CN1352204A - Process for preparing high molecular double active center olefine polymerization catalyst - Google Patents
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Abstract
本发明涉及一种高分子化双活性中心烯烃聚合催化剂的制备方法,该方法将含有烯烃基的铁系吡啶双亚胺化合物和含烯烃基的茂金属化合物与苯乙烯在引发剂的作用下将金属化合物通过C-Cα键连接到高分子链上形成高分子化双活性中心烯烃聚合催化剂,其表达式为[P(ComFe-co-S-co-Com M)],P表示共聚物,S为聚苯乙烯,co表示共聚,Com Fe表示铁系催化剂,Com M表示茂金属催化剂。双活性中心在聚合过程中同时发生催化作用,并产生协同效应,这类催化剂催化乙烯聚合具有较高的催化活性,所得聚合物具有独特的性质,适合于气相和淤浆聚合工艺。The present invention relates to a preparation method of a polymerized double-active center olefin polymerization catalyst. In the method, an iron-based pyridine bisimine compound containing an olefin group, a metallocene compound containing an olefin group, and styrene are synthesized under the action of an initiator. The metal compound is connected to the polymer chain through the C-Cα bond to form a polymerized double-active center olefin polymerization catalyst, and its expression is [P(ComFe-co-S-co-Com M)], P represents the copolymer, S It is polystyrene, co means copolymerization, Com Fe means iron-based catalyst, and Com M means metallocene catalyst. The dual active centers catalyze simultaneously during the polymerization process and produce synergistic effects. This kind of catalyst has high catalytic activity in catalyzing ethylene polymerization, and the obtained polymer has unique properties, which are suitable for gas phase and slurry polymerization processes.
Description
技术领域:本发明涉及一种烯烃聚合催化剂,具体地说涉及一种高分子化双活性中心烯烃聚合催化剂;Technical field: the present invention relates to an olefin polymerization catalyst, in particular to a polymerized double-active center olefin polymerization catalyst;
本发明还涉及一种上述催化剂的制备方法;The present invention also relates to a preparation method of the above-mentioned catalyst;
本发明还涉及上述催化剂在烯烃聚合中,尤其是在乙烯聚合中的应用。The invention also relates to the use of the aforementioned catalysts in the polymerization of olefins, especially in the polymerization of ethylene.
背景技术:聚烯烃是现代高分子材料工业的支柱产业,而催化剂则是聚烯烃产业的核心。近几年,烯烃聚合催化剂的发展已远远超出了传统活性中心为IVB族前过渡金属的范围,后过渡金属烯烃聚合催化剂已经成为研究的新热点(Lettl S.D,Johnson L.K,Brookhart M,Chem.Rev2000,100,1169;Britovsek G.J.P,Gibson V.C,Wass D.F,Angew.Chem.Iht.Ed,1999,38,428)。但是传统前过渡金属催化剂在现代工业生产中正发挥着巨大的作用,如何结合前过渡金属催化剂和后过渡金属催化剂的优点以制备结构和性能新颖的聚烯烃材料成为目前重要的研究方向。中国专利(98125651.1,1998;00121820.4,2000)分别公开了高分子化茂金属烯烃聚合催化剂的制备方法和高分子化后过渡金属“茂后”烯烃聚合催化剂的制备方法。这两种方法均适用于单一金属中心催化剂的高分子负载化。Background technology: polyolefin is the pillar industry of modern polymer material industry, and catalyst is the core of polyolefin industry. In recent years, the development of olefin polymerization catalysts has gone far beyond the scope of the traditional active center being the early transition metals of IVB group, and the late transition metal olefin polymerization catalysts have become a new hotspot of research (Lettl S.D, Johnson L.K, Brookhart M, Chem. Rev 2000, 100, 1169; Britovsek G.J.P, Gibson V.C, Wass D.F, Angew. Chem. Iht. Ed, 1999, 38, 428). However, traditional early transition metal catalysts are playing a huge role in modern industrial production. How to combine the advantages of early transition metal catalysts and late transition metal catalysts to prepare polyolefin materials with novel structures and properties has become an important research direction. Chinese patents (98125651.1, 1998; 00121820.4, 2000) respectively disclose a preparation method of a polymerized metallocene olefin polymerization catalyst and a preparation method of a polymerized post-transition metal "post-molecular" olefin polymerization catalyst. Both methods are suitable for the polymer support of single metal center catalysts.
发明内容:本发明的目的是提供一种高分子化双活性中心烯烃聚合物催化剂,该类催化剂结构中有两个活性中心,在催化烯烃聚合时这两个活性中心同时发生催化作用,相互协作。Summary of the invention: The purpose of the present invention is to provide a high molecular weight double active center olefin polymer catalyst, which has two active centers in the catalyst structure, and these two active centers simultaneously catalyze and cooperate with each other when catalyzing olefin polymerization .
本发明的又一目的是提供一种高分子化双活性中心烯烃聚合催化剂的制备方法,该制备方法工艺简单,过程易控制。Another object of the present invention is to provide a method for preparing a polymerized double active center olefin polymerization catalyst, which has a simple process and is easy to control.
本发明的另一目的是提供高分子化双活性中心烯烃聚合物催化剂在烯烃聚合,尤其是在乙烯聚合中的应用,所得聚烯烃产品具有独特的性能。Another object of the present invention is to provide a polymerized double-active-center olefin polymer catalyst for use in olefin polymerization, especially in ethylene polymerization, and the obtained polyolefin product has unique properties.
为实现上述目的,本发明提供的高分子化双活性中心烯烃聚合物催化剂由A和B两组分组成,A组分表达式为[P(Com Fe-co-S-co-Com M)],P表示共聚物,S为聚苯乙烯,co表示共聚,Com Fe表示铁系催化剂,ComM表示茂金属催化剂,具体结构式如下: In order to achieve the above object, the polymerized double active center olefin polymer catalyst provided by the present invention is composed of A and B two components, and the expression of A component is [P(Com Fe-co-S-co-Com M)] , P represents a copolymer, S represents polystyrene, co represents a copolymerization, Com Fe represents an iron-based catalyst, ComM represents a metallocene catalyst, and the specific structural formula is as follows:
ComFe:R1,R2,R3,R4分别为H,CH3,i-Pr,t-Bu其中之一;R5为H或allyl,X为Cl或Br; ComFe: R 1 , R 2 , R 3 , R 4 are one of H, CH 3 , i-Pr, t-Bu; R 5 is H or allyl, X is Cl or Br;
ComM:R6分别为H, 其中之一;R7分别为 其中之一;M为Ti,Zr或Hf;X为Cl或Br; ComM: R 6 are H, One of them; R 7 are One of them; M is Ti, Zr or Hf; X is Cl or Br;
高分子化双活性中心烯烃聚合催化剂模型:R1=R2=R3=R4=CH3;R5=R6=R7=allyl;M=Zr;X=Cl;High molecular weight double active center olefin polymerization catalyst model: R 1 =R 2 =R 3 =R 4 =CH 3 ; R 5 =R 6 =R 7 =allyl; M = Zr; X = Cl;
B组分为甲基铝氧烷(MAO)、改进甲基铝氧烷(MMAO)或五氟苯硼。Component B is methylalumoxane (MAO), modified methylalumoxane (MMAO) or pentafluorophenylboron.
本发明提供的高分子化双活性中心烯烃聚合催化剂至今还未见文献或专利报道。The polymerized double active center olefin polymerization catalyst provided by the present invention has not been reported in literature or patents so far.
本发明提供的一种高分子化双活性中心烯烃聚合催化剂的制备方法,将含有烯烃基的铁系吡啶双亚胺化合物和含烯烃基的茂金属化合物与苯乙烯在引发剂的作用下将金属化合物通过C-Cα键连接到高分子链上形成高分子化双活性中心烯烃聚合催化剂。The invention provides a method for preparing a polymerized double-active center olefin polymerization catalyst. The iron-based pyridine bis-imine compound containing an alkene group and the metallocene compound containing an alkene group and styrene are used as an initiator to convert the metal The compound is connected to the polymer chain through a C-Cα bond to form a polymerized double active center olefin polymerization catalyst.
催化剂的制备过程如下:The preparation process of the catalyst is as follows:
1、烯烃基芳胺的制备1. Preparation of alkenyl arylamine
其结构式为:R为H,Me,i-Pr,t-Bu其中之一Its structural formula is: R is one of H, Me, i-Pr, t-Bu
芳胺和烯烃基氯或烯烃基溴按摩尔比2∶1,加热反应得N-烯烃基芳胺,产率30.0-84.3%,N-烯烃基芳胺和过量ZnCl2在甲苯溶剂中加热回流发生重排反应生成4-烯烃基芳胺或2-烯烃基芳胺。产率25.2-70.9%。Aromatic amine and alkenyl chloride or alkenyl bromide in a molar ratio of 2:1, heating and reacting to obtain N-alkenyl arylamine, yield 30.0-84.3%, N-alkenyl arylamine and excess ZnCl in toluene solvent Heated to reflux A rearrangement reaction occurs to generate 4-alkenyl arylamine or 2-alkenyl arylamine. Yield 25.2-70.9%.
2、烯烃基环戊二烯的制备2. Preparation of alkenyl cyclopentadiene
其结构式为:R为 其中之一Its structural formula is: R is one of them
等摩尔的环戊二烯与氯代烯烃或溴代烯烃,在四丁基溴化铵为相转移剂下在NaOH水溶液中反应得到烯烃基取代的环戊二烯。产率40-70%。Equimolar cyclopentadiene reacts with chlorinated olefin or brominated olefin in NaOH aqueous solution under tetrabutylammonium bromide as a phase transfer agent to obtain alkene-substituted cyclopentadiene. Yield 40-70%.
3、烯烃基铁系催化剂Com Fe的制备3. Preparation of olefin-based iron-based catalyst Com Fe
首先2.6-二乙酰基吡啶与烯烃基胺进行两步酸催化的缩合反应制备出相应的吡啶二亚胺配体,如果该配体结构对称则两步缩合反应可以一步完成,此时胺与2.6-二乙酰基吡啶摩尔比为2∶1。由已制备得的吡啶二亚胺配体与FeX2反应即可制得含烯烃基的吡啶双亚胺化合物,产率90-95%。First, 2.6-diacetylpyridine and alkenyl amine undergo two-step acid-catalyzed condensation reaction to prepare the corresponding pyridinediimine ligand. If the ligand structure is symmetrical, the two-step condensation reaction can be completed in one step. At this time, the amine and 2.6 - The diacetylpyridine molar ratio is 2:1. The alkene group-containing pyridine diimine compound can be prepared by reacting the prepared pyridine diimine ligand with FeX2 , and the yield is 90-95%.
其制备反应过程如下:Its preparation reaction process is as follows:
以甲醇为溶剂,甲酸为催化剂,烯烃基芳胺与2.6-二乙酰基吡啶缩合反应生成三齿吡啶二亚胺配体。Com Fe的制备在无氧无水及高纯氩气保护条件下进行。以四氢呋喃为溶剂30-40mL,吡啶二亚胺配体与FeCl2·4H2O按摩尔比1.05∶1投料,室温搅拌2-3小时,得蓝色溶液,真空浓缩,加正己烷沉淀出蓝色粉末,过滤,真空干燥,产率90-95%。With methanol as solvent and formic acid as catalyst, alkenyl arylamine is condensed with 2.6-diacetylpyridine to generate tridentate pyridinediimine ligand. The preparation of Com Fe was carried out under the protection conditions of anaerobic, anhydrous and high-purity argon. Use 30-40 mL of tetrahydrofuran as solvent, feed pyridinediimine ligand and FeCl 2 4H 2 O at a molar ratio of 1.05:1, stir at room temperature for 2-3 hours to obtain a blue solution, concentrate in vacuo, add n-hexane to precipitate blue Color powder, filtered, vacuum-dried, yield 90-95%.
4、烯烃基茂金属催化剂Com M的制备4. Preparation of olefin-based metallocene catalyst Com M
首先由烯烃基环戊二烯与等摩尔的正丁基锂反应制备出相应的烯烃基环戊二烯的锂盐,如果要制备结构对称的烯烃基茂金属催化剂则由摩尔比为2∶1的烯烃基环戊二烯锂盐与MCl4反应;如果要制备结构不对称的烯烃基茂金属催化剂则分别加入等摩尔的两种烯烃基环戊二烯的锂盐与等摩尔的MCl4反应。产率60-75%。First, the lithium salt of the corresponding alkenyl cyclopentadiene is prepared by reacting alkenyl cyclopentadiene with equimolar n-butyllithium. If a structurally symmetrical alkenyl metallocene catalyst is to be prepared, the molar ratio is 2:1 The lithium salt of alkene-based cyclopentadiene reacts with MCl 4 ; if an asymmetric alkene-based metallocene catalyst is to be prepared, two equimolar lithium salts of alkene-based cyclopentadiene are added to react with equimolar MCl 4 . Yield 60-75%.
其制备反应过程如下:Its preparation reaction process is as follows:
将烯烃基环戊二烯加入到四氢呋喃溶液中,在冰盐浴的条件下,滴加等摩尔数的正丁基锂,在室温下搅拌2-3小时,然后缓慢地加入含等当量的MCl4的四氢呋喃溶液,溶液呈深红色,室温下搅拌反应6-8小时,蒸去溶剂,加入甲苯离心除去锂盐,将清液抽干,再用己烷洗涤数次即得产物,产率60-75%。Add alkenyl cyclopentadiene to tetrahydrofuran solution, under the condition of ice-salt bath, dropwise add equimolar n-butyllithium, stir at room temperature for 2-3 hours, then slowly add an equivalent amount of MCl 4 tetrahydrofuran solution, the solution was dark red, stirred and reacted at room temperature for 6-8 hours, evaporated the solvent, added toluene and centrifuged to remove lithium salt, drained the clear liquid, and washed several times with hexane to obtain the product, the yield was 60 -75%.
5、高分子化双活性中心烯烃聚合催化剂的制备5. Preparation of polymerized double-active center olefin polymerization catalyst
在无水无氧条件下,将含有烯烃基的铁系催化剂Com Fe,含烯烃基的茂金属催化剂Com M,苯乙烯,偶氮二异丁腈,依次加入到干燥的甲苯中混合均匀,然后在水浴中共聚,用正己烷作沉淀剂,得共聚物的固体粉末,再用正己烷洗涤三次,烘干即可。Under anhydrous and oxygen-free conditions, the iron-based catalyst Com Fe containing olefin groups, the metallocene catalyst Com M containing olefin groups, styrene, and azobisisobutyronitrile were sequentially added to dry toluene and mixed evenly, and then Copolymerize in a water bath and use n-hexane as a precipitating agent to obtain a solid powder of the copolymer, which is then washed three times with n-hexane and dried.
本发明提供的高分子化双活性中心烯烃聚合物催化剂在烯烃聚合,尤其在催化乙烯聚合反应中,是在无水无氧条件下进行,在反应体系中依次加入甲苯100-2000mL,甲基铝氧烷(MAO)或改进甲基铝氧烷(MMAO),高分子化双活性中心催化剂与MAO或MMAO摩尔比Al/(Fe+M)=350-3500,乙烯1-20atm,于-15-80℃反应1小时,用含重量比为1%盐酸的乙醇溶液终止反应,将所得产物过滤,用乙醇洗涤数次,于40℃真空干燥24小时。The polymerized double active center olefin polymer catalyst provided by the present invention is carried out under anhydrous and oxygen-free conditions in olefin polymerization, especially in catalyzing ethylene polymerization reaction, and 100-2000 mL of toluene, methyl aluminum Oxane (MAO) or improved methylalumoxane (MMAO), the molar ratio of polymerized double-active center catalyst to MAO or MMAO is Al/(Fe+M)=350-3500, ethylene 1-20atm, at -15- React at 80°C for 1 hour, terminate the reaction with ethanol solution containing 1% hydrochloric acid by weight, filter the obtained product, wash with ethanol several times, and dry in vacuum at 40°C for 24 hours.
具体实施方式如下:The specific implementation is as follows:
实施例1 烯烃基芳胺的制备Example 1 Preparation of alkenyl arylamine
2.6-二异丙基苯胺0.2mol和烯丙基氯0.1mol加热回流10小时,冷却放置12小时后,倾入400mL水中,加入氢氧化钠使溶液呈碱性,乙醚萃取,真空减压蒸馏得N-烯丙基苯胺18.33g,产率84.3%.以100mL甲苯为溶剂加入N-烯丙基苯胺0.084mol和过量ZnCl2,氩气氛下回流5小时,冷却倾入氢氧化钠的水溶液中,分离有机层,下层不溶物溶于热的浓盐酸中后再倾入上述碱溶液中乙醚萃取合并有机层,无水硫酸镁干燥,真空浓缩后减压蒸馏得4-烯丙基苯胺12.92g。产率70.9%。2. 0.2 mol of 6-diisopropylaniline and 0.1 mol of allyl chloride were heated and refluxed for 10 hours, cooled and placed for 12 hours, poured into 400 mL of water, added sodium hydroxide to make the solution alkaline, extracted with ether, and distilled under vacuum to obtain 18.33 g of N-allyl aniline, yield 84.3%. Add 0.084 mol of N-allyl aniline and excess ZnCl 2 with 100 mL of toluene as a solvent, reflux for 5 hours under an argon atmosphere, cool and pour into an aqueous solution of sodium hydroxide, The organic layer was separated, and the insoluble matter in the lower layer was dissolved in hot concentrated hydrochloric acid, and then poured into the above alkali solution to extract with ether and the combined organic layer was dried over anhydrous magnesium sulfate, concentrated in vacuo, and distilled under reduced pressure to obtain 12.92 g of 4-allylaniline. Yield 70.9%.
实施例2 烯烃基芳胺的制备Example 2 Preparation of alkenyl arylamine
苯胺0.24mol和烯丙基溴0.12mol加热回流8小时,冷却放置10小时后,倾入200mL水中,加入氢氧化钠使溶液呈碱性,乙醚萃取,真空减压蒸馏得N-烯丙基苯胺8.645g,产率54.17%.以200mL甲苯为溶剂加入N-烯丙基苯胺0.065mol和过量ZnCl2,氩气氛下回流8小时,冷却倾入氢氧化钠的水溶液中,分离有机层,下层不溶物溶于热的浓盐酸中后再倾入上述碱溶液中乙醚萃取合并有机层,无水硫酸镁干燥,真空浓缩后减压蒸馏得2-烯丙基苯胺2.18g。产率25.2%。0.24mol of aniline and 0.12mol of allyl bromide were heated and refluxed for 8 hours, cooled and placed for 10 hours, poured into 200mL of water, added sodium hydroxide to make the solution alkaline, extracted with ether, and distilled under vacuum to obtain N-allyl aniline 8.645g, yield 54.17%. Add 0.065mol of N-allylaniline and excess ZnCl 2 to 200mL of toluene as solvent, reflux for 8 hours under argon atmosphere, cool and pour into aqueous solution of sodium hydroxide, separate the organic layer, the lower layer is insoluble The product was dissolved in hot concentrated hydrochloric acid, and then poured into the above alkali solution for ether extraction and combined organic layers, dried over anhydrous magnesium sulfate, concentrated in vacuo, and distilled under reduced pressure to obtain 2.18 g of 2-allylaniline. Yield 25.2%.
实施例3 烯烃基芳胺的制备Example 3 Preparation of alkenyl arylamine
4-特丁基苯胺0.2mol和烯丙基氯0.1mol加热回流9小时,冷却放置11小时后,倾入300mL水中,加入氢氧化钠使溶液呈碱性,乙醚萃取,真空减压蒸馏得N-烯丙基-2-特丁基苯胺5.67g,产率30.0%.以50mL甲苯为溶剂加入N-烯丙基-2-特丁基苯胺0.03mol和过量ZnCl2,氩气氛下回流6小时,冷却倾入氢氧化钠的水溶液中,分离有机层,下层不溶物溶于热的浓盐酸中后再倾入上述碱溶液中乙醚萃取合并有机层,无水硫酸镁干燥,真空浓缩后减压蒸馏得4-烯丙基-2-特丁基苯胺3.54g。产率62.4%。0.2 mol of 4-tert-butylaniline and 0.1 mol of allyl chloride were heated and refluxed for 9 hours, cooled and placed for 11 hours, poured into 300 mL of water, added sodium hydroxide to make the solution alkaline, extracted with ether, and distilled under vacuum to obtain N -Allyl-2-tert-butylaniline 5.67g, yield 30.0%. Add 0.03mol of N-allyl-2-tert-butylaniline and excess ZnCl 2 with 50mL of toluene as solvent, and reflux for 6 hours under argon atmosphere , cooled and poured into an aqueous solution of sodium hydroxide, the organic layer was separated, the insoluble matter in the lower layer was dissolved in hot concentrated hydrochloric acid, and then poured into the above alkali solution to extract the combined organic layer, dried over anhydrous magnesium sulfate, concentrated in vacuo and then decompressed Distillation gave 3.54 g of 4-allyl-2-tert-butylaniline. Yield 62.4%.
实施例4 烯烃基环戊二烯的制备Example 4 Preparation of alkenyl cyclopentadiene
在玻璃Schlenk瓶中依次加入100mL的33%的NaOH,0.5mol环戊二烯,0.5mol烯丙基氯,在2g四丁基溴化铵为相转移剂下,冰浴中搅拌2小时,室温下搅拌6小时之后,油相洗至中性,采用无水碳酸钾干燥后,减压蒸馏下得到烯丙基环戊二烯36.75。产率70.0%。Add 100 mL of 33% NaOH, 0.5 mol cyclopentadiene, and 0.5 mol allyl chloride to a glass Schlenk bottle successively, and stir in an ice bath for 2 hours under the condition of 2 g of tetrabutylammonium bromide as a phase transfer agent. After stirring at low temperature for 6 hours, the oil phase was washed to neutrality, dried with anhydrous potassium carbonate, and distilled under reduced pressure to obtain allyl cyclopentadiene 36.75. Yield 70.0%.
实施例5 烯烃基环戊二烯的制备Example 5 Preparation of alkenyl cyclopentadiene
在玻璃Schlenk瓶中依次加入120mL的33%的NaOH,0.6mol环戊二烯,0.5mol 3-溴1-丁烯,在3g四丁基溴化铵为相转移剂下,冰水浴中搅拌2小时,室温下搅拌7小时之后,油相洗至中性,采用无水碳酸钾干燥后,减压蒸馏下得到3-环戊二烯基-1-丁烯26.78g。产率45.01%。Add 120 mL of 33% NaOH, 0.6 mol cyclopentadiene, and 0.5 mol 3-bromo-1-butene to a glass Schlenk bottle, and stir in an ice-water bath for 2 After stirring at room temperature for 7 hours, the oil phase was washed to neutrality, dried with anhydrous potassium carbonate, and then distilled under reduced pressure to obtain 26.78 g of 3-cyclopentadienyl-1-butene. Yield 45.01%.
实施例6 烯烃基环戊二烯的制备Example 6 Preparation of alkenyl cyclopentadiene
在玻璃Schlenk瓶中依次加入110mL的33%的NaOH,0.5mol环戊二烯,0.5mol4-溴苯乙烯,在2.5g四丁基溴化铵为相转移剂下,冰水浴中搅拌2小时,室温下搅拌6.5小时之后,油相洗至中性,采用无水碳酸钾干燥后,减压蒸馏下得到苯乙烯基环戊二烯33.40g。产率40.0%。Add 110 mL of 33% NaOH, 0.5 mol cyclopentadiene, and 0.5 mol 4-bromostyrene in a glass Schlenk bottle, and stir in an ice-water bath for 2 hours under 2.5 g of tetrabutylammonium bromide as a phase transfer agent. After stirring at room temperature for 6.5 hours, the oil phase was washed to neutrality, dried with anhydrous potassium carbonate, and distilled under reduced pressure to obtain 33.40 g of styrylcyclopentadiene. Yield 40.0%.
实施例7 烯烃基铁系催化剂Com Fe的制备Example 7 Preparation of olefin-based iron-based catalyst Com Fe
以甲醇为溶剂,甲酸为催化剂,4-烯丙基苯胺与2.6-二乙酰基吡啶缩合反应生成三齿吡啶二亚胺配体C39H51N3。Com Fe的制备在无氧无水及高纯氩气保护下进行。以四氢呋喃为溶剂30mL,该吡啶二亚胺配体4.0mmol与FeCl2·4H2O 3.8mmol室温搅拌2小时,得蓝色溶液,真空浓缩,加正己烷沉淀出蓝色粉末,过滤,真空干燥得C39H51N3FeCl22.48g,产率95%。Using methanol as a solvent and formic acid as a catalyst, 4-allylaniline and 2.6-diacetylpyridine are condensed to generate tridentate pyridinediimine ligand C 39 H 51 N 3 . The preparation of Com Fe was carried out under the protection of oxygen, anhydrous and high-purity argon. Using tetrahydrofuran as solvent 30mL, 4.0mmol of the pyridinediimine ligand and FeCl 2 4H 2 O 3.8mmol were stirred at room temperature for 2 hours to obtain a blue solution, which was concentrated in vacuo, added n-hexane to precipitate a blue powder, filtered, and dried in vacuo 2.48 g of C 39 H 51 N 3 FeCl 2 was obtained with a yield of 95%.
实施例8 烯烃基铁系催化剂Com Fe的制备Example 8 Preparation of olefin-based iron-based catalyst Com Fe
以甲醇为溶剂,甲酸为催化剂,2-特丁基-4-烯丙基苯胺,2.6-二甲基苯胺与2.6-二乙酰基吡啶缩合反应生成三齿吡啶二亚胺配体C30H35N3。Com Fe的制备在无氧无水及高纯氩气保护条件下进行。以四氢呋喃为溶剂40mL,该吡啶二亚胺配体1.51mmol与FeCl2·4H2O 1.44mmol室温搅拌3小时,得蓝色溶液,真空浓缩,加正己烷沉淀出蓝色粉末,过滤,真空干燥得C30H35N3FeCl20.73lg,产率90%。With methanol as solvent and formic acid as catalyst, 2-tert-butyl-4-allylaniline, 2.6-dimethylaniline and 2.6-diacetylpyridine are condensed to generate tridentate pyridinediimine ligand C 30 H 35 N 3 . The preparation of Com Fe was carried out under the protection conditions of anaerobic, anhydrous and high-purity argon. Using tetrahydrofuran as solvent 40mL, 1.51mmol of the pyridinediimine ligand and FeCl 2 4H 2 O 1.44mmol were stirred at room temperature for 3 hours to obtain a blue solution, which was concentrated in vacuo, added n-hexane to precipitate a blue powder, filtered, and dried in vacuo 0.73 lg of C 30 H 35 N 3 FeCl 2 was obtained with a yield of 90%.
实施例9 烯烃基铁系催化剂Com Fe的制备Example 9 Preparation of olefin-based iron-based catalyst Com Fe
以甲醇为溶剂,甲酸为催化剂,2-烯丙基苯胺与2.6-二乙酰基吡啶缩合反应生成三齿吡啶二亚胺配体C27H27N3。Com Fe的制备在无氧无水及高纯氩气保护条件下进行。以四氢呋喃为溶剂35mL,该吡啶二亚胺配体2.27mmol与FeCl2·4H2O 2.16mmol室温搅拌2.5小时,得蓝色溶液,真空浓缩,加正己烷沉淀出蓝色粉末,过滤,真空干燥得C27H27N3FeCl21.044g,产率93%。With methanol as solvent and formic acid as catalyst, 2-allylaniline and 2.6-diacetylpyridine are condensed to generate tridentate pyridinediimine ligand C 27 H 27 N 3 . The preparation of Com Fe was carried out under the protection conditions of anaerobic, anhydrous and high-purity argon. Using tetrahydrofuran as solvent 35mL, 2.27mmol of the pyridinediimine ligand and FeCl 2 4H 2 O 2.16mmol were stirred at room temperature for 2.5 hours to obtain a blue solution, concentrated in vacuo, added n-hexane to precipitate a blue powder, filtered, and dried in vacuo 1.044 g of C 27 H 27 N 3 FeCl 2 was obtained with a yield of 93%.
实施例10 烯烃基茂金属催化剂Com M的制备Example 10 Preparation of olefin-based metallocene catalyst Com M
将烯丙基环戊二烯4.14mmol加入到四氢呋喃溶液中,在冰盐浴的条件下,滴加等摩尔数的正丁基锂,在室温下搅拌2小时,然后缓慢地加入含等当量的ZrCl4的四氢呋喃溶液,溶液呈深红色,室温下搅拌反应6小时,蒸去溶剂,加入甲苯离心除去锂盐,将清液抽干,再用己烷洗涤数次即得产物C16H16ZrCl20.574g,产率75%。Add 4.14mmol of allylcyclopentadiene to the tetrahydrofuran solution, under the condition of ice-salt bath, dropwise add n-butyllithium of equimolar number, stir at room temperature for 2 hours, then slowly add The tetrahydrofuran solution of ZrCl 4 , the solution is dark red, stirred and reacted at room temperature for 6 hours, evaporated the solvent, added toluene and centrifuged to remove lithium salt, drained the clear liquid, and washed several times with hexane to obtain the product C 16 H 16 ZrCl 2 0.574g, yield 75%.
实施例11 烯烃基茂金属催化剂Com M的制备Example 11 Preparation of olefin-based metallocene catalyst Com M
将3-环戊二烯基-1-丁烯2.17mmol,烯丙基环戊二烯2.17mmol加入到四氢呋喃溶液中,在冰盐浴的条件下,滴加4.34mmol的正丁基锂,在室温下搅拌3小时,然后缓慢地加入含等当量的TiCl4的四氢呋喃溶液,溶液呈深红色,室温下搅拌反应8小时,蒸去溶剂,加入甲苯离心除去锂盐,将清液抽干,再用己烷洗涤数次即得产物C17H18TiCl2 0.444g,产率60%。2.17mmol of 3-cyclopentadienyl-1-butene and 2.17mmol of allylcyclopentadiene were added to the tetrahydrofuran solution, and 4.34mmol of n-butyllithium was added dropwise under the condition of an ice-salt bath. Stir at room temperature for 3 hours, then slowly add tetrahydrofuran solution containing equivalent TiCl4 , the solution is dark red, stir and react at room temperature for 8 hours, evaporate the solvent, add toluene and centrifuge to remove lithium salt, drain the clear liquid, and then After washing several times with hexane, 0.444 g of the product C 17 H 18 TiCl 2 was obtained, with a yield of 60%.
实施例12 烯烃基茂金属催化剂Com M的制备Example 12 Preparation of olefin-based metallocene catalyst Com M
将苯乙烯基环戊二烯1.79mmol,环戊二烯1.79mmol加入到四氢呋喃溶液中,在冰盐浴的条件下,滴加3.58mmol的正丁基锂,在室温下搅拌2.5小时,然后缓慢地加入含等当量的ZrCl4的四氢呋喃溶液,溶液呈深红色,室温下搅拌反应7.5小时,蒸去溶剂,加入甲苯离心除去锂盐,将清液抽干,再用己烷洗涤数次即得产物C18H14ZrCl2 0.431g,产率61.4%。Add 1.79 mmol of styryl cyclopentadiene and 1.79 mmol of cyclopentadiene to the tetrahydrofuran solution, add 3.58 mmol of n-butyllithium dropwise under the condition of an ice-salt bath, stir at room temperature for 2.5 hours, and then slowly Add the tetrahydrofuran solution containing equivalent ZrCl4 , the solution is deep red, stir and react at room temperature for 7.5 hours, evaporate the solvent, add toluene and centrifuge to remove lithium salt, drain the clear liquid, and wash it several times with hexane to obtain Product C 18 H 14 ZrCl 2 0.431 g, yield 61.4%.
实施例13 高分子化双活性中心烯烃聚合催化剂的制备Example 13 Preparation of polymerized double-active center olefin polymerization catalyst
在无水无氧条件下,将实施例7制备铁系催化剂C39H51N3FeCl20.2mmol,实施例10制备的茂金属催化剂C16H16ZrCl20.7mmol,苯乙烯5mL,偶氮二异丁腈1.0wt%,依次加入到干燥的甲苯中混合均匀,然后在80℃的水浴中共聚10小时后,冷却至室温,离心,上层清液用正己烷作沉淀剂,得固体粉末,再用正己烷洗涤三次,烘干即可。测定铁含量为0.256wt%,锆含量为1.57wt%。Under anhydrous and oxygen-free conditions, 0.2 mmol of the iron-based catalyst C 39 H 51 N 3 FeCl 2 prepared in Example 7, 0.7 mmol of the metallocene catalyst C 16 H 16 ZrCl 2 prepared in Example 10, 5 mL of styrene, and azo 1.0 wt% of diisobutyronitrile was added to dry toluene and mixed evenly, then copolymerized in a water bath at 80°C for 10 hours, cooled to room temperature, centrifuged, and the supernatant was made of n-hexane as a precipitating agent to obtain a solid powder. Then wash it three times with n-hexane and dry it. The iron content was determined to be 0.256 wt%, and the zirconium content was 1.57 wt%.
实施例14 高分子化双活性中心烯烃聚合催化剂的制备Example 14 Preparation of high molecular weight double active center olefin polymerization catalyst
在无水无氧条件下,将实施例8制备的铁系催化剂C30H35N3FeCl20.5mmol,实施例12制备的茂金属催化剂C18H14ZrCl20.5mmol,苯乙烯8mL,偶氮二异丁腈1.0wt%,依次加入到干燥的甲苯中混合均匀,然后在80℃的水浴中共聚11小时后,冷却至室温,离心,上层清液用正己烷作沉淀剂,得固体粉末,再用正己烷洗涤三次,烘干即可。测定铁含量为0.214wt%,锆含量为0.419wt%。Under anhydrous and oxygen-free conditions, 0.5 mmol of the iron-based catalyst C 30 H 35 N 3 FeCl 2 prepared in Example 8, 0.5 mmol of the metallocene catalyst C 18 H 14 ZrCl 2 prepared in Example 12, 8 mL of styrene, and Add 1.0wt% nitrogen bisisobutyronitrile to dry toluene and mix evenly, then copolymerize in a water bath at 80°C for 11 hours, cool to room temperature, centrifuge, and use n-hexane as a precipitating agent in the supernatant to obtain a solid powder , then washed three times with n-hexane and dried. The iron content was determined to be 0.214 wt%, and the zirconium content was 0.419 wt%.
实施例15 高分子化双活性中心烯烃聚合催化剂的制备Example 15 Preparation of high molecular weight double active center olefin polymerization catalyst
在无水无氧条件下,实施例9制备的铁系催化剂C27H27N3FeCl20.7mmol,实施例11制备的茂金属催化剂C17H18TiCl2 0.4mmol,苯乙烯10mL,偶氮二异丁腈1.0wt%,依次加入到干燥的甲苯中混合均匀,然后在80℃的水浴中共聚12小时后,冷却至室温,离心,上层清液用正己烷作沉淀剂,得固体粉末,再用正己烷洗涤三次,烘干即可。测定铁含量为0.532wt%,钛含量为0.467wt%。Under anhydrous and oxygen-free conditions, iron-based catalyst C 27 H 27 N 3 FeCl 2 0.7 mmol prepared in Example 9, metallocene catalyst C 17 H 18 TiCl 2 0.4 mmol prepared in Example 11, styrene 10 mL, azo 1.0 wt% of diisobutyronitrile was sequentially added to dry toluene and mixed uniformly, then copolymerized in a water bath at 80°C for 12 hours, cooled to room temperature, centrifuged, and the supernatant was made of n-hexane as a precipitating agent to obtain a solid powder. Then wash it three times with n-hexane and dry it. The iron content was determined to be 0.532 wt%, and the titanium content was 0.467 wt%.
实施例16 乙烯聚合Example 16 Ethylene Polymerization
乙烯聚合在无水无氧条件下进行,在反应体系中依次加入甲苯100mL,甲基铝氧烷,实施例13制备的高分子化双活性中心催化剂0.02g,Al/(Fe+Zr)=350,乙烯1atm,于-15℃反应1小时,用含重量比为1%盐酸的乙醇溶液终止反应,将所得产物过滤,用乙醇洗涤数次,于40℃真空干燥24小时得聚乙烯1.76g。Ethylene polymerization is carried out under anhydrous and oxygen-free conditions, and 100 mL of toluene, methyl aluminoxane, and 0.02 g of the polymerized double-active center catalyst prepared in Example 13 are successively added to the reaction system, Al/(Fe+Zr)=350 , ethylene 1atm, reacted at -15°C for 1 hour, terminated the reaction with an ethanol solution containing 1% hydrochloric acid by weight, filtered the resulting product, washed several times with ethanol, and dried in vacuum at 40°C for 24 hours to obtain 1.76g of polyethylene.
实施例17 乙烯聚合Example 17 Ethylene Polymerization
乙烯聚合在无水无氧条件下进行,在反应体系中依次加入甲苯500mL,改进甲基铝氧烷,实施例13制备的高分子化双活性中心催化剂0.02g,Al/(Fe+Zr)=1400,乙烯5atm,于30℃反应1小时,用含重量比为1%盐酸的乙醇溶液终止反应,将所得产物过滤,用乙醇洗涤数次,于40℃真空干燥24小时得聚乙烯19.25g。Ethylene polymerization is carried out under anhydrous and oxygen-free conditions, 500 mL of toluene is added to the reaction system successively, and methyl aluminoxane is improved, and the polymerized double-active center catalyst prepared in Example 13 is 0.02 g, Al/(Fe+Zr)= 1400, ethylene 5 atm, reacted at 30°C for 1 hour, terminated the reaction with ethanol solution containing 1% hydrochloric acid by weight, filtered the resulting product, washed several times with ethanol, and dried in vacuum at 40°C for 24 hours to obtain 19.25 g of polyethylene.
实施例18 乙烯聚合Example 18 Ethylene Polymerization
乙烯聚合在无水无氧条件下进行,在反应体系中依次加入甲苯2000mL,改进甲基铝氧烷,实施例14制备的高分子化双活性中心催化剂0.04g,Al/(Fe+Zr)=3500,乙烯4atm,于45℃反应1小时,用含重量比为1%盐酸的乙醇溶液终止反应,将所得产物过滤,用乙醇洗涤数次,于40℃真空干燥24小时得聚乙烯6.48g。Ethylene polymerization is carried out under anhydrous and oxygen-free conditions, and 2000 mL of toluene is added successively to the reaction system to improve methyl aluminoxane, 0.04 g of the polymerized double-active center catalyst prepared in Example 14, Al/(Fe+Zr)= 3500, ethylene 4atm, reacted at 45°C for 1 hour, terminated the reaction with ethanol solution containing 1% hydrochloric acid by weight, filtered the obtained product, washed several times with ethanol, and dried in vacuum at 40°C for 24 hours to obtain 6.48g of polyethylene.
实施例19 乙烯聚合Example 19 Ethylene Polymerization
乙烯聚合在无水无氧条件下进行,在反应体系中依次加入甲苯2000mL,甲基铝氧烷,实施例15制备的高分子化双活性中心催化剂0.02g,Al/(Fe+Ti)=1700,乙烯20atm,于80℃反应1小时,用含重量比为1%盐酸的乙醇溶液终止反应,将所得产物过滤,用乙醇洗涤数次,于40℃真空干燥24小时得聚乙烯21.74g。Ethylene polymerization is carried out under anhydrous and oxygen-free conditions, and 2000 mL of toluene, methyl aluminoxane, and 0.02 g of the polymerized double-active center catalyst prepared in Example 15 are successively added to the reaction system, Al/(Fe+Ti)=1700 , Ethylene 20atm, reacted for 1 hour at 80°C, terminated the reaction with an ethanol solution containing 1% hydrochloric acid by weight, filtered the resulting product, washed several times with ethanol, and dried in vacuum at 40°C for 24 hours to obtain 21.74g of polyethylene.
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004067586A3 (en) * | 2002-12-09 | 2004-12-29 | Safetec Gmbh | Mixed bimetallic olefin polymerisation catalyst |
| US7034157B2 (en) * | 2003-10-23 | 2006-04-25 | Fina Technology, Inc. | Catalyst components, process for their preparation and their use as catalyst components in polymerization of olefins |
| US7119155B2 (en) | 2002-10-25 | 2006-10-10 | Exxonmobil Chemical Patents Inc. | Polymerized catalyst composition II |
| US7176158B2 (en) | 2002-10-25 | 2007-02-13 | Exxonmobil Chemical Patents Inc. | Polymerization catalyst composition |
| US7319083B2 (en) | 2002-10-25 | 2008-01-15 | Exxonmobil Chemical Patents Inc. | Polymerized catalyst composition |
| CN100395268C (en) * | 2006-05-11 | 2008-06-18 | 复旦大学 | Nitrogen-nitrogen bidentate ligand tricoordinate monovalent nickel olefin polymerization catalyst and preparation method thereof |
| CN100519596C (en) * | 2003-04-14 | 2009-07-29 | 托塔尔石油化学产品研究弗吕公司 | Hollow polyethylene particles |
| CN106632764A (en) * | 2016-10-17 | 2017-05-10 | 曲阜师范大学 | Iron-based catalyst, preparation method of iron-based catalyst, and application of iron-based catalyst in isoprene polymerization |
| CN113045691A (en) * | 2021-03-23 | 2021-06-29 | 中国科学院青岛生物能源与过程研究所 | Method for preparing low molecular weight polyisobutylene by coordination polymerization of iron catalyst |
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2001
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7119155B2 (en) | 2002-10-25 | 2006-10-10 | Exxonmobil Chemical Patents Inc. | Polymerized catalyst composition II |
| US7176158B2 (en) | 2002-10-25 | 2007-02-13 | Exxonmobil Chemical Patents Inc. | Polymerization catalyst composition |
| US7319083B2 (en) | 2002-10-25 | 2008-01-15 | Exxonmobil Chemical Patents Inc. | Polymerized catalyst composition |
| WO2004067586A3 (en) * | 2002-12-09 | 2004-12-29 | Safetec Gmbh | Mixed bimetallic olefin polymerisation catalyst |
| CN100519596C (en) * | 2003-04-14 | 2009-07-29 | 托塔尔石油化学产品研究弗吕公司 | Hollow polyethylene particles |
| US7034157B2 (en) * | 2003-10-23 | 2006-04-25 | Fina Technology, Inc. | Catalyst components, process for their preparation and their use as catalyst components in polymerization of olefins |
| CN100395268C (en) * | 2006-05-11 | 2008-06-18 | 复旦大学 | Nitrogen-nitrogen bidentate ligand tricoordinate monovalent nickel olefin polymerization catalyst and preparation method thereof |
| CN106632764A (en) * | 2016-10-17 | 2017-05-10 | 曲阜师范大学 | Iron-based catalyst, preparation method of iron-based catalyst, and application of iron-based catalyst in isoprene polymerization |
| CN106632764B (en) * | 2016-10-17 | 2018-10-26 | 曲阜师范大学 | A kind of Fe-series catalyst and preparation method thereof and the application in isoprene polymerization |
| CN113045691A (en) * | 2021-03-23 | 2021-06-29 | 中国科学院青岛生物能源与过程研究所 | Method for preparing low molecular weight polyisobutylene by coordination polymerization of iron catalyst |
| CN113045691B (en) * | 2021-03-23 | 2022-08-05 | 中国科学院青岛生物能源与过程研究所 | Method for preparing low molecular weight polyisobutylene by coordination polymerization of iron catalyst |
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