α-二亚胺镍/Cp*TiCl3复式催化剂制备双峰长支链聚乙烯

合成了一种后过渡金属镍化合物 [二 N ,N′ (α 萘基 ) 2 ,3 丁二亚胺镍二溴化物 ][C1 0 H7—NC(CH3)C(CH3)N—C1 0 H7]NiBr2 ,此化合物在MAO活化下催化乙烯聚合能得到含有末端双键的低分子量聚乙烯 ,即长链α 烯烃 .此化合物和一种单茂钛化合物五甲基环戊二烯基三氯化钛 (Cp TiCl3)所组成的复式催化剂 ,用MAO活化后两种主催化剂具有良好协同作用 ,能使单一乙烯聚合制备出双峰型长支链的聚乙烯 .1 3C NMR表明由此复式催化剂制得的聚乙烯不但含有甲基、乙基、丙基、丁基、戊基支链而且还含有相当多的长支链 (支链长度大于或等于 6 ) .催化剂的摩尔比 (Ni Ti)、Al(MAO) (Ni+Ti)摩尔比和聚合温度等聚合条件对催化活性及聚合物的结构与性能有明显影响 .GPC测试表明所得到的支化聚乙烯分子量呈双峰分布 .     

α-二亚胺镍复式催化剂/MAO制备高支化的长支链聚乙烯

研究了由两种α-二亚胺镍催化剂[Cat1:α-萘基-丁二亚胺二溴化镍,Cat2:2,6-二异丙基苯基苊二亚胺二溴化镍]组成的复式镍催化剂在MAO活化下催化单一乙烯聚合.可制备得到支化度高达上百个支链(每1000个碳),长支链的比例占到30%左右的聚乙烯.13C-NMR、GPC、DSC、WAXD、DMA结果表明此复式催化剂催化乙烯聚合可得到分子量较高、分子量分布较窄的长支链聚乙烯弹性体.在合适的条件下,此复式催化体系还具有促进提高催化活性的良好协同作用,其聚合活性比两种单一催化剂都高(4·6×105g PE/mol Ni·h).     

负载型二亚胺镍催化剂制备支化聚乙烯的结构与性能

负载型二亚胺镍催化剂制备支化聚乙烯的结构与性能;二亚胺镍配合物; 负载催化剂; 支化聚乙烯     

α-二亚胺镍(Ⅱ)配合物-TiCl4复合催化剂催化乙烯原位聚合制备支化聚乙烯

制备了α-二亚胺镍()配合物[C6H5—NC(CH3)—C(CH3)N—C6H5]NiBr2(NiL)-TiCl4负载在MgCl2-SiO2载体上的复合催化剂(NiL-TiCl4/MgCl2-SiO2),以AlR3为助催化剂(不用MAO)催化乙烯聚合.研究了NiL和TiCl4负载方法、NiL/TiCl4摩尔比、助催化剂种类及聚合反应温度等对催化剂性能的影响.用IR和13CNMR表征聚合产物支化度及支链结构;用GC-MS监测聚合反应.实验结果表明,NiL-TiCl4复合催化剂具有齐聚原位共聚特性,可催化乙烯原位聚合,合成支化聚乙烯.     

含溴α-二亚胺镍(Ⅱ)配合物的合成、表征及催化乙烯聚合反应

合成了一种新型含溴α-二亚胺及其镍配合物,采用<'1>H NMR、<'13>C NMR、FTIR、元素分析和XPS等方法进行表征.用配合物作为催化剂,以甲基铝氧烷(MAO)为助催化剂催化乙烯聚合得到高支化度的聚乙烯,并研究了聚合条件(如AL/Ni摩尔比、聚合温度以及配体结构)对催化活性的影响,结果表明,在反应温度为25...     

镍配位催化乙烯聚合新进展

在烯烃聚合领域中,催化剂决定了所得聚合物的分子量与分布以及微观结构,进而影响聚烯烃材料的物理与机械性能。镍配合物催化乙烯聚合反应中,既会获得齐聚物也可能获得聚合物,有意思的是所得聚乙烯材料较容易呈现弹性体材料的性质。因此,加强镍配合物催化剂的研究有助于筛选更高活性和优良性能的催化剂体系,制备新型聚乙烯弹性体材料,甚至为该类乙烯聚合中试研究做铺垫。本文综述了近年来镍配合物催化乙烯聚合研究的新进展,重点讨论了配合物结构对于催化活性、热稳定性以及聚合产物微结构的影响与规律。     

空间位阻与氟效应协同增强镍系乙烯聚合

烯烃聚合在工业上是最重要的化学反应之一. 过渡金属催化剂是烯烃聚合反应发展的核心, 其中水杨醛亚胺后过渡金属中性镍催化剂由于杂质耐受性强与无需助催化剂的双重优势备受青睐. 为增强镍催化剂的催化性能, 空间位阻效应或者氟效应策略已有广泛报道; 然而将两者结合形成协同策略仍鲜有研究. 在本工作中, 对位氢和空间位阻取代基(苯基、萘基和蒽基)与邻位氟取代基被同时引入至水杨醛亚胺中性镍催化剂中, 利用空间位阻效应与氟效应来协同增强镍系乙烯聚合. 系统研究空间位阻效应、氟效应、聚合反应温度、聚合时间对乙烯聚合反应的活性、分子量、支化度的影响. 结果表明, 邻位氟取代基显著提升活性、催化剂寿命与聚合物分子量, 降低聚合物支化度; 对位空间位阻取代基的体积根据催化活性或聚合物分子量的需求而定, 但对聚合物支化度几乎无影响. 本工作发展了一种新的调控水杨醛亚胺镍烯烃聚合催化剂手段.     

水杨醛亚胺镍配合物催化的乙烯水相聚合

在含表面活性剂的水相体系中, 用一系列水杨醛亚胺镍配合物催化乙烯聚合, 得到了高分子量低支化度聚乙烯. 研究表明水杨醛亚胺镍配合物中苯环上取代基的电子效应和空间位阻对乙烯聚合活性和聚合物的分子量有所影响. 提高配合物酚氧环上取代基的吸电子性, 聚合活性相应增加, 但聚乙烯的分子量降低; 而增加苯胺环上取代基的空间位阻, 聚合活性和聚乙烯的分子量均增加. 粘度法测得由水相聚合得到的聚乙烯的分子量在10⁴～10⁵范围内. DSC测得该聚乙烯的结晶度在50%～70%之间, 熔点在115～137 ℃范围内. GPC分析表明用环辛二烯合镍[Ni(COD)₂]助催化乙烯, 聚乙烯的分子量分布随酚氧环上取代基电负性增加而从双峰到单峰变化, 动态流变学研究进一步说明了聚乙烯分子量及其分布的变化.     

负载苊二亚胺镍/烷基铝催化单一乙烯制备高支化聚乙烯

1995年,Brookhart 等人以大体积α-二亚胺为配体制备了Ni（Ⅱ）和Pd（Ⅱ）的配合物,作为乙烯聚合催化剂,能有效的抑制反应过程中的β-H消除反应,从而实现了促进链增长的目的,得到了高分子量的聚合物.这类催化体系一般是以二亚胺镍的溴化物为主催化剂,MAO作助催化剂,均相催化乙烯聚合.     

同核双金属烯烃聚合催化剂

与单核金属配合物催化剂相比,双核金属配合物催化剂所具的双金属活性中心对烯烃聚合催化活性和所得聚合物的性能(包括聚合物微结构、分子量大小和分子量分布)产生了重要影响。本文综述了双金属配合物作为均相催化剂催化乙烯聚合及共聚合的最新研究,归纳思路包括不同的金属类型,即基于前过渡金属(Zr, Ti, Hf) 和后过渡金属(Ni, Fe, Co) 的双核金属组合; 不同的配体化合物,即CGC配体、酚氧亚胺配体、氮杂环胺配体、α-二亚胺和亚胺吡啶配体等。这些研究表明,前过渡金属催化剂不仅解决了乙烯自聚还实现了乙烯与α-烯烃共聚;后过渡金属催化剂高效催化乙烯自聚合,其中铁和钴催化剂获得高度线性聚乙烯,镍催化剂则产生多支链聚乙烯。     

Single and binary catalyst systems based on nickel and palladium in polymerization of ethylene

The catalyst (N,N‐bis(2,6‐dibenzhydryl‐4‐ethoxyphenyl)butane‐2,3‐diimine)nickel dibromide, a late transition metal catalyst, was prepared and used in ethylene polymerization. The effects of reaction parameters such as polymerization temperature, co‐catalyst to catalyst molar ratio and monomer pressure on the polymerization were investigated. The α‐diimine nickel‐based catalyst was demonstrated to be thermally robust at a temperature as high as 90 °C. The highest activity of the catalyst (494 kg polyethylene (mol cat)^?1 h^?1) was obtained at [Al]/[Ni] = 600:1, temperature of 90 °C and pressure of 5 bar. In addition, the performance of a binary catalyst using nickel‐ and palladium‐based complexes was compared with that of the corresponding individual catalytic systems in ethylene polymerization. In a study of the catalyst systems, the average molecular weight and molecular weight distribution for the binary polymerization were between those for the individual catalytic polymerizations; however, the binary catalyst activity was lower than that of the two individual ones. The obtained polyethylenes had high molecular weights in the region of 10⁵ g mol^?1. Gel permeation chromatography analysis showed a narrow molecular weight distribution of 1.44 for the nickel‐based catalyst and 1.61 for the binary catalyst system. The branching density of the polyethylenes generated using the binary catalytic system (30 branches/1000 C) was lower than that generated using the nickel‐based catalyst (51/1000 C). X‐ray diffraction study of the polymer chains showed higher crystallinity with lower branching of the polymer obtained. Also Fourier transform infrared spectra confirmed that all obtained polymers were low‐density polyethylene.     

Enhancing performance of α-diiminonickel precatalyst for ethylene polymerization by substitution with the 2,4-bis(4,4'-dimethoxybenzhydryl)-6-methylphenyl group

High activities in ethylene polymerization predetermine α-diiminonickel precatalysts for potential industrial applications. In our study, we have synthesized and characterized a series of unsymmetrical 1-(2,4-bis(4,4′-dimethoxybenzhydryl)-6-MeC₆H₂N)-2-arylimino-acenaphthylene nickel(II) halides. The single-crystal X-ray diffraction study of representative compounds reveals distorted tetrahedral geometry. On activation with either Me₂AlCl or modified methylaluminoxane, these nickel complexes exhibit high activities of the order of 10⁶ g of PE (mol of Ni)⁻¹ h⁻¹ and produce polyethylene of generic application characterized by high molecular weight, narrow molecular weight distribution, and moderate degree of branching. The substituents at the ligands affect the catalytic performance of the nickel complexes and tune the microstructure of the resultant polyethylene.     

双吡唑亚胺镍/甲基铝氧烷催化降冰片烯的聚合

合成了两种双吡唑亚胺镍配合物: 双-N-(苯基-1-3,5-二甲基吡唑基亚甲基)苯基亚胺二溴化镍(Cat.1)和双-4-甲氧基-N-(苯基-1-3,5-二甲基吡唑基亚甲基)苯基亚胺二溴化镍(Cat.2). 研究了Cat.1/MAO和Cat.2/MAO催化体系对降冰片烯(NBE)单体聚合的催化性能, 考察了各种聚合条件, 如温度、Al/Ni摩尔比及催化剂浓度对降冰片烯的催化效率、单体转化率、聚合物分子量及分子量分布的影响. 研究结果表明, Cat.1/MAO和Cat.2/MAO催化体系对降冰片烯聚合具有较高的催化效率, 可达到105 g PNBE/(mol Ni)数量级, 所得聚降冰片烯(PNBE)的重均分子量在105以上, 分子量分布指数在2左右. 聚合产物的1H NMR和FTIR谱分析结果表明, 该聚合反应是以单体的乙烯基加成聚合机理进行的.     

Ethylene/1‐octene copolymerization studies with in situ supported metallocene catalysts: Effect of polymerization parameters on the catalyst activity and polymer microstructure

Ethylene and 1‐octene copolymerizations were carried out with an in situ supported rac‐[dimethylsilylbis(methylbenzoindenyl)] zirconium dichloride catalyst. In a previous study, it was found that some in situ supported metallocenes produced polyethylene/α‐olefin copolymers with broad and bimodal short chain branching distributions and narrow molecular weight distributions. The ability to produce polyolefins with multimodal microstructural distributions in a single metallocene and a single reactor is attractive for producing polymers with balanced properties with simpler reactor technology. In this study, a factorial experimental design was carried out to examine the effects of the polymerization temperature and ethylene pressure, the presence of hydrogen and an alkylaluminum activator, and the level of the comonomer in the feed on the catalyst activity, short chain branching distribution, and molecular weight distribution of the polymer. The temperature had the most remarkable effect on the polymer microstructure. At high 1‐octene levels, the short chain branching distribution of the copolymer broadened significantly with decreasing temperature. Several factor interactions, including the hydrogen and alkylaluminum concentrations, were also observed, demonstrating the sensitivity of the catalyst to the polymerization conditions. For this catalyst system, the responses to the polymerization conditions are not easily predicted from typical polymerization mechanisms, and several two‐factor interactions seem to play an important role. Given the multiple‐site nature of the catalyst, it has been shown that predicting the polymerization activity and the resulting microstructure of the polymer is a challenging task. © 2002 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 40: 4426–4451, 2002     

PREPARATION OF HIGHLY BRANCHED POLYETHYLENE WITH ACENAPHTHENEDIIMINE NICKEL CHLORIDE/DIETHYLALUMINUM CHLORIDE CATALYST

The homogeneous catalyst system [ArN = C(Nap)- C(Nap)= Nar]NiCl2 (Nap = 1,8-naphthdiyl, Ar = 2,6-diisopropylphenyl)/AlEt2Cl has been prepared and examined for ethylene polymerization. Polymerization conditions such as cocatalyst, Al/Ni molar ratio and polymerization temperature (Tp) have a great effect on catalytic activity and properties of polyethylenes (PE). The activity of 5.1 × 105g PE/mol Ni. H was obtained by the catalyst, activated with AlEt2Cl at 120 of Al/Ni ratio and 30℃. Especially, Tp had a pronounced influence on branches and molecular weight of PE. Branching degree of PE increased with increasing temperature whereas their molecular weight decreased correspondingly. At Tp lower than about 70℃, the resultant PE was an elastic material. When Tp was higher than 70℃, the product was a viscous oil. The resultant PE was confirmed by 13C-NMR to contain significant amounts of not only methyl but also ethyl, propyl, butyl,amyl, and longer branches (longer than six carbons). According to gel permeation chromatographic measurement, the weightaverage molecular weights of the polymers obtained ranged from 3.6 × 103 to 2.3 × 105.     

SYNTHESIS OF BRANCHED POLYETHYLENE USING (α-DIIMINE)NICKEL(Ⅱ) -TiCl4 COMBINED AND SUPPORTED CATALYST

(a-Diimine)nickel(Ⅱ) {[C6H5 - N = C(CH3) - C(CH3) = N - C6H5]NiBr2}-TiCl4 abbreviated as NiL-TiCl4combined catalyst which is supported on MgCl2-SiO2 carrier has been prepared, by using alkyl aluminum (AlR3) as the cocatalyst in place of methylaluminoxane (MAO) to catalyze ethylene oligomerization and copolymerization in situ. The influences of procedure for supporting NiL-TiCl4, the molar ratio of NiL to TiCl4, cocatalyst type and polymerization temperature on the catalytic performance were studied. The degree of branching and the composition of the branched chain of polymers produced have been investigated by IR and 13C-NMR spectra. The results show that the combined catalyst can synthesize the branched polyethylene with various banched chains .The polymerization reaction was monitored by gas chromatography and mass spectrometry (GC-MS). The results show that this catalyst promotes the oligomerization and copolymerization in situ for ethylene.     

双组分茂金属催化剂催化乙烯聚合的研究

选择能形成支链的不对称桥联茂金属化合物Me2 C[(Cp) (Ind) ]ZrCl2 和非桥联的不同结构的茂金属化合物二氯二 (烯基取代环戊二烯 )锆如 ( Cp) 2 ZrCl2 ,(Cp) 2 ZrCl2 和 (Cp) 2 ZrCl2 ,以MAO为助催化剂 ,分别组成三组双组分茂金属催化剂的催化体系 ,催化乙烯聚合 .结果表明 ,两类催化剂组成的双组分茂金属催化体系催化乙烯聚合能得到支化的宽分子量分布的聚乙烯 ;聚合温度和改变两种茂金属催化剂的摩尔比对催化活性和分子量有很大影响 .因此可以利用改变双组分茂金属催化剂的摩尔比例和聚合温度来调控聚合物的分子量和分子量分布 .改变两种茂金属催化剂的摩尔比和聚合温度也能使聚合物的结晶度发生改变     

Synthesis of long‐chain‐branched polyethylene by ethylene homopolymerization with a novel nickel(II) α‐diimine catalyst

Long‐chain‐branched polyethylene with a broad or bimodal molecular weight distribution was synthesized by ethylene homopolymerization via a novel nickel(II) α‐diimine complex of 2,3‐bis(2‐phenylphenyl)butane diimine nickel dibromide ({[2‐C₆H₄(C₆H₅)]? N?C? (CH₃)C(CH₃)?N? [2‐C₆H₄(C₆H₅)]}NiBr₂) that possessed two stereoisomers in the presence of modified methylaluminoxane. The influences of the polymerization conditions, including the temperature and Al/Ni molar ratio, on the catalytic activity, molecular weight and molecular weight distribution, degree of branching, and branch length of polyethylene, were investigated. The resultant products were confirmed by gel permeation chromatography, gas chromatography/mass spectrometry, and ¹³C NMR characterization to be composed of higher molecular weight polyethylene with only isolated long‐branched chains (longer than six carbons) or with methyl pendant groups and oligomers of linear α‐olefins. The long‐chain‐branched polyethylene was formed mainly through the copolymerization of ethylene growing chains and macromonomers of α‐olefins. The presence of methyl pendant groups in the polyethylene main chain implied a 2,1‐insertion of the macromonomers into [Ni]? H active species. © 2005 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 43: 1325–1330, 2005