茂钛均相催化剂丁二烯聚合研究

由五甲基单茂钛化合物Cp TiL3 和甲基铝氧烷 (MAO)组成的催化体系进行丁二烯聚合 .考察具有不同辅助配体L的主催化剂Cp TiL3 及外加三异丁基铝 (TIBA)对聚合的选择性 ;讨论了聚合温度、AlMAO Ti摩尔比和催化剂浓度对聚合反应的影响 .发现外加适量TIBA有助于提高催化活性 ,而且随着TIBA用量的增加聚丁二烯分子量增加 .结合钛氧化态分析 ,说明催化体系中Ti(Ⅲ )活性中心更有利于丁二烯聚合     

单茂钛催化剂催化丁烯-1聚合及高分子量无规聚丁烯-1的合成与表征

Kaminsky等 [1,2 ] 用二茂基 ( Cp,Ind,Flu)过渡金属 ( Ti,Zr和 Hf)化合物 /MAO催化剂催化丁烯 - 1聚合 ,得到间规 -等规或间规 -等规 -无规的混合物 ,聚合物的分子量为 5 0 0 0 0至 1 5 0 0 0 0 .Rossi[3] 用( CH3) 2 Si( H4 Ind) 2 Zr Cl2 /MAO研究了丁烯 - 1的等规聚合 ,产物分子量仅 2 0 0 0左右 .林尚安等[4 ,5] 采用单茂钛催化剂 Cp* Ti( OBz) 3/MAO催化丁烯 - 1聚合 ,产物为立体多嵌段聚丁烯 - 1 .但目前尚未见到有关采用茂金属催化剂催化丁烯 - 1聚合制备高分子量无规弹性体聚丁烯 - 1的报道 .我们用单茂钛 Cp* Ti( OC…     

单取代芳氧钛合成与催化乙烯及乙烯与α-烯烃共聚

使用廉价原料和简单工艺方法合成了芳氧钛类烯烃聚合和共聚催化剂,得到了(2-OMe C6H4O)Ti Cl3(C1),(2,4-Me2C6H3O)Ti Cl3(C2),Ti Cl3(1,4-OC6H4O)Ti Cl3(C3),Ti Cl3(1,4-OC6H2O-Me2-2,5)Ti Cl3(C4)以及相应的(Ar O)2Ti Cl2类络合物Ti Cl2(OC6H4-OMe-2)2(C5)和Ti Cl2(OC6H3-Me2-2,6)2(C6).通过1H NMR,13C NMR,MS以及元素分析进行了结构表征,确认了化学组成,以甲基铝氧烷(MAO)为助催化剂,Ar OTi Cl3/MAO体系显示了对乙烯聚合和共聚的高活性,13C NMR结果表明,聚合物中1-己烯插入率最高达6.88%(摩尔分数),而且得到的聚合物呈现高度支化,除了α-烯烃支链,还有甲基、乙基和长支链,并对其形成机理进行了研究,此外,对聚合温度、时间及共聚单体浓度对聚合反应的影响也进行了探讨.     

芳二酚-茂型钛配合物[O,O]CpTiCl的合成及其催化乙烯聚合性能研究

制备了含二元芳香酚类配体 [O ,O]的茂型钛配合物 [O ,O]CpTiCl,并通过元素分析、IR、1 H NMR表征了其组成与结构 .结果表明 ,二元芳香酚类配体中两个O原子同时与金属中心原子Ti相连 ,形成环状结构 .研究表明 ,茂型钛配合物 [O ,O]CpTiCl在助催化剂甲基铝氧烷 (MAO)作用下 ,于 30℃、1 0 1× 10 5 Pa乙烯压力下即可催化乙烯聚合 ,并显示较高的活性 ,远高于未引入配体 [O ,O]的CpTiCl3的活性 ,并且 [O ,O]CpTiCl的催化活性依非茂酚类配体中芳香环的增大而下降 (C6 H4O2 ) >(C1 2 H8O2 ) >(C2 0 H1 2 O2 ) .此外 ,[O ,O]CpTiCl MAO体系催化活性随铝 钛比的增加呈上升而后衰减型 ,当铝 钛比为 5 0 0到 30 0 0之间时活性最高 ,所得聚乙烯具有双峰分布特征 ,其重均分子量Mw =12 5× 10 4,分子量分布为Mw Mn =7 4     

新型茂钛催化剂合成聚乙烯-b-间规聚苯乙烯嵌段共聚物的研究Ⅰ.嵌段共聚合反应

以五甲基茂基三苄氧基钛 [Cp Ti(OBz) 3]为主催化剂、改性甲基铝氧烷 (mMAO)为助催化剂 ,进行乙烯与苯乙烯的嵌段共聚合反应 .讨论了乙烯预聚温度、预聚时间、主催化剂的浓度、Al(mMAO) Ti摩尔比、苯乙烯的浓度以及外加三异丁基铝 (TIBA)等条件对共聚反应的影响 .发现适宜的共聚反应条件为 ,预聚温度为40℃ ;主催化剂的浓度为 6 6 7× 10 - 4 mol L ;铝钛摩尔比为 2 0 0 .共聚反应的催化效率随预聚时间的延长而降低 ;嵌段共聚物中苯乙烯链节含量随苯乙烯的浓度的增加而增加 ;外加TIBA对嵌段共聚物的形成及催化效率的提高起关键性作用     

CpTiCl2(OR)/MAO体系催化苯乙烯间规聚合的研究

茂金属催化剂广泛应用于催化α-烯烃和苯乙烯的定向聚合. 与传统的Ziegler-Natta催化剂相比, 茂金属催化剂催化活性中心单一, 聚合过程立体定向性强, 且往往得到用常规方法所不能得到的新型聚合物［1～5］. Ishihara等［6］首次采用钛金属有机化合物与甲基铝氧烷(MAO)体系催化苯乙烯聚合, 分离得到间规聚苯乙烯, 从此揭开了苯乙烯定向聚合的新篇章, 合成了大量茂金属有机化合物, 用于催化苯乙烯间规聚合, 其中半夹心结构的茂金属化合物CpTiX3［7,8］, IndTiCl3［3,4,9,10］［Cp=(未)取代环戊二烯基, Ind=(未)取代茚基; X=Cl, F, 烷氧基等］具有最好的催化活性及间规定向性. (CpHMe4)TiF3［8］催化活性高达1.01×108 g PS/(mol Ti*h), 间规度≥95%.     

复合茂钛催化剂制备宽分子量分布间规聚苯乙烯的研究

采用新型茂钛化合物Cp^*Ti(O-Ph-OCH3)3(A)／CpTi(O-Ph-OCH3)3(B)和Cp^*Ti(O-Ph-OCH3)3(A)／Cp^*Ti(O-Ph-F),(C)作为复合催化剂,在甲基铝氧烷(MAO)、三异丁基铝(TIBA)激活下进行苯乙烯间规聚合。采用A／B复合催化剂可通过调节两种茂钛催化剂的摩尔配比,得到宽分子量分布的间规聚苯乙烯(s-PS);而采用A／C复合催化剂得到的产物分子量分布基本不变。对不同聚合条件下得到的s-PS产物进行了GPC分析。     

α-二亚胺镍/Cp*TiCl3复式催化剂制备双峰长支链聚乙烯

合成了一种后过渡金属镍化合物 [二 N ,N′ (α 萘基 ) 2 ,3 丁二亚胺镍二溴化物 ][C1 0 H7—NC(CH3)C(CH3)N—C1 0 H7]NiBr2 ,此化合物在MAO活化下催化乙烯聚合能得到含有末端双键的低分子量聚乙烯 ,即长链α 烯烃 .此化合物和一种单茂钛化合物五甲基环戊二烯基三氯化钛 (Cp TiCl3)所组成的复式催化剂 ,用MAO活化后两种主催化剂具有良好协同作用 ,能使单一乙烯聚合制备出双峰型长支链的聚乙烯 .1 3C NMR表明由此复式催化剂制得的聚乙烯不但含有甲基、乙基、丙基、丁基、戊基支链而且还含有相当多的长支链 (支链长度大于或等于 6 ) .催化剂的摩尔比 (Ni Ti)、Al(MAO) (Ni+Ti)摩尔比和聚合温度等聚合条件对催化活性及聚合物的结构与性能有明显影响 .GPC测试表明所得到的支化聚乙烯分子量呈双峰分布 .     

β-二酮-茂基二氯化钛/MAO催化体系用于苯乙烯间规聚合

制备了 β 二酮类配体 [O ,O]的茂基二氯化钛配合物CpTi(dbm)Cl2 .实验证明 ,这类配合物在助催化剂甲基铝氧烷MAO作用下 ,可催化苯乙烯间规聚合 .显示较高的活性 (10 7× 10 5gPS molTi·h) .所得聚合物具有较高的间规度 .CpTi(dbm)Cl2 MAO体系催化活性随铝 钛比的增加呈上升而后衰减 ,当铝 钛比为 5 0 0左右时活性最高 ;聚合温度较高时会导致催化活性下降 .对聚合物进行了1 3C NMR表征     

茂钛催化剂苯乙烯/1-丁烯嵌段共聚物的合成与表征

用 η5 五甲基环戊二烯基三苄氧基钛 /改性甲基铝氧烷 (Cp Ti(OBz) 3/mMAO)催化剂对苯乙烯 / 1 丁烯嵌段共聚合进行了研究 .考察了外加三异丁基铝 (TIBA) ,1 丁烯预聚合时间及苯乙烯浓度对聚合结果的影响 .发现外加TIBA的量对催化活性的影响存在峰值 ,[TIBA]=2 6mmol/L时催化活性最大 ,达到 12 2kgP/gTih ;催化活性随 1 丁烯预聚时间延长而降低 ;苯乙烯的浓度较低时 ,催化活性随其浓度增大而增大 ,但当苯乙烯的浓度大于 4 18mol/L时 ,催化活性变化不明显 .对嵌段共聚物用丁酮 ,四氢呋喃和氯仿连续萃取分离 ,四氢呋喃和氯仿中的可溶级份是嵌段共聚物sPS b PB ,占共聚合产物的 2 1 0～ 41 3wt % .对嵌段共聚物用13C NMR ,DSC ,WAXD和FTIR等手段进行了表征     

茂钛化合物／改性MAO催化剂制备聚丙烯-b-间规聚苯乙烯嵌段共聚物

以五甲基环戊二烯基三苄氧基钛化合物 [Cp Ti(OBz) 3 ]为主催化剂 ,改性甲基铝氧烷作助催化剂 ,采用单体顺序投入法 ,合成了聚丙烯 b 间规聚苯乙烯嵌段共聚物 .外加三异丁基铝可以使活性中心的氧化态由Ti(Ⅳ )还原为Ti(Ⅲ ) ,从而提高苯乙烯共聚单体的转化率 .实验表明此催化体系对共聚物的合成具有较高活性 ,适宜的茂钛化合物浓度可阻止活性中心被丙烯预聚物包埋 .抽除残余丙烯气也可促进苯乙烯的共聚合 .对聚合产物进行溶剂连续萃取 ,可分离出嵌段共聚物 ,并用 13 CNMR和DSC进行结构表征     

Novel Complex Catalyst of η3‐(Pentamethylcyclopentadienyl)dimethylaluminum/Titanium(IV) Butoxide (Cp*AlMe2/Ti(OBu)4) for Syndiotactic Polystyrene

A novel metallocene catalyst was prepared from the reaction of (η³‐pentamethylcyclopentadienyl)dimethylaluminum (Cp*AlMe₂) and titanium(IV) n‐butoxide Ti(OBu)₄. The resulting titanocene Cp*Ti(OBu)₃ was combined with methylaluminoxane (MAO)/tri‐iso‐butylaluminum (TIBA) to carry out the syndiotactic polymerization of styrene. The resulting syndiotactic polystyrene (sPS) possesses high syndiotacticity according to ¹³C NMR. Catalytic activity and the molecular weight of the resulting sPSs were discussed in terms of reaction temperature, concentration of MAO, amounts of scavenger TIBA added, and the hydrogen pressure applied during polymerization.     

单茂钛催化剂的苯乙烯间规聚合和乙烯聚合的比较

考察三甲基铝（ＴＭＡ） 部分水解法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ｍ ＭＡＯ 的产量及ｍ ＭＡＯ 中ＴＭＡ 含量的影响;以五甲基茂基三苄氧基钛［Ｃｐ ＊ Ｔｉ（ＯＢｚ）３］／ｍ ＭＡＯ 组成的均相催化体系,分别考察ｍ ＭＡＯ 的用量［ 即Ａｌ／Ｔｉ 摩尔比］ 及ｍ ＭＡＯ 中ＴＭＡ 含量对苯乙烯间规聚合和乙烯聚合的影响．通过分析Ｃｐ ＊ Ｔｉ（ＯＢｚ）３／ｍ ＭＡＯ 催化体系钛氧化态的分布,发现Ｔｉ（ Ⅲ） 活性中心有利于合成间规聚苯乙烯;而Ｔｉ（ Ⅳ） 活性中心有利于合成聚乙烯．苯乙烯间规聚合时,外加三异丁基铝（ＴＩＢＡ） ,将提高催化活性,同时可节省ＭＡＯ 用量．     

(η5-Pentamethylcyclopentadienyl)trimethyltitanium as a precursor for the syndiospecific polymerization of styrene

An equimolar mixture of Cp*Ti(CH₃)₃ (2) and Ph₃C⁺[B(C₆F₅)₄]^? (1) forms a highly active and syndioselective catalyst for the polymerization of styrene, producing 96% syndiotactic polystyrene (PS) at an activity of 0.91 × 10⁷ g PS (mol Ti)^?1 (mol styrene)^?1 h^?1. Both activity and syndioselectivity can be increased using tri–isobutylaluminum (TIBA) to scavenge the system. ESR measurements indicate that the polymerization proceeds via titanium(IV) intermediates. Catalysts derived from 2/methylaluminoxane (MAO) as well as Cp*TiCl₃/MAO also function as syndioselective styrene polymerization catalysts, but are less active than the ‘cationic’; system derived from 1 and 2.     

Polymerization of vinyl chloride with half‐titanocene/methylaluminoxane catalysts

The polymerization of vinyl chloride (VC) with half‐titanocene /methylaluminoxane (MAO) catalysts is investigated. The polymerization of VC with the Cp*Ti(OCH₃)₃/MAO catalyst (Cp* = η⁵‐pentamethylcyclopentadienyl) afforded high‐molecular‐weight poly(vinyl chloride) (PVC) in good yields, although the polymerization proceeded at a slow rate. With the Cp*TiCl₃/MAO catalyst, the polymer was also obtained, but the polymer yield was lower than that with the Cp*Ti(OCH₃)₃/MAO catalyst. The polymerization of VC with the Cp*Ti(OCH₃)₃/MAO catalyst was influenced by the MAO/Ti mole ratio and reaction temperature, and the optimum was observed at the MAO/Ti mole ratio of about 10. The optimum reaction temperature of VC with the Cp*Ti(OCH₃)₃/MAO catalyst was around 20 °C. The stereoregularity of PVC obtained with the Cp*Ti(OCH₃)₃/MAO catalyst was different from that obtained with azobisisobutyronitrile, but highly stereoregular PVC could not be synthesized. From the elemental analyses, the ¹H and ¹³C NMR spectra of the polymers, and the analysis of the reduction product from PVC to polyethylene, the polymer obtained with Cp*Ti(OCH₃)₃/MAO catalyst consisted of only regular head‐to‐tail units without any anomalous structure, whereas the Cp*TiCl₃/MAO catalyst gave the PVC‐bearing anomalous units. The polymerization of VC with the Cp*Ti(OCH₃)₃/MAO catalyst did not inhibit even in the presence of radical inhibitors such as 2,2,6,6,‐tetrametylpiperidine‐1‐oxyl, indicating that the polymerization of VC did not proceed via a radical mechanism. © 2002 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 41: 248–256, 2003     

非MAO的茂钛均相催化体系催化苯乙烯间规聚合——[Cp~*TiMe_3]/[Ph_3C]~+[B(C_6F_5)_4]~-催化体系

非ＭＡＯ的茂钛均相催化体系催化苯乙烯间规聚合———［ＣｐＴｉＭｅ３］／［Ｐｈ３Ｃ］＋［Ｂ（Ｃ６Ｆ５）４］－催化体系许光学林尚安（中山大学高分子研究所广州５１０２７５）关键词茂钛络合物，茂金属催化剂，苯乙烯，间规聚苯乙烯间规聚苯乙烯（ｓＰＳ）由于具...     

茂钛催化剂苯乙烯原位间规聚合制备sPS/蒙脱土纳米复合材料

聚合物基纳米复合材料具有常规有机 /无机复合材料所没有的结构和形态 ,其性能较普通的聚合物复合材料更优异 ,因而引起人们的广泛关注 [1～ 4 ] .近年来的研究表明 ,运用插层聚合和熔融插层等方法可使某些具有层状结构的硅酸盐与聚合物产生特殊的界面作用 ,并以纳米尺寸均匀分     

Heterolytic cleavage of dihydrogen promoted by sulfido-bridged tungsten-ruthenium dinuclear complexes

A series of sulfido-bridged tungsten-ruthenium dinuclear complexes Cp*W(mu-S)(3)RuX(PPh(3))(2) (4a; X = Cl, 4b; X = H), Cp*W(O)(mu-S)(2)RuX(PPh(3))(2) (5a; X = Cl, 5b; X = H), and Cp*W(NPh)(mu-S)(2)RuX(PPh(3))(2) (6a; X = Cl, 6b; X = H) have been synthesized by the reactions of (PPh(4))[Cp*W(S)(3)] (1), (PPh(4))[Cp*W(O)(S)(2)] (2), and (PPh(4))[Cp*W(NPh)(S)(2)] (3), with RuClX(PPh(3))(3) (X = Cl, H). The heterolytic cleavage of H(2) was found to proceed at room temperature upon treating 5a and 6a with NaBAr(F)(4) (Ar(F) = 3, 5-C(6)H(3)(CF(3))(2)) under atmospheric pressure of H(2), which gave rise to [Cp*W(OH)(mu-S)(2)RuH(PPh(3))(2)](BAr(F)(4)) (7a) and [Cp*W(NHPh)(mu-S)(2)RuH(PPh(3))(2)](BAr(F)(4)) (8), respectively. When Cp*W(O)(mu-S)(2)Ru(PPh(3))(2)H (5b) was treated with a Br?nstead acid, [H(OEt(2))(2)](BAr(F)(4)) or HOTf, protonation occurred exclusively at the terminal oxide to give [Cp*W(OH)(mu-S)(2)RuH(PPh(3))(2)](X) (7a; X = BAr(F)(4), 7b; X = OTf), while the hydride remained intact. The analogous reaction of Cp+W(mu-S)(3)Ru(PPh(3))(2)H (4b) led to immediate evolution of H(2). Selective deprotonation of the hydroxyl group of 7a or 7b was induced by NEt(3) and 4b, generating Cp*W(O)(mu-S)(2)Ru(PPh(3))(2)H (5b). Evolution of H(2) was also observed for the reactions of 7a or 7b with CH(3)CN to give [Cp*W(O)(mu-S)(2)Ru(CH(3)CN)(PPh(3))(2)](X) (11a; X = BAr(F)(4), 11b; X = OTf). We examined the H/D exchange reactions of 4b, 5b, and 7a with D(2) and CH(3)OD, and found that facile H/D scrambling over the W-OH and Ru-H sites occurred for 7a. Based on these experimental results, the mechanism of the heterolytic H(2) activation and the reverse H(2) evolution reactions are discussed.     

SYNTHESIS OF NOVEL THIOPHENEDIMETHYLENE BRIDGED HOMOBINUCLEAR METALLOCENES AND THEIR CATALYTIC PROPERTIES FOR ETHYLENE POLYMERIZATION

By treating disodium(thiophenedirnethylene)dicyclopentadienide C_4H_2S(CH_2C_5H_4Na)_2 with two equivalent of CpTiCl_3 or CpZrCl_3 DME at 0℃ in THF,two new thiophenedimethylene bridged binuclear metallocenes [Cl_2MC_5H_5][C_5H_4CH_2C_4H_2SCH_2C_5H_4][C_5H_5MCl_2](M=Ti 3,M=Zr 4)were synthesized in high yield and their structures were characterized by ~1H-NMR.These complexes were used as catalysts for ethylene polymerization in the presence of methylaluminoxane(MAO).The effects of polymerization temperature,time,concentration of catalyst,molar ratio of MAO/Cat on polymerization were studied in detail.The catalytic activities of thiophenedimethylene bridged binuclear metallocene catalysts(3,4)reached 2.44×10~5 g PE mol~(-1)·cat~(-1)·h~(-1),9.61×10~5 g PE mol~(-1)·cat~(-1)·h~(-1) respectively,which are higher than that of pheneyldimethylene bridged binuclear metallocene catalysts and much higher than that of corresponding mononuclear metallocenes(Cp_2TiCl_2 and Cp_2ZrCl_2).The molecular weight distribution curves of polyethylenes produced by binuclear metallocene catalysts(3,4)and by mononuclear metallocene catalyst have only single peak,but the former(MWD=3.5-4.7)is obviously broader than the latter(MWD=2.0-2.2).