单茂钛/甲基铝氧烷催化剂乙烯/丙烯共聚合研究

改性甲基铝氧烷(mMAO)激活五甲基茂基三氯化钛(Cp TiCl3)催化乙烯 丙烯共聚合,控制两种单体的进料配比,得到单元序列分布不同的共聚物.混合单体中含有少量丙烯,共聚合活性高于相同聚合条件下乙烯均聚合的活性.用1 3C -NMR测定共聚物分子链的微观结构和单元序列分布,计算出单体的竞聚率;结果表明共聚物分子链中两种单体的序列分布均匀.混合单体中丙烯含量较大时,共聚物为完全无规共聚物;而当丙烯含量少时,丙烯链节或短的聚丙烯链段均匀分布于聚乙烯链段之间.共聚物经DSC分析,也证明不存在长序列的聚乙烯链段;因此,即便在进料气体中丙烯含量很少的情况下,共聚物仍然没有明显的熔融温度和结晶性.     

Tools and strategies for processing diffusion-ordered 2D NMR spectroscopy (DOSY) of a broad,featureless resonance: an application to methylaluminoxane (MAO)

DOSY has been extremely successful in many studies of molecular weight distributions, especially when the components are separable along the chemical shift axis. However, an unresolved NMR resonance yields the familiar problem of overlapping exponential decays. In a study of methylaluminoxane (MAO), a set of data processing and simulation tools were developed: read Bruker data files (Matlab); preliminary non-linear least-squares fit with f-test (Matlab); movie generation of the fits (Matlab); conversion of diffusion coefficients to molecular masses through molecular volumes (Gaussian-98); and simulation of DOSY data sets for various molecular mass distributions (Mathematica). These tools are presented here and briefly compared with other DOSY analysis methods.Electronic Supplementary Material Supplementary material is available in the online version of this article at . The following Matlab and Mathematica files are made available: Plot_Raw_DOSY.m, Fit_Two_Component.m (which calls One_Gaussian_LEASTSQ.m, Two_Gaussian_LEASTSQ.m, and pFTest.m), and DOSY_theory.nb. Note: Matlab v5.2 optimization toolbox, as supplied, lacked a confidence interval subroutine; upon our request, confint.m was provided to the authors by Mathworks, Inc. Newer versions of Matlab have a similar program already included in the optimization     

COPOLYMERIZATION OF ETHYLENE WITH 1-OCTENE USING Et(Ind)2ZrCl2/MAO CATALYST

Copolymerization of ethylene/1-octene was carried out in toluene withvarious concentrations of comonomer in the feed using Et(Ind)_2ZrCl_2/MAO (methyl alu-minoxane) as catalyst. It was found that with the increase of 1-octene concentration in thefeed the content of 1-octene in the copolymer increases, while the density, melting point,crystallinity and intrinsic viscosity of copolymer decrease. A copolymer with very lowdensity, containing 11.5 mol% of 1-octene (VLLDPE) can be produced with this catalystsystem. The effect of temperature and zirconium aluminum mole ratio of the catalyst onthe copolymerization was also investigated. The results of ~(13)C NMR determination of thecopolymer showed that the 1-octene units in the copolymer are principally isolated.     

茂钛催化剂间规聚苯乙烯-b-聚丙烯嵌段共聚物的合成及产物分离与表征

以茂基三正丙氧基钛［ＣｐＴｉ（Ｏ ｎ Ｐｒ）３］和改性的甲基铝氧烷（ＭＡＯ）为催化体系，用于合成间规聚苯乙烯 ｂ 聚丙烯嵌段共聚物．丙烯先预聚，然后加入苯乙烯进行嵌段共聚合反应，具有较高的催化效率（９５００ｇＰ／ｇＴｉ）．研究了丙烯预聚合时间，共聚合反应温度、催化体系组份及浓度等聚合条件对嵌段共聚合反应的影响．共聚反应总产物经沸丁酮、沸庚烷和４０℃四氢呋喃（ＴＨＦ）等溶剂的连续抽提分离，发现嵌段共聚物主要存在于沸丁酮的可溶级份中．将各分离级份用１３Ｃ ＮＭＲ、Ｘ 射线衍射和ＤＳＣ等分析手段进行结构表征并加以讨论．     

单茂钛化合物/MAO/AlR_3均相催化体系合成sPS与aPP研究

先考察部分水解三甲基铝（ＴＭＡ）制备固体改性甲基铝氧烷（ｍ ＭＡＯ）时，反应物Ｈ２Ｏ和ＴＭＡ的摩尔比对固体产物ｍ ＭＡＯ中ＴＭＡ含量的影响；然后考察不同的钛化合物特别是茂钛化合物（ＬｎＴｉＸｎ′，ｎ＝１，２，ｎ′＝２，３）和ｍ ＭＡＯ组成的均相催化体系分别进行苯乙烯间规聚合和丙烯无规聚合的效果作比较．在此基础上分析以茂基三正丙氧基钛［ＣｐＴｉ（ＯＰｒｎ）３］为主催化剂，不同ＴＭＡ含量的ｍ ＭＡＯ为助催化剂，及外加各种烷基铝（ＡｌＲ３）所组成的催化体系中钛的氧化数，同时对苯乙烯间规聚合和丙烯无规聚合进行比较研究，从中发现活性中心钛的氧化数以Ｔｉ（Ⅲ）为主时有利于苯乙烯间规聚合，不利于丙烯无规聚合；而氧化数以Ｔｉ（Ⅳ）为主时则对丙烯无规聚合有利．苯乙烯间规聚合时，外加烷基铝可节省ＭＡＯ用量．     

Theoretical Study on Molecular Structures of Methylaluminoxane Nanotubes

Density functional theory was used to optimize structures of different methylaluminoxane nanotubes with general formula [(AlOMe)₂]_n, [(AlOMe)₃]_n and [(AlOMe)₄]_n cycle unit, where n ranges from 1 to 10. To explore the stability of nanotubes, the binding energies and total energies are calculated. The results indicate that [(AlOMe)₃]_n and [(AlOMe)₄]_n have the stable structure of nanotubes. When n is 3, they have the most stable structure in all systems. Moreover, [(Al₅O₅)]_n and [(Al₇O₇)]_n are also considered, but their dimers have irregular and distorted structures. So [(Al₅O₅)]_n and [(Al₇O₇)]_n nanotubes are impossible to exist.     

茂钛催化剂聚1-丁烯的合成

茂金属催化烯烃聚合以其高活性、定向性等特点受到广泛重视.Ｋａｍｉｎｓｋｙ[1～4]等用二茂基(Ｃｐ、Ｉｎｄ和Ｆｌｕ)过渡金属(Ｔｉ、Ｚｒ和Ｈｆ)化合物/ＭＡＯ催化剂催化1丁烯聚合,可得到间规(ｓＰＢ)、无规(ａＰＢ)或等规(ｉＰＢ)聚1丁烯.Ｌｉｎ[5]和Ｗｕ[6]分别用单茂基的ＣｐＴｉ(ＯＰｒ)3/ＭＡＯ和ＣｐＴｉ(ＯＢｚ)3/ＭＡＯ催化剂进行丙烯聚合,都得到无规聚丙烯(ａＰＰ),并研究了催化体系中Ｔｉ氧化态分布,认为Ｔｉ+4有利于α烯烃聚合.有关用单茂钛化合物/ＭＡＯ催化体系催化1丁烯聚合的研究目前较少文献报道.本文用新型茂钛催化剂—…     

新型茂钛催化剂的分子设计与苯乙烯间规聚合

合成了CpTiCl₃/MAO、Cp^*TiCl₃/MAO、Cp^*Ti(OCH₂CH＝CH₂)₃/MAO和cp^*Ti(OMe)₃/MAO四种均相催化体系.结果发现,[Cp^*Ti(OCH₂CH＝CH₂)₃]/甲基铝氧烷(MAO)催化体系热稳定性较高,在333～363K下进行苯乙烯问规聚合具有最高的催化活性;聚合反应产物用沸丁酮抽提8h,不溶部分间规聚苯乙烯(sPS)占总聚合产物重量的98%以上,sPS的分子量Mv达到4.15×10⁵～2.46×10⁵范围,熔融温度高达543K.     

Synthesis and structural characterization of ethylene–norbornene copolymer with high norbornene content catalyzed by β-diketiminato nickel/methylaluminoxane

Ethylene–norbornene (E–N) copolymerizations were carried out by using β-diketiminato nickel complexes CH{C(CF₃)NAr}₂NiBr (Ar = 2,6-ⁱPr₂C₆H₃, 1; Ar = 2,6-Me₂C₆H₃, 2) in the presence of methylaluminoxane (MAO). Complex 1 bearing bulky isopropyl ortho substituents showed higher activity than 2 for the E–N copolymerization. The activity of the catalytic systems increased with increasing the feed ratio of norbornene/ethylene (N/E), and gave the E–N copolymers with high norbornene content more than 75 mol%. In the microstructures of copolymers generated with the catalytic systems, norbornene microblocks with a length of two or three norbornene units have been detected. Results have shown that the activity and the content of norbornene in copolymer depend on the N/E feed ratio.     

Polymerization of hydroxyl functional polypropylene by metallocene catalysis

Propylene was copolymerized with 10-undecen-1-ol with use of dimethylsilanyl-bis-(2-methyl-4-phenyl-1-indenyl)zirconium dichloride as catalyst activated with methylaluminoxane (MAO) and triisobutylaluminum (TIBA). Comonomer incorporations as high as 2.0 mol% or 8.2 wt% were obtained without serious activity losses. Concentration of MAO, aluminum/comonomer ratio and pressure had some effect on polymerization activity and yield. However, changing the proportion of MAO in the cocatalyst mixture of MAO and TIBA proved to be most efficient way to enhance polymerization activity. Still, the result was a compromise between high functionality content, polymerization activity and molecular weight.