Ziegler-Natta配位聚合反应机理的量子化学研究——Cossee机理中活性中心的构型及其有关的关键步骤

 本文采用ASED-MO理论对丙烯聚合的 Ziegler-Natta 催化过程的机理进行了理论研究。按照Cossee机理进行计算,得到了和实验事实基本一致的结果。认为该机理基本上是合理的,并对其中的关键步骤进行了理论解释,而对其中一些尚有争论的问题,如催化中心的稳定构型、丙烯分子和活性中心之间的配位作用、链增长过程和催化循环等问题提出了自己的见解。     

桥联茂钛配合物催化丙烯聚合反应选择性的理论研究

采用密度泛函方法对3种不同类型的硅桥联茂钛配合物[Me_2SiN(Me_4Cp)TiCl_2(A),Me_2SiCpFluTiCl_2(B)及Me_2SiInd_2TiCl_2(C)]催化丙烯聚合反应的选择性进行了理论研究.计算结果表明,硅桥联茂金属配体的空间结构是其催化烯烃聚合反应的区域选择性和立体选择性的主要原因.聚合过程中,α-烯烃配位有1,2插入(一级插入)和2,1插入(二级插入)2种方式,3种硅桥联茂金属催化剂均表现为烯烃的一级插入,这种区域选择性与催化剂硅桥联配体的刚性结构密切相关.对烯烃聚合反应链增长机理进行了理论计算,结果表明,具有Cs对称性的Me_2SiN(Me_4Cp)TiCl_2和Me_2SiCpFluTiCl_2催化丙烯聚合分别得到无规立构和间规立构的聚烯烃产物,而具有C_2对称性的Me_2SiInd_2TiCl_2催化丙烯聚合得到等规立构的聚烯烃产物,与实验结果一致.     

无外给电子体的Ziegler-Natta丙烯聚合复相催化剂研究进展

从新型给电子体、催化剂性能、活性中心模型、催化和聚合机理研究及理论模拟这了无外给电子体的Ｚｉｅｇｌｅｒ－Ｎａｔｔａ丙烯聚合复相催化剂的研究进展。     

Catalytic reactions of C4 hydrocarbons on the fluid catalytic cracking catalyst

利用小型固定流化床实验装置,对C4烃类在催化裂化催化剂上催化转化反应规律进行了实验研究,考察了不同反应温度及空速对C4烃类催化转化反应的产物分布和组成的影响。实验结果表明,催化裂化催化剂对C4烃类具有一定芳构化和裂化性能,在适宜的反应条件下,可增产芳烃和丙烯;在C4烃类催化转化过程中,丁烯是主要的反应物,而丁烷几乎不反应;低反应温度有利于增产芳烃,高反应温度有利于增产丙烯。较低的空速对增产芳烃和丙烯都有利。根据双分子反应机理和反应结果,建立了C4烃类在催化裂化催化剂上催化转化过程的反应网络。对C4烃类催化转化历程分析表明,中间产物碳五和碳六烯烃较弱的二次裂化性能是C4烃类在催化裂化催化剂上催化转化过程中乙烯和丙烯产率较低的主要原因。     

Ni-Al二元催化体系的原位核磁共振研究

1.概述 本世纪50年代Ziegler-Natta催化体系的发现使均相络合催化研究得到突飞猛进的发展。各种各样的Ziegler-Natta催化剂已广泛被用于烯烃聚合的工业生产中。与此同时对此催化剂的作用机理和催化活性物种也做了大量的研究。在提出的许多机理中,虽然金属氢化物机理在理论上已越来越多地被人们所接受,但仍需有新的更使人信服的实验来证实。 1971年Jones在研究Ni(acac)_2和Et_2AlOEt组成的催化剂催化丙烯齐聚反应时提出了氢化物机理;1979年Keim在用镍络合物作为丙烯齐聚催化剂时,曾指出其反应过     

丙烯直接环氧化Cu基催化剂的研究进展与挑战

作为一种重要的化工原料,环氧丙烷年产量近千万吨,然而目前工业上制备环氧丙烷的方法仍然面临着成本高、副产物多以及污染严重等问题。直接氧气氧化法进行丙烯环氧化因为具有原子经济、环保等优点受到了越来越多的关注。但是,催化过程中丙烯的α-H和环氧丙烷都具有很高的活性,使得在高转化率的条件下提升环氧丙烷选择性成为一个巨大的挑战。研究者们发现相较于其他币族金属,Cu基催化剂表现出更优异的丙烯直接环氧化反应性能。本综述总结梳理了近年来关于Cu基催化剂催化丙烯直接环氧化反应的研究成果,聚焦于Cu基催化剂改性方法,并对Cu基催化剂依然存在的问题和挑战进行深入探讨。     

External Electron Donor Technology in the Preparation of Polypropylene

从外给电子体在聚丙烯制备中的作用出发,从外给电子体种类、外给电子体对活性中心的影响和外给电子体的作用机理等方面,综述了丙烯聚合催化体系中外给电子体技术的研究进展,重点介绍了外给电子体的位阻效应和电子效应对丙烯聚合催化体系的影响,指出了性能优异的外给电子体应具备的结构特征,即带有大位阻烃类取代基和小位阻烷氧基取代基的硅烷类化合物,介绍了复合外给电子体技术和丙烯共聚中外给电子体的作用,并对聚丙烯制备中外给电子体技术的发展趋势进行了展望。     

含钼体系的极谱催化波的研究进展

近年来,许多学者研究过渡金属和氧化剂的络合物溶液的极谱催化电流。其中,以钼作为催化剂,以氯酸盐、硝酸盐、高氯酸盐和过氧化氢作为氧化剂的催化波研究较多。1963年高小霞、史殿久小结了这四种含钼体系的催化波及其应用。十几年来,国内外学者进一步研究了原有钼的四种催化波的性质和催化过程的机理,并扩大了应用。另外,还研究了一些其它氧化剂的催化电流。国内的研究工作主要是利用含钼体系的催化波作为灵敏的分析方法,扩大了方法的实用范围。国外则主要研究催化波的理论问题,     

用工业废气二氧化碳合成可降解塑料聚碳酸丙烯酯

设计了一篇反映现代化学内容的高中化学教学材料。通过研究实例,介绍可降解塑料聚碳酸丙烯酯的结构、降解机理,用工业废气二氧化碳与环氧丙烷催化共聚合成聚碳酸丙烯酯的原理,以及工业中实际工艺流程等知识。     

叔丁醇溶剂中TS-1催化丙烯环氧化的动力学研究

研究了叔丁醇溶剂中TS-1催化丙烯环氧化反应的本征动力学，反应条件为:温度303.15K～323.15K，丙稀压力0.3 MPa～0.6 MPa。根据反应机理及组分在TS-1上的吸附特点建立了如下的机理模型方程式： 根据实验数据，我们对机理模型进行了参数估值。检验结果表明拟合效果较好，反应符合Eley-Rideal机理，丙烯环氧化反应发生在吸附态的过氧化氢与游离态的丙烯之间。     

双金属氧联醇盐催化环硫丙烷的开环聚合

研究了环硫丙烷以铝锌双金属氧联醇盐为催化剂在甲苯中的聚合动力学及分子量分布。结果表明,环硫丙烷的聚合速度对单体浓度是二级关系,对催化剂浓度是半级关系。聚合系统中催化剂存在缔合,认为环硫丙烷以双分子配位增长。测得聚合活化能为12.2±0.5kcal/mol,计算了单体及溶剂的链转移常数。通过淋洗液中加氯化锂的GPC工作研究了分子量及其分布随转化率的变化。     

RING-OPENING POLYMERIZATION OF PROPYLENE SULFIDE CATALYZED BY BIMETALLIC OXO ALKOXIDE

It was shown that the polymerization rate of propylene sulfide is second order with respect tomonomer concentration and half order with respect to catalyst concentration. A mechanism ofbimolecular coordinated propagation of propylene sulfide and association of the catalyst in thepolymerization system were proposed. The activation energy of polymerization was measured as12.2±0. 5 kcal/mole. Chain transfer constants of monomer and solvent were calculated. Thechange of molecular weight and molecular weight distribution with conversion was followed by GPCwhich was improved by adding LiCl to eluant.     

双金属氰化物络合物催化环氧烷烃开环聚合的特征

合成了Co Zn双金属氰化物 (DMC)络合物催化剂 ,以X 射线衍射、元素分析、红外光谱等手段进行了表征 ,考察了该催化体系下环氧丙烷开环聚合的反应特性 ,并初步探讨了聚合反应的机理 .研究发现 ,Co Zn双金属氰化物催化剂具有很高的催化活性 ,适合于中高分子量聚醚的合成 ,但是碱性起始剂起阻聚作用 ;在该催化体系下聚合物分子量可控 ,不饱和度很低 (<0 .0 14meq g) ,分批加料聚合所得到的聚合物分子量分布较窄 (Mn Mw <1.4 ) ,而一步加料聚合所得到的聚合物分子量分布变宽 ;1 3C NMR分析表明聚合物主链具有无规立构分布的特点 ,且链节分布几乎都为头 尾方式 .聚合过程中活性链与非活性链之间可能存在一个交换反应 ;虽然聚合反应有终止 ,但与聚合物链长没有关系 ,聚合物链的终止是可逆的 .     

由Mg(nBu)2制备的MgCl2载体催化剂的烯烃聚合动力学

讨论了催化剂ＣＤ，ＣＭ和ＣＤ－Ａ的乙烯和丙烯聚合动力学曲线，只有催化剂ＣＤ在丙烯聚合时加入外给电子体其动力学曲线为上升－衰减型，其它均为衰减型，催化剂ＣＤ丙烯聚合活性高于催化剂ＣＭ。丙烯聚合时加入外给电子体使总活性中心浓度降低，但等规中心浓度反应增加。同种载体制备的催化剂ＣＤ和ＣＤ－Ａ载钛过程中加入内给电子体，可使其聚合活性增加，在一定范围内，随Ａｌ／Ｔｉ增加，在一定范围内，随Ａｌ／Ｔｉ增加，催化     

SIMULATION OF EFFECTS OF REACTIVE IMPURITIES ON PROPYLENE POLYMERIZATION IN LOOP REACTORS THROUGH GENERATION FUNCTION TECHNIQUE

The estimation of the amount of reactive impurities in a loop reactor is of strategic importance to the propylene polymerization industry. It is essential to investigate the level of impurities in order to develop reliable monitoring and control strategies. This paper described one approach based on generation function technique with the following two steps. First, a new mechanism for propylene polymerization was proposed by considering the effects of the reactive impurities in the material on the propylene polymerization. Second, a series of equations of population balance for the propylene polymerization in loop reactors were established based on the proposed mechanism. Accordingly, the equations were transformed into the mathematic matrix through the generation function technique to investigate the effects of the reactive impurities on the propylene polymerization. Significant effects of the reactive impurities were analyzed through computational simulation. The results show that the concentration of active centre on catalysts and the polymerization conversion both decrease with the increase of the initial concentration of any reactive impurity; hydrogen concentration decreases with the increase of the initial concentration of ethylene or butylenes, whereas, it increases with the increase of the initial concentration of propadiene; the simulated weight average molecular weight and the molecular weight distribution index of polymer resins both increase with the increase of the initial concentration of ethylene or butylenes. They decrease with the increase of the initial concentration of propadiene.     

Cationic Polymerization of Cyclic Sulfides

Abstract

The mechanism of the cationic polymerization of several thietanes and of propylene sulfide under the influence of triethyloxonium tetrafluoroborate in methylene chloride is described. The thietane polymerizations stop at limited conversions because of a termination reaction occurring between the reactive chain ends (cyclic sulfonium salts) and the sulfur atoms of the polymer chain. The maximum conversions obtained under identical conditions differ markedly for the different monomers. Ratios of rate constants of propagation (k_p) to rate constants of termination (k_t) have been calculated. The differences in k _p/k_t. values for the different monomers are explained in terms of differences in basicity and differences in steric hindrance of the monomers compared to the corresponding polymers. In the case of propylene sulfide it is proposed that the main termination reaction is the formation of 12-membered ring sulfonium salts by an intramolecular reaction of the third sulfur of the growing polymer chain with the reactive chain end (three-membered ring sulfonium salt). This terminated polymer is able to reinitiate the polymerization, for example, by reaction of a monomer molecule at the exocyclic carbon atom of the sulfonium salt function. The cyclic tetramer of propylene sulfide is formed in this reaction. After complete polymerization, formation of cyclic tetramer continues, probably via a backbiting mechanism. In methylene chloride as solvent, the absolute value of the rate constant of propagation for 3,3-dimethylthietane changes with changing concentration of initiator and by adding different amounts of indifferent electrolyte to the reaction mixture. From these changes, and assuming that the value of the dissociation constant of the growing chain-ends is close to values of dissociation constants of low molecular weight sulfonium salts, separate rate constants for propagation via free ions and ion-pairs were calculated. The propagation constant of free ions is about 70 times higher than that of ion pairs in methylene chloride at 20°C. Free ions and ion pairs are nearly equally reactive in nitrobenzene.     

Kinetic isotope effect 13C of cationic polymerization of oxygen-containing heterocycles. Structure of active centres. Mechanism of chain propagation

The results of studying the kinetic isotope effect of cationic polymerization of some oxygen-containing heterocycles are summarized. The use of this method made it possible to establish the oxonium mechanism of chain propagation and the existence of the step of preliminary monomer coordination on an active centre, preceding the polymeric chain propagation step.     

Ziegler-Natta催化配位聚合反应中AlR_3组分对催化剂活性影响的理论研究

本文采用ASED-MO法对Ziegler-Natta型催化剂催化的α-烯烃聚合过程中AlR_3组分对催化剂活性的影响进行了研究.得到了无AlR_3组分存在和一系列不同AlR_3存在时链增长过程的能量变化和相应的活化能.通过比较看出,AlR_3存在可以明显增强催化剂活性.同时运用分子轨道分析的方法探讨了AlR_3增强催化活性的原因.     

A novel consecutive chain transfer reaction to p-methylstyrene and hydrogen during metallocene-mediated olefin polymerization.

This paper describes the first example of consecutive chain transfer reaction, first to p-methylstyrene (or styrene) and then to hydrogen, during metallocene-catalyzed propylene polymerization by rac-Me(2)Si[2-Me-4-Ph(Ind)](2)ZrCl(2)/MAO complex. The PP molecular weight is inversely proportional to the molar ratio of [p-methylstyrene]/[propylene] and [styrene]/[propylene] with the chain transfer constants of k(tr)/k(p) = 1/6.36 and 1/7.5, respectively. Although hydrogen does not influence the polymer molecular weight, it greatly affects the catalyst activity. Each PP chain formed contains a terminal p-methylstyrene (or styrene) unit. The terminal p-MS unit can be metalated to form a stable polymeric anion for living anionic polymerization to prepare new PP diblock copolymers, such as PP-b-PS, which are very difficult to prepare by other methods. The overall process resembles a transformation reaction from metallocene to living anionic polymerization.