对甲基酚醛树脂热裂解产物的固体^13C NMR

对甲基酚醛树脂热裂解产物的固体~（１３）ＣＮＭＲ谢德民，张建国，王存国，王荣顺（东北师范大学化学系，长春，１３００２４）关键词对甲基酚醛树脂，裂解，固体~（１３）Ｃ，ＮＭＲ酚醛树脂经热裂解制备的聚并苯导电材料在空气中稳定，由裂解温度可控制碳化程度，其本...     

丙烯／长链α－烯烃共聚物的~（13）C—NMR和红外光谱法测定组成

丙烯／长链α－烯烃共聚物的~（１３）Ｃ—ＮＭＲ和红外光谱法测定组成陈辉，王建国，景凤英，庞德仁，黄葆同（中国科学院长春应用化学研究所，长春，１３００２２）关键词丙烯／长链α－烯烃共聚物，（１３）~Ｃ—ＮＭＲ，红外光谱法，组成测定聚丙烯（ＰＰ）作为通用塑...     

锆茂均相催化体系催化乙烯与降冰片烯共聚合的研究

锆茂均相催化体系催化乙烯与降冰片烯共聚合的研究谢光华，王金梅，张盛庆（中国科学院化学研究所，北京，１０００８０）关键词锆茂均相催化体系，乙烯，降冰片烯，共聚合金属二茂基化合物与甲基铝氧烷（ＭｅｔｈｙｌａｌｕｎｕｎｏｘａｎｅＭＡＯ）组成以甲苯为溶剂的均...     

聚环氧氯丙烷γ辐射效应的NMR研究

用~（１３）Ｃ和~１ＨＮＭＲ波谱，探讨了聚环氧氯丙烷（ＰＥＰＣＨ）的辐射效应，结果表明随着辐射剂量的增加，本体聚合物的~（１３）ＣＮＭＲ谱中各基团的分辨率得以提高，~１ＨＮＭＲ谱中出现了裂解产物共振峰，Ｔ~１变短，表明ＰＥＰＣＨ在限量空气氛中的辐射效应以大分子裂解反应为主，并通过特性粘度的测定，得到了证实。     

苯乙烯－乙烯共聚物的合成及其结构性能的研究

用负载型钛系催化剂ＭｇＣｌ_２／ＴｉＣｌ_４，ＮｄＣｌ_３／ＡｌＥｔ_３（ＳＮ－１催化剂）制备出组份比例变化的苯乙烯－乙烯共聚产物．共聚产物通过溶剂萃取分离、~１３Ｃ－ＮＭＲ、ＩＲ、动态粘弹谱进行表征，并初步进行了与聚苯乙烯（ａＰＳ）共混作用的研究．结果表明，ＳＮ－１催化剂能有效地催化苯乙烯与乙烯共聚合．共聚产物为含有均聚聚苯乙烯的共聚物复合物，其中的２５ｍｏｌ％的苯乙烯参加了共聚．共聚产物与ａＰＳ共混可明显提高ａＰＳ的冲击强度和断裂伸长率．     

TiCl_4／SiO_2－MgCl_2载体催化剂下的乙烯／己烯－1共聚反应

ＴｉＣｌ_４／ＳｉＯ_２－ＭｇＣｌ_２载体催化剂下的乙烯／己烯－１共聚反应陈辉，张学全，黄葆同王展望，杨永然（中国科学院长春应用化学研究所长春１３００２２）（辽阳化纤公司化工三厂辽阳）关键词乙烯，己烯，共聚，Ｚｉｅｇｌｅｒ－Ｎａｔｔａ催化剂乙烯／α－烯?..     

新型五甲基茂基三苄氧基钛/甲基铝氧烷催化剂合成苯乙烯-乙烯共聚物及其表征

以五甲基茂基三苄氧基钛［Ｃｐ＊ Ｔｉ（ＯＢｚ）３］ 和甲基铝氧烷（ ＭＡＯ） 组成的催化体用本体法合成出苯乙烯 乙烯共聚物Ｐｏｌｙ（Ｓ ｃｏ Ｅ） ．考察了共聚温度,共聚时间,Ａｌ／Ｔｉ 摩尔比,主催化剂浓度［Ｔｉ］ 等条件对共聚反应的影响．共聚产物经沸丁酮,沸四氢呋喃（ＴＨＦ） 连续抽提分离,发现共聚物主要存在于ＴＨＦ 可溶级分中．可溶级分经ＤＳＣ,１３Ｃ ＮＭＲ,ＷＡＸＤ,ＤＭＡ 等手段分析,证明苯乙烯 乙烯共聚物为具有单一玻璃化转变温度（ Ｔｇ） 无熔融温度的无规共聚物,显示弹性体的粘弹性行为．     

新型五甲基茂基三苄氧基钛／甲基铝氧烷催化剂合成苯乙烯—乙烯共聚？…

以五甲基茂基三苄氧基钛〔Ｃp＊Ｔi（ＯＢz）３〕和甲基铝氧烷（ＭＡＯ）组成的催化体 用本体法合成出苯乙烯－乙烯共聚物Ｐoly（Ｓ－ｃｏ－Ｅ）。考察了共聚温度,共聚时间 ,Ａ１／Ｔi摩尔比,主催化剂浓度〔Ｔi〕等条件对共聚反应的影响。共聚产物经沸丁酮,沸四氢呋喃（ＴＨＦ）连续抽提分离,发现共聚物主要存在于ＴＨＦ可溶级分中。可溶级分经ＤＳＣ,＾１３Ｃ－ＮＭＲ,ＷＡＸＤ,ＤＭＡ等手段分析,证明苯乙烯－乙烯共聚物为     

苯乙烯－乙烯共聚物的合成及其结构性能的研究

用负载型钛系催化剂ＭｇＣｌ２／ＴｉＣｌ４，ＮｄＣｌ３／ＡｌＥｔ３（ＳＮ－１催化剂）制备出组份比例变化的苯乙烯－乙烯共聚产物，共聚产物通过溶剂萃取分离，＾１３Ｃ－ＮＭＲ，ＩＲ，动态粘弹谱进行表征，并初步进行了与聚苯乙烯共混作用的研究。结果表明，ＳＮ－１催化剂能有效地催化苯乙烯与乙烯共聚合，共聚产物为含有均聚聚苯乙烯的共聚复合物，其中约２５ｍｏｌ％的苯乙烯参加了共聚。共聚产物与ａＰＳ共混可明显提高ａＰ     

双（环戊二烯基）二氯化锆载体催化剂催化乙烯／α—烯烃共聚合

合成了３种Ｚｒ／甲基铝氧烷（ＭＡＯ）／ＳｉＯ２型载体催化剂，考察了不同ＭＡＯ投料量对载锆反应及催化活性的影响，研究了乙烯聚合及乙烯／α－烯烃共聚合，结果表明，该催化剂对己烯和辛烯有很强的共聚作用，而对癸烯的共聚能力较弱，解释了α－烯烃碳链增长对乙烯／α－烯烃共聚催化活性的影响，ＳＥＭ分析表明，α－烯烃的加入有利于聚合物形态原改善。     

有机-无机复合载体茂锆催化剂的制备及乙烯聚合

合成了组成为聚(4-乙烯基吡啶)-硅胶(SAV)的有机-无机复合载体茂锆催化剂,并用固体13C-NMR谱、元素分析(EA)、光电子能谱(XPS)等方法进行了表征.发现由SAV负载的茂锆催化剂可在相对较低的甲基铝氧烷(Al/Zr=600)用量下聚合乙烯.其活性(1.12×103kg PE/mol Zr.h)远高于SiO2负载的茂锆催化剂(0.22×103kg PE/mol Zr.h).     

Supported metallocene catalysts prepared by impregnation of MAO modified silica by a metallocene/monomer solution

Silica supported (butylcyclopentadienyl)₂ZrCl₂/MAO catalysts were synthesized according to the “incipient wetness” method from a solution of metallocene in a liquid monomer. The monomer was allowed to polymerize yielding a catalyst containing polyhexene (PH), polystyrene (PS) or polyoctadiene (PO). One catalyst containing no polymer was also synthesized. The catalysts were used to polymerize ethene at 70°C and 4 bar total pressure. The measured average activities were 5 300 kg PE/(mol Zr · h) for (BuCp)₂ZrCl₂/MAO/PH/SiO₂, 8 600 kg PE/(mol Zr · h) for (BuCp)₂ZrCl₂/MAO/PS/SiO₂, 3 400 kg PE/(mol Zr · h) for (BuCp)₂ZrCl₂/MAO/PO/SiO₂ and 5 700 kg PE/(mol Zr · h) for (BuCp)₂ZrCl₂/MAO/SiO₂. The polyhexene, polystyrene or polyoctadiene in the catalyst forms a protective layer around the active sites. Even after exposure to air for five hours these catalysts retain some polymerization activity.     

Metallocene–methylaluminoxane catalysts for olefin polymerization. I. Trimethylaluminum as coactivator

Ethylene was polymerized by Cp₂ZrCl₂–methylaluminoxane (MAO) catalysts where a portion of the MAO was replaced with trimethyl aluminum (TMA). At a total Al to Zr ratio of 1070, there is neither appreciable loss of productivity nor change in polymerization profile for TMA/MAO ≤ 10. The productivity is reduced only by two- to three-fold for TMA/MAO ≤ 100 accompanied by a 10 min induction period. Aging of this catalyst did not affect the induction period, but improves its productivity. The kinetic isotope effect for radiolabeling with tritiated methanol is 2.0. About 40% of the Zr is active for the catalyst with {99 [TMA] + 1[MAO]} to Zr ratio of 100. The rate constants for propagation and chain transfer were obtained. The mechanisms for the mixed TMA and MAO cocatalyst system are discussed. The results of this work have important practical significance. MAO is a hazardous material to synthesize and only in low yields. The replacement of > 90% of MAO with TMA represents a substantial saving since as much as 0.1M of the former is commonly used for a polymerization.     

SIMULATION MODELING ON THE COORDINATION MECHANISM OF ETHYLENE MONOMER ON VARIOUS PREREDUCED Cr(Ⅱ)O_x/SiO_2 PHILLIPS POLYETHYLENE MODEL CATALYSTS

As one of the most important catalysts in polyethylene industry,Phillips catalyst(CrO_x/SiO_2)was quite unique for its activation by ethylene monomer without using any activator like alkyl-aluminium or MAO.In this work,the density functional theory(DFT)calculation combined with paired interacting orbitals(PIO)method was applied for the theoretical studies on coordination reaction mechanism between ethylene monomer and two model catalysts namely Cr(Ⅱ)(OH)_2(M1) and silsesquioxane-supported Cr(Ⅱ)(M2)as sur...     

Metal content determination in polymerization catalysts by direct methods

Metal contents in polymerization catalysts were comparatively determined by Rutherford backscattering spectrometry (RBS), X-ray photoelectron spectroscopy (XPS) and X-ray fluorescence (XRF) spectroscopy. Catalysts were prepared by grafting metallocene onto bare silica or onto silica chemically modified with methylaluminoxane (MAO). Catalysts were compressed as self-supporting pellets (RBS and XRF), or mounted on adhesive copper tape (XPS). The proximity of the mass of the atomic nuclei did not allow resolution by RBS of the signals corresponding to Zr and Nb, nor Si and Al in catalyst systems such as (nBuCp)₂ZrCl₂/Cp₂NbCl₂/MAO/SiO₂. On the other hand, Zr, Nb, Si and Al lines were completely resolved in an XRF spectrum. For supported metallocenes on bare silica, XPS measurement was ca. 40% higher than that obtained by RBS. Silica-supported zirconocene showed good agreement in Zr content determination by XRF and RBS.     

Immobilization of η-cyclopentadienyltris(dimethylamido)zirconium polymerization catalysts on a chlorosilane- and HMDS-modified mesoporous silica surface: a new concept for supporting metallocene amides towards heterogeneous single-site-catalysts

The modification of a mesoporous silica surface with Si(Ind)(CH₃)₂Cl and the immobilization of CpZr(NMe₂)₃ on this surface was studied via IR-spectroscopy. To reduce side reactions, the indenyl-modified silica was reacted with hexamethyldisilazane (HMDS) under IR-control before the CpZr(NMe₂)₃-immobilization. The role of the hydroxyl group protection with HMDS is discussed. The surface modifications have been repeated via Schlenk technique at the same conditions and the surface modifications were studied with ¹³C CP MAS–NMR, ¹H MAS–NMR, elemental-, SEM- and BET-analysis. The surface species of the resulting catalysts are discussed. The precatalysts have been treated with methylaluminoxane (MAO) (Al:Zr (mol:mol)=500:1) and the resulting Zr contents (leaching-effect) are discussed. All catalysts have been tested in ethylene and propylene polymerization.     

Metallocene–methylaluminoxane catalyst for olefin polymerization. II. Bis-η5-(neomenthyl cyclopentadienyl)zirconium dichloride

Bis(neomenthyl cyclopentadienyl)zirconium dichloride/methyl aluminoxane (η⁵-(NMCp)₂ZrCl₂/MAO) catalyst has been investigated for ethylene polymerization. About 51% of the Zr forms active sites more or less instantaneously according to quenching with tritiated methanol. There is an initial drop of rate of polymerization, R_p, of about 30% which remains constant thereafter. The catalytic activity increases monotonically with temperature; it is proportional to [MAO]^1.75 at a constant [Zr] = 1.5 μM and proportional to [Zr]^?1.2 at a constant [MAO] = 64.5 mM. At very large [MAO]/[Zr], the catalyst has extremely high activity; κ_p = 5 × 10³ (Ms)^?1 at 50°C. There is also facile chain transfer to aluminum, κ = 0.14 s^?1 at 50°C. Both κ_p and κ are about 30 times greater than the corresponding rate constants for MgCl₂ supported TiCl₃ catalysts. The TiCl₃/MgCl₂ and (NMCp)₂/MAO catalysts have nearly the same activation energy for propagation (ca. 7 kcal/mol^?1). The higher activity of the latter is due to its larger preexponential factor in κ_p. The dependence of catalytic activity on the [MAO]/[Zr] ratio may be explained by rapid association-dissociation equilibria of MAO involving acid-base and/or electron deficient bridge complexation.     

Hydrogen transfer reactions of supported metallocene catalysts

The evolution of methane from methylaluminoxane (MAO) solutions is enhanced in the presence of homogeneous metallocenes. This reaction serves as a model for the deactivation of metallocene catalysts. By supporting different metallocenes on a silica/MAO carrier the deactivation reaction by alpha-hydrogen transfer among metallocene active sites and aluminum alkyls can be suppressed. The suppression of alpha-hydrogen transfer is proven for different Al/Zr ratios and by near independence of the polymerization activity on the catalyst aging time, after reaching maximum activity. Aluminum alkyls and MAO leach Cp₂ZrCl₂ from the carrier, the leached metallocene is only active in polymerization if MAO is present.     

Effect of methylaluminoxane/transition-metal ratio on the physical properties and chemical composition distributions of ethylene-hexene copolymers produced by a rac-Et(Ind)2ZrCl2/TiCl4/MAO/SMB catalyst

A silica-magnesium bisupport (SMB) was prepared by a sol-gel method for use as a support for the impregnation of TiCl₄ and rac-Et(Ind)₂ZrCl₂. The prepared rac-Et(Ind)₂ZrCl₂/TiCl₄/MAO(methylaluminoxane)/SMB catalyst was applied to the ethylene-hexene copolymerization under the conditions of variable Al(MAO)/Zr ratio and fixed Al(TEA, triethylaluminum)/Ti ratio. The effect of Al(MAO)/Zr ratio on the physical properties and chemical composition distributions of ethylene-hexene copolymers produced by a rac-Et(Ind)₂ZrCl₂/TiCl₄/MAO/SMB catalyst was investigated. The catalytic activity of rac-Et(Ind)₂ZrCl₂/TiCl₄/MAO/SMB was steadily increased with increasing Al(MAO)/Zr ratio from 200 to 500. The ethylene-hexene copolymer produced with Al(MAO)/Zr = 300, 400, and 500 showed two melting points at around 110 °C and 130 °C, while that produced with Al(MAO)/Zr = 200 showed one melting point at 136 °C. The number of chemical composition distribution (CCD) peaks was increased from 4 to 7 and the short chain branches of ethylene-hexene copolymer were distributed over lower temperature region with increasing Al(MAO)/Zr ratio. The lamellas in the copolymer were distributed over lower temperature region and the small lamellas in the copolymer were increased with increasing Al(MAO)/Zr ratio. The rac-Et(Ind)₂ZrCl₂/TiCl₄/MAO/SMB catalyst preferably produced a ethylene-hexene copolymer with non-blocky sequence ([EHE]) with increasing Al(MAO)/Zr ratio.     

Routes to reduce aluminium co-catalyst content for zirconocene activation in olefin polymerization

In this paper, we investigate different routes to lower drastically the amount of methylaluminoxane (MAO) required to activate racEt(Ind)₂ZrX₂ catalysts towards olefin polymerization. A first approach consists in replacing Cl ligands by more easily extractable X groups such as Me, CH₂Ph or NMe₂ groups. A second method focuses on the preparation of TMA-depleted MAO either by pumping off TMA from commercial MAO or by exploring new synthetic source to MAO via non-hydrolytic processes such as the reaction of TMA with benzophenone. Both methods allowed us to produce polyolefins with a maximal catalytic activity for Al/Zr ratios not exceeding 150, i.e. ratio 20 times lower than those required in the presence of commercial MAO.