后过渡金属配合物催化乙烯齐聚与聚合的研究进展

后过渡金属配合物催化乙烯齐聚和聚合研究,不仅拓展了后过渡金属配合物的应用 ,而且为探求烯烃聚合催化剂提供了新机遇,成为当前催化研究中的热点课题.本文综述了后过渡金属铁、钴、镍配合物催化乙烯齐聚和聚合的国内外最新研究进展.     

镍配合物催化乙烯齐聚和聚合的进展

继SHOP催化体系采用镍配合物催化乙烯齐聚制备端烯烃在研究和应用中获得成功以来,由于后过渡金属上容易产生β-氢消除反应,镍配合物催化乙烯的研究搁置了近二十年。然而,近十年里,镍配合物催化乙烯齐聚和聚合研究再次受到催化剂研究者的重视,进入了飞速发展的新时期。本文综述近三年间这个领域的发展,特别是我国学者在这个领域的贡献,展示了镍配合物在乙烯齐聚和乙烯聚合制备支化聚烯烃中的巨大潜力,促进该领域研究的发展。     

后过渡金属催化乙烯齐聚与聚合进展

石化工业最重要的产品是聚烯烃,其中大部分与聚乙烯相关,α-烯烃不仅是重要的共聚单体,也是精细化工的基本原料,乙烯工业发展程度代表了一个国家石化技术的水平。后过渡金属催化剂作为新型催化体系,能够高效催化乙烯齐聚和聚合,并且乙烯聚合可制备新型聚乙烯树脂。通过对配体的修饰,提高后过渡金属配合物催化活性,增加催化体系的热稳定性,仍然是当前催化剂设计的重要课题;实现对所得聚乙烯微观结构的控制,提高聚烯烃宏观性质是产业化的重要基础。本文基于配合物催化剂配体骨架设计为基础,集中讨论了铁、钴和镍配合物用于乙烯聚合和齐聚的性质比较;特别是集中展示了我们近期研究工作,综述了后过渡金属催化剂的新进展。     

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。     

乙烯齐聚催化剂研究进展

综述了乙烯齐聚催化剂的研究进展.按照碳链的原子数目,简要介绍了α-烯烃的用途.按照后过渡金属催化剂和前过渡金属催化剂分类介绍了乙烯齐聚催化剂的研究情况,并重点介绍了乙烯三聚催化剂的研究进展,给出了部分聚合机理.文章最后介绍了α-烯烃除用乙烯齐聚催化剂方法外,还有石蜡热裂解、烷烃催化裂解、烷烃脱氢、烯烃二聚和歧化等方法制备.乙烯齐聚法所得产品线性化程度高,聚合度分布窄,分离费用低,产品质量好.在我国,石蜡裂解法为主要生产方法,因此在我国开展乙烯齐聚的研究,开发具有自主知识产权的齐聚催化剂,具有十分重要的意义.     

Ind2Zr(OC6H4Me-P)2和EtnAICL3-n催化乙烯齐聚的研究

茂金属催化剂 ( Kaminsky催化剂 )是 80年代发展起来的烯烃聚合高效催化剂 [1] ,有关其催化烯烃聚合的研究很多 [2～ 4 ] .近年来 ,Kaminsky型催化剂催化乙烯齐聚合成低碳α烯烃的研究已有报道 [5] .由乙烯齐聚得到的直链低碳α烯烃是生产线性低密度聚乙烯 ( LL DPE)和高密度聚乙烯 ( HDPE)的共聚单体 .以茚基锆化合物与烷基铝组成的 Ziegler- Natta催化体系催化乙烯齐聚尚未见报道 .本文考察了Ind2 Zr( OC6H4 Me- p) 2 和各种乙基铝组成的二元催化体系对乙烯齐聚的催化性能 .1　实验部分　　二茚基锆配合物 Ind2 Zr Cl2 和 Ind2 …     

镍配合物催化乙烯低聚/聚合的研究进展

催化乙烯低聚或聚合的镍配合物催化剂研究,不仅帮助提供探索乙烯配位聚合机理的催化剂模型,更为重要的帮助探讨不同催化剂模型下的催化剂活性和选择性,为工业界寻找具有潜在应用价值的高效催化剂奠定基础.同时,利用镍配合物催化剂容易导致所得聚烯烃树脂产生支链的特点,有望制备具有优异性能的支化聚烯烃树脂.本文综述了近年来镍配合物在乙烯低聚或聚合催化剂研究方面的进展,并特别强调了催化剂结构和催化性能之间的内在规律.     

膦胺铬和双膦铬催化乙烯选择性齐聚研究进展

乙烯选择性齐聚制备线性α-烯烃是在学术界和工业界均受到高度重视,具有目标产物选择性高、产品易分离和经济效益显著等特点。铬系配合物催化剂在催化乙烯选择性齐聚反应中综合性能较好,有良好的发展和应用前景。近年来的研究表明,配体结构对催化剂性能有重要影响;反应体系中通入H 2可以改善齐聚产物的分布并抑制低聚物的生成;开发不以甲基铝氧烷为助催化剂的催化体系可降低催化剂成本;而乙烯选择齐聚机理及金属中心氧化态对催化剂的设计有重要的指导意义。本文主要从以上几个方面介绍了膦胺铬和双膦铬配合物在催化乙烯选择性齐聚中的研究进展,分析了目前乙烯选择性四聚工业化急需解决的问题,展望了该领域未来的发展方向。     

树状PAMAM改性纳米二氧化硅负载镍催化剂的制备及催化乙烯齐聚性能

以纳米二氧化硅为载体,树状聚酰胺-胺(PAMAM)镍络合物为催化活性中心,通过共价负载制备了一种具有良好催化活性和循环利用性的PAMAM改性纳米二氧化硅负载镍催化剂(化合物G).采用元素分析、傅里叶变换红外光谱(FTIR)、 X射线衍射(XRD)和扫描电子显微镜(SEM)表征了化合物G的组成及形貌.研究了该类负载镍催化剂催化乙烯齐聚的性能,考察了齐聚条件对其性能的影响.结果表明,化合物G具有良好的催化乙烯齐聚活性和循环利用性.基于灰色关联分析得出反应压力是影响乙烯齐聚活性的最主要因素,反应温度是影响乙烯齐聚选择性的最主要因素.当以甲基铝氧烷(MAO)为助催化剂,反应压力0.7 MPa, n(Al)/n(Ni)为500,反应温度为35℃,主催化剂用量为5μmol时,化合物G催化乙烯齐聚活性为3.75×105 g/(mol Ni·h),齐聚产物中C4～C8烯烃选择性为94.98%.化合物G的树状效应使其金属负载量、催化乙烯齐聚活性和C8烯烃的选择性均高于氨基化改性纳米二氧化硅负载镍(化合物E);且化合物G经3次回收循环使用后,催化乙烯齐聚活性为3.12×105 g/(mol Ni·h),齐...     

苯并咪唑类过渡金属配合物:新型乙烯齐聚与聚合催化剂

苯并咪唑杂环具有良好的配位选择性,能与多种金属形成配合物.这些配合物往往具有优良的生理、荧光、催化等性能.综述了近年来含有苯并咪唑衍生物的过渡金属配合物的合成方法及其在催化乙烯齐聚和聚合方面的研究进展,并讨论了配合物的结构因素如取代基的电子效应、位阻效应等对配合物催化性能的影响规律.     

The mechanism of ethylene polymerization by nickel salicylaldiminato catalysts - Agostic interactions and their kinetic isotope effects

The ethylene polymerization reaction of a neutral nickel catalyst was studied by DFT calculations at the Becke3LYP/6-31G(d) level of theory. As in related cases a β-agostic bond stabilizes the nickel alkyl ground states. Transition states for the insertion of the olefin show a distinct α-agostic interaction, which has not been observed for late metal polymerization catalysts before. An ethylene-alkyl complex was identified as the resting state of the reaction. The overall barrier height of the reaction amounts to 17.54 kcal/mol, which slightly increases to 17.60 kcal/mol for the polymerization of deuterated ethylene. Therefore, a small positive kinetic isotope effect (k_H/k_D = 1.09) can be calculated, which is caused by the α-agostic interaction in the transition state. A comparison to other late metal based polymerization systems reveals that the ethylene coordination step of highly active catalysts is significantly lower in energy compared to catalysts which are only moderately active.     

Reactor blending with early/late transition metal catalyst combinations in ethylene polymerization

Ethylene is polymerized by heterobimetallic combinations of early and late transition metal catalysts. Dual combinations of zirconocenes and cationic nickel and iron catalysts with multidentate nitrogen‐donor ligands are described. Reactor blends of linear and branched ethylene homopolymers are obtained. With zirconocene / nickel complex catalyst combinations, addition of hydrogen selectively reduces the molecular weight of the linear polyethylene formed by the metallocene catalyst.     

Effect of catalyst transition metal and ancillary ligand on syndiospecific polymerization of styrene

In the coordination polymerization of styrene, selected transition metal complexes of metals other than group 4 elements and non-metallocenes have been investigated in comparison to a known half-metallocene titanium complex with regard to the catalytic activity as well as to the thermal and molecular properties of the polymers synthesized. Whereas iron catalysts lead to syndiotactic polystyrenes, catalysts with nickel as the transition metal result only in atactic polymers with an enhanced isotactic content.In addition to the influence of the transition metal, the effect of a broad variation of the ancillary ligands of a specific half-sandwich titanocene, octahydrofluorenyl titanium trimethoxide, on polymerization activity and polymer properties has been investigated and discussed in detail.     

Design of Thermally Stable Amine–Imine Nickel Catalyst Precursors for Living Polymerization of Ethylene: Effect of Ligand Substituents on Catalytic Behavior and Polymer Properties

Nickel complexes bearing amine–imine ligands with various backbone substituents were synthesized and employed as ethylene polymerization catalysts on activation with Et₂AlCl. The substituent on the backbone carbon atom of the amine moiety is decisive for the living nature of ethylene polymerization. A bulky amine–imine nickel precursor with a tert‐butyl group on the carbon atom of the amine group can polymerize ethylene in a living fashion at an elevated temperature of 65 °C, which is the highest temperature of living polymerization of ethylene with late transition‐metal catalysts. The wide applicable temperature range for living polymerization and sensitivity of the branch structure of the polyethylene to temperature enable precise synthesis of di‐ and triblock polyethylenes featuring different branched segments by sequential tuning of the polymerization temperature.     

乙酰基萘酚钛配合物[O,O]_nTiCl_(4-n)的合成、负载及催化乙烯聚合反应的研究

合成一类新型非茂钛 乙酰基萘酚钛配合物 [O ,O]nTiCl4 n,该系列催化剂可在较温和的条件下催化乙烯聚合 ,其催化活性在 10 4gPE (molTi·h)左右 ;由于配合物在溶剂中存在缔合现象 ,是导致活性降低和产物分子量分布加宽 .通过将乙酰基萘酚钛配合物 [O ,O]nTiCl4 n负载到MgCl2 上 ,可以大大提高催化活性 ,使之达到 10 6 gPE (molTi·h)以上 .负载后的催化剂反应平稳 ,寿命较长 .而且反应的铝钛比较低 ,并可以使用烷基铝作助催化剂 .负载催化剂所得的聚合物分子量要高于均相所得聚合物分子量 ,且分子量分布变窄 .用粉末X 衍射考察了负载催化剂的结构 .通过X 射线光电子能谱的分析 ,考察负载前后钛、镁、氯元素的电子结合能变化对催化乙烯聚合活性的影响 .     

A Self‐Supporting Strategy for Gas‐Phase and Slurry‐Phase Ethylene Polymerization using Late‐Transition‐Metal Catalysts

The polyolefin industry is dominated by gas‐phase and slurry‐phase polymerization using heterogeneous catalysts. In contrast, academic research is focused on homogeneous systems, especially for late‐transition‐metal catalysts. The heterogenization of homogeneous catalysts is a general strategy to provide catalyst solutions for existing industrial polyolefin synthesis. Herein, we report an alternative, potentially general strategy for using homogeneous late‐transition‐metal catalysts in gas‐phase and slurry‐phase polymerization. In this self‐supporting strategy, catalysts with moderate chain‐walking capabilities produced porous polymer supports during gas‐phase ethylene polymerization. Chain walking, in which the metal center can move up and down the polymer chain during polymerization, ensures that the metal center can travel along the polymer chain to find suitable sites for ethylene enchainment. This strategy enables simple heterogenization of catalysts on solid supports for slurry‐phase polymerization. Most importantly, various branched ultra‐high‐molecular‐weight polyethylenes can be prepared under various polymerization conditions with proper catalyst selection.