稀土络合催化环氧乙烷聚合

以稀土化合物-二(2-乙基己基)膦酸钕[Nd(P_(204)_3],三异丁基铝和水组成的络合催化剂,引发环氧乙烷聚合.结果表明,稀土络合催化剂是制备高分子量聚环氧乙烷的新型催化剂.聚合反应速度与环氧乙烷浓度呈一级关系,与Nd(P_(204))_3浓度呈一级关系.聚合的总活化能E_α=33.8kJ/mol,表观速率常数K_p=1.67×10~(-3)s~(-1)·mol~(-1)·1     

稀土络合催化苯乙炔直接成膜聚合 Ⅰ.环烷酸钕盐络合催化苯乙炔直接成膜聚合

首次应用环烷酸钕-三异丁基铝络合催化体系在己烷-甲苯混合溶剂中,于室温下使苯乙炔直接聚合成膜获得成功。研究了成膜聚合反应特征及动力学行为。发现溶剂及聚合温度的选择是成膜的关键。成膜的临界条件为:[Nd]>1×10~(-5)mol/ml;[M]≥1×10~(-4)mol/ml;Al/Nd>1(摩尔比)。成膜聚合具有典型的链锁聚合反应特征,在适宜的聚合条件下,转化率可达96.5％。在不同溶剂和不同温度下聚合反应速率不同。聚苯乙炔膜可为黄色、橙色或红色,这与聚合时间、温度、单体浓度以及己烷/甲苯(体积比)有关。     

甲基丙烯酸丁酯的Nd（Oct）3—Al（i—Bu）3配合催化聚合

甲基丙烯酸丁酯(BMA)在2-乙基己酸钕[Nd(Oct)_3]和三异丁基铝[Al(i-Bu)_3]配合催化下的聚合反应结果表明。以正己烷和石油醚为溶剂的聚合转化率高于甲苯和四氢呋喃体系。4种不同配体的钕盐的聚合转化率差别不大。但是,以Nd(Oet)_3-Al(i-Bu)_3为催化剂时聚甲基丙烯酸丁酯的分子量最高。聚合反应速度与单体浓度和催化剂浓度均成一次方关系。甲基丙烯酸丁酯的聚合反应活化能为47.40kJ/mol。     

稀土络合催化苯乙炔直接成膜聚合 Ⅲ.各种稀土环烷酸盐络合催化苯乙炔直接成膜聚合

采用十四种稀土(La、Ce、Pr、Nd、Sm、Eu、Gd、Dy、Ho、Er、Tm、Yb、Lu、Y)环烷酸盐-三异丁基铝络合催化体系,在室温下均能使苯乙炔(PA)于混合溶剂中直接成膜聚合。成膜聚合的最佳条件大致相同;[Ln(naph)_3]=3×10~(-5)mol/ml,[M]=3×10~(-4)mol/ml,Al/Ln:7,V_h/V_t=1。不同稀土元素显示的催化活性次序为Gd>Lu>Nd～Ce>Ho>Sm>Dy～Eu>Er>Pr>>La>Y～Tm>Yb。苯乙炔在含苯溶剂中反应活性较高,在卤代烃中反应活性很低。混合溶剂比单组分溶剂更有利于成膜聚合并有高的催化活性和高的分子量。各种稀土聚苯乙炔膜的结构和性能基本相同。稀土聚苯乙炔为片层结晶,具有较高的结晶性。     

超高分子量聚苯乙烯的合成和聚合反应动力学

杯芳烃钕与Mg(n Bu) 2 、HMPA所组成的三元络合催化剂用于苯乙烯配位聚合能以高收率制得超高分子量聚苯乙烯 .以甲苯为溶剂 ,在一定条件下制成三元配位催化剂 ,当 [Nd]=8× 10 - 4mol L ,[St]=4 .0mol L ,Mg Nd =2 0 .0 (摩尔比 ) ,HMPA Mg =1.0 (摩尔比 ) ,5 0℃聚合 4 5min ,聚合转化率可达到 80 %左右 .所得聚苯乙烯的重均分子量高达 2 10× 10 4 ,分子量分布指数为 1.6 1.间规聚苯乙烯含量为 81% .动力学研究表明 ,聚合反应速率与单体和主催化剂 杯 [6 ]芳烃钕的浓度分别呈 1次方关系 ,聚合反应的表观活化能为 4 1.7kJ mol     

稀土络合催化苯乙炔直接成膜聚合 Ⅴ.苯乙炔在钕、铁混合络合催化体系中的直接成膜聚合

乙酰丙酮(AA)、苯酰丙酮(BA)为配体的钕(Nd)、铁(Fe)混合催化剂与三异丁基铝[Al(i-Bu)_3]组成络合催化体系,能使苯乙炔在甲苯/己烷混合溶剂中直接聚合成膜。研究了其聚合反应规律及动力学行为,并对聚苯乙炔膜进行了全面表征,揭示了钕、铁两组分催化剂具有协同催化效应。     

稀土络合催化苯乙烯-马来酸酐配位共聚

本文首次应用稀土配位催化剂NdL_3-A1(i-Bu)_3,在苯溶剂中,50℃下使苯乙烯-马来酸酐共聚,制得富于交替,数均分子量高达6—8.5×10~5的白色粉末共聚物。系统地研究了共聚合反应的特征及动力学行为,共聚合反应具有低的表现活化能(10.5kJ/mol),并且不被对苯二酚所阻聚。不同配体稀土(钕)催化剂活性次序为:Nd(naph)_3>Nd(P_(507))_3～NdCl_3·6H_2O>Nd(P_(204))_3>Nd(acac)_3·3H_2O,并且,初步揭示了共聚合反应的机理——两种单体形成电荷转移络合物参与增长的配位共聚。     

稀土-其它过渡金属混合催化剂用于共轭双烯烃的聚合——Ⅳ.(NdCl_3+FeCl_3)·nphen-HAI(i-Bu)_2体系对异戊二烯的聚合

本文报道由(NdCl_3+FeCl_3)·nphen-HAl(i-Bu)_2催化体系引发异戊二烯聚合的结果。在适当Nd/Pe比下,该体系对异戊二烯聚合的活性可超过单一钕或铁催化剂的活性,同时随催化剂中钕和铁含量的不同,所得产物的微观结构变化很大,当体系中钕含量由100％→0时,产物的顺-1,4结构含量由94.4％→22.1％,而3,4结构含量由5.6％→77.9％。Al/M(N=Nd+Fe)比、单体浓度和聚合温度不仅对聚合活性有影响,对产物的微观结构影响也较大。事实表明,该聚合体系中存在着两种过渡金属(Nd和Fe)活性中心,它们按各自的机理进行异戊二烯的聚合。     

稀土络合催化苯乙炔直接成膜聚合 Ⅴ.苯乙炔在钕、铁混合络合催化体系中的直接成膜聚合

 乙酰丙酮(AA)、苯酰丙酮(BA)为配体的钕(Nd)、铁(Fe)混合催化剂与三异丁基铝[Al(i-Bu)₃]组成络合催化体系,能使苯乙炔在甲苯/己烷混合溶剂中直接聚合成膜。研究了其聚合反应规律及动力学行为,并对聚苯乙炔膜进行了全面表征,揭示了钕、铁两组分催化剂具有协同催化效应。     

稀土催化异戊二烯—马来酸酐交替共聚

首次用 Nd( naph) 3 -Al Et3 催化体系合成异戊二烯 -马来酸酐交替共聚物 .实验结果表明 ,共聚反应适宜条件为 :[M]总 =2 .6mol/L( [Ip]/[MAn]=1 ) ,n( Al) /n( Nd) =1 0 ,[Nd]=5× 1 0 -3 mol/L,甲苯 /二氧六环混合溶剂 (体积比为 2 /5) ,于 5℃聚合 2 h.共聚物收率达到 70 % .用元素分析、 IR和 13 C NMR对共聚物进行表征 ,所得共聚物为交替结构     

Copolymerization of butadiene and styrene with neodymium naphthenate based catalyst

Copolymerization of butadiene (Bd) and styrene (St) was carried out in toluene at 50 °C by a conventional rare earth catalytic system, Nd(naph)₃-Al(i-Bu)₃-Al(i-Bu)₂Cl. It exhibited a high catalytic activity and high stereospecificity in the copolymerization. The influences of the conditions in polymerization on the yield, composition, microstructure and molecular weight of copolymer were thoroughly studied. According to the 13C-NMR spectrum, the resultant copolymer containing 18% St units, and the diad fraction of St-trans Bd or St-vinyl Bd can hardly be found in its 13C-NMR. The cis-1,4 content of Bd unit of the copolymer decreased little with the increase of St content. The GPC curves indicate the presence of two kinds of active sites in the polymerization.     

THE POLYMERIZATION OF EPICHLOROHYDRIN WITH Nd(i-oPr)_3-Al(i-Bu)_3 SYSTEM

Epichlorohydrin (ECH) was polymerized with a rare earth catalytic system: Nd (i-OPr)_3-Al (i-Bu)_3. The effects of Al/Nd molar ratio, solvents, the polymerization time and temperature,the aging time and temperature of the catalyst preparation were studied. The results showed thatat a low Al/Nd molar ratio (4) of the Nd(i-OPr)_3-Al(i-Bu)_3 system ECH polymerized at a lowtemperature (248K) with a high conversion. The average molecular weight ofpolyepichlorohydrin (PECH) ranged from 1×10~5 to 3×10~5.     

Styrene polymerization with rare earth catalysts using a magnesium alkyl cocatalyst

A new highly active rare earth coordination catalyst composed of rare earth phosphonate, di-n-butylmagnesium (MgBu), and hexamethyl phosphoramide (HMPA) for the polymerization of styrene has been developed for the first time. High molecular weight polystyrene (M̄_ν = 50–70 × 10⁴) in 100% conversion could be prepared at following conditions: [Nd] = 6–8 × 10⁻⁴ mol/L, [St] = 3.0 mol/L, Mg/Nd = 11, and HMPA/Mg = 1–1.5 (molar ratio). The catalytic activity of this new catalyst is 3530 g PSt/g Nd. Kinetics study shows that the polymerization rate is of first order with respect to both monomer concentration and catalyst concentration, and activation energy of the polymerization is 40.1 kJ/mol. © 1996 John Wiley & Sons, Inc.     

稀土配位催化马来酸酐-苯乙烯-N-苯基马来酰亚胺三元共聚合

采用稀土配位催化剂研究了马来酸酐、苯乙烯和N 苯基马来酰亚胺的三元共聚合反应 .考察了Al La物质的量的比、不同稀土元素、催化剂浓度、聚合反应时间、单体配比等因素对共聚合反应的影响 .利用核磁、红外、热分析等方法对共聚物进行了初步的表征     

铁系催化剂催化降冰片烯与丙烯酸甲酯共聚合

研究了Fe(acac)3-Al(i-Bu)3(acac=乙酰丙酮)催化降冰片烯(NB)与丙烯酸甲酯(MA)共聚反应条件影响、第三组份影响及催化剂铁铝比影响.并用核磁共振、红外光谱和元素分析方法研究了共聚物的组成,用热分析方法研究了共聚物的分解温度,并用电镜分析了共聚物的膜结构.结果表明,铁系催化剂在温和的反应条件下有较好的催化性能,并可获得能够形成有序多孔膜的共聚物.     

Poly(styrene‐b‐isobutylene) multiarm star‐block copolymers

Multiarm star‐branched polymers based on poly(styrene‐b‐isobutylene) (PS‐PIB) block copolymer arms were synthesized under controlled/living cationic polymerization conditions using the 2‐chloro‐2‐propylbenzene (CCl)/TiCl₄/pyridine (Py) initiating system and divinylbenzene (DVB) as gel‐core‐forming comonomer. To optimize the timing of isobutylene (IB) addition to living PS⊕, the kinetics of styrene (St) polymerization at −80°C were measured in both 60 : 40 (v : v) methyl cyclohexane (MCHx) : MeCl and 60 : 40 hexane : MeCl cosolvents. For either cosolvent system, it was found that the polymerizations followed first‐order kinetics with respect to the monomer and the number of actively growing chains remained invariant. The rate of polymerization was slower in MCHx : MeCl (k_app = 2.5 × 10⁻³ s⁻¹) compared with hexane : MeCl (k_app = 5.6 × 10⁻³ s⁻¹) ([CCl]_o = [TiCl₄]/15 = 3.64 × 10⁻³M; [Py] = 4 × 10⁻³M; [St]_o = 0.35M). Intermolecular alkylation reactions were observed at [St]_o = 0.93M but could be suppressed by avoiding very high St conversion and by setting [St]_o ≤ 0.35M. For St polymerization, k_app = 1.1 × 10⁻³ s⁻¹ ([CCl]_o = [TiCl₄]/15 = 1.82 × 10⁻³M; [Py] = 4 × 10⁻³M; [St]_o = 0.35M); this was significantly higher than that observed for IB polymerization (k_app = 3.0 × 10⁻⁴ s⁻¹; [CCl]_o = [Py] = [TiCl₄]/15 = 1.86 × 10⁻³M; [IB]_o = 1.0M). Blocking efficiencies were higher in hexane : MeCl compared with MCHx : MeCl cosolvent system. Star formation was faster with PS‐PIB arms compared with PIB homopolymer arms under similar conditions. Using [DVB] = 5.6 × 10⁻²M = 10 times chain end concentration, 92% of PS‐PIB arms (M_n,PS = 2600 and M_n,PIB = 13,400 g/mol) were linked within 1 h at −80°C with negligible star–star coupling. It was difficult to achieve complete linking of all the arms prior to the onset of star–star coupling. Apparently, the presence of the St block allows the PS‐PIB block copolymer arms to be incorporated into growing star polymers by an additional mechanism, namely, electrophilic aromatic substitution (EAS), which leads to increased rates of star formation and greater tendency toward star–star coupling. © 1999 John Wiley & Sons, Inc. J Polym Sci A: Polym Chem 37: 1629–1641, 1999     

稀土催化异戊二烯聚合动力学的研究

用膨胀计研究了Ln(Naph)_3-Al(i-Bu)_3-Al_2Et_3Cl_3催化异戊二烯聚合动力学。发现在低聚合速度条件下体系显示稳态聚合特征,在较高聚合速度条件下聚合初期速度有一增长过程。建立了聚合速度方程并估算了增长链平均寿命、增长链浓度、催化剂效率以及链增长速度常数。