三氟甲基磺酸三甲基硅酯/四氯化钛复合体系引发 1, 3-戊二烯的阳离子聚合

研究了以三氟甲基磺酸三甲基硅酯[(CH~3)~3SiOSO~2CH~3,TMSOFf]为主引发剂,TiCl~4为共引发剂的复合引发体系对1,3-戊二烯(PD)的聚合行为。TMSOTf/TiCl~4复合体系引发PD不但比单独的TiCl~4引发具有更高的引发活性,而且提高了聚合物分子量,能把聚合反应速率提高8.8倍,把聚合物的收率从TiCl~4引发的62.5%提高到95%以上。对该复合体系聚合PD的动力学,反应机理所作的研究表明:TMSOTf和TMSOTf/TiCl~4都是通过它们与体系中残存水通过水解生成的质子酸引发进行的,聚合反应属一级反应。在该体系中加入酮类后,产率和分子量均降低,但均随着酮类的位阻的增加而增大。     

三甲基硅化合物复合体系引发1,3-戊二烯阳离子聚合研究

研究了三甲基硅化合物 ,主要是三甲基硅酯和三甲基硅氯化物 (TMSCI)与路易斯酸所形成的复合引发体系引发聚合 ,1,3 戊二烯 (PD)的聚合反应行为 ,考察了引发体系引发PD聚合所得聚合物的产率 ,分子量及分子量分布 ,聚合反应速率和聚合反应机理等 ;研究了多种给电体———醚、酮对聚合反应的影响     

(CH_3)_3SiOSO_2CF_3/SbCl_3阳离子引发体系引发1,3-戊二烯聚合

研究了三氟甲基磺酸三甲基硅酯／三氯化锑（（ＣＨ３）３ＳｉＯＳＯ２ＣＦ３／ＳｂＣｌ３）复合引发体系对１,３ 戊二烯的聚合行为．在（ＣＨ３）３ＳｉＯＳＯ２ＣＦ３引发剂中加入ＳｂＣｌ３后,使聚合反应速率提高了２４倍,产率从（ＣＨ３）３ＳｉＯＳＯ２ＣＦ３引发的５５％提高到８０％以上,分子量提高１７倍．在聚合体系中加入酮类后,产率和分子量相对于（ＣＨ３）３ＳｉＯＳＯ２ＣＦ３／ＳｂＣｌ３配比为０２：１时引发所得聚合物均呈下降趋势;但对不同的酮来说,随着酮的位阻的增大,聚合物的产率和分子量均增大．聚合物的１Ｈ ＮＭＲ图和红外谱图数据均证明该聚合反应是通过（ＣＨ３）３ＳｉＯＳＯ２ＣＦ３与体系中残存的水水解所形成的质子酸ＨＯＳＯ２ＣＦ３与ＳｂＣｌ３反应所形成的复合体系引发进行的．     

光辅助引发制备聚甲基丙烯酰氧乙基三甲基氯化铵

在紫外灯照射和引发剂作用下,通过水溶液聚合法制备聚甲基丙烯酰氧乙基三甲基氯化铵(PDMC).考察了氧化-还原引发体系、氧化-还原和偶氮类引发剂用量、单体浓度、溶液pH、引发温度和络合荆用量等因素对产物特性黏数的影响,并与无光照条件下的聚合结果进行了对比.用红外光谱对所得产物进行了表征.结果表明:光辅助引发可以显著促进DMC的聚合反应.采用硫酸亚铁-过硫酸铵引发剂体系,在引发剂质量分数为0.002 0%,单体质量分数为75%,pH=4,引发温度为10℃,络合剂质量分数为0.003 0%时,所得聚合物的特性黏数达8.4 dL/g以上.     

FeBr3/Me6TREN催化MMA反向原子转移自由基聚合研究

对FeBr3/Me6TREN催化的反向原子转移自由基聚合进行了研究.在不同的催化剂、引发剂的配比、聚合温度和配体用量等条件下,该催化体系催化的MMA聚合反应动力学为一级反应,聚合物分子量可控,分子量分布很窄,说明该体系催化的聚合反应为活性可控聚合.通过实验计算了反应的活化能,并利用UV光谱对催化剂进行了研究.     

TiCl_4共引发异丁烯正离子聚合合成反应活性聚异丁烯

由H2O/TiCl4/甲醇或乙醚体系引发异丁烯在二氯甲烷与己烷混合溶剂中进行正离子聚合,探讨甲醇用量、聚合时间等因素对正离子聚合以及产物分子量、分子量分布和末端基结构的影响,并在此基础上探讨TiCl4共引发混合C4馏分中异丁烯选择性正离子聚合以制备活性聚异丁烯的可行性.结果表明,含氧试剂对聚合反应起到明显的调节作用,可适当稳定碳正离子活性中心,降低链增长速率,降低聚合产物的分子量(Mn=1600~4600),使分子量分布明显变窄(Mw/Mn=1.35~2.05),并可调节大分子链末端基结构及其含量.降低聚合体系中微量单体浓度以及适当延长聚合反应时间,均有利于提高聚异丁烯大分子链末端α-双键结构含量.通过TiCl4共引发异丁烯正离子聚合制备出末端α-双键含量可以达到70%以上的低分子量高反应活性聚异丁烯.此外,该引发体系还可引发混合C4馏分原料中异丁烯进行高选择性正离子聚合,得到Mn=2000、Mw/Mn=2.59、端基α-双键含量为38.9%的聚异丁烯.     

1,3戊二烯阳离子聚合体系交联反应的研究

研究了芳烃、卤代烃和醚对正己烷介质中AlCl3 引发的 1 ,3 戊二烯阳离子聚合反应的影响 ,讨论了这些组分对交联反应的抑制作用 .聚合体系引入芳烃后通过链转移机理抑制了凝胶的生成 ;卤代烃在聚合反应中可与AlCl3 形成复合引发体系参与引发过程 ,并可避免凝胶生成 ,也能作为链转移剂通过链转移机理抑制交联反应 ;醚类在聚合反应中的作用为 :与AlCl3 络合参与引发反应使得聚合物分子量升高 ,或与碳阳离子作用降低其活性并抑制交联反应 .     

一种大分子引发剂的引发作用研究

将溶液聚合合成的α-甲基苯乙烯(AMS)和甲基丙烯酸缩水甘油酯(GMA)的低相对分子质量共聚物(计为PAG)作为大分子引发剂,分别研究了PAG引发单体甲基丙烯酸甲酯(MMA)和苯乙烯(St)的本体聚合反应,采用GPC和FTIR等手段对聚合产物进行了表征.研究结果表明,在加热到一定温度时,PAG具有引发作用,可以引发MMA和St进行本体聚合反应;聚合产物具有再引发功能,且其分子量与聚合物产率和聚合反应时间之间均有较好的线性关系.     

苯氧铜/正丁基锂体系引发MMA负离子聚合及其活性特征的研究

采用苯氧铜/正丁基锂(PhOCu/n-BuLi)体系引发MMA聚合, 通过GPC, ¹H NMR对聚合物进行了表征. 实验结果表明, 该体系聚合反应速度较快, 温度、引发体系组成是影响聚合物分子量及其分布、单体转化率、引发剂引发效率、聚合物的立构规整性的主要因素; －40 ℃时分子量分布比较窄, 但引发效率也比较低(大约15%). 低引发效率、宽分子量分布与引发剂的聚集状态有关. 分子量与单体浓度、引发剂浓度的关系说明, 该体系具有一定程度的活性聚合特点.     

紫外光引发丙烯酰胺分散聚合研究

以聚丙烯酸接枝壬基酚聚氧乙烯(PAA -g -NPEO)作分散剂,紫外光(UV)引发丙烯酰胺(AM )在叔丁醇 水(TBA /H2 O)体系中进行了分散聚合.考察了聚合反应特征以及醇水比、初始单体浓度、引发剂浓度、分散剂浓度、表面入射光强、反应温度、液层厚度等参数对聚合产物粒径及分子量的影响.结果表明该聚合体系不存在诱导期,反应速度快,光照4 0min转化率可达到90 % ,产物分子量达6 . 5×10 6 .透射电镜(TEM)观察显示所得聚合物粒子基本为球形,粒径分布较为均匀.     

环戊二烯基(或茚基)二氯化钕体系催化丁二烯聚合反应动力学

<正> 环戊二烯基(或茚基)轻烯土二氯化物C_5H_5NdCl_2·nC_4H_8O(C_5H_5为环戊二烯基、C_4H_8O为四氢呋喃、Ln代表Pr或Nd、n=0,1,2,3)、C_5H_5LnCl_2·HCl·nC_4H_8O、C_9H_7LnCl_2·nC_4H_8O和C_9H_7LnCl_2·HCl·nC_4H_8O(C_9H_7为茚基)能与烷基铝组合形成一类新型丁二烯聚合催化剂,虽然稀土催化丁二烯聚合反应动力学已有报道,但是其催化体系、聚合条件和研究方法各不相同。过去的研究多应用稳态动力学处理方法侧重于聚合速度的研究。本文的目的在于通过聚合物活性链的变化,考察C_5H_5NdCl_2·nC_4H_8O     

(CH3)3SiCl/TiCl4 INITIATING SYSTEM FOR CATIONIC POLYMERIZATION OF 1,3-PENTADIENE

Cationic polymerizations of 1,3-pentadiene (PD) initiated by trimethylsilyl chloride (TMSCl) incombination with TiCl_4 were carried out in n-hexane at 30℃. The yield of polymer was greatly increased bythe addition of TMSCl, indicating that the TMSCl/TiCl_4 combination is an efficient initiating system for PDcationic polymerization. However, the introduction of TMSCl gave rise to a drop in the molecular weight ofthe polymer. Kinetic results demonstrated that the polymerization initiated by TMSCl/TiCl_4 is 4.5 times fasterthan that induced by TiCl_4 alone. Various ethers were used to mediate the TMSCl/TiCl_4 initiating system.Adding diphenyl ether could increase both the yield and molecular weight of the polymer. Structural evidenceillustrates that the polymerization is indeed initiated by TiCl_4 in combination with HCl resulting fromhydrolysis by adventitious water.     

Polymerization of n-Octylallene with Rare Earth Catalyst Composed of Ln(P204)3/Al(i-Bu)3

Polymerization of n‐octylallene was successfully carried out using a conventional binary rare earth catalytic system composed of rare earth tris(2‐ethylhexylphosphonate) (Ln(P₂₀₄)₃) and tri‐isobutyl aluminum (Al(i‐Bu)₃) for the first time. The effects of catalyst, solvent, reaction time and temperature on the polymerization of n‐octylallene were studied. The resulting poly(n‐octylallene) has weight‐average molecular weight of 11000, molecular weight distribution of 1.4 and 96% yield under the moderate reaction conditions: [Al]/[Y] =50 (molar ratio), [n‐octylallene]/[Y] =100 (molar ratio), polymerized at 80°C for 20 h in bulk. The poly(n‐octylallene) obtained consisted of 1,2‐ and 2,3‐polymerized units, and was characterized by FT‐IR, ¹H NMR and GPC. Further investigation shows that the polymerization of n‐octylallene has some living polymerization characteristics, preparing the polymer with controlled molecular weight and narrower molecular weight distribution.     

膦亚胺半茂钛催化体系合成无规聚丙烯弹性体的研究

采用2种膦亚胺半茂化合物[(t-Bu)_3P=N]CpTiCl_2(PT1)和[(t-Bu)_3P=N]CpTiMe_2(PT2)为主催化剂,分别以甲基铝氧烷(MAO)或[Ph_3C][B(C_6F_5)_4]为助催化剂用于丙烯聚合研究.详细考察了不同n(Al)/n(Ti)、反应温度、反应压力、反应时间等因素对丙烯聚合活性、分子量与分子量分布及其分子结构的影响.还与典型的(rac-[En(IndH_4)_2]ZrCl_2)(1),CpTiCl_3(2)及Cp_2TiCl_2(3)催化剂的催化效果进行了比较.凝胶渗透色谱(GPC)、核磁共振氢谱与碳谱(1H/13C-NMR)、示差扫描量热分析(DSC)和红外(FTIR)分析结果表明:这2种催化剂催化丙烯聚合的活性可高达3.25×10~6g聚合物/molTi×h,重均分子量高达4.4×10~5,分子量分布2.0.降低温度及升高反应压力和延长反应时间都能使聚丙烯分子量增加.观察到聚合初期产物分子量随聚合时间线性增大.在-100~200oC范围内没有观察到熔融峰出现,但在-3.7~-2.6oC区间可以观察到有玻璃化转变温度出现.序列结构分析表明,所生成的聚丙烯为无规结构,但二元组r(62.28%)高于m(37.72%),意味着聚合过程中有间规聚合倾向.[mr/(2mm+mr)]+[mr/(2rr+mr)]=1.04的计算结果进一步说明,由此类催化剂体系催化丙烯聚合生成的产物立体结构序列分布服从伯努利统计模型,聚合主要以1,2-插入方式为主,同时含有少量2,1-插入.     

笼形聚羧酸钒(Ⅳ)—硫脲体系引发丙烯腈聚合动力学

研究了笼形聚羧酸钒(PV)-硫脲(TU)体系在硝酸溶液中引发丙烯腈(AN)聚合动力学。表观聚合速度(R_p)是 R_p=9.7×10~5e~(-10500)/RT[AN]~1.0[PV]~0.50[TU]~0.76[HNO_3]~1.5聚合诱导期(τ)随反应条件而变化,聚合温度越高,引发种浓度越大,聚合诱导期越短,但与单体浓度的变化无关。 1/τ=4.6×10~(12)e~(-13500)/RT[AN]~0[PV][TU]~(-3/2)[HNO_3]~3=K_τ·R_i聚合物分子量随单体浓度增大而提高,但随聚合温度及引发种浓度增大而下降,即 笼形聚羧酸钒—硫脲体系引发丙烯腈聚合的动力学参数和引发机理与杨梅型聚羧酸钒—硫脲体系在相同的条件下引发聚合的行为有明显的区别,认为是和两种树脂大分子链的空间结构所引起的传质阻力有关。     

Similarities and differences of epoxide, aldehyde and peroxide initiators for Cp2TiCl-catalyzed styrene living radical polymerizations

Cp₂TiCl is the first example of a single electron transfer (SET) agent that both provides initiating radicals from three different types of functionalities (i.e. radical ring opening of epoxides and reduction of aldehydes and peroxides) and doubles as mediator for the living radical polymerization of styrene (St) by reversibly endcapping the growing polymer chains. An initiator (I) comparison was performed using 1,4-butanediol diglycidyl ether (BDE), benzaldehyde (BA) and benzoyl peroxide (BPO) as models. The investigation of the effect of reaction variables was carried out over a wide range of experimental conditions ([Cp₂TiCl₂]/[I] = 0.5/1-4/1; [Zn]/[Cp₂TiCl₂] = 0.5/1-3/1, [St]/[I] = 50/1-400/1 and T = 60-130 °C) to reveal living polymerization features such as a linear dependence of molecular weight on conversion and narrow molecular weight distribution (M_w/M_n) for each initiator class. However, progressively lower polydispersities and larger initiator efficiencies are obtained with increasing the [Cp₂TiCl₂]/[I] and [Zn]/[Cp₂TiCl₂] ratios and with decreasing temperature. Accordingly, optimum conditions correspond to [St]/[I]/[Cp₂TiCl₂]/[Zn] = [50-200]/[1]/[2-3]/[4-6] at 70-90 °C. By contrast to peroxides, aldehydes and the more reactive epoxides provide alcohol end groups useful in block or graft copolymers synthesis.     

Synthesizing UHMWPE Using Ziegler-Natta Catalyst System of MgCl2(ethoxide type)/ TiCl4/tri-isobutylaluminum

Summery: A Ziegler-Natta catalyst of MgCl₂ (ethoxide type)/TiCl₄ has been synthesized. In order to obtain ultra high molecular weight polyethylene (UHMWPE) tri-isobutylaluminum which is less active to chain transfer was used as cocatalyst. Slurry polymerization was carried out for the polymerization of ethylene while, dilute solution viscometry was performed for the viscosity average molecular weight (Mv) measurement. The effect of [Al]/[Ti] molar ratio, temperature, monomer pressure and polymerization time on the Mv and productivity of the catalyst have been investigated. The results showed increasing [Al]/[Ti] ratio in the range of 78–117, decreased the Mv of the obtained polymer from 7.8 × 10⁶ to 3.7 × 10⁶ however, further increase of the ratio, resulted in decreased of by much slower rate up to [Al]/[Ti] = 588. The higher pressure in the range of 1–7 bars showed the higher the Mv of the polymer obtained, while increasing temperature in the range of 50 to 90 °C decreased the Mv from 9.3 × 10⁶ to 3.7 × 10⁶. The Mv rapidly increase with polymerization time in the first 15 minutes of the reaction, this increase was slowly up to the end of the reaction (120 min). Increasing [Al]/[Ti] ratio raised productivity of the catalyst in the range studied. Rising reaction temperature from 50 to 75 °C increased the productivity of the catalyst however, further increase in the temperature up to the 90 °C decreased activity of the catalyst. Monomer pressure in the range 1 to 7 bars yields higher productivity of the catalyst. Also by varying polymerization conditions synthesizing of UHMWPE with Mv in the range of 3 × 10⁶ to 9 × 10⁶ was feasible.     

活性正离子聚合制备聚(异丁烯-b-α-甲基苯乙烯)嵌段共聚物

以2-氯-2,4,4-三甲基戊烷(TMPCl)/TiCl4/质子捕捉剂(DtBP)为引发剂体系,引发异丁烯聚合,随后加入1,1-二(4-甲基苯基)乙烯作为封端剂稳定末端碳正离子,再引入四异丙醇钛(Ti(OiPr)4),降低Lewis酸性,继续引发α-甲基苯乙烯聚合,实现活性正离子聚合制备聚(异丁烯-b-α-甲基苯乙烯)嵌段共聚物.考察了α-甲基苯乙烯聚合时间对单体转化率、产物的dn/dc值、分子量及其分布的影响以及四异丙醇钛对聚合速率的影响.并通过体积排斥色谱法/紫外检测器/示差折光指数/多角激光光散射、1H-NMR以及DSC以对产物进行表征.实验结果表明,嵌段共聚物分子量分布窄(MWD≤1.2),单体转化率与分子量呈线性关系,聚合速率对单体浓度呈一级动力学关系,具有活性聚合的特征.Ti(OiPr)4能有效稳定活性中心,降低聚合速率.聚(异丁烯-b-α-甲基苯乙烯)嵌段共聚物的DSC测试发现明显的两个Tg,表明存在微相分离结构.     

Imidazolium ionic liquids with short polyoxyethylene chains

It has been observed by us earlier that imidazolium ionic liquids ([bmim][BF₄] react with paraformaldehyde giving in nearly quantitative yield imidazolium ionic liquids substituted at 2‐position with hydroxymethyl group ([bhmim][BF₄]). In this article, we describe the application of those ionic liquids (after converting hydroxyl group into alkoxide anion by reaction with sodium hydride) as initiators for anionic polymerization of ethylene oxide (EO). Up to DP_n ～ 30 polymerization proceeds without side reactions, and the product is exclusively low‐molecular‐weight polyoxyethylene containing imidazolium head group (POE‐IL) with DP_n equal to [EO]/[bhmim] ratio. By increasing [EO]/[bhmim] ratio further, side reaction start to interfere, and macromolecules that does not contain imidazolium head groups are also formed, as evidenced by analysis of MALDI TOF spectra. Blending of POE‐IL with high‐molecular‐weight POE leads to significant reduction of crystallinity of POE. © 2008 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 46: 6961–6968, 2008