庚烯-1单体单元对胆甾型侧链液晶共聚砜热转变温度的调节

合成并用红外光谱法、核磁共振法和高效凝胶渗透色谱法表征了胆甾（烷）醇十一碳烯酸酯分别与庚烯 １、二氧化硫进行自由基共聚合得到的一系列不同组成的三元胆甾型侧链液晶共聚砜，用温控式偏振光显微镜观测了产物的液晶性能．结果表明：随庚烯 １单体单元组份含量的增加，该三元共聚砜的液晶相转变温度均降低，采用庚烯 １单体参与共聚的方法可以有效地调节胆甾型侧链液晶共聚砜的热转变温度．     

新型以咔唑为主链的能量转移型发光聚合物

用Suzuki偶合反应合成了一系列以咔唑为主链，与不同的芳香环和杂环化合物 共聚的新型电致发光无规共聚物．这些共聚物溶于普通的有机溶剂，发较强的荧光 ．咔唑链段为共聚物提供了很好的空穴传输和空穴注入性能．与咔唑共聚的窄能隙 单体，如蒽(ANT)、噻吩(Th)、2，1，3-苯并噻二唑(BTDZ)、2，1，3—苯并硒二唑 (BseDZ)和4，7—二噻吩—2，1，3—苯并噻二唑(DBT)在聚合物中含量小于50％时 成为陷阱中心．还观察到极为有效的分子内能量转移．由于共聚单体的能隙不同， 这些电致发光共聚物的发光范围可覆盖整个可见光谱区．研究结果表明，用咔唑作 为宽带主体，与少量低带隙单体共聚，有可能成为一种合成同时兼有优异空穴注入 特性，又能广泛调节发光颜色的新的发光聚合物体系．     

丙烯腈在聚丙烯上接枝共聚

丙烯腈在聚丙烯上非均相接枝共聚，得杨梅形氰基树脂。研究了接枝共聚条件对单体转化率和接枝率的影响。表观聚合速度可表示为，碰撞频率因子和聚合活化能分别是1．36×1011s-1和99．2kJ．mol-1。从光学显微镜观察到改性树脂在水中接枝连束的分布状态。丙烯腈和二乙烯基苯在聚丙烯上接校共聚，再经二甲苯率取，得笼形氰基树脂。二乙烯基苯在单体中的相对含量对树脂的溶胀性能和笼孔尺寸有很大的影响，制取功能材料时应予适当调节。扫描电镜照片展示了笼形树脂的笼腔和网络结构形态。     

苯乙烯－乙烯共聚物的合成及其结构性能的研究

用负载型钛系催化剂ＭｇＣｌ_２／ＴｉＣｌ_４，ＮｄＣｌ_３／ＡｌＥｔ_３（ＳＮ－１催化剂）制备出组份比例变化的苯乙烯－乙烯共聚产物．共聚产物通过溶剂萃取分离、~１３Ｃ－ＮＭＲ、ＩＲ、动态粘弹谱进行表征，并初步进行了与聚苯乙烯（ａＰＳ）共混作用的研究．结果表明，ＳＮ－１催化剂能有效地催化苯乙烯与乙烯共聚合．共聚产物为含有均聚聚苯乙烯的共聚物复合物，其中的２５ｍｏｌ％的苯乙烯参加了共聚．共聚产物与ａＰＳ共混可明显提高ａＰＳ的冲击强度和断裂伸长率．     

苯乙烯交联共聚中致孔剂的致孔作用.Ⅱ

分别阐述了良和非良混合溶剂，及非良与非良混合溶剂的致孔作用。在良／非良混合溶剂存在下通过调节两种溶剂的比例，可控制共聚全的孔径和孔容的大小，只要交联度合适，可是比表面积较大的共聚体，在非良／非良混合溶剂存在下，可通过调节两种溶剂的比较，控制其适当的混合溶度参数，所得共聚体的比表面积也大。     

氢气对负载型Z-N高效催化剂的乙烯-丙烯共聚产物链结构影响

用球形的负载型Ziegler-Natta（Z-N）高效催化剂，经丙烯均聚一乙烯丙烯气相共聚两段串联反应工艺制备的聚丙烯／乙丙共聚物（PP／EPR）合金具有优良的抗冲击性能，是聚丙烯的重要高性能化改性品种，已实现大批量生产，对这类反应器合金的结构表征和结构性能关系的研究表明，其共聚物组分中既有起弹性体作用的乙丙无规共聚物，也含有相当量的乙丙多嵌段共聚物．这种多嵌段共聚物既与无规共聚物（EPR）相容，又与PP基体相容，在合金中起相容剂作用，对材料高抗冲性能的形成起着重要作用．然而，负载型Z-N高效催化剂催化乙丙共聚合的产物结构及其影响因素至今鲜见系统的研究，调控PP／EPR合金中共聚物结构的原理尚不明确．氢气在聚烯烃生产中广泛用作分子量调节剂，在PP／EPR合金的生产中同样要用氢气调节PP和EPR组分的分子量．但是，加氢对共聚物的链结构有何影响则鲜见系统的研究．本文初步研究了用Z—N高效催化剂合成的乙丙共聚物的结构特征，着重考察了聚合体系中加入链转移剂氢气对共聚物结构的影响．     

醋酸乙烯酯-丙烯酸丁酯乳液共聚乳胶粒形态演化过程的模拟

将簇迁移动力学拓展应用到共聚形态的研究中，对醋酸乙烯酯 丙烯酸丁酯从间歇到不同加料速率下的半连续乳液共聚实验的乳胶粒形态演化过程进行了模拟，模拟从共聚 均聚转折点开始．结果说明：半连续加料时，随着加料速率加快，相分离程度增加，间歇反应时形成了核壳结构．乳胶粒形态模拟结果与文献对此共聚乳胶粒形态的实验表征结果类似．     

丙烯腈和甲基丙烯酸酯基团转移共聚的竞聚率

丙烯腈和甲基丙烯酸酯基团转移共聚的竞聚率邹友思，郭金全，兰涛，戴李宗，潘容华（厦门大学化工系，厦门，３６１００５）关键词基团转移共聚．竞聚率．丙烯腈．甲基丙烯酸酯近年来对基团转移共聚竞聚率的研究较活跃［１～３］，一般认为甲基丙烯酸酯和丙烯酸酯两类单体...     

环氧乙烷和环氧丙烷共聚体系的等温结晶和熔融

环氧乙烷（ＥＯ）和环氧丙烷（ＰＯ）共聚体系的等温结晶前期符合Ａｖｒａｍｉ方程。ＰＯ组分含量增加，Ａｖｒａｍｉ指数ｎ值由１．８到２．４，体系的结晶生长速率与共聚体系的组成和结晶度有关，ＥＯ／ＰＯ共聚体系的平衡熔点随ＰＯ含量的增加而降低。随Ｔｃ增大，△Ｈｍ与△Ｓｍ呈线性降低。     

N－烯丙基咔唑与甲基丙烯酸甲酯高温共聚合

Ｎ－烯丙基咔唑不能均聚合，但可与甲基丙烯酸甲酯在高温下共聚合。测定了２００—２６０℃时两单体共聚合竞聚率，１度为２５０℃时，ｒ１和ｒ２均小于１。共聚物分子量随着共聚温度升高而降低．结果表明，共聚体系中，增长反应与降解反应同时存在．该反应可能是自由基过程．     

RATE OF REGULATED COPOLYMERIZATION INVOLVING CO_2

在二氧化碳与环氧丙烷的共聚反应中，加入某些调节剂可以得到所需要分子量和官能度的共聚物。这是因为在活泼氢和催化剂活性中心之间有链转移反应发生。我们提出了共聚反应的机理并导出了相应的共聚反应速度方程式，这一机理和速度方程式与实验相符。     

卟啉铝催化下二氧化碳与氧化环己烯共聚反应研究

利用四苯基卟啉氯化铝(TPPAlCl)与双三苯基膦氯化铵(PPNCl)组成的二元催化剂催化二氧化碳与氧化环己烯共聚合,80℃下反应9h,二氧化碳-氧化环己烯共聚物(PCHC)的收率为97.2％,分子量分布窄(Mw/Mn=1.12),但数均分子量仅为6.8×103.研究发现溶剂的浓度和极性变化对聚合过程中的链转移反应影响...     

双金属氰化络合物催化环氧丙烷和邻苯二甲酸酐共聚

采用双金属氰化络合物 (DMC)催化环氧丙烷 (PO)和邻苯二甲酸酐 (PA)共聚 ,探讨了共聚合特征 ,并用IR、1 H NMR和GPC对共聚物的结构和分子量进行了表征 .发现DMC催化剂对该共聚反应速度快 ,转化率高 ,是该反应的有效催化剂 ,催化剂浓度为 6 0mg kg时 ,90℃下 ,以THF作溶剂共聚反应 3h ,转化率可达94 0 % .聚合速度甚至比DMC催化PO均聚还快 .该共聚反应可在多种溶剂中进行 ,极性溶剂更有利于共聚合 ,溶液聚合温度比本体共聚低 ,合适的溶液共聚温度在 90～ 10 0℃之间 .共聚产物的分子量受催化剂用量、反应温度和体系中水份含量的影响 ,数均分子量在数百至数千之间 .考察该共聚体系的动力学表明 ,该共聚反应速率对单体浓度呈一级关系     

丙烯腈与衣康酸在DMSO/H_2O中的聚合及聚合物性能表征

采用丙烯腈 (AN)与衣康酸 (IA)为共聚单体 ,以偶氮二异丁腈为引发剂在混合介质二甲基亚砜 水(DMSO H2 O)中自由基沉淀共聚合 ,合成了高分子量的聚丙烯腈 .通过正交设计方法研究了聚合反应条件 ,如反应温度、单体浓度、混合介质DMSO H2 O配比等对聚合反应的转化率的影响 ,还重点探讨了混合介质DMSO H2 O配比对转化率和粘均分子量的影响 .采用DSC ,TG ,IR等手段研究了PAN均聚物及 (PAN co IA)的结构与性能 .研究结果表明 ,增加反应温度 ,降低单体浓度 ,降低喂料AN IA配比中IA的含量 ,均有利于提高聚合反应的转化率 .AN与IA共聚反应的转化率随着反应介质中DMSO含量的增加而降低 ,同时聚合物的粘均分子量也降低 .对于喂料AN IA配比中IA含量相同的P(AN co IA)共聚物 ,高分子量P(AN co IA)共聚物比常规低分子量的放热峰起始温度低 ,放热峰宽     

HCAⅡ-inspired Catalysts for Making Carbon Dioxide-based Copolymers: The Role of Metal-hydroxide Bond

The general characteristics of the active center of the catalysts(including zinc-cobalt(III) double metal cyanide complex [Zn-Co(Ⅲ) DMCC]) for the copolymerization reaction of carbon dioxide(CO_2) with epoxide are summarized. By comparing the active center, catalytic performance of the Zn-Co(Ⅲ) DMCC(and other catalysts) with HCAII enzyme in the organism for activating CO_2(COS and CS_2), we proposed that the metal-hydroxide bond(M-OH), which is the real catalytic center of human carbonic anhydride Ⅱ(HCAⅡ), is also the catalytic(initiating) center for the copolymerization. It accelerates the copolymerization and forms a closed catalytic cycle through the chain transfer reaction to water(and thus strictly meets the definition of the catalyst). In addition, the metal-hydroxide bond catalysis could well explain the oxygen/sulfur exchange reaction(O/S ER) in metal(Zn, Cr)-catalyzed copolymerization of COS(and CS_2) with epoxides. Therefore, it is very promising to learn from HCAⅡ enzyme to develop biomimetic catalyst for highly active CO_2/epoxide copolymerization in a well-controlled manner under mild conditions.     

GRAFT COPOLYMERIZATION OF METHYL ACRYLATE ONTO CHITOSAN INITIATED BY POTASSIUM DIPERIODATONICKELATE (IV)

ABSTRACT

A novel redox system, potassium diperiodatonickelate [Ni (IV)]‐chitosan, was employed to initiate the graft copolymerization of methyl acrylate (MA) onto chitosan in alkali aqueous solution. The effects of reaction variables such as monomer concentration, initiator concentration, reaction time, pH and temperature were determined. By means of a series of copolymerization, the grafting conditions were optimized. The maximum grafting percentage obtained was 404.1% when 0.3 g chitosan was copolymerized with 1.8 mL monomer at 35°C for 5 hours with [Ni (IV)]=9.4×10^?4 M and the total volume was 20 mL. Ni (IV)-chitosan system is found to be an efficient redox initiator for this graft copolymerization. A single electron transfer mechanism is proposed to explain the formation of radicals and the initiation. The grafted copolymers were characterized by IR and X-ray diffraction diagrams. The thermal stability of chitosan and chitosan-g-PMA was studied by thermogravimetric analysis (TGA).     

Mechanism of graft copolymerization of styrene onto deproteinized natural rubber

High conversion and high grafting efficiency attained by graft copolymerization of styrene onto deproteinized natural rubber (DPNR) was investigated with respect to the molecular weight of grafted polystyrene. The graft copolymerization was performed with tert-butyl hydroperoxide/tetraethylenepentamine as an initiator after deproteinization of natural rubber with urea. Grafted polystyrene was isolated from the resulting graft copolymer by ozonolysis reaction. After the ozonolysis of the graft copolymer of DPNR and polystyrene (DPNR-g-PS), the molecular weight of grafted polystyrene was determined by size exclusion chromatography. Effects of initiator and monomer concentrations were investigated with respect to the molecular weight of the grafted polystyrene, which was found to depend on not only the number of active site generated on the rubber particle but also the feed of styrene. Deactivation and chain transfer of the active sites were attributed to effective amount of styrene used for the graft copolymerization.     

BDIE·[Zn-Al]催化二氧化碳与氧化环己烯的共聚反应

用α二亚胺型BDIE配体(N,N′(2,6二异丙基苯基)乙二亚胺)与氧联锌铝醇盐([ZnAl])以配位的方式制备了高位阻催化体系BDIE·[ZnAl],并催化二氧化碳与氧化环己烯共聚.研究了各种因素对该反应的影响,发现最适宜的反应条件为BDIE[ZnAl]的摩尔比为0.5、反应温度为80℃、催化剂浓度为0.1gmL、二氧化碳压力为2MPa.在此条件下反应24h其催化效率达到31.6gg与其它高位阻体系相比,该催化剂用成本低的异丙醇铝和无水醋酸锌代替二乙锌,聚合操作过程简单,是一种有发展前景的催化体系.     

Copolymerization of cyclohexene oxide with CO2 by using intramolecular dinuclear zinc catalysts

The intramolecular dinuclear zinc complexes generated in situ from the reaction of multidentate semi-azacrown ether ligands with Et(2)Zn, followed by treatment with an alcohol additive, were found to promote the copolymerization of CO(2) and cyclohexene oxide (CHO) with completely alternating polycarbonate selectivity and high efficiency. With this type of novel initiator, the copolymerization could be accomplished under mild conditions at 1 atm pressure of CO(2), which represents a significant advantage over most catalytic systems developed for this reaction so far. The copolymerization reaction was demonstrated to be a living process as a result of the narrow polydispersities and the linear increase in the molecular weight with conversion of CHO. In addition, the solid-state structure of the dinuclear zinc complex was characterized by X-ray crystal structural analysis and can be considered as a model of the active catalyst. On the basis of the various efforts made to understand the mechanisms of the catalytic reaction, including MALDI-TOF mass analysis of the copolymers' end-groups, the effect of alcohol additives on the catalysis and CO(2) pressure on the conversion of CHO, as well as the kinetic data gained from in situ IR spectroscopy, a plausible catalytic cycle for the present reaction system is outlined. The copolymerization is initiated by the insertion of CO(2) into the Zn--OEt bond to afford a carbonate-ester-bridged complex. The dinuclear zinc structure of the catalyst remains intact throughout the copolymerization. The bridged zinc centers may have a synergistic effect on the copolymerization reaction; one zinc center could activate the epoxide through its coordination and the second zinc atom may be responsible for carbonate propagation by nucleophilic attack by the carbonate ester on the back side of the cis-epoxide ring to afford the carbonate. The mechanistic implication of this is particularly important for future research into the design of efficient and practical catalysts for the copolymerization of epoxides with CO(2.).     

CHEMICAL MODIFICATION OF THE SURFACE OF CALCIUM ALGINATE GEL BEADS

The chemical modification of the surface of calcium alginate gel beads (CAGB) via grafting copolymerization with vinyl acetate (VAc) was studied. The optimum reaction conditions with activation and graft copolymerization two steps were explored. First, 5 grams CAGB with 2.5 mm initial diameter was initiated with 0.0493 mol/L K2S208 at 51℃ for 30 min in 15 mL 1% PVA/H2O. Then 4.34 mol/L VAc was added dropwise and the reaction was allowed to proce at 48℃ for 3 h. The grafting efficiency could come up to 30%. It was found the stability of modified CAGB in the air and in electrolyte solutions was greatly improved.