用双官能团引发剂进行的基团转移嵌段共聚研究

本文用二种双官能团引发剂进行基团转移嵌段共聚研究,得到了一系列实测分子量和理论分子量相近、分子量分布较窄的A-B-A型嵌段共聚物。用GPC、~1H-NMR、DSC等手段对嵌段共聚物进行了表征,证明确是两相嵌段共聚丙烯酸酯。发现位阻较大的单体作为第二单体时不利于聚合。过高的催化剂用量使嵌段共聚的总转化率降低。使用极性较大的溶剂可缩短第一步聚合的诱导期,但不影响第二步聚合的诱导期,即极性较大的溶剂有利于催化剂的离解。单体浓度增大使共聚物的分子量减小,多分散性指数增大。可通过单体投料比改变共聚物的热形变温度。     

六甲基环三硅氧烷（D3）阴离子开环聚合机理与动力学研究

本文从聚合机理和反应动力学两方面综述了近年来六甲基环三硅氧烷（D3）的阴离子开环聚合研究进展。Frye等人提出在非极性的碳氢溶剂中会形成引发剂的的三种加成物质,在不加入促进剂的情况下不会进行D3的开环聚合,这一开环聚合机理成为随后D3阴离子开环聚合机理研究的基础,研究者采用MALDI-TOF研究聚合机理得到的结论证实了这一机理的正确性,促进剂、溶剂、引发剂的类型和聚合步骤会改变活性链末端的缔合和解缔合的平衡能力,对D3开环过程中的反咬和再分布副反应有显著影响。D3开环聚合增长速率对单体浓度为一级,不同的促进剂和引发剂会显著改变活性链末端的缔合能力,从而显著影响聚合动力学。     

淀粉乙酸酯的阴离子接枝己内酯聚合研究

将淀粉在二甲基甲酰胺、吡啶存在下 ,以乙酸酐进行部分乙酰化 ,制备取代度为 0 7～ 1 9的淀粉乙酸酯 (St Ac) .以萘钠与淀粉乙酸酯中残余的羟基反应 ,将羟基转化为醇盐 (ONa) ,引发己内酯进行阴离子开环接枝聚合 ,合成了淀粉 聚己内酯接枝共聚物 (St g PCL) .采用凝胶渗透色谱法 (GPC)研究了接枝前后聚合物分子量的变化情况 ,并以接枝率、单体转化率对接枝反应进行了表征 .研究了接枝条件如温度、溶剂、引发剂和单体的用量对接枝率及单体转化率的影响 .研究发现随着反应温度升高 ,接枝率、单体转化率呈S曲线变化 ,单体浓度、引发剂浓度的增大有利于接枝反应的进行 .     

降冰片烯开环易位聚合反应的分子量及分子量分布控制

使用Grubbs催化剂催化降冰片烯单体进行开环易位聚合反应, 研究了催化剂搅拌溶解时间、聚合反应的溶剂极性和三苯基膦的加入等反应条件对降冰片烯单体ROMP反应分子量及分子量分布的影响, 从而得到降冰片烯ROMP反应的最佳条件.     

正丁基锂四氢呋喃引发α-甲基苯乙烯阴离子平衡聚合动力学及反应机理研究

本文研究了以正丁基锂为引发剂,四氢呋喃为添加剂,环己烷为溶剂中的α-甲基苯乙烯阴离子平衡聚合动力学。讨论了体系中的反应活性种;提出了聚合机理;得到了聚合温度为20℃时的平衡单体浓度与活性种速率常数及添加剂浓度之间的关系式。     

（＋）-甲基丙烯酸{2,5-双[4′-（（S）-2-甲基丁氧基）苯基]苯基}酯的合成及其螺旋选择性自由基聚合

设计合成了手性单体（＋）-甲基丙烯酸{2,5-双[4′-（（S）-2-甲基丁氧基）苯基]苯基}酯,并进行了自由基溶液聚合.相比于单体,聚合物的比旋光度有显著的同向增长,且在其圆二色光谱上对应于三联苯侧基以及酯基的吸收区域呈现明显的Cotton效应,说明其主链可能采取某一旋向占优的螺旋构象.研究了聚合条件对聚合物旋光性质的影响.结果表明,采用极性大的芳香族溶剂或增加单体浓度有利于获得旋光度大的聚合物;随聚合温度增加,聚合物旋光度先增加后减小,在80℃时聚合达到最大值.该聚合物比甲基丙烯酸三芳基甲基酯类光学活性螺旋链聚合物具有更好的化学结构稳定性和立体结构稳定性.     

活性阴离子聚合及其单体的研究进展

适用于活性阴离子聚合的单体拓展研究是有关活性阴离子聚合的一项重要的研究工作.本文重点介绍了近十年在活性阴离子聚合领域出现的新型单体的结构设计、合成及其聚合过程的研究进展.文中涉及到的新型单体主要包括非(弱)极性类单体、极性单体及其它单体.进一步细分,非(弱)极性类单体分为苯乙烯衍生物类单体和丁二烯衍生物类单体,极性单体中含有丙烯酸酯类单体、丙烯酰胺类单体、氯乙烯以及N-乙烯基咔唑,其它单体包括异氰酸酯类、烯酮类以及杂环类单体.最后本文对上述这些新型单体中的一些单体用于复杂大分子拓扑结构的设计合成情况也作了简要介绍.     

H2O/TiCl4/ED 体系引发异丁烯控制正离子聚合中的影响因素研究

在亲核试剂(ED)如吡啶(Py)、N,N-二甲基乙酰胺(DMA)或三乙胺(TEA)存在下,由引发剂H2O和共引发剂TiCl4组成引发体系,在二氯甲烷/正己烷混合溶剂中进行异丁烯(IB)正离子聚合,考察了溶剂极性、聚合温度及异丁烯浓度对聚合反应转化率、产物分子量和分子量分布的影响.试验结果表明,随聚合体系溶剂极性增大,聚合速率加快,相近转化率时聚合产物的分子量分布变窄.随着聚合温度降低,聚合速率明显提高,聚合物的分子量增加,活化能为负值,活性链端发生链转移或链终止等副反应的几率减小,当聚合温度为-60℃时,可以抑制活性链端的β-H脱除反应和链转移副反应,并得到大分子链末端全部为叔氯基团的聚异丁烯(PIB).当[IB]0≤2.5mol/L时,随[IB]0增加,聚合转化率有所增加,聚合产物的GPC谱图均为单峰分布,分子量增大,而分子量分布基本保持不变,对于加入Py的聚合体系,分子量分布指数在1.33~1.45范围内,对于加入TEA的聚合体系,分子量分布指数在1.47~1.60范围内,并求出在加入Py和TEA的聚合体系中活性链向单体的链转移常数CM分别为5.5×10-4和6.6×10-4.     

丁二酸酐与SnCl2·2H2O共催化含水乳酸缩聚制备高分子量聚乳酸

用丁二酸酐与SnCl2.2H2O共催化含水乳酸本体缩聚,合成黏均分子量为6×104的聚乳酸.合成反应时间短,聚乳酸产率高、纯度好.单体为含水10%～15%的乳酸.聚合方法环境友好,不使用任何共沸溶剂.讨论了催化剂用量、反应温度、聚合时间等对聚合反应的影响,并用红外光谱和核磁共振光谱对合成的聚乳酸进行了表征.     

稀土催化丁二烯顺式聚合过程中的环化改性

采用ＮｄＣｌ３·３ｉ－ＰｒＯＨ－ＡｌＥｔ３稀土催化剂进行丁二烯的顺式聚合，在聚合过程中引入烯丙基氯，进行分子内环化反应以及单体的环聚反应．考察了稀土催化剂用量、ｎ（烯丙基氯）／ｎ（ＡｌＥｔ３）、环化时间、反应温度、单体浓度等对环化反应的影响，并对产物进行了红外光谱、核磁共振光谱的表征     

Effect of the nature of a solvent on pseudoliving free-radical polymerization of styrene mediated by TEMPO

The kinetics and mechanism of the pseudoliving free-radical polymerization of styrene are studied for the first time under the conditions of reversible inhibition by TEMPO nitroxides. An abnormal decline in the reduced rate of polymerization, which is inconsistent with a decrease in the concentration of the monomer, and an increase in the steady-state concentration of the free nitroxide are discovered. The main quantitative characteristics of the pseudoliving process are determined, namely, the rate constants of reinitiation and reversible recombination, and the constant of pseudoliving equilibrium between dormant and growing chains. It is shown that the polarity of a medium and the concentration of the monomer determine the character of polymerization in a solution: With an increase in the polarity of the solvent, the pseudoliving equilibrium constant increases, the reduced rate of styrene polymerization decreases, and the molecularmass-distribution of the polymer formed at initial conversions narrows. The smaller the concentration of styrene in the reaction system, the more pronounced the above differences associated with the solvent nature.     

Dispersion polymerization of styrene in alcohol media: Effect of initiator concentration,solvent polarity,and temperature on the rate of polymerization

The effects of three different variables (initiator concentration, polarity of the solvent and reaction temperature) on the rate of dispersion polymerization of styrene in alcohols have been investigated. It was found that the rate of polymerization increases with the initiator (AIBN) concentration at the 0% conversion level and becomes independent of it at higher monomer conversions. More significant was the result that the rate was also found to increase with solvent polarity. This is consistent with thermodynamic equilibrium calculations which account for the partitioning behavior of monomer and solvent in both the solution and the particle phases. The results further suggest the existence of two different kinetic regions: one at low conversions, where the reaction takes place primarily in the solution phase, and one at high conversions, where the reaction takes place primarily in the particle phase. © 1997 John Wiley & Sons, Inc. J Polym Sci A: Polym Chem 35 : 2907–2915, 1997     

等离子体引发丙烯酰胺水溶液聚合

用两种等离子体引发丙烯酰胺水溶液聚合的方法 ,制备了线性超高分子量聚丙烯酰胺 .研究了放电时间、放电功率、单体的初始浓度及溶液的pH值等对聚合产物的影响     

Study of Kinetics of Dispersion Polymerization of Styrene in Organic Media

The kinetics of dispersion polymerization of styrene in alcohol/methyl or butyl cellosolve was investigated with dried-weigh methods. The reaction parameters, such as concentration of initiator, polymerization temperature, and solvent, play an important role in determine polymerization rate. It was found that polymerization rate increases with the reaction temperature. The apparent activation energy is of 42.2kJ/mole and 52.6kJ/mole for the initial polymerization stage and the stationary polymerization interval. The polymerization rate increases with the concentration of the initiator with approximately 0.67 order dependence at conversion about 5%. It was described that the relation of conversion with the Hansen Parameters of media in detail by analysis of solvent dispersion, polarity and hydrogen bonding contributions. More significant was the result that polymerization rate versus conversion curve consisted of 3 intervals (2 non-stationary and 1 stationary one). The plateau of polymerization rate was observed in the curve of polymerization rate vs. monomer conversion.     

Synthesis and characterization of poly(ϵ-caprolactone)-poly(ethylene glycol) block copolymer

Poly(ϵ-caprolactone)–poly(ethylene glycol)–poly(ϵ-caprolactone) triblock copolymers (PECL) covering a wide range of poly(ethylene glycol) (PEG) lengths were synthesized with alkali metal alkoxide derivatives of poly(ethylene glycol). The effects of various factors, such as amount of the initiator, reaction time and temperature, polarity of solvent, length of PEG segment, and counterion on the polymerization were investigated. The copolymers were characterized by ¹H-NMR, IR, GPC, and DSC. It was found that THF system is superior to toluene system. The conversion of the monomer increased with increase of the initiator concentration. High molecular weight of the copolymer and high conversion of the monomer was obtained at below 30°C within 5 min. The polymerization process was studied by GPC and the coexistence of propagation and transesterification reaction was found, which leaded to relatively broad molecular weight distribution of the copolymers. © 1997 John Wiley & Sons, Inc.     

Ring-opening polymerization of ε-caprolactone using rare earth tris(4-tert-butylphenolate)s as a single component initiator

Ring-opening polymerization of ε-caprolactone has been carried out by using single component rare earth tris(4-tert-butylphenolate)s initiators for the first time. The influences of rare earth element, solvent, monomer and initiator concentration as well as reaction time on the polymerization were investigated. The kinetics indicated that the polymerization rate is first-order with respect to monomer concentration and initiator concentration, respectively. The overall activation energy of the ring-opening polymerization amounts to 51.9 kJ/mol. Mechanism studies showed that monomer inserted into the growing chains with the acyl-oxygen bond scission rather than the break of alkyl-oxygen bond.     

A study of the polymerization of styrene initiated by K-THF-GIC system

In this paper, the polymerization of styrene initiated by potassium (K)-tetrahydrofuran (THF)-graphite intercalation compound (GIC) (K-THF-GIC) was studied. The mechanism of the polymerization was determined to be anionic polymerization according to its characteristics. The effect of the concentration of the initiator and monomer was studied. It was found that the polymerization mainly occurred on the surface and edge of the intercalated graphite. It was also shown that the polarity of solvent has little effect on the polymerization yield in this system.     

Cyclopolymerization of diallylcyanamide

A soluble polymer of cyclic structure has been obtained by radical polymerization of diallyleyanamide. A kinetic analysis of the polymerization indicated that the overall rate of the system is first-order with respect to concentration of initiator and either first- or second-order with respect to monomer concentration, depending on the solvent used. The molecular weight of the polymer is independent of the concentration of the initiator and the monomer. The intramolecular abstraction of hydrogen is proposed as a termination reaction.     

Kinetic studies of nonaqueous polymerization of methyl methacrylate initiated by ferric laurate–n-hexyl amine system

The polymerization of methyl methacrylate was studied in carbon tetrachloride medium with ferric laurate, a metal soap, in combination with n-hexyl amine as the initiator system at 60°C. The rate of polymerization was found to be linear with the monomer concentration and proportional to the square root of both ferric ion and amine concentration. A reaction scheme involving initial complex formation between ferric ion and amine and subsequent reaction of the complex with the solvent molecule to produce free radicals responsible for initiation of polymerization has been postulated to account for the observed results.