限定几何构型茂金属催化剂催化乙烯/1-己烯共聚研究

以自制的限定几何构型茂金属催化剂为主催化剂,甲基铝氧烷为助催化剂,对乙烯/1-己烯共聚性能进行研究,考察溶剂、Al与Zr物质的量比、聚合温度、聚合压力和共聚单体浓度等工艺条件对催化剂活性以及聚合物性能的影响。确定乙烯/1-己烯共聚合的工艺条件为:以正庚烷为溶剂,Al与Zr物质的量比为700~1 000,聚合温度(100~120)℃,聚合压力(1.2~2.0)MPa,优选1-己烯浓度为(0.8~1.8)mol·L~(-1)。     

双核茂金属催化剂催化乙烯／1-己烯共聚合

合成了[CpTiCl2]2 {μ,μ-[(Me2Si)2 (η5-C5H3)2]}双核茂金属化合物,用1H NMR和IR分析进行了表征.合成的化合物经硅胶作载体负载,以MAO作助催化剂,催化乙烯/1-己烯共聚合.考察了茂金属用量,茂金属与硅胶/MAO处理温度,MAO的用量对负载催化剂的影响,以及1-己烯用量对聚合产物的影响.反应温度65℃,在1-己烯浓度为0.25 mol·L-1条件下共聚活性可达4.01×106 gPE/mol Ti·h,催化所得聚乙烯的相对分子质量分布为7.32,1-己烯插入率8.45%.     

双核茂金属催化剂催化乙烯／1-己烯共聚合

制备[CpTiCl2]2{μ,μ-[(Me2Si)2(η5-C5H3)2]}双核茂金属化合物,用1H NMR和IR分析进行了表征.合成的化合物经硅胶作载体负载,以MAO作助催化剂,催化乙烯/1-己烯共聚合.考察了茂金属用量,茂金属与硅胶/MAO处理温度,MAO的用量对负载催化剂的影响,以及己1烯-用量对聚合产物的影响.反应温度65℃,在1-己烯浓度为0.25mol/L条件下共聚活性可达4.01× 106gPE/molTi·h,催化所得聚乙烯的相对分子质量分布为7.32,己1烯-插入率8.45.     

均相稀土催化苯乙烯均聚及其与异戊二烯共聚

采用新型稀土催化体系氯代三氟乙酸钕－烷基铝－卤代烃,引发苯乙烯均聚及其与异戊二烯共聚。 催化体系各组分及陈化方式、Ｘ和Ａｌ种及用量,溶剂种类等因素对苯乙烯聚合的影响,并用稀土催化实现了Ｓｔ－Ｉｐ嵌段共聚。用ＩＲ,ＮＭＲ及ＤＳＣ等方法表征了聚合物的结构,合成出的Ｓｔ－Ｉｐ二嵌段共聚物中,Ｉｐ链节以反式－１,４－结构为主,含少量３,４－结构,几科不含顺式－１,４－结构。     

茂金属加合物技术首次工业试验

采用中国石油化工股份有限公司茂金属加合物技术制备茂金属加合物,并进行负载化研究;完成了茂金属加合物催化剂催化乙烯聚合以及乙烯与α-烯烃共聚合的淤浆、环管淤浆、气相流化床工艺的中试;在中试的基础上,茂金属加合物催化剂于60kt／a气相流化床聚乙烯生产装置上成功进行了工业试验。探索了茂金属催化剂与Ziegler催化剂的切换技术,研究了催化剂组成和聚合工艺参数对聚乙烯树脂性能的影响。用所得茂金属聚乙烯树脂加工成的薄膜具有较好的透明性,并表现出了优异的落镖冲击强度和撕裂强度。     

茂锆金属催化剂催化乙烯聚合研究

主要考察了含锆的茂金属催化剂中催化乙烯反应条件优化研究,在最优条件下催化聚合反应所得的产物与吉林石化公司聚乙烯厂聚乙烯产品进行分析对比.对茂锆金属催化剂催化乙烯聚合反应条件研究表明,适宜的助催化剂[Al]与主催化剂[Cat]的摩尔比在1 500左右,适宜的主催化剂浓度在1.5×10-4 mol/L左右,最佳聚合温度60℃,此时催化剂的活性可达到106 gPE/(molCat·h).从物理性能、热性能、相对支化度、相对分子质量及其分布分析可知,制备出的负载茂锆金属催化剂在最优反应条件下催化乙烯聚合所得的产物与吉林石化公司聚乙烯产品性质基本一致,符合产品的指标,支链分布均匀,分子量分布更窄.同时对茂锆金属催化剂主、助催化剂催化乙烯聚合的作用和机理进行了探讨.     

茂金属加合物技术的工业应用试验

根据中国石化集团公司开发的茂金属加合物专利技术,进行了活性组分负载化研究,完成了茂金属加合物催化剂催化乙烯以及乙烯与α-烯烃共聚的淤浆、环管淤浆、气相流化床工艺的中试试验.在中试的基础上进行了茂金属加合物催化剂气相流化床聚乙烯工艺的工业应用试验,探索了茂金属催化剂与Ziegler催化剂之间的切换技术,开发了催化剂结构和配方以及聚合工艺参数对聚乙烯树脂牌号的调控技术.得到百吨级薄膜牌号的茂金属聚乙烯树脂,并对工业应用试验产品进行了加工研究.     

负载茂金属催化剂催化乙烯气相聚合

研究了负载茂金属催化剂(n-BuNeCp)_2ZrCl_2/SiO_2的乙烯气相聚合行为及其催化聚合产品的性能。三乙基铝加入聚合体系后可降低负载茂金属催化剂的初始活性,有利于聚合过程中的温度控制。气相聚合产品聚乙烯的重均分子量为(1 42～2.28)×10~5,相对分子质量分布为2.6～3.1,熔点在135℃以上,结晶度约为60%,聚乙烯产物颗粒形态以球形为主.堆密度大于0.35 g/cm~3。     

茂金属双峰聚乙烯的研究进展

概述了用复合茂金属催化体系法和工艺法制备双峰聚乙烯的研究进展,讨论了２组分比例,及聚合温度、聚合压力、氢气用量对茂金属双峰聚乙烯制备的影响规律。     

茂金属乙烯/苯乙烯共聚物的开发

综述了近１０年来国内外在茂金属催化剂合成乙烯／本乙烯共聚物方面的研究状况,着重介绍了用限定几何形催化剂开发的ＥＳ共聚物的结构及物理机械性能。     

Mathematical Modeling of Homopolymerization on Supported Metallocene Catalysts

Summary: In this paper, a mathematical model describing olefin polymerization with metallocene catalysts is presented. It is an improvement of a previous model, the “particle growth model” (PGM) proposed by, among others, one of the authors of the present work and derives from the so‐called “multigrane model” (MGM). The main differences between this work and others is a more sophisticated approach to fragmentation with respect to the MGM. Additionally, there is a more specific modeling for the unfragmented core with respect to the PGM. The numerical results obtained by the model are compared with experimental data. The results of this work allow to extend the PGM to catalysts with lower activity. The importance of those catalysts depends on the fact that high activity catalysts could bring, in some cases, too poor polymer morphology.

Geometrical representation of the micro‐ and macroparticle.     

半炼蜡裂解 1-己烯用于聚乙烯共聚单体研究

以半炼蜡裂解1-己烯为原料,在2L不锈钢釜中进行了与乙烯共聚的淤浆聚合和气相搅拌聚合试验研究,聚合工艺条件为:压力1.03MPa;p(H2)/p(C2H4)=0.28/0.75MPa,1mLAlEt3溶液(1mmol/mL);淤浆聚合和气相搅拌聚合温度分别为80℃和85℃。研究结果表明,半炼蜡裂解1-己烯可以与乙烯进行共聚反应,其共聚性能与进口的1-己烯相当。     

Study on copolymerization of ethylene/1‐hexene catalyzed by a novel polystyrene‐supported metallocene catalyst

Ethylene/1‐hexene copolymerization was carried out with polystyrene‐supported metallocene catalyst. It was found that the kinetic of the copolymerization was strongly influenced by the steric hindrance of carrier. The influences of 1‐hexene concentration in the feed on catalyst productivity and comonomer reactivity were investigated. The microstructure of resultant copolymer was analyzed by ¹³C NMR. It was found that the different carriers have slight effect on the composite of copolymer. © 2006 Wiley Periodicals, Inc. J Appl Polym Sci 102: 1574–1577, 2006     

Polymerization of ethylene and ethylene/1‐hexene over Ziegler‐Natta/Metallocene hybrid catalysts supported on SiO2 prepared by a sol‐gel method

A silica support for use in olefin polymerization was prepared by the gelation of a stable, colloidal phase of silica sol using a MgCl₂ solution as the initiator. The Ziegler‐Natta/Metallocene hybrid catalysts prepared using this support exhibited characteristics of both Ziegler‐Natta and metallocene catalysts. The polymers produced by the hybrid catalysts showed a bimodal molecular weight distribution pattern and two different melting points, corresponding to products arising from each catalyst. This suggests that the hybrid catalysts acted as individual active species and produced a blend of polymers. © 2000 John Wiley & Sons, Inc. J Appl Polym Sci 78: 2318–2326, 2000     

乙烯三聚制1-己烯的研究

采用异辛酸铬-吡咯-三乙基铝（Cr-N-Al)三元催化体系,进行了乙烯三聚制1-己烯的研究。在Cr离子浓度为0.2-0.4mmol/L,Cr:N:Al为1：3：20,反应温度为90℃,反应时间为3h,反应压力为4-5MPa的条件下催化剂效率达17-22kg/g,催化剂活性为15-17kg/g.h,己烯的选择性达50%左右,其中1-己烯含量为96%-97%。     

Kinetic study of olefin polymerization with a supported metallocene catalyst. II. Ethylene/1‐hexene copolymerization in gas phase

A kinetic study of ethylene/1‐hexene copolymerization is conducted with a supported metallocene catalyst in a gas‐phase reactor. The investigation into the kinetics of ethylene/1‐hexene copolymerization includes the effects of operational parameters such as the reaction temperature, pressure, and comonomer concentration. The large variations in gas‐phase composition using only an initial charge of 1‐hexene are illustrated by experiment. To remedy this, the ability to control the comonomer composition of 1‐hexene online for the entire duration of the reaction is demonstrated. Online perturbation techniques are implemented to determine key kinetic parameters such as the activation energies for propagation and catalyst deactivation. From pressure perturbation results, a reaction rate order close to 1 is obtained for ethylene in the presence of 1‐hexene. Finally, all the parameters obtained from the study are compared to those determined from ethylene–propylene (E–P) copolymerization. © 2001 John Wiley & Sons, Inc. J Appl Polym Sci 80: 1096–1119, 2001     

乙烯-醋酸乙烯酯共聚物对茂金属聚乙烯的改性研究

以添加不同比例的茂金属聚乙烯 (mLLDPE) /乙烯 醋酸乙烯酯 (EVA)共混物为研究对象 ,考察了EVA含量对mLLDPE/EVA共混物的力学性能、热性能、流变性能、动态力学性能和形态结构的影响。研究结果表明 ,EVA添加到mLLDPE中 ,增加了mLLDPE的剪切敏感度、降低了mLLDPE的熔融粘度、改善了mLLDPE的流动性和加工性 ;在一定的添加比例范围内mLLDPE和EVA具有很好的相容性 ,可以在改善mLLDPE加工性能、引入极性基团的同时又保持与纯mLLDPE相近的力学性能 ,但会导致共混物材料的刚性下降 ,柔性增加。热分析数据说明 ,mLLDPE/EVA共混体系中 ,在EVA含量较小时共混物存在大量共晶 ,与mLLDPE有很好的相容性 ,无论是熔融曲线还是降温曲线都只出现一个峰。当EVA含量增大时 ,mLLDPE/EVA共混物出现相分离 ,曲线出现双峰 ,但两峰值呈现靠近趋势 ,预示mLLDPE/EVA共混物中仍存在少量共结晶     

纳米钯／乙二醇体系催化Suzuki反应的研究

采用乙二醇作为溶剂,利用其还原性和含羟基官能团的性质和结构特征,将二价钯现场还原成具有催化活性的零价纳米钯,并通过乙二醇双齿羟基稳定生成的零价纳米钯,用于催化Suzuki反应。该体系无需配体,既能催化一系列芳基碘化物和芳基溴化物与苯硼酸反应,以优良产率生成偶联产物。由于乙醚微溶于乙二醇,因此,反应完成后,可通过萃取的方法分离产物,分离后的体系不需任何纯化即可循环使用,是一种简单高效的绿色化学反应体系。     

Copolymerization of ethylene and 1-octene by homogeneous and different supported metallocenic catalysts

In this work, the performance of the homogeneous catalyst system based on Et(Flu)₂ZrCl₂/MAO was evaluated on the copolymerization of ethylene and 1-octene. Characteristics of some of the produced polymers were also investigated. A study was performed to compare this system with that of Cp₂ZrCl₂/MAO. The influence of different support materials for the Cp₂ZrCl₂ was also evaluated, using silica, MgCl₂, and the zeolite sodic mordenite NaM. An increase in activity was observed in relation to the comonomer addition for the two homogeneous catalysts. The copolymers produced by the Et(Flu)₂ZrCl₂/MAO system showed higher molecular weight and narrower molecular weight distribution. We verified that the catalyst supported on SiO₂ was the most active one, although the copolymers produced with the catalyst supported on NaM showed higher molecular weight and lower molecular weight distribution. © 2001 John Wiley & Sons, Inc. J Appl Polym Sci 82: 724–730, 2001