α,α’-邻苯二甲基桥联茚基钐胺化物（C9H6CH2C6H4CH2C9H6）SmNPh2催化甲基丙烯酸甲酯聚合

文章以α,α’-邻苯二甲基桥联茚基钐胺化物(C9H6CH2C6H4CH2C9H6)Sm NPh2为催化剂,对甲基丙烯酸甲酯聚合反应进行了研究,考察了催化剂用量、反应时间及反应温度对甲基丙烯酸甲酯聚合的影响,并且用粘度法对聚合产物的粘均分子量进行了表征。发现α,α’-邻苯二甲基桥联茚基钐胺化物(C9H6CH2C6H4CH2C9H6)Sm NPh2对甲基丙烯酸甲酯聚合反应具有较高的催化活性。温度降低,聚合反应转化率增加,聚合产物粘均分子量升高;催化剂用量增加,聚合反应转化率增大,聚合产物的粘均分子量下降;延长反应时间,转化率和分子量都增大。     

(C9H6CH2C6H4CH2C9H6)Sm催化MMA聚合的研究

文章以α,α’-邻苯二甲基桥联茚基钐胺化物(C9H6CH2C6H4CH2C9H6)Sm为催化剂,对甲基丙烯酸甲酯聚合反应进行了研究,考察了催化剂用量、反应时间及反应温度对甲基丙烯酸甲酯聚合的影响,并且用粘度法对聚合产物的粘均分子量进行了表征。发现α,α’-邻苯二甲基桥联茚基钐胺化物(C9H6CH2C6H4CH2C9H6)Sm对甲基丙烯酸甲酯聚合反应具有较高的催化活性。温度降低,聚合反应转化率增加,聚合产物粘均分子量升高;催化剂用量增加,聚合反应转化率增大,聚合产物的粘均分子量下降;延长反应时间,转化率和分子量都增大。     

TiCl4/SiO2负载型催化剂用于丁二烯聚合Ⅱ.聚合条件及聚合动力学

使用以球磨法制备的 SiO2负载 TiCl4催化剂进行丁二烯溶液聚合，考察了聚合条件对催化效率的影响以及在 20～ 60℃下的聚合动力学。确定了适宜的聚合条件：以加氢汽油为溶剂， Al/Ti摩尔比为 20, Ti/Bd摩尔比为 2× 10－ 4, 50℃聚合 10 h以上。溶液聚合动力学研究结果表明，本体系在低转化率下为稳态聚合，其稳态聚合速率方程为 Rp=kpf[Ti]0[Bd],聚合的表观活化能为 11.4 kJ/mol。     

TiCl4/SiO2负载型催化剂用于丁二烯聚合Ⅱ.聚合条件及聚合动力学

使用以球磨法制备的SiO2负载TiCl4催化剂进行丁二烯溶液聚合,考察了聚合条件对催化效率的影响以及在20～60℃下的聚合动力学.确定了适宜的聚合条件以加氢汽油为溶剂,Al/Ti摩尔比为20,Ti/Bd摩尔比为2×10-4,50℃聚合10h以上.溶液聚合动力学研究结果表明,本体系在低转化率下为稳态聚合,其稳态聚合速率方程为Rp=kpf[Ti]0[Bd],聚合的表观活化能为11.4kJ/mol.     

甲基丙烯酸甲酯在Nd[O(i-Pr)]3-Al(i-Bu)3-CCl4中配位活性聚合

以Nd[O(i-Pr)]3-Al(i-Bu)3-CCl4为三元络合体系,在甲苯中催化甲基丙烯酸甲酯(MMA)聚合.发现PMMA相对分子质量与转化率呈线性关系,聚合速率与MMA和Nd[O(i-Pr)]3的浓度分别呈一级关系,聚合表观活化能为74.1 kJ/mol.所得PMMA间规摩尔分数约64%.用该催化体系合成了嵌段共聚物PMMA-b-P(HO),表明异丙氧基钕体系在甲苯中催化MMA聚合反应是配位活性聚合.     

茂金属催化苯乙烯苯体间规聚合

采用新型茂金属催化剂体系进行苯乙烯本体间规聚合。研究了催化剂浓度,聚合温度和时间对聚合速率,聚合物分子量和颗粒形态的影响,成功地制得了高转化率下外观满意的粉体间规聚苯乙烯,避免了聚合过程中的凝胶或结块。     

钨系催化合成1,2-聚丁二烯的研究——Ⅱ.助催化剂对聚合活性的影响

在WCl_6-C_4H_(?)OH催化体系中各种助催化剂对聚合活性的影响表明,以Al(i-Bu)_(?)为助催化剂体系的聚合活性最高,AlEt_2Cl和AlEt_3体系的聚合活性相近;CH_3PhOH/Al(i-Bu)_3=1(mol比)的助催化剂体系和Al(i-Bu)_3体系的聚合活性相近,但适宜Al/W(mol比)的范围增宽,醇类作助催化剂的配位体时,体系的聚合活性降低;在实验条件下,Al(i-Bu)_2H体系无聚合活性;以AlEt_3、Al(i-Bu)_3、Al(i-Bu)_2OPhCH_3和Al(i-Bu)_2OC_4H_(?)分别作助催化剂时,对产物分子量影响较小,并均能得到1,2-结构含量大于85％的1,2-聚丁二烯。     

甲基丙烯酸甲酯在Nd[O（i—Pr）]—Al（i—Bu）3—CCl4中配位活性聚合

以Nd[O(i-Pr)]3-A1(i-Bu)3-CCl4为三元络合体系，在甲苯中催化甲基丙烯酸甲酯(MMA)聚合。发现PMMA相对分子质量与转化率呈线性关系，聚合速率与MMA和Nd[O(i-Pr)]3的浓度分别呈一级关系，聚合表观活化能为74．1kJ／mol。所得PMMA间规摩尔分数约64％。用该催化体系合成了嵌段共聚物PMMA-b-P(H0)，表明异丙氧基钕体系在甲苯中催化MMA聚合反应是配位活性聚合。     

稀土催化剂本体聚合合成高顺式-1,4-结构含量液体聚异戊二烯(英文)

以Nd(vers)3、Al(i-Bu)2H和Me2SiCl2为均相催化剂,采用本体聚合法合成液体聚异戊二烯(LIR)。结果表明,LIR的合成过程平稳;产物的顺式-1,4 -结构摩尔分数高达96.0%以上、特性黏数低、数均分子量低、分子量分布窄。     

rac-Et(1-Ind)_2ZrCl_2/MAO催化1-癸烯聚合制备高粘度润滑油

茂金属催化体系具有超高活性和单一活性中心,是催化α-癸烯聚合的理想催化剂。用茂金属催化体系rac-Et(1-Ind)2Zr Cl2/MAO对1-癸烯聚合制备高粘度润滑油基础油进行了研究,提出了反应体系可能的聚合机理。考察了催化剂浓度、Al和Zr物质的量之比、反应温度和反应时间对聚合产物性能的影响。结果表明,在Zr和1-癸烯物质的量之比为8×10-5,Al和Zr物质的量之比为100,反应温度为50℃,反应时间为60 min时,1-癸烯的转化率为91.6%。聚合产物的整体性能较为优异,运动粘度(100℃)为393.9 mm2/s,粘度指数为271,数均分子量为9 091,分子量分布为1.691 3。     

苯乙烯的间歇-半连续RAFT细乳液聚合

进行了苯乙烯的间歇-半连续RAFT细乳液聚合,考察了半连续段的起点、单体滴加速率及最终胶乳固含量的影响。结果发现：从最终胶乳的稳定性考虑,半连续聚合的起点选择在间歇聚合的高转化率时期更好;若综合考虑胶乳的稳定性、分子量及其分布、固含量、乳化剂及共稳定剂在胶乳中的残留率等因素,半连续聚合的起点可适当提前,但必须在间歇聚合成核期结束后。过早容易引起乳液的失稳;过迟会延长反应时间,降低聚合物的制备效率,导致死聚物链含量升高。聚合体系的稳定性与胶乳的固含量密切相关,最终固含量不宜超过40％。采用间歇-半连续二段聚合工艺可以制得窄分子量分布(PDI＝～1.3),低乳化剂及共稳定剂残留量（～1.5%,质量）的高分子量聚合物(≈8×10⁴g•mol^-1)。     

Particle formation mechanism in radical polymerization in miniemulsion based on in situ surfactant formation without high energy homogenization

Conventional radical polymerization of styrene at 70 °C in aqueous miniemulsion generated using the in situ surfactant technique, without use of high energy mixing, has been investigated in detail. The surfactant potassium oleate was formed in situ by reaction between oleic acid and potassium hydroxide at the styrene/water interface. The particle formation mechanism was investigated by use of pyrene as a probe, revealing that under suitable conditions with an oil-phase initiator, particle formation occurs primarily via monomer droplet nucleation. The droplet/particle stability is however inferior to that in a typical miniemulsion generated employing ultrasonication, as manifested by a marked increase in droplet/particle size with conversion and a bimodal droplet/particle size distribution by weight. The droplet/particle stability increases with increasing amount of oleic acid, hexadecane, water, and the ratio potassium hydroxide:oleic acid, respectively.     

Chemospecific ring-opening polymerization of α-methylenemacrolides

α-Methylenemacrolides having various groups, such as aromatic, ether, and amine, were enzymatically, anionically, and radically polymerized. The polymerization with the lipase catalyst successfully afforded polymers only through the ring-opening process, whereas the vinyl polymerizations selectively proceeded by using anionic and radical initiators. The polyesters obtained by the enzymatic polymerization have a polymerizable methacrylic methylene group in the main-chain, in addition to the aromatic and polar groups, and were further radically polymerized to quantitatively produce a cross-linked polymer gel.     

Accelerated pressure synthesis and characterization of 2-oxazoline block copolymers

The cationic ring-opening polymerization of 2-oxazolines in acetonitrile was investigated under pressure conditions utilizing methyl tosylate as initiator of which the single crystal X-ray structure is described as well. The polymerization kinetics were studied and compared with previously reported microwave-assisted pressure polymerizations. Moreover, a series of block copolymers was synthesized in an automated parallel synthesis robot utilizing this pressure polymerization method. The resulting block copolymers were characterized with both differential scanning calorimetry and contact angle measurements to determine the effect of copolymer composition on glass transition temperature, melting point and surface energy. Atomic force microscopy was applied to further investigate the possible phase separation.     

Synthesis of latex particles by ring-opening metathesis polymerization

This paper reviews the recent discoveries that were achieved by our group in the field of particle synthesis via ring-opening metathesis polymerization (ROMP). Both polynorbornene and polybutadiene-based particles were prepared by the respective ROMP of norbornene and cyclooctadiene initiated by (PCy₃)₂Cl₂RuCHPh using several methods of polymerization in dispersed media, such as dispersion, suspension and miniemulsion. Depending upon the process implemented, particles size was found to range from 300 nm to 20 μm.     

微乳液聚合研究新进展

对微乳液聚合的特点、聚合机理及动力学影响因素进行了总结和评述，指出了今后微乳液聚合研究的几个关键问题。     

等离子体引发丙烯酸(2-乙基)已酯乳液聚合

采用等离子体引发聚合的方法 ,进行了丙烯酸 ( 2 -乙基 )已酯 (简称 EHA)的乳液聚合。考察了后聚合时间、放电功率、乳化剂浓度对聚合转化率及特性粘数的影响。并对丙烯酸酯等离子体引发本体、乳液聚合进行了比较     

超声引发聚合反应的研究

综述了超声波在一些聚合方法中的应用。     

Microwave-Assisted RAFT Polymerization

Advances in controlled radical polymerization (CRP) have facilitated access to well-defined polymers with controlled molecular weight, topology, and functionality. However, despite the benefits afforded by many CRP techniques, control over these key polymer attributes often comes at the expense of polymerization rate. One method proposed for accelerating chemical synthesis is microwave heating. This review highlights recent examples of microwave heating being applied during reversible addition-fragmentation chain transfer (RAFT) polymerization. In addition to successfully leading to homopolymers from a variety of monomers, block copolymers have also been prepared by microwave-assisted RAFT, which suggests that the high polymerization rates observed do not necessarily lead to significant end group loss from termination. Despite significant debate regarding the origin of rate enhancement observed during microwave-assisted reactions, the reports included herein provide insight into mechanisms by which well-defined functional polymers can be prepared in an accelerated fashion.     

水性含硅聚合物涂料的制备与应用

乳液聚合法是制备水性含硅聚合物最常见、最有效的方法。介绍了种子乳液聚合、核/壳乳液聚合、无皂乳液聚合、微乳液聚合、互穿网络聚合等制备水性含硅聚合物的方法,并对水性含硅聚合物涂料的应用做了探讨。