml of 0.05 mol/L IndTiCl 3 in toluene solution were injected into the ampoule in sequence, and placed in a pre-heated to 50 ° C Polymerized in an oil bath for 0.5 hour to obtain 1.0996 g of polystyrene, with a catalytic activity of 9.19×10 6 g PS/(mol Ti·mol S·hour), and a measured syndiotactic polystyrene weight content of 86.4%. 【Example 4】
11毫升苯乙烯,1毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升化合物IndTiCl2(OMe)的甲苯溶液依次注射入安培瓶中,放置于预先恒温至90℃的油浴中聚合2小时,得1.8724克聚苯乙烯,催化活性为1.96×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为87.7%。【实施例5】11 ml of styrene, 1 ml of methylaluminoxane toluene solution with a concentration of 1.53 mol/L, and 0.1 ml of 0.05 mol/L compound IndTiCl 2 (OMe) in toluene were injected into the ampoule in sequence, and placed in a pre-heated Polymerize in an oil bath at 90° C. for 2 hours to obtain 1.8724 g of polystyrene, with a catalytic activity of 1.96×10 6 g PS/(mole Ti mole S hour), and the measured syndiotactic polystyrene weight content is 87.7%. . 【Example 5】
11毫升苯乙烯,1毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升化合物IndTiCl2(OMe)的甲苯溶液依次注射入安培瓶中,放置于预先恒温至70℃的油浴中聚合1小时,得1.6544克聚苯乙烯,催化活性为3.46×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为90.3%。【比较例2】11 ml of styrene, 1 ml of methylaluminoxane toluene solution with a concentration of 1.53 mol/L, and 0.1 ml of 0.05 mol/L compound IndTiCl 2 (OMe) in toluene were injected into the ampoule in sequence, and placed in a pre-heated Polymerize in an oil bath at 70° C. for 1 hour to obtain 1.6544 grams of polystyrene, with a catalytic activity of 3.46×10 6 grams of PS/(mole Ti mole S hour), and the measured syndiotactic polystyrene weight content is 90.3%. . 【Comparative example 2】
11毫升苯乙烯,1毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升IndTiCl3的甲苯溶液依次注射入安培瓶中,放置于预先恒温至70℃的油浴中聚合1小时,得1.4586克聚苯乙烯,催化活性为3.05×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为86.6%。【实施例6】11 ml of styrene, 1 ml of methylalumoxane toluene solution with a concentration of 1.53 mol/L, and 0.1 ml of 0.05 mol/L IndTiCl 3 in toluene solution were injected into the ampoule in sequence, and placed in a pre-heated to 70°C Polymerized in an oil bath for 1 hour to obtain 1.4586 g of polystyrene, with a catalytic activity of 3.05×10 6 g PS/(mol Ti·mol S·hour), and a measured syndiotactic polystyrene weight content of 86.6%. [Example 6]
11毫升苯乙烯,1毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升化合物IndTiCl2(OMe)的甲苯溶液依次注射入安培瓶中,放置于预先恒温至25℃的油浴中聚合0.5小时,得0.9766克聚苯乙烯,催化活性为4.08×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为85.2%。【实施例7】11 ml of styrene, 1 ml of methylaluminoxane toluene solution with a concentration of 1.53 mol/L, and 0.1 ml of 0.05 mol/L compound IndTiCl 2 (OMe) in toluene were injected into the ampoule in sequence, and placed in a pre-heated Polymerize in an oil bath at 25° C. for 0.5 hour to obtain 0.9766 gram of polystyrene, the catalytic activity is 4.08×10 6 gram PS/(mole Ti mole S hour), and the recorded syndiotactic polystyrene weight content is 85.2% . [Example 7]
2毫升苯乙烯,8.5毫升甲苯,1.6毫升浓度1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.24毫升的0.0025摩尔/升化合物IndTiCl2(OMe)的甲苯溶液依次注射入安培瓶中,放置于预先恒温至50℃的油浴中聚合1小时,得0.1337克聚苯乙烯,催化活性为1.28×107克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为98.1%。【实施例8】2 milliliters of styrene, 8.5 milliliters of toluene, 1.6 milliliters of methylalumoxane toluene solution with a concentration of 1.53 mol/L, and 0.24 milliliters of 0.0025 mol/liter compound IndTiCl 2 (OMe) in toluene were injected into the ampoule in sequence, and placed Polymerize for 1 hour in an oil bath with a constant temperature at 50°C in advance to obtain 0.1337 g of polystyrene, with a catalytic activity of 1.28× 107 g PS/(mole Ti·mol S·hour), and the weight content of syndiotactic polystyrene was measured was 98.1%. [Embodiment 8]
(化合物A的制备):在氩气保护下,将烷基醇(其中R为乙基)的正己烷和四氢呋喃混合溶液缓慢滴加于正丁基锂的正己烷溶液中,烷基醇与丁基锂的摩尔比为1∶1.2,反应生成的锂盐溶液冷至-50℃,与烷基醇等摩尔数的IndTiCl3的二氯甲烷溶液缓慢滴加于该溶液中,0.5小时滴完,自然升至30℃,搅拌反应16小时,过滤,清液抽干,所得固体用二氯甲烷及正己烷重结晶,得深红色晶体产率为58%。分析测试结果如下(Preparation of Compound A): Under the protection of argon, slowly add the mixed solution of n-hexane and tetrahydrofuran (THF) in n-butyllithium in the n-hexane solution of alkanol (wherein R is ethyl) under the protection of argon. The molar ratio of base lithium is 1:1.2, the lithium salt solution generated by the reaction is cooled to -50°C, and the dichloromethane solution of IndTiCl 3 with an equal molar number of alkyl alcohol is slowly added dropwise to the solution, and the drop is completed in 0.5 hours. Naturally raised to 30°C, stirred and reacted for 16 hours, filtered, and the clear liquid was sucked dry. The obtained solid was recrystallized with dichloromethane and n-hexane to obtain dark red crystals with a yield of 58%. The analysis test results are as follows
分子式:C11H12Cl2OTi;质谱显示分子离子峰278(5,M+)。Molecular formula: C 11 H 12 Cl 2 OTi; mass spectrum shows molecular ion peak 278 (5, M + ).
红外光谱数据(cm-1):3300s,1620m,1460w,1390w,1050w,880s,825s。Infrared spectrum data (cm -1 ): 3300s, 1620m, 1460w, 1390w, 1050w, 880s, 825s.
核磁数据(1H NMR,ppm):7.79(dd,2H,J=6.3Hz,J=3.0Hz),7.45(dd,2H,J=6.3Hz,J=3.0Hz),6.84(d,2H,J=3.4Hz),6.80(t,1H,J=3.4Hz),4.60(q,2H,J=5.3Hz),1.31(t,3H,J=5.3Hz)。NMR data ( 1 H NMR, ppm): 7.79(dd, 2H, J=6.3Hz, J=3.0Hz), 7.45(dd, 2H, J=6.3Hz, J=3.0Hz), 6.84(d, 2H, J = 3.4 Hz), 6.80 (t, 1H, J = 3.4 Hz), 4.60 (q, 2H, J = 5.3 Hz), 1.31 (t, 3H, J = 5.3 Hz).
元素分析数据:实测,C:47.21% H:4.29%Elemental analysis data: measured, C: 47.21% H: 4.29%
计算,C:47.36% H:4.34%【实施例9】Calculation, C: 47.36% H: 4.34% [Example 9]
(化合物B的制备):在氩气保护下,将烷基醇(其中R为异丙基)的正己烷溶液缓慢滴加于正丁基锂的正己烷溶液中,烷基醇与丁基锂的摩尔比为1∶1,反应生成的锂盐溶液冷至-60℃,与烷基醇摩尔比为1∶1.2的IndTiCl3的二氯甲烷溶液缓慢滴加于该溶液中,0.5小时滴完,自然升至35℃,搅拌反应16小时,过滤,清液抽干,所得固体用二氯甲烷及正己烷重结晶,得深红色晶体产率为76%。分析测试结果如下(Preparation of Compound B): Under the protection of argon, the n-hexane solution of alkyl alcohol (wherein R is isopropyl) is slowly added dropwise to the n-hexane solution of n-butyl lithium, and the alkyl alcohol and butyl lithium The molar ratio of the lithium salt is 1:1, the lithium salt solution generated by the reaction is cooled to -60°C, and the dichloromethane solution of IndTiCl 3 with a molar ratio of 1:1.2 to the alkyl alcohol is slowly added dropwise to the solution, and the drop is completed in 0.5 hours. , naturally rose to 35°C, stirred and reacted for 16 hours, filtered, and the clear liquid was sucked dry, and the obtained solid was recrystallized with dichloromethane and n-hexane to obtain dark red crystals with a yield of 76%. The analysis test results are as follows
分子式:C12H14Cl2OTi;质谱显示分子离子峰292(2,M+)。Molecular formula: C 12 H 14 Cl 2 OTi; mass spectrum shows molecular ion peak 292 (2, M + ).
红外光谱数据(cm-1):3330s,1613m,1458w,1392w,1360w,1315w,1200w,1168w,1114w,1050w,884s,768s。Infrared spectrum data (cm -1 ): 3330s, 1613m, 1458w, 1392w, 1360w, 1315w, 1200w, 1168w, 1114w, 1050w, 884s, 768s.
核磁数据(1H NMR,ppm):7.80(dd,2H,J=6.3Hz,J=3.1Hz),7.45(dd,2H,J=6.3Hz,J=3.1Hz),6.82(d,2H,J=3.4Hz),6.78(t,1H,J=3.4Hz),4.92(m,1H,J=6.1Hz),1.38(d,6H,J=6.1Hz)。NMR data ( 1 H NMR, ppm): 7.80(dd, 2H, J=6.3Hz, J=3.1Hz), 7.45(dd, 2H, J=6.3Hz, J=3.1Hz), 6.82(d, 2H, J=3.4Hz), 6.78(t, 1H, J=3.4Hz), 4.92(m, 1H, J=6.1Hz), 1.38(d, 6H, J=6.1Hz).
元素分析数据:实测,C:48.81% H:4.76%Elemental analysis data: measured, C: 48.81% H: 4.76%
计算,C:49.19% H:4.82%【实施例10】Calculation, C: 49.19% H: 4.82% [Example 10]
(化合物C的制备):在氩气保护下,将烷基醇(其中R为环己基)的正己烷溶液缓慢滴加于正丁基锂的正己烷溶液中,烷基醇与丁基锂的摩尔比为1∶1.1,反应生成的锂盐溶液冷至-60℃,与烷基醇摩尔比为1∶1.2的IndTiCl3的二氯甲烷溶液缓慢滴加于该溶液中,0.5小时滴完,自然升至30℃,搅拌反应16小时,过滤,清液抽干,所得固体用二氯甲烷及正己烷重结晶,得桔红色晶体产率为61%。分析测试结果如下(Preparation of Compound C): Under the protection of argon, the n-hexane solution of alkyl alcohol (wherein R is cyclohexyl) is slowly added dropwise in the n-hexane solution of n-butyllithium, the mixture of alkyl alcohol and butyllithium The molar ratio is 1:1.1, the lithium salt solution generated by the reaction is cooled to -60°C, and the dichloromethane solution of IndTiCl3 with an alkyl alcohol molar ratio of 1:1.2 is slowly added dropwise to the solution, and the drop is completed in 0.5 hours. Naturally raised to 30°C, stirred and reacted for 16 hours, filtered, and the clear liquid was sucked dry. The obtained solid was recrystallized with dichloromethane and n-hexane to obtain orange-red crystals with a yield of 61%. The analysis test results are as follows
分子式:C15H18Cl2OTi;质谱显示分子离子峰332(0.6,M+)。Molecular formula: C 15 H 18 Cl 2 OTi; mass spectrum shows molecular ion peak 332 (0.6, M + ).
红外光谱数据(cm-1):3300s,2930m,2865m,1615m,1460w,1398w,1370w,1055m,1020w,885s,770s。Infrared spectrum data (cm -1 ): 3300s, 2930m, 2865m, 1615m, 1460w, 1398w, 1370w, 1055m, 1020w, 885s, 770s.
核磁数据(1H NMR,ppm):7.78(dd,2H,J=6.4Hz,J=3.0Hz),7.41(dd,2H,J=6.4Hz,J=3.0Hz),6.82(d,2H,J=3.4Hz),6.79(t,1H,J=3.4Hz),4.70(m,1H),2.3~1.0(m,10H)。NMR data ( 1 H NMR, ppm): 7.78 (dd, 2H, J=6.4Hz, J=3.0Hz), 7.41 (dd, 2H, J=6.4Hz, J=3.0Hz), 6.82 (d, 2H, J=3.4Hz), 6.79(t, 1H, J=3.4Hz), 4.70(m, 1H), 2.3~1.0(m, 10H).
元素分析数据:实测,C:53.93% H:5.35%Elemental analysis data: measured, C: 53.93% H: 5.35%
计算,C:54.09% H:5.45%【实施例11】Calculation, C: 54.09% H: 5.45% [Example 11]
聚合反应在一烘烤充氩三次的安培瓶中进行。2毫升苯乙烯,3.4毫升甲苯,6.6毫升浓度1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.05毫升的0.05摩尔/升化合物A的甲苯溶液依次注射入安培瓶中,放置于预先恒温至50℃的油浴中聚合1小时。用重量浓度含10%HCl的乙醇终止聚合反应,经过滤、洗涤处理后,所得聚合物于80℃下真空干燥24小时至恒重,得0.2109克聚苯乙烯,催化活性为4.85×106克PS/(摩尔Ti·摩尔S·小时)。在丁酮中回流2小时,除去无规聚苯乙烯,测得间规聚苯乙烯重量含量为99.6%,所得聚合物熔点为275℃。【实施例12】Polymerizations were carried out in a baked argon-filled ampule three times. 2 milliliters of styrene, 3.4 milliliters of toluene, 6.6 milliliters of 1.53 mol/liter methylalumoxane toluene solution, and 0.05 milliliter of 0.05 mol/liter compound A toluene solution were sequentially injected into the ampoule, and placed in a pre-heated to Polymerization was carried out in an oil bath at 50°C for 1 hour. Terminate the polymerization reaction with ethanol containing 10% HCl in weight concentration. After filtering and washing, the obtained polymer is vacuum-dried at 80°C for 24 hours to constant weight to obtain 0.2109 g of polystyrene with a catalytic activity of 4.85×10 6 g PS/(mole Ti·mole S·hour). Reflux in methyl ethyl ketone for 2 hours to remove atactic polystyrene, the measured weight content of syndiotactic polystyrene is 99.6%, and the melting point of the obtained polymer is 275°C. [Example 12]
2毫升苯乙烯,3.4毫升甲苯,6.6毫升浓度1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.05毫升的0.05摩尔/升化合物B的甲苯溶液依次注射入安培瓶中,放置于预先恒温至50℃的油浴中聚合1小时,得0.1736克聚苯乙烯,催化活性为3.99×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为99.1%,聚合物的熔点为273℃。【实施例13】2 milliliters of styrene, 3.4 milliliters of toluene, 6.6 milliliters of 1.53 mol/liter methylalumoxane toluene solution, and 0.05 milliliter of 0.05 mol/liter compound B toluene solution were sequentially injected into the ampoule, and placed in a pre-heated to Polymerize in an oil bath at 50°C for 1 hour to obtain 0.1736 gram of polystyrene, the catalytic activity is 3.99×10 6 gram PS/(mole Ti mole S hour), and the recorded syndiotactic polystyrene weight content is 99.1%. The melting point of the polymer was 273°C. [Example 13]
11毫升苯乙烯,0.5毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.05毫升的0.05摩尔/升化合物A的甲苯溶液依次注射入安培瓶中,放置于预先恒温至50℃的油浴中聚合0.5小时,得1.6676克聚苯乙烯,催化活性为1.39×107克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为90.1%。【比较例3】11 ml of styrene, 0.5 ml of methylaluminoxane toluene solution with a concentration of 1.53 mol/L, and 0.05 ml of 0.05 mol/L Compound A in toluene were injected into the ampoule in sequence, and placed in a pre-heated to 50°C Polymerized in an oil bath for 0.5 hour to obtain 1.6676 g of polystyrene, the catalytic activity was 1.39×10 7 g PS/(mole Ti·mol S·hour), and the measured weight content of syndiotactic polystyrene was 90.1%. [Comparative Example 3]
11毫升苯乙烯,0.5毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.05毫升的0.05摩尔/升IndTiCl3的甲苯溶液依次注射入安培瓶中,放置于预先恒温至50℃的油浴中聚合0.5小时,得1.0996克聚苯乙烯,催化活性为9.19×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为86.4%。【实施例14】11 ml of styrene, 0.5 ml of methylalumoxane toluene solution with a concentration of 1.53 mol/L, and 0.05 ml of 0.05 mol/L IndTiCl 3 in toluene solution were injected into the ampoule in sequence, and placed in a pre-heated to 50 ° C Polymerized in an oil bath for 0.5 hour to obtain 1.0996 g of polystyrene, with a catalytic activity of 9.19×10 6 g PS/(mol Ti·mol S·hour), and a measured syndiotactic polystyrene weight content of 86.4%. [Example 14]
11毫升苯乙烯,1毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升化合物A的甲苯溶液依次注射入安培瓶中,放置于预先恒温至50℃的油浴中聚合0.5小时,得1.5117克聚苯乙烯,催化活性为6.32×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为88.4%。【实施例15】11 ml of styrene, 1 ml of methylalumoxane toluene solution with a concentration of 1.53 mol/L, and 0.1 ml of 0.05 mol/L Compound A in toluene were injected into the ampoule in sequence, and placed in a pre-heated to 50°C After polymerization in an oil bath for 0.5 hour, 1.5117 g of polystyrene was obtained, the catalytic activity was 6.32×10 6 g PS/(mole Ti·mol S·hour), and the measured weight content of syndiotactic polystyrene was 88.4%. [Example 15]
11毫升苯乙烯,1毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升化合物A的甲苯溶液依次注射入安培瓶中,放置于预先恒温至70℃的油浴中聚合1小时,得1.7452克聚苯乙烯,催化活性为3.65×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为91.2%。【比较例4】11 ml of styrene, 1 ml of methylalumoxane toluene solution with a concentration of 1.53 mol/L, and 0.1 ml of 0.05 mol/L compound A in toluene were injected into the ampoule in sequence, and placed in a pre-heated to 70°C Polymerized in an oil bath for 1 hour to obtain 1.7452 g of polystyrene, with a catalytic activity of 3.65×10 6 g PS/(mol Ti·mol S·hour), and a measured syndiotactic polystyrene weight content of 91.2%. [Comparative Example 4]
11毫升苯乙烯,1毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升IndTiCl3的甲苯溶液依次注射入安培瓶中,放置于预先恒温至70℃的油浴中聚合1小时,得1.4586克聚苯乙烯,催化活性为3.05×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为86.6%。【实施例16】11 ml of styrene, 1 ml of methylalumoxane toluene solution with a concentration of 1.53 mol/L, and 0.1 ml of 0.05 mol/L IndTiCl 3 in toluene solution were injected into the ampoule in sequence, and placed in a pre-heated to 70°C Polymerized in an oil bath for 1 hour to obtain 1.4586 g of polystyrene, with a catalytic activity of 3.05×10 6 g PS/(mol Ti·mol S·hour), and a measured syndiotactic polystyrene weight content of 86.6%. [Example 16]
11毫升苯乙烯,1毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升化合物A的甲苯溶液依次注射入安培瓶中,放置于预先恒温至90℃的油浴中聚合2小时,得2.2418克聚苯乙烯,催化活性为2.34×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为90.7%。【实施例17】11 ml of styrene, 1 ml of methylaluminoxane toluene solution with a concentration of 1.53 mol/L, and 0.1 ml of 0.05 mol/L Compound A in toluene were injected into the ampoule in sequence, and placed in a pre-heated to 90°C Polymerized in an oil bath for 2 hours to obtain 2.2418 g of polystyrene, with a catalytic activity of 2.34×10 6 g PS/(mol Ti·mol S·hour), and a measured syndiotactic polystyrene weight content of 90.7%. [Example 17]
11毫升苯乙烯,1毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升化合物A的甲苯溶液依次注射入安培瓶中,放置于预先恒温至25℃的油浴中聚合0.5小时,得0.9050克聚苯乙烯,催化活性为3.78×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为83.1%。【实施例18】11 ml of styrene, 1 ml of methylaluminoxane toluene solution with a concentration of 1.53 mol/L, and 0.1 ml of 0.05 mol/L compound A in toluene were injected into the ampoule in sequence, and placed in a pre-heated to 25°C After polymerization in an oil bath for 0.5 hour, 0.9050 g of polystyrene was obtained, the catalytic activity was 3.78×10 6 g PS/(mole Ti·mol S·hour), and the measured weight content of syndiotactic polystyrene was 83.1%. [Example 18]
11毫升苯乙烯,1毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升化合物B的甲苯溶液依次注射入安培瓶中,放置于预先恒温至50℃的油浴中聚合0.5小时,得0.9711克聚苯乙烯,催化活性为4.06×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为85.2%。【实施例19】11 ml of styrene, 1 ml of methylaluminoxane toluene solution with a concentration of 1.53 mol/L, and 0.1 ml of 0.05 mol/L compound B in toluene were injected into the ampoule in sequence, and placed in a pre-heated to 50°C After polymerization in an oil bath for 0.5 hour, 0.9711 g of polystyrene was obtained, the catalytic activity was 4.06×10 6 g PS/(mole Ti·mol S·hour), and the measured weight content of syndiotactic polystyrene was 85.2%. [Example 19]
11毫升苯乙烯,1毫升浓度为1.53摩尔/升的甲基铝氧烷甲苯溶液,以及0.1毫升的0.05摩尔/升化合物C的甲苯溶液依次注射入安培瓶中,放置于预先恒温至50℃的油浴中聚合0.5小时,得0.7794克聚苯乙烯,催化活性为3.26×106克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯重量含量为79.2%。11 ml of styrene, 1 ml of methylaluminoxane toluene solution with a concentration of 1.53 mol/L, and 0.1 ml of 0.05 mol/L compound C in toluene were injected sequentially into the ampoule and placed in a pre-heated to 50°C After polymerization in an oil bath for 0.5 hour, 0.7794 g of polystyrene was obtained, the catalytic activity was 3.26×10 6 g PS/(mole Ti·mol S·hour), and the measured weight content of syndiotactic polystyrene was 79.2%.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00127437 CN1116320C (en) | 2000-11-15 | 2000-11-15 | Catalyst for syndiotatic phenylethylene polymerization |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00127437 CN1116320C (en) | 2000-11-15 | 2000-11-15 | Catalyst for syndiotatic phenylethylene polymerization |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1352205A CN1352205A (en) | 2002-06-05 |
| CN1116320C true CN1116320C (en) | 2003-07-30 |
Family
ID=4592452
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00127437 Expired - Fee Related CN1116320C (en) | 2000-11-15 | 2000-11-15 | Catalyst for syndiotatic phenylethylene polymerization |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1116320C (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103421131B (en) * | 2012-05-16 | 2016-01-13 | 中国石油化工股份有限公司 | High activity double center indene metallocene titanium composition |
| CN103421130B (en) * | 2012-05-16 | 2016-01-13 | 中国石油化工股份有限公司 | High activity double center metallocene titanium composition |
-
2000
- 2000-11-15 CN CN 00127437 patent/CN1116320C/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN1352205A (en) | 2002-06-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1059448C (en) | Process and catalyst for producing syndiotactic polyolefins | |
| AU622337B2 (en) | Process for the preparation of cycloolefin polymers | |
| CN1273503C (en) | Polypropylene preparation | |
| CN87106984A (en) | Hafnium Metallocene Catalysts for Olefin Polymerization | |
| CN1116320C (en) | Catalyst for syndiotatic phenylethylene polymerization | |
| JP2004536124A (en) | Novel multinuclear semimetallocene catalyst and method for producing styrene-based polymer using the same | |
| CN1132856C (en) | Catalyst for polymerizing semi-metallocene with olefin and its preparing process and application | |
| CN1130394C (en) | Catalyst for preparation of syndiotactic polystyrene | |
| WO1996015160A1 (en) | Polymerization catalyst and process for producing styrene polymer therewith | |
| CN1352201A (en) | Indenyl metal titanium compound and its preparing method and use | |
| CN1174017C (en) | Process for preparing polynorbornene by using β-diketone titanium non-metallocene catalyst | |
| CN1208354C (en) | Metallocene titanium compound and use thereof | |
| KR20110077883A (en) | Catalyst for producing poly (1-butene) and method for producing poly (1-butene) using same | |
| CN1176928C (en) | Titanocene compounds and their uses | |
| CN114874258B (en) | Binuclear cyclopentadienyl group IV metal catalyst for polymerization of styrene and its derivative, its preparation method, composition and application | |
| CN1155605C (en) | Substituted indenyl metal titanium compound and its preparation method and use | |
| CN1371923A (en) | Process for preparing high molecular double-activity centre olefine polymerizing catalyst containing silicon bridged group metallocene | |
| CN1098271C (en) | Cyclopentadiene titanium compound | |
| CN1093140C (en) | Catalyst for preparing syndiotactic poly styrene | |
| CN1259327C (en) | Cyclopentadienyl metal titanium compound and its use | |
| CN121159606A (en) | A metallocene compound, its preparation method and application | |
| CN1233667C (en) | Metallocene titanium compound and use thereof | |
| CN1252101C (en) | Catalyst for preparing syndiotactic polystyrene | |
| CN1207315C (en) | Catalyst for preparing syndiotacti polystyrene | |
| KR100503359B1 (en) | Metallocene catalyst for styrene polymerization and polymerization process using the same |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20030730 Termination date: 20171115 |