CN1155605C - Substituted indenyl metal titanium compound and its preparation method and use - Google Patents
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- 125000003454 indenyl group Chemical group C1(C=CC2=CC=CC=C12)* 0.000 title claims abstract description 25
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 25
- 239000002184 metal Substances 0.000 title claims abstract description 25
- 150000003609 titanium compounds Chemical class 0.000 title claims abstract description 25
- YBYIRNPNPLQARY-UHFFFAOYSA-N 1H-indene Natural products C1=CC=C2CC=CC2=C1 YBYIRNPNPLQARY-UHFFFAOYSA-N 0.000 title claims abstract description 24
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims abstract description 57
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 20
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 13
- MDTDQDVMQBTXST-UHFFFAOYSA-K 2h-inden-2-ide;titanium(4+);trichloride Chemical class Cl[Ti+](Cl)Cl.C1=CC=C2[CH-]C=CC2=C1 MDTDQDVMQBTXST-UHFFFAOYSA-K 0.000 claims abstract description 7
- 239000007818 Grignard reagent Substances 0.000 claims abstract description 7
- 150000004795 grignard reagents Chemical class 0.000 claims abstract description 7
- 125000000753 cycloalkyl group Chemical group 0.000 claims abstract description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 120
- -1 cycloalkyl alcohol Chemical compound 0.000 claims description 15
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical group ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 12
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 10
- MZRVEZGGRBJDDB-UHFFFAOYSA-N N-Butyllithium Chemical group [Li]CCCC MZRVEZGGRBJDDB-UHFFFAOYSA-N 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 4
- 239000003960 organic solvent Substances 0.000 claims description 4
- 230000035484 reaction time Effects 0.000 claims description 4
- 229910052744 lithium Inorganic materials 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 2
- 239000003208 petroleum Substances 0.000 claims description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 2
- 239000004793 Polystyrene Substances 0.000 abstract description 43
- 230000003197 catalytic effect Effects 0.000 abstract description 28
- 229920002223 polystyrene Polymers 0.000 abstract description 25
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 15
- 150000001875 compounds Chemical class 0.000 abstract description 3
- 239000012141 concentrate Substances 0.000 abstract 1
- 238000009776 industrial production Methods 0.000 abstract 1
- 238000006467 substitution reaction Methods 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 29
- CPOFMOWDMVWCLF-UHFFFAOYSA-N methyl(oxo)alumane Chemical compound C[Al]=O CPOFMOWDMVWCLF-UHFFFAOYSA-N 0.000 description 23
- 229920010524 Syndiotactic polystyrene Polymers 0.000 description 21
- 239000010936 titanium Substances 0.000 description 21
- 239000003708 ampul Substances 0.000 description 18
- 229920000642 polymer Polymers 0.000 description 11
- 238000002844 melting Methods 0.000 description 9
- 230000008018 melting Effects 0.000 description 9
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000013078 crystal Substances 0.000 description 4
- 238000002330 electrospray ionisation mass spectrometry Methods 0.000 description 4
- 229910052719 titanium Inorganic materials 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- 125000005234 alkyl aluminium group Chemical group 0.000 description 3
- 229910052786 argon Inorganic materials 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical group 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- SIPUZPBQZHNSDW-UHFFFAOYSA-N bis(2-methylpropyl)aluminum Chemical compound CC(C)C[Al]CC(C)C SIPUZPBQZHNSDW-UHFFFAOYSA-N 0.000 description 1
- 150000001639 boron compounds Chemical class 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000002178 crystalline material Substances 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
- 230000007547 defect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- BBIDBFWZMCTRNP-UHFFFAOYSA-N ethylalumane Chemical compound CC[AlH2] BBIDBFWZMCTRNP-UHFFFAOYSA-N 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910003002 lithium salt Inorganic materials 0.000 description 1
- 159000000002 lithium salts Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 125000002524 organometallic group Chemical group 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
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- 125000001424 substituent group Chemical group 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
- VOITXYVAKOUIBA-UHFFFAOYSA-N triethylaluminium Chemical compound CC[Al](CC)CC VOITXYVAKOUIBA-UHFFFAOYSA-N 0.000 description 1
- MCULRUJILOGHCJ-UHFFFAOYSA-N triisobutylaluminium Chemical compound CC(C)C[Al](CC(C)C)CC(C)C MCULRUJILOGHCJ-UHFFFAOYSA-N 0.000 description 1
- JLTRXTDYQLMHGR-UHFFFAOYSA-N trimethylaluminium Chemical compound C[Al](C)C JLTRXTDYQLMHGR-UHFFFAOYSA-N 0.000 description 1
- 150000003755 zirconium compounds Chemical class 0.000 description 1
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- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Abstract
本发明涉及取代茚基金属钛化合物及其制备方法和用途。本发明通过采用如下取代结构茚基金属钛化合物:其中R1、R2和R3均为H、C1~C4烷基,R1、R2和R3不能同时为H,R4为C6~C10的环烷基。其制备方法,主要由其相应的醇的溶液与烷基锂或格氏试剂反应,然后加入相应取代茚基三氯化钛溶液反应,经过滤、浓缩、结晶得产物。所得的化合物对苯乙烯间规聚合具有高的催化活性,并可制得高间规度的聚苯乙烯,可用于工业生产中。
The invention relates to a substituted indenyl metal titanium compound and a preparation method and use thereof. The present invention adopts the following substitution structure indenyl metal titanium compound: wherein R 1 , R 2 and R 3 are all H, C 1 ~ C 4 alkyl, R 1 , R 2 and R 3 cannot be H at the same time, and R 4 is C 6 -C 10 cycloalkyl. Its preparation method is mainly to react the corresponding alcohol solution with alkyllithium or Grignard reagent, then add the corresponding substituted indenyl titanium trichloride solution to react, filter, concentrate and crystallize to obtain the product. The obtained compound has high catalytic activity for the syndiotactic polymerization of styrene, and can prepare polystyrene with high syndiotacticity, which can be used in industrial production.
Description
技术领域Technical field
本发明涉及取代茚基金属钛化合物及其制备方法和用途。The invention relates to a substituted indenyl metal titanium compound and a preparation method and use thereof.
背景技术 Background technique
苯乙烯通过自由基聚合得到的无规聚苯乙烯(atactic Polystyrene,aPS),具有质硬,透明,绝缘性,易加工的优点,已被广泛应用于包装,建筑,医药,电子,汽车,日用品等行业。但由于结构的无规性,其软化温度约为100℃,导致其易碎,耐热和耐化学腐蚀性差。Atactic Polystyrene (aPS), obtained by free radical polymerization of styrene, has the advantages of hardness, transparency, insulation, and easy processing, and has been widely used in packaging, construction, medicine, electronics, automobiles, and daily necessities and other industries. However, due to the randomness of the structure, its softening temperature is about 100°C, which makes it brittle and poor in heat resistance and chemical corrosion resistance.
1955年Natta等用TiCl4/AlEt3催化体系得到了等规聚苯乙烯(isotactic Polystyrene,iPS),熔点为240℃,具有高晶体性,但由于其结晶速度太慢而没有实现工业化。In 1955, Natta et al. used TiCl 4 /AlEt 3 catalytic system to obtain isotactic polystyrene (isotactic Polystyrene, iPS), with a melting point of 240°C and high crystallinity, but its crystallization rate was too slow to achieve industrialization.
最近Ishihara等用钛化合物和甲基铝氧烷(MAO)组成的均相有机金属催化体系[(U.S.Pat.4680353(1987)]获得了间规聚苯乙烯(syndiotactic Polystyrene,sPS),它是一种结晶性材料,熔点约为270℃,具有快结晶速度,低比重,低介电常数,好的耐热、耐化学腐蚀等优点,因此其有更广泛的工业前景。Recently, Ishihara et al obtained syndiotactic polystyrene (syndiotactic Polystyrene, sPS) with a homogeneous organometallic catalyst system [(U.S.Pat.4680353 (1987)] composed of titanium compound and methylaluminoxane (MAO), which is a A crystalline material with a melting point of about 270°C. It has the advantages of fast crystallization speed, low specific gravity, low dielectric constant, good heat resistance, and chemical corrosion resistance, so it has broader industrial prospects.
文献中用于合成间规聚苯乙烯的催化剂包括卤化钛,四烷氧基钛,四烷基钛,钛酸酯,茂钛,以及相应的锆化合物。Catalysts used in the literature for the synthesis of syndiotactic polystyrene include titanium halides, tetraalkoxytitaniums, tetraalkyltitaniums, titanates, titanocenes, and the corresponding zirconium compounds.
其中尤以半夹心化合物(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)与MAO或B(C6F5)3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,相应的专利很多。Among them, the catalytic system composed of semi-sandwich compound (a trichlorotitanium, a trialkyltitanium, a trialkoxytitanium, and various compounds substituted with alocene) and MAO or B(C 6 F 5 ) 3 etc. The catalytic polymerization of styrene monomers has remarkable syndiotactic orientation and high catalytic activity, and there are many corresponding patents.
发明内容Contents of Invention
本发明所要解决的技术问题之一是克服以往技术中存在获得的茚基化合物用于苯乙烯间规聚合过程中,催化活性较低的缺陷,提供一种新的取代茚基金属钛化合物。该取代茚基金属钛化合物用于苯乙烯间规聚合过程中,具有高的催化活性,且保持聚苯乙烯较高的间规度。One of the technical problems to be solved by the present invention is to overcome the defect of low catalytic activity of indenyl compounds obtained in the prior art when used in the syndiotactic polymerization of styrene, and provide a new substituted indenyl metal titanium compound. The substituted indenyl metal titanium compound is used in the syndiotactic polymerization process of styrene, has high catalytic activity, and maintains a relatively high syndiotactic degree of polystyrene.
本发明所要解决的技术问题之二是为了解决获得取代茚基金属钛化合物所需的制备方法。The second technical problem to be solved by the present invention is to solve the preparation method required to obtain the substituted indenyl metal titanium compound.
本发明所要解决的技术问题之三是为了解决取代茚基金属钛化合物的用途。The third technical problem to be solved by the present invention is to solve the use of substituted indenyl metal titanium compounds.
为解决上述技术问题之一,本发明采用的技术方案如下:一种取代茚基金属钛化合物,其结构具有以下通式:In order to solve one of the above-mentioned technical problems, the technical scheme adopted in the present invention is as follows: a substituted indenyl metal titanium compound, whose structure has the following general formula:
其中R1、R2和R3均为H、C1~C4的烷基,但R1、R2和R3不能同时为H,R4为C6~C10的环烷基。Wherein R 1 , R 2 and R 3 are all H, C 1 -C 4 alkyl, but R 1 , R 2 and R 3 cannot be H at the same time, and R 4 is C 6 -C 10 cycloalkyl.
典型的例子为:1-CH3IndTiCl2(OMe),1-CH3IndTiCl2(OEt),1-CH3IndTiCl2(OnPr),1-CH3IndTiCl2(OiPr),1-CH3IndTiCl2(OnBu),1-CH3IndTiCl2(OtBu), 1-CH3IndTiCl2(OPh), 1-CH3IndTiCl2(OCH2Ph),2-CH3IndTiCl2(OMe),2-CH3IndTiCl2(OEt)2-CH3IndTiCl2(OnPr),2-CH3IndTiCl2(OiPr),2-CH3IndTiCl2(OnBu),2-CH3IndTiCl2(OiBu)2-CH3IndTiCl2(OPh),2-CH3IndTiCl2(OCH2Ph),1-PhCH2IndTiCl2(OMe),1-PhCH2IndTiCl2(OEt),1-PhCH2IndTiCl2(OnPr),1-PhCH2IndTiCl2(OiPr),1-PhCH2IndTiCl2(OnBu),1-PhCH2IndTiCl2(OiBu),1-PhCH2IndTiCl2(OPh),1-PhCH2IndTiCl2(OCH2Ph),2-PhCH2IndTiCl2(OMe),2-PhCH2IndTiCl2(OEt),2-PhCH2IndTiCl2(OnPr),2-PhCH2IndTiCl2(OiPr),2-PhCH2IndTiCl2(OnBu),2-PhCH2IndTiCl2(OiBu),2-PhCH2IndTiCl2(OPh),2-PhCH2IndTiCl2(OCH2Ph),1,2-Me2IndTiCl2(OMe),1,2-Me2IndTiCl2(OEt),1,2-Me2IndTiCl2(OnPr),1,2-Me2IndTiCl2(OiPr),1,2-Me2IndTiCl2(OnBu),1,2-Me2IndTiCl2(O1Bu),1,2-Me2IndTiCl2(OPh),1,2-Me2IndTiCl2(OCH2Ph),1,3-Me2IndTiCl2(OMe),1,3-Me2IndTiCl2(OEt),1,3-Me2IndTiCl2(OnPr),1,3-Me2IndTiCl2(OiPr),1,3-Me2IndTiCl2(OnBu),1,3-Me2IndTiCl2(OiBu),1,3-Me2IndTiCl2(OPh),1,3-Me2IndTiCl2(OCH2Ph)Typical examples are: 1-CH 3 IndTiCl 2 (OMe), 1-CH 3 IndTiCl 2 (OEt), 1-CH 3 IndTiCl 2 ( On Pr), 1-CH 3 IndTiCl 2 (O i Pr), 1 -CH 3 IndTiCl 2 ( On Bu), 1-CH 3 IndTiCl 2 (O t Bu), 1-CH 3 IndTiCl 2 (OPh), 1-CH 3 IndTiCl 2 (OCH 2 Ph), 2-CH 3 IndTiCl 2 (OMe), 2-CH 3 IndTiCl 2 (OEt) 2-CH 3 IndTiCl 2 ( On Pr), 2-CH 3 IndTiCl 2 (O i Pr), 2-CH 3 IndTiCl 2 ( On Bu), 2-CH 3 IndTiCl 2 (O i Bu) 2-CH 3 IndTiCl 2 (OPh), 2-CH 3 IndTiCl 2 (OCH 2 Ph), 1-PhCH 2 IndTiCl 2 (OMe), 1-PhCH 2 IndTiCl 2 (OEt), 1-PhCH 2 IndTiCl 2 (O n Pr), 1-PhCH 2 IndTiCl 2 (O i Pr), 1-PhCH 2 IndTiCl 2 ( On Bu), 1-PhCH 2 IndTiCl 2 (O i Bu), 1-PhCH 2 IndTiCl 2 (OPh), 1-PhCH 2 IndTiCl 2 (OCH 2 Ph), 2-PhCH 2 IndTiCl 2 (OMe), 2-PhCH 2 IndTiCl 2 (OEt), 2-PhCH 2 IndTiCl 2 (O n Pr), 2-PhCH 2 IndTiCl 2 (O i Pr), 2-PhCH 2 IndTiCl 2 ( On Bu), 2-PhCH 2 IndTiCl 2 (O i Bu), 2-PhCH 2 IndTiCl 2 (OPh), 2-PhCH 2 IndTiCl 2 (OCH 2 Ph), 1,2-Me 2 IndTiCl 2 (OMe), 1,2-Me 2 IndTiCl 2 (OEt), 1,2- Me 2 IndTiCl 2 ( On Pr), 1,2-Me 2 IndTiCl 2 (O i Pr), 1,2-Me 2 IndTiCl 2 ( On Bu), 1,2-Me 2 IndTiCl 2 (O 1 Bu ), 1,2-Me 2 IndTiCl 2 (OPh), 1,2-Me 2 IndTiCl 2 (OCH 2 Ph), 1,3-Me 2 IndTiCl 2 (OMe), 1,3-Me 2 IndTiCl 2 (OEt), 1,3-Me 2 IndTiCl 2 ( On Pr), 1,3-Me 2 IndTiCl 2 (O i Pr), 1,3-Me 2 IndTiCl 2 (On Bu ), 1,3-Me 2 IndTiCl 2 (O i Bu), 1,3-Me 2 IndTiCl 2 (OPh), 1,3-Me 2 IndTiCl 2 (OCH 2 Ph)
为解决上述技术问题之二,本发明采用的技术方案如下:一种取代茚基金属钛化合物的制备方法,首先将经脱水处理的C6~C10的环烷基醇的溶液与烷基锂或Na,K,格氏试剂反应,然后加入含1、2、3位上分别被R1、R2和R3取代的茚基三氯化钛溶液,其中取代茚基三氯化钛与C6~C10的环烷基醇的摩尔比为1∶0.8~1.5,C6~C10的环烷基醇与烷基锂或Na,K,格氏试剂的摩尔比为1∶0.8~1.5,在惰性气氛保护下,在滴加温度为-78~0℃,滴毕后反应温度为10~100℃,反应时间为1~30小时条件下反应,然后经过滤、浓缩,用有机溶剂重结晶,得产物取代茚基金属钛化合物。In order to solve the above-mentioned technical problem 2, the technical scheme adopted by the present invention is as follows: a preparation method of a substituted indenyl metal titanium compound, firstly, a solution of a dehydrated C 6 -C 10 cycloalkyl alcohol is mixed with an alkyllithium Or Na, K, Grignard reagent reaction, and then add indenyl titanium trichloride solution containing 1, 2, and 3 positions respectively substituted by R 1 , R 2 and R 3 , wherein substituted indenyl titanium trichloride and C The molar ratio of 6 -C 10 cycloalkyl alcohol is 1:0.8-1.5, the molar ratio of C 6 -C 10 cycloalkyl alcohol and alkyl lithium or Na, K, and Grignard reagent is 1:0.8-1.5 , under the protection of an inert atmosphere, the dropwise temperature is -78 ~ 0 ° C, the reaction temperature after the drop is 10 ~ 100 ° C, and the reaction time is 1 ~ 30 hours. Then, it is filtered, concentrated, and reconstituted with an organic solvent. Crystallization, the product substituted indenyl metal titanium compound.
上述制备方法中取代茚基三氯化钛与C6~C10的环烷基醇的摩尔比优选范围为1∶1~1.2,C6~C10的环烷基醇与烷基锂或Na,K,格氏试剂的摩尔比为1∶1~1.2,烷基锂优选方案为正丁基锂,滴加温度优选范围为-60~-30℃,反应温度优选范围为25~35℃,反应时间优选范围为8~16小时,有机溶剂选自二氯甲烷、四氢呋喃、甲苯、正己烷或石油醚及其混合物,惰性气氛所用的气体可用氩气或氮气。In the above preparation method, the molar ratio of the substituted indenyl titanium trichloride to the C 6 -C 10 cycloalkyl alcohol preferably ranges from 1:1 to 1.2, and the C 6 -C 10 cycloalkyl alcohol to the alkyllithium or Na , K, the molar ratio of the Grignard reagent is 1:1~1.2, the preferred scheme of alkyllithium is n-butyllithium, the preferred range of dropping temperature is -60~-30°C, and the preferred range of reaction temperature is 25~35°C, The reaction time preferably ranges from 8 to 16 hours. The organic solvent is selected from dichloromethane, tetrahydrofuran, toluene, n-hexane or petroleum ether and mixtures thereof. The gas used in the inert atmosphere can be argon or nitrogen.
为解决上述技术问题之三,本发明采用的技术方案如下:将取代茚基金属钛化合物,用于催化苯乙烯间规聚合。In order to solve the third technical problem above, the technical scheme adopted in the present invention is as follows: the substituted indenyl metal titanium compound is used to catalyze the syndiotactic polymerization of styrene.
本发明的取代茚基金属钛化合物用于苯乙烯间规聚合反应的催化体系是由上述的取代茚基金属钛化合物与助催化剂两部分组成。The catalytic system of the substituted indenyl metal titanium compound used in the syndiotactic polymerization of styrene of the present invention is composed of the above-mentioned substituted indenyl metal titanium compound and a cocatalyst.
苯乙烯类单体与催化剂中钛的摩尔比为1000∶1到500000∶1,最好为5000∶1到300000∶1。The molar ratio of styrene monomer to titanium in the catalyst is 1000:1 to 500000:1, preferably 5000:1 to 300000:1.
助催化剂为MAO(甲基铝氧烷)或硼化合物BX1X2X3或它的盐,其中X1,X2,X3可以相同,也可以不同,X1,X2和X3均为C1~C20氟代碳氢化合物取代基。The cocatalyst is MAO (methylaluminoxane) or boron compound BX 1 X 2 X 3 or its salt, wherein X 1 , X 2 , X 3 can be the same or different, and X 1 , X 2 and X 3 are all It is a C 1 -C 20 fluorohydrocarbon substituent.
在催化剂和助催化剂组成的催化体系中也可以包括烷基铝或烷基氢铝化合物,烷基为C1~C6,如三甲基铝,三乙基铝,三异丁基铝,二乙基氢化铝,二异丁基氢化铝等。烷基铝或烷基氢铝与钛的摩尔比为0~2000∶1,最好为0~500∶1。The catalytic system composed of catalyst and cocatalyst may also include alkylaluminum or alkylaluminum hydrogen compound, the alkyl group is C 1 -C 6 , such as trimethylaluminum, triethylaluminum, triisobutylaluminum, di Ethyl aluminum hydride, diisobutyl aluminum hydride, etc. The molar ratio of alkylaluminum or alkylaluminum hydrogen to titanium is 0-2000:1, preferably 0-500:1.
聚合反应在溶剂状态或本体聚合,在前一种情况下,溶剂为脂肪烃或芳香烃,最好为甲苯,溶剂与单体的体积比为0~10∶1。The polymerization reaction is in solvent state or bulk polymerization, in the former case, the solvent is aliphatic hydrocarbon or aromatic hydrocarbon, preferably toluene, and the volume ratio of solvent to monomer is 0~10:1.
聚合温度为20~100℃。The polymerization temperature is 20-100°C.
聚合时间为0.5~10小时,最好为0.5~2小时。The polymerization time is 0.5 to 10 hours, preferably 0.5 to 2 hours.
通过试验证明,本发明的取代茚基金属钛化合物组成的催化体系具有很高的催化活性,尤其是用于苯乙烯类单体的聚合,最高可以得到95.3%高间规度聚苯乙烯,催化活性最高为1.32×107克聚苯乙烯/(摩尔钛·摩尔苯乙烯·小时),减少了在聚合物中残留金属含量,降低了生产成本,提高了生产效率,取得了较好的效果。Tests have proved that the catalytic system composed of the substituted indenyl metal titanium compound of the present invention has very high catalytic activity, especially for the polymerization of styrene monomers, and can obtain up to 95.3% high-syndiotactic polystyrene. The highest activity is 1.32×10 7 g polystyrene/(mole titanium·mole styrene·hour), which reduces the residual metal content in the polymer, reduces production cost, improves production efficiency, and achieves better results.
下面通过实施例对本发明作进一步的阐述:The present invention will be further elaborated below by embodiment:
具体实施方式 Detailed ways
【实施例1】【Example 1】
在氩气保护下,在2.5毫升(4.73毫摩尔)正丁基锂的正己烷溶液中缓慢滴加0.218克(4.73毫摩尔)乙醇的正己烷溶液(5.7毫升),反应生成的锂盐溶液冷至-40℃,缓慢滴加1.340克(4.73毫摩尔)1-CH3IndTiCl3的二氯甲烷溶液(20毫升),1小时滴完,自然升至30℃,搅拌反应10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0.615克1-CH3IndTiCl2(OEt)红色晶体,产率为44.4%,m.p.=97~100℃。分析测试结果如下Under argon protection, in 2.5 milliliters (4.73 millimoles) n-hexane solution of n-butyllithium, slowly add dropwise 0.218 grams (4.73 millimoles) of ethanol's n-hexane solution (5.7 milliliters), the lithium salt solution that reaction generates is cold To -40°C, slowly add 1.340 g (4.73 mmol) of 1-CH 3 IndTiCl 3 dichloromethane solution (20 ml) dropwise, drop it in 1 hour, naturally rise to 30°C, stir for 10 hours, filter, clear The liquid was pumped to dryness, and the obtained solid was recrystallized with dichloromethane and n-hexane to obtain 0.615 g of 1-CH 3 IndTiCl 2 (OEt) red crystals, the yield was 44.4%, and mp=97-100°C. The analysis test results are as follows
分子式:C12H14Cl2OTi;Molecular formula: C 12 H 14 Cl 2 OTi;
M.S.(EI):292(11,M+)。MS (EI): 292 (11, M + ).
1H NMR(CDCl3,δ):7.75~7.72(m,2H,IndH2),7.47~7.40(m,2H,IndH2),6.70(d,1H,J=2.9,IndH),6.58(d,1H,J=2.9,IndH),3.35(q,2H,J=6.9,OCH2CH3),2.64(s,3H,IndH3),1.34(t,3H,J=6.9,OCH2CH3)。 1 H NMR (CDCl 3 , δ): 7.75-7.72 (m, 2H, IndH 2 ), 7.47-7.40 (m, 2H, IndH 2 ), 6.70 (d, 1H, J=2.9, IndH), 6.58 (d , 1H, J=2.9, IndH), 3.35 (q, 2H, J=6.9, OCH 2 CH 3 ), 2.64 (s, 3H, IndH 3 ), 1.34 (t, 3H, J=6.9, OCH 2 CH 3 ).
E.A.:实测,C:49.18%H:4.82%E.A.: Measured, C: 49.18% H: 4.82%
计算,C:49.11%H:4.81%Computing, C: 49.11% H: 4.81%
【实施例2】[Example 2]
所有操作均同于实施例1,除了用甲醇代替乙醇,最后得到1-CH3IndTiCl2(OMe)红色晶体,产率为73.6%,m.p.=110~115℃。分析测试结果如下All operations were the same as in Example 1, except that methanol was used instead of ethanol, and finally 1-CH 3 IndTiCl 2 (OMe) red crystals were obtained with a yield of 73.6% and mp=110-115°C. The analysis test results are as follows
分子式:C11H12Cl2OTi;Molecular formula: C 11 H 12 Cl 2 OTi;
M.S.(EI):278(6,M+)。MS (EI): 278 (6, M + ).
1H NMR(CDCl3,δ):7.76~7.68(m,2H,IndH2),7.47~7.44(m,2H,IndH2),6.72(d,1H,J=3.3,IndH),6.61(d,1H,J=3.3,IndH),4.36(s,3H,OCH3),2.64(s,3H,IndH3) 1 H NMR (CDCl 3 , δ): 7.76-7.68 (m, 2H, IndH 2 ), 7.47-7.44 (m, 2H, IndH 2 ), 6.72 (d, 1H, J=3.3, IndH), 6.61 (d , 1H, J=3.3, IndH), 4.36 (s, 3H, OCH 3 ), 2.64 (s, 3H, IndH 3 )
E.A.:实测,C:52.37% H:5.65%E.A.: Measured, C: 52.37% H: 5.65%
计算,C:52.14% H:5.70%Computing, C: 52.14% H: 5.70%
【实施例3】[Example 3]
所有操作均同于实施例1,除了用异丙醇代替乙醇,最后得到1-CH3IndTiCl2(OiPr)红色晶体,产率为32.3%,m.p.=59~61℃。分析测试结果如下All operations were the same as in Example 1, except that isopropanol was used instead of ethanol, and finally 1-CH 3 IndTiCl 2 (O i Pr) red crystals were obtained with a yield of 32.3% and mp=59-61°C. The analysis test results are as follows
分子式:C13H16Cl2OTi;Molecular formula: C 13 H 16 Cl 2 OTi;
M.S.(EI):306(6,M+)。MS (EI): 306 (6, M + ).
1H NMR(CDCl3,δ):7.75~7.73(m,2H,IndH2),7.45~7.41(m,2H,IndH2),6.68(d,1H,J=3.3,IndH),6.57(d,1H,J=3.3,IndH),4.97(m,1H,J=6.1,OCH(CH3)2),2.63(s,3H,IndH3),1.31(d,6H,J=6.1,OCH(CH3)2) 1 H NMR (CDCl 3 , δ): 7.75-7.73 (m, 2H, IndH 2 ), 7.45-7.41 (m, 2H, IndH 2 ), 6.68 (d, 1H, J=3.3, IndH), 6.57 (d , 1H, J=3.3, IndH), 4.97(m, 1H, J=6.1, OCH(CH 3 ) 2 ), 2.63(s, 3H, IndH 3 ), 1.31(d, 6H, J=6.1, OCH( CH 3 ) 2 )
E.A.:实测,C:50.87%H:5.25%E.A.: Measured, C: 50.87% H: 5.25%
计算,C:50.71%H:5.30%Computing, C: 50.71% H: 5.30%
【实施例4】【Example 4】
所有操作均同于实施例1,除了用环己基代替乙醇,最后得到 红色晶体,产率为37.3%,m.p.=84~86℃。分析测试结果如下All operations are the same as in Example 1, except that ethanol is replaced with cyclohexyl, and finally Red crystals, yield 37.3%, mp=84-86°C. The analysis test results are as follows
分子式:C16H20Cl2OTi;Molecular formula: C 16 H 20 Cl 2 OTi;
M.S.(EI):346(1,M+)。MS (EI): 346 (1, M + ).
1H NMR(CDCl3,δ):7.76~7.73(m,2H,IndH2),7.48~7.42(m,2H,IndH2),6.68(d,1H,J=3.3,IndH),6.58(d,1H,J=3.3,IndH),4.75(m,1H, ),2.63(s,3H,IndH3),1.90~1.28(m,10H,) 1 H NMR (CDCl 3 , δ): 7.76-7.73 (m, 2H, IndH 2 ), 7.48-7.42 (m, 2H, IndH 2 ), 6.68 (d, 1H, J=3.3, IndH), 6.58 (d , 1H, J=3.3, IndH), 4.75(m, 1H, ), 2.63(s, 3H, IndH 3 ), 1.90~1.28(m, 10H, )
E.A.:实测,C:55.36%H:5.81%E.A.: Measured, C: 55.36% H: 5.81%
计算,C:55.26%H:5.92%Computing, C: 55.26% H: 5.92%
【实施例5】【Example 5】
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,4毫升甲苯,6毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.05毫升浓度为0.05摩尔/升的1-CH3IndTiCl2(OiPr)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100℃下真空干燥至恒重,得0.3169克聚苯乙烯,产率为17.5%,催化活性为7.29×106克PS/(摩尔Ti摩尔S·小时),其中PS为聚苯乙烯,S为苯乙烯。Polymerizations were carried out in a baked argon-filled ampule three times. 2 mL of styrene, 4 mL of toluene, 6 mL of 1.72 mol/L MAO in toluene, and 0.05 mL of 0.05 mol/L 1-CH 3 IndTiCl 2 (O i Pr ) in toluene were sequentially injected into the ampoule placed in an oil bath whose temperature was previously constant to 50°C for polymerization for 1 hour. Terminate the polymerization reaction with ethanol containing 10% HCl. After filtering and washing, the obtained polymer is vacuum-dried to constant weight at 100° C. to obtain 0.3169 g of polystyrene, with a yield of 17.5% and a catalytic activity of 7.29×10 6 g PS/(mole Ti mole S·hour), wherein PS is polystyrene, and S is styrene.
在丁酮中抽提2小时,除去无规聚苯乙烯,测得间规聚苯乙烯含量为95.2%。It was extracted in butanone for 2 hours to remove atactic polystyrene, and the measured syndiotactic polystyrene content was 95.2%.
所得聚合物熔点为271℃。The resulting polymer had a melting point of 271°C.
【实施例6】[Example 6]
2毫升苯乙烯,4毫升甲苯,6毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.05毫升浓度为0.05摩尔/升的 甲苯溶液依次注射入安培瓶中,在50℃的油浴中聚合1小时。用含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100℃下真空干燥至恒重,得0.3359克聚苯乙烯,产率为18.5%,催化活性为7.72×106克PS/(摩尔Ti·摩尔S·小时)。2 mL of styrene, 4 mL of toluene, 6 mL of MAO in toluene at a concentration of 1.72 mol/L, and 0.05 mL of MAO at a concentration of 0.05 mol/L The toluene solution was sequentially injected into the ampoule, and polymerized in an oil bath at 50°C for 1 hour. Terminate the polymerization reaction with ethanol containing 10% HCl, after filtering and washing, the obtained polymer is vacuum-dried to constant weight at 100°C to obtain 0.3359 g of polystyrene, with a yield of 18.5% and a catalytic activity of 7.72×10 6 g PS/(mole Ti·mole S·hour).
测得间规聚苯乙烯含量为94.8%。The measured syndiotactic polystyrene content was 94.8%.
所得聚合物熔点为271℃。The resulting polymer had a melting point of 271°C.
【比较例1】[Comparative Example 1]
2毫升苯乙烯,4毫升甲苯,6毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.05毫升浓度为0.05摩尔/升的1-CH3IndTiCl3甲苯溶液依次注射入安培瓶中,在50℃的油浴中聚合1小时。用含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100℃下真空干燥至恒重,得0.1277克聚苯乙烯,产率为7.1%,催化活性为2.94×106克PS/(摩尔Ti·摩尔S·小时)。2 mL styrene, 4 mL toluene, 6 mL MAO toluene solution with a concentration of 1.72 mol/L, and 0.05 mL 1-CH 3 IndTiCl 3 toluene solution with a concentration of 0.05 mol/L were sequentially injected into the ampoule, at 50 °C polymerized in an oil bath for 1 hour. Terminate the polymerization reaction with ethanol containing 10% HCl, after filtering and washing, the obtained polymer is vacuum-dried to constant weight at 100°C to obtain 0.1277 g of polystyrene, the yield is 7.1%, and the catalytic activity is 2.94×10 6 g PS/(mole Ti·mole S·hour).
测得间规聚苯乙烯含量为93.2%。The measured syndiotactic polystyrene content was 93.2%.
所得聚合物熔点为271℃。The resulting polymer had a melting point of 271°C.
【实施例7】[Example 7]
11毫升苯乙烯,0.9毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.1毫升浓度为0.05摩尔/升的1-CH3IndTiCl2(OEt)的甲苯溶液依次注射入安培瓶中,在50℃的油浴中聚合1小时,得1.3588克聚苯乙烯,产率为13.6%,催化活性为2.84×106克PS/(摩尔Ti·摩尔S·小时)。11 ml of styrene, 0.9 ml of a toluene solution of MAO with a concentration of 1.72 mol/L, and 0.1 ml of a toluene solution of 1-CH 3 IndTiCl 2 (OEt) with a concentration of 0.05 mol/L were sequentially injected into the ampoule, at 50°C Polymerized in an oil bath for 1 hour to obtain 1.3588 g of polystyrene, with a yield of 13.6%, and a catalytic activity of 2.84×10 6 g PS/(mol Ti·mol S·hour).
测得间规聚苯乙烯含量为95.3%。The measured syndiotactic polystyrene content was 95.3%.
【比较例2】【Comparative Example 2】
11毫升苯乙烯,0.9毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.1毫升浓度为0.05摩尔/升的1-CH3IndTiCl3的甲苯溶液依次注射入安培瓶中,在50℃的油浴中聚合1小时,得0.6523克聚苯乙烯,产率为6.6%,催化活性为1.36×106克PS/(摩尔Ti·摩尔S·小时)。11 mL of styrene, 0.9 mL of MAO in toluene with a concentration of 1.72 mol/L, and 0.1 mL of 1-CH 3 IndTiCl 3 in toluene with a concentration of 0.05 mol/L were sequentially injected into the ampoule and placed in an oil bath at 50 °C. Medium polymerization for 1 hour yielded 0.6523 g of polystyrene with a yield of 6.6% and a catalytic activity of 1.36×10 6 g PS/(mol Ti·mol S·hour).
测得间规聚苯乙烯含量为93.2%。The measured syndiotactic polystyrene content was 93.2%.
【实施例8】[Embodiment 8]
11毫升苯乙烯,0.9毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.1毫升浓度为0.05摩尔/升的1-CH3IndTiCl2(OEt)的甲苯溶液依次注射入安培瓶中,在70℃的油浴中聚合1小时,得1.6691克聚苯乙烯,产率为16.8%,催化活性为3.49×106克PS/(摩尔Ti·摩尔S·小时)。11 ml of styrene, 0.9 ml of a toluene solution of MAO with a concentration of 1.72 mol/L, and 0.1 ml of a toluene solution of 1-CH 3 IndTiCl 2 (OEt) with a concentration of 0.05 mol/L were sequentially injected into the ampoule, at 70°C Polymerized in an oil bath for 1 hour to obtain 1.6691 g of polystyrene, the yield was 16.8%, and the catalytic activity was 3.49×10 6 g PS/(mol Ti·mol S·hour).
测得间规聚苯乙烯含量为87.5%。The syndiotactic polystyrene content was measured to be 87.5%.
【比较例3】[Comparative Example 3]
11毫升苯乙烯,0.9毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.1毫升浓度为0.05摩尔/升的1-CH3IndTiCl3的甲苯溶液依次注射入安培瓶中,在70℃的油浴中聚合1小时,得0.9920克聚苯乙烯,产率为10.0%,催化活性为2.07×106克PS/(摩尔Ti·摩尔S·小时)。11 mL of styrene, 0.9 mL of MAO in toluene with a concentration of 1.72 mol/L, and 0.1 mL of 1- CH3IndTiCl3 with a concentration of 0.05 mol/L in toluene were sequentially injected into the ampoule and placed in an oil bath at 70 °C. Medium polymerization for 1 hour yielded 0.9920 g of polystyrene with a yield of 10.0% and a catalytic activity of 2.07×10 6 g PS/(mol Ti·mol S·hour).
测得间规聚苯乙烯含量为93.2%。The measured syndiotactic polystyrene content was 93.2%.
【实施例9】[Example 9]
11毫升苯乙烯,0.9毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.1毫升浓度为0.05摩尔/升的1-CH3IndTiCl2(OMe)的甲苯溶液依次注射入安培瓶中,在50℃的油浴中聚合1小时,得1.6515克聚苯乙烯,产率为16.6%,催化活性为3.45×106克PS/(摩尔Ti·摩尔S·小时)。11 ml of styrene, 0.9 ml of MAO toluene solution with a concentration of 1.72 mol/L, and 0.1 ml of a toluene solution of 1-CH 3 IndTiCl 2 (OMe) with a concentration of 0.05 mol/L were injected into the ampoule in sequence. Polymerized in an oil bath for 1 hour to obtain 1.6515 g of polystyrene, the yield was 16.6%, and the catalytic activity was 3.45×10 6 g PS/(mol Ti·mol S·hour).
测得间规聚苯乙烯含量为91.5%。The measured syndiotactic polystyrene content was 91.5%.
所得聚合物熔点为270℃。The resulting polymer had a melting point of 270°C.
【实施例10】【Example 10】
11毫升苯乙烯,0.9毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.1毫升浓度为0.05摩尔/升的1-CH3IndTiCl2(OMe)的甲苯溶液依次注射入安培瓶中,在70℃的油浴中聚合1小时,得1.6332克聚苯乙烯,产率为16.4%,催化活性为3.41×106克PS/(摩尔Ti·摩尔S·小时)。11 ml of styrene, 0.9 ml of MAO toluene solution with a concentration of 1.72 mol/L, and 0.1 ml of a toluene solution of 1-CH 3 IndTiCl 2 (OMe) with a concentration of 0.05 mol/L were injected into the ampoule in sequence. Polymerized in an oil bath for 1 hour to obtain 1.6332 g of polystyrene with a yield of 16.4% and a catalytic activity of 3.41×10 6 g PS/(mol Ti·mol S·hour).
测得间规聚苯乙烯含量为95.3%。The measured syndiotactic polystyrene content was 95.3%.
所得聚合物熔点为268℃。The resulting polymer had a melting point of 268°C.
【实施例11】[Example 11]
11毫升苯乙烯,0.9毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.1毫升浓度为0.05摩尔/升的1-CH3IndTiCl2(OMe)的甲苯溶液依次注射入安培瓶中,在90℃的油浴中聚合1小时,得1.8034克聚苯乙烯,产率为18.1%,催化活性为3.77×106克PS/(摩尔Ti·摩尔S·小时)。11 ml of styrene, 0.9 ml of MAO toluene solution with a concentration of 1.72 mol/L, and 0.1 ml of a toluene solution of 1-CH 3 IndTiCl 2 (OMe) with a concentration of 0.05 mol/L were injected into the ampoule in sequence, at 90°C Polymerized in an oil bath for 1 hour to obtain 1.8034 g of polystyrene with a yield of 18.1%, and a catalytic activity of 3.77×10 6 g PS/(mol Ti·mol S·hour).
测得间规聚苯乙烯含量为92.1%。The measured syndiotactic polystyrene content was 92.1%.
所得聚合物熔点为268℃。The resulting polymer had a melting point of 268°C.
【比较例4】[Comparative Example 4]
11毫升苯乙烯,0.9毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.1毫升浓度为0.05摩尔/升的1-CH3IndTiCl3的甲苯溶液依次注射入安培瓶中,在90℃的油浴中聚合1小时,得0.7006克聚苯乙烯,产率为7.0%,催化活性为1.46×106克PS/(摩尔Ti·摩尔S·小时)。11 mL of styrene, 0.9 mL of MAO in toluene with a concentration of 1.72 mol/L, and 0.1 mL of 1-CH 3 IndTiCl 3 in toluene with a concentration of 0.05 mol/L were sequentially injected into the ampoule and placed in an oil bath at 90 °C. Medium polymerization for 1 hour yielded 0.7006 g of polystyrene with a yield of 7.0% and a catalytic activity of 1.46×10 6 g PS/(mol Ti·mol S·hour).
测得间规聚苯乙烯含量为87.0%。The syndiotactic polystyrene content was measured to be 87.0%.
【实施例12】[Example 12]
11毫升苯乙烯,0.9毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.1毫升浓度为0.05摩尔/升的1-CH3IndTiCl2(OiPr)的甲苯溶液依次注射入安培瓶中,在50℃的油浴中聚合1小时,得0.6229克聚苯乙烯,产率为6.3%,催化活性为1.32×106克PS/(摩尔Ti摩尔S·小时)。11 ml of styrene, 0.9 ml of MAO toluene solution with a concentration of 1.72 mol/L, and 0.1 ml of 1-CH 3 IndTiCl 2 (O i Pr) toluene solution with a concentration of 0.05 mol/L were injected into the ampoule in sequence, Polymerized in an oil bath at 50° C. for 1 hour to obtain 0.6229 g of polystyrene with a yield of 6.3% and a catalytic activity of 1.32×10 6 g PS/(mole Ti mole S·hour).
测得间规聚苯乙烯含量为94.8%。The measured syndiotactic polystyrene content was 94.8%.
【实施例13】[Example 13]
11毫升苯乙烯,0.9毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.1毫升浓度为0.05摩尔/升的 的甲苯溶液依次注射入安培瓶中,在90℃的油浴中聚合1小时,得1.6069克聚苯乙烯,产率为16.1%,催化活性为3.36×106克PS/(摩尔Ti·摩尔S·小时)。11 ml of styrene, 0.9 ml of MAO in toluene at a concentration of 1.72 mol/L, and 0.1 ml of 0.05 mol/L The toluene solution was injected into the ampoule successively, and polymerized in an oil bath at 90° C. for 1 hour to obtain 1.6069 grams of polystyrene, with a yield of 16.1%, and a catalytic activity of 3.36×10 6 grams of PS/(mole Ti mole S ·Hour).
测得间规聚苯乙烯含量为91.4%。The measured syndiotactic polystyrene content was 91.4%.
【实施例14】[Example 14]
11毫升苯乙烯,0.9毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.1毫升浓度为0.05摩尔/升的1-CH3IndTiCl2(OtBu)的甲苯溶液依次注射入安培瓶中,在70℃的油浴中聚合1小时,得0.7215克聚苯乙烯,产率为15.2%,催化活性为1.51×106克PS/(摩尔Ti·摩尔S·小时)。11 milliliters of styrene, 0.9 milliliters of MAO toluene solution with a concentration of 1.72 mol/L, and 0.1 milliliters of 1-CH 3 IndTiCl 2 (O t Bu) toluene solution with a concentration of 0.05 mol/liter were injected into the ampoule in sequence, Polymerization in an oil bath at 70°C for 1 hour yielded 0.7215 g of polystyrene with a yield of 15.2% and a catalytic activity of 1.51×10 6 g PS/(mole Ti·mol S·hour).
测得间规聚苯乙烯含量为92.5%。The syndiotactic polystyrene content was measured to be 92.5%.
【实施例15】[Example 15]
11毫升苯乙烯,0.45毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.05毫升浓度为0.05摩尔/升的1-CH3IndTiCl2(OMe)的甲苯溶液依次注射入安培瓶中,在50℃的油浴中聚合1小时,得2.7110克聚苯乙烯,产率为27.2%,催化活性为1.13×107克PS/(摩尔Ti·摩尔S·小时)。11 ml of styrene, 0.45 ml of MAO toluene solution with a concentration of 1.72 mol/L, and 0.05 ml of a toluene solution of 1-CH 3 IndTiCl 2 (OMe) with a concentration of 0.05 mol/L were injected into the ampoule in sequence. Polymerized in an oil bath for 1 hour to obtain 2.7110 g of polystyrene with a yield of 27.2%, and a catalytic activity of 1.13×10 7 g PS/(mol Ti·mol S·hour).
测得间规聚苯乙烯含量为86.2%。The syndiotactic polystyrene content was measured to be 86.2%.
【实施例16】[Example 16]
11毫升苯乙烯,0.45毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.05毫升浓度为0.05摩尔/升的1-CH3IndTiCl2(OEt)的甲苯溶液依次注射入安培瓶中,在50℃的油浴中聚合1小时,得3.1681克聚苯乙烯,产率为31.8%,催化活性为1.32×107克PS/(摩尔Ti·摩尔S·小时)。11 ml of styrene, 0.45 ml of MAO toluene solution with a concentration of 1.72 mol/L, and 0.05 ml of 1-CH 3 IndTiCl 2 (OEt) toluene solution with a concentration of 0.05 mol/L were sequentially injected into the ampoule, and heated at 50°C Polymerized in an oil bath for 1 hour to obtain 3.1681 g of polystyrene with a yield of 31.8%, and a catalytic activity of 1.32×10 7 g PS/(mol Ti·mol S·hour).
测得间规聚苯乙烯含量为83.4%。The syndiotactic polystyrene content was measured to be 83.4%.
所得聚合物熔点为266℃。The resulting polymer had a melting point of 266°C.
【实施例17】[Example 17]
11毫升苯乙烯,0.45毫升浓度为1.72摩尔/升的MAO甲苯溶液,以及0.05毫升浓度为0.05摩尔/升的1-CH3IndTiCl2(OEt)的甲苯溶液依次注射入安培瓶中,在90℃的油浴中聚合1小时,得2.3977克聚苯乙烯,产率为24.1%,催化活性为1.00×107克PS/(摩尔Ti·摩尔S·小时),测得间规聚苯乙烯含量为89.4%。11 ml of styrene, 0.45 ml of MAO toluene solution with a concentration of 1.72 mol/L, and 0.05 ml of 1-CH 3 IndTiCl 2 (OEt) toluene solution with a concentration of 0.05 mol/L were injected into the ampoule in sequence, and heated at 90°C Polymerize 1 hour in the oil bath of 2.3977 gram polystyrenes, productive rate is 24.1%, catalytic activity is 1.00 * 10 gram PS/(mole Ti mole S hours), record syndiotactic polystyrene content as 89.4%.
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