用于乙烯齐聚高选择性制 1-辛烯反应的Cr(Ⅲ)基催化剂体系

将四元催化剂体系(乙酰丙酮铬-膦胺型配体-助催化剂甲基铝氧烷-促进剂六氯乙烷)用于乙烯齐聚制1-辛烯反应,考察了促进剂、助催化剂、Al/Cr摩尔比、反应温度和反应压力等对催化剂的活性和1-辛烯的选择性的影响.结果表明,该四元催化剂体系比三元催化剂体系(铬化合物-膦胺型配体-甲基铝氧烷)对乙烯齐聚反应具有更高的1-辛烯选择性.产物除有1-辛烯外,还有较大量的1-己烯、甲基环戊烷和亚甲基环戊烷.甲基铝氧烷是高选择性生成1-辛烯必不可少的助催化剂.作为促进剂的六氯乙烷可以使乙酰丙酮铬更有利于催化乙烯齐聚反应生成1-辛烯.     

气相色谱法测定1-己烯的纯度

介绍了乙烯齐聚合成1.己烯产品的分析方法,采用校正面积归一法测定组份的含量,相对标准偏差小于1%.     

吡啶亚胺基酞菁镍系催化剂催化乙烯齐聚性能及其动力学研究

以四氨基镍酞菁、吡啶-2-甲醛和NiCl2·6H2O为原料,先后经过席夫碱反应和络合反应得到一种新型吡啶亚胺基酞菁配体及其镍系催化剂。合成产物的结构通过红外光谱(FTIR)、紫外(UV-Vis)、核磁共振氢谱(¹H-NMR)、电感耦合等离子体质谱(ICP-MS)、同步热分析(TG-DSC)及电喷雾电离质谱(ESI-MS)等方法进行表征。对其催化乙烯齐聚性能进行考察,并研究了该反应的动力学。催化乙烯齐聚实验结果表明,当溶剂为环己烷、助催化剂为甲基铝氧烷(MAO)、催化剂用量为5μmol/L、齐聚压力为1.0 MPa、齐聚温度为35℃、Al/Ni摩尔比为500时,吡啶亚胺基酞菁镍系催化剂的活性可达8.82×10⁵ g/(mol Ni·h),丁烯和己烯的含量分别为58.22%和39.85%。对吡啶亚胺基酞菁镍系催化剂催化乙烯齐聚反应动力学方程进行拟合计算,结果表明该反应对催化剂摩尔浓度的反应级数为1.24,对齐聚压力的反应级数为0.95,当活性中心的浓度为5μmol/L、齐聚压力为1.0 MPa、齐聚温度为5～35℃时,该反应的表观活化能为71.4...     

乙烯齐聚过程生成癸烯的催化体系研究进展

癸烯作为有机合成的基础原料,是现代化工生产中不可或缺且用量逐年增加的长链烯烃之一,目前工业上还没有一条采用乙烯齐聚法直接生产癸烯的工艺路线。乙烯通过齐聚反应可以制备长链烯烃,本文针对乙烯齐聚生成癸烯的反应,详细地阐述了国内外Cr催化体系的研究现状和取得的研究成果,包括催化剂的结构对产物癸烯选择性的影响、乙烯齐聚过程中发生乙烯、己烯共聚生成癸烯的聚合反应机理等;同时阐述了用于乙烯齐聚反应的Ni催化体系的研究现状,包括催化剂的结构与癸烯选择性之间的关系,配体树枝状大分子的结构对癸烯选择性的影响等。此外,还介绍了Fe、Ti、Zr等其他催化体系在催化乙烯齐聚生成癸烯方面所取得的研究进展,目的是为开发癸烯催化剂提供理论依据。     

超支化铬系催化剂的合成及乙烯齐聚性能研究

以正辛胺和十二胺为原料,分别制备了两种超支化PNP配体,通过引入金属铬活性位点的方法合成了具有不同烷基链长度的超支化PNP铬系催化剂.采用红外光谱(IR)、核磁共振磷谱(~(31)P-NMR)、核磁共振氢谱(~1H-NMR)、紫外光谱(UV)和质谱(MS)等表征方法证明合成催化剂的结构与理论结构预测相符.详细考察了催化剂用量、溶剂种类、反应条件以及配合物结构对乙烯齐聚性能的影响.实验结果显示,超支化PNP铬系催化剂在甲苯作溶剂,甲基铝氧烷(MAO)做助催化剂时表现出良好的催化乙烯齐聚性能,产物主要为低碳烯烃.在最佳条件下,催化活性最高可达到1.69×10~5 g·(mol Cr·h)~(-1),己烯和辛烯的选择性为43.3%以上.相同聚合条件下,其催化活性随着端基烷基链长度的增加而下降.     

基于[PNP]配体的铬催化剂体系选择性催化乙烯齐聚的研究进展

乙烯选择性三聚和四聚催化反应为制备1-己烯和1-辛烯提供了重要途径.在报道和披露的众多结构和组成的催化剂体系中,我们选择[PNP]配位骨架的铬催化剂体系,对其发展和应用进行了综述.论文以结构与催化性能的关联性为主线,阐述[PNP]骨架以及N和P上取代基的电子和立体空间效应对催化性能的影响.从目前的研究态势来看,[PNP]配位骨架的铬催化剂体系在乙烯选择性齐聚生产1-辛烯等线性α-烯烃方面具有发展潜力.     

基于5-氨基邻甲酚的膦配体的合成及在乙烯齐聚中的应用

以5-氨基邻甲酚与二苯基氯化膦为原料,通过取代反应合成了一种含有PNP和P—O结构的膦配体并确定了其结构.通过与Cr(acac)_3原位生成以及与Cr Cl3(THF)_3预制的方法制成配合物作为主催化剂,以甲基铝氧烷(MAO)为助催化剂,形成催化体系用于催化乙烯齐聚反应,考察了溶剂种类、反应温度、反应压力及Al/Cr摩尔比对该催化剂的活性和选择性的影响,并与原位生成的邻位和对位氨基酚类膦配体催化体系催化乙烯齐聚反应效果进行了对比.试验结果表明,以环己烷为溶剂,MAO为助催化剂,当反应温度为50℃、反应压力为2.5 MPa、Al/Cr摩尔比为700的条件下,该催化剂的活性最高达5.91×10~6 g/(mol·Cr·h),液相产物中1-辛烯选择性高达72.94%,1-己烯和1-辛烯总的选择性为82.11%.     

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.     

TiCl4/XROH/MgCl2/Et3Al催化剂合成宽分子量分布乙烯/1-己烯共聚物

采用MgCl₂负载TiCl₄及1,3-二氯-2-丙醇给电子体(XROH),与三乙基铝助催化剂组成的催化剂体系,合成了1-己烯共聚率高且宽分子量分布的乙烯/1-己烯共聚物。 讨论了催化体系的组成、配比和聚合条件对乙烯/1-己烯共聚合行为,共聚物结构、分子量及分子量分布的影响。 结果表明,n(Ti)∶n(Mg)=10∶1,n(XROH)∶n(MgCl₂)=2.6∶1,n(Al)∶n(Ti)=100∶1,乙烯压力0.45 MPa,聚合温度80 ℃,聚合时间2 h,共聚单体(1-hexene)浓度0.25 mol/L时,催化效率达23.2 kg/g cat。 采用¹³C NMR、X-ray、SEM、WAXD、DSC、GPC等测试技术对催化剂、共聚物的结构进行了表征。 结果表明,在Zieglar-Natta(Z-N)催化体系中,给电子体多卤代醇与TiCl4结合,载体MgCl2的晶体结构发生了变化。 结晶度降低,有利于催化剂负载量的提高(ω(Ti)=4.8%)和催化效率增大。 催化体系产生了多种活性中心,使聚烯烃分子量分布变宽(15~20)。 多卤代醇还可增强1-己烯与乙烯的共聚能力,在共聚物中1-己烯的摩尔分数达5.1%。     

氮配位单茂金属烯烃聚合催化剂

本文综述了近些年来以含氮基团为阴离子配体的单茂金属化合物作为烯烃精确聚合的催化剂的研究。氮配位单茂金属催化剂在烯烃聚合中显示出独特的特性,特别是对于乙烯的共聚合,不仅能得到Ziegler-Natta催化剂和传统茂金属催化剂不能合成的新的共聚物,还有优于其他单茂金属催化剂的共聚活性。环戊二烯基和含氮阴离子配体的改性是所得催化剂聚合效果的关键。本文涉及了乙烯均聚以及乙烯与α-烯烃(己烯-1、辛烯-1等)、苯乙烯和环烯烃(降冰片烯、四环十二碳烯等)的共聚合。     

环氧乙烷和环氧丙烷开环聚合*

环氧乙烷和环氧丙烷的开环聚合产物在表面活性剂工业和聚氨酯工业得到了极为广泛的应用.本文综述了近几年来发展的用于环氧乙烷和环氧丙烷开环聚合的各类催化剂体系,分别讨论了各类催化剂体系对环氧乙烷和环氧丙烷的不同作用机制,考察了反应物结构对反应活性和选择性的影响,重点介绍了配位络合催化剂体系在环氧乙烷和环氧丙烷开环聚合反应中的应用,并指出了今后研究的方向.     

Kinetics of ethylene polymerization reactions with chromium oxide catalysts

Principal kinetic data are presented for ethylene homopolymerization and ethylene/1‐hexene copolymerization reactions with two types of chromium oxide catalyst. The reaction rate of the homopolymerization reaction is first order with respect to ethylene concentration (both for gas‐phase and slurry reactions); its effective activation energy is 10.2 kcal/mol (42.8 kJ/mol). The r₁ value for ethylene/1‐hexene copolymerization reactions with the catalysts is ～30, which places these catalysts in terms of efficiency of α‐olefin copolymerization with ethylene between metallocene catalysts (r₁ ～ 20) and Ti‐based Ziegler‐Natta catalysts (r₁ in the 80–120 range). GPC, DSC, and Crystaf data for ethylene/1‐hexene copolymers of different compositions produced with the catalysts show that the reaction products have broad molecular weight and compositional distributions. A combination of kinetic data and structural data for the copolymers provided detailed information about the frequency of chain transfer reactions for several types of active centers present in the catalysts, their copolymerization efficiency, and stability. © 2008 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 46: 5315–5329, 2008     

Hydrosilylation of ethylene

Hydrosilylation of ethylene with trialkoxysilanes in the presence of Pt(0) complexes as catalysts affords ethyltrialkoxysilanes in almost quantitative yields. No impurities of vinyltrialkoxysilanes were detected. Experiments and ab initio calculations showed that the Pt(0) catalysts are considerably more active in ethylene hydrosilylation than Pt(II) catalysts.     

乙烯齐聚合成线性 α-烯烃镍系催化剂

利用SHOP型工艺由乙烯齐聚制备线性α-烯烃不仅具有工业应用价值，而且具有很高的学术意义。SHOP型工艺的工业化引起了人们对基于P^∩O配位型及其他配位型镍催化剂的广泛的研究兴趣。镍系催化剂具有活性高、选择性好、产品分布可调、反应条件温和等优良性能。本文介绍了镍系催化剂的类型和性能等，并对影响催化性能的因素进行了分析。     

过渡金属乙烯齐聚与聚合催化剂研究进展

综述了近年来过渡金属配合物催化乙烯齐聚与聚合的最新进展;介绍了乙烯齐聚或聚合的反应时间、反应温度、乙烯压力、助催化剂用量等反应条件及配体上不同取代基对前过渡金属(铬,锆,钛,钒)和后过渡金属(铁,钴,镍,铜)配合物的催化活性和齐聚或聚合产物的影响;分别以钛和镍配合物催化剂为例,介绍了前过渡金属和后过渡金属催化乙烯齐聚或聚合的机理。     

纳米Cr2O3系列催化剂上CO2氧化乙烷脱氢制乙烯反应

 采用溶胶－凝胶法和共沸蒸馏法耦合技术制备了纳米Cr2O3催化剂，并采用共沉淀法和共沸蒸馏法耦合技术制备了纳米Cr2O3／Al2O3，Cr2O3／ZrO2和Cr2O3／MgO复合催化剂．应用BET，XRD，XPS，TPR和TEM等物理化学方法对催化剂的结构和物化性质进行了表征，并考察了该系列催化剂上CO2氧化乙烷脱氢制乙烯的反应性能．结果表明，纳米Cr2O3催化剂上乙烷和CO2的转化率均明显高于常规Cr2O3催化剂，但乙烯的选择性低于常规Cr2O3催化剂；纳米复合催化剂中的复合成分显著影响催化剂的催化性能．其中，10％Cr2O3／MgO纳米复合催化剂在温度为973K时，乙烷转化率和乙烯选择性分别可达到61．54％和94．79％．纳米催化剂表面Cr的还原性以及Cr6＋／Cr3＋比值是影响乙烷转化率和乙烯选择性的重要因素．     

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.     

Kinetics of propylene and ethylene polymerization reactions with heterogeneous ziegler-natta catalysts: Recent results

The article discusses recent results of kinetic analysis of propylene and ethylene polymerization reactions with several types of Ti-based catalysts. All these catalysts, after activation with organoaluminum cocatalysts, contain from two to four types of highly isospecific centers (which produce the bulk of the crystalline fraction of polypropylene) as well as several centers of reduced isospecificity. The following subjects are discussed: the distribution of active centers with respect to isospecificity, the effect of hydrogen on polymerization rates of propylene and ethylene, and similarities and differences between active centers in propylene and ethylene polymerization reactions over the same catalysts. Ti-based catalysts contain two families of active centers. The centers of the first family are capable of polymerizing and copolymerizing all α-olefins and ethylene. The centers of the second family efficiently polymerize only ethylene. Differences in the kinetic effects of hydrogen and α-olefins on polymerization reactions of ethylene and propylene can be rationalized using a single assumption that active centers with alkyl groups containing methyl groups in the β-position with respect to the Ti atom, Ti-CH(CH₃)R, are unusually unreactive in olefin insertion reactions. In the case of ethylene polymerization reactions, such an alkyl group is the ethyl group (in the Ti-C₂H₅ moiety) and, in the case of propylene polymerization reactions, it is predominantly the isopropyl group in the Ti-CH(CH₃)₂ moiety. Published in Russian in Vysokomolekulyarnye Soedineniya, Ser. A, 2008, Vol. 50, No. 11, pp. 1911–1934. The text was submitted by the authors in English.     

Living copolymerization of ethylene with norbornene catalyzed by bis(pyrrolide-imine) titanium complexes with MAO

Bis(pyrrolide-imine) Ti complexes in conjunction with methylalumoxane (MAO) were found to work as efficient catalysts for the copolymerization of ethylene and norbornene to afford unique copolymers via an addition-type polymerization mechanism. The catalysts exhibited very high norbornene incorporation, superior to that obtained with Me(2)Si(Me(4)Cp)(N-tert-Bu)TiCl(2) (CGC). The sterically open and highly electrophilic nature of the catalysts is probably responsible for the excellent norbornene incorporation. The catalysts displayed a marked tendency to produce alternating copolymers, which have stereoirregular structures despite the C(2) symmetric nature of the catalysts. The norbornene/ethylene molar ratio in the polymerization medium had a profound influence on the molecular weight distribution of the resulting copolymer. At norbornene/ethylene ratios larger than ca. 1, the catalysts mediated room-temperature living copolymerization of ethylene and norbornene to form high molecular weight monodisperse copolymers (M(n) > 500,000, M(w)/M(n) < 1.20). (13)C NMR spectroscopic analysis of a copolymer, produced under conditions that gave low molecular weight, demonstrated that the copolymerization is initiated by norbornene insertion and that the catalyst mostly exists as a norbornene-last-inserted species under living conditions. Polymerization behavior coupled with DFT calculations suggested that the highly controlled living polymerization stems from the fact that the catalysts possess high affinity and high incorporation ability for norbornene as well as the characteristics of a living ethylene polymerization though under limited conditions (M(n) 225,000, M(w)/M(n) 1.15, 10-s polymerization, 25 degrees C). With the catalyst, unique block copolymers [i.e., poly(ethylene-co-norbornene)(1)-b-poly(ethylene-co-norbornene)(2), PE-b-poly(ethylene-co-norbornene)] were successfully synthesized from ethylene and norbornene. Transmission electron microscopy (TEM) indicated that the PE-b-poly(ethylene-co-norbornene) possesses high potential as a new material consisting of crystalline and amorphous segments which are chemically linked.     

Asymmetric Cationic [P,O] Type Palladium Complexes in Olefin Homopolymerization and Copolymerization

Metal‐catalyzed ethylene homopolymerization and ethylene‐polar monomer copolymerization to produce new kinds of polyolefins with novel microstructures are of great interest. So far, there are some disadvantages for traditional transition metal catalyst systems. Therefore, it is critical to develop new catalysts or alternative strategies. In recent years, some cationic [P, O] palladium complexes have been demonstrated with the abilities to obtain oligomers and the high molecular weight polymers. Most importantly, these complexes showed high activity and generated polymers with specific microstructures when used for copolymerization of ethylene with industrially relevant polar monomers. This review summarizes several types of high performance cationic [P, O] palladium catalysts in ethylene oligomerization, ethylene homopolymerization and the copolymerization of ethylene with polar monomers. Specially, the regulation of steric and electronic effects at specific sites of the metal complexes was focused.