三氟化硼引发四氢呋喃聚合的研究——以环氧氯丙烷为促进剂

<正> 四氢呋喃(THF)通过正离子开环聚合而制得的聚丁二醇(PTMG)是生产嵌段聚醚聚氨酯及嵌段聚醚聚酯弹性材料的重要原料。目前制备PTMG所采用的引发剂都是强酸型的,如高氯酸、氟磺酸或发烟硫酸等,对设备腐蚀严重。用酸性较弱的三氟化硼引发聚合在文献上也有一些研究报道,但尚难以采用,其主要困难在于实际应用的     

四氢呋喃开环聚合的研究——Ⅳ.发烟硫酸-高氯酸引发四氢呋喃及环氧丙烷的共聚合

用21％或28％发烟硫酸-高氯酸引发四氢呋喃及环氧丙烷(THF:PO=100:5-15(克))进行共聚合反应,收率为50—60％,四氢呋喃的损耗不超过10—15％,产物分子量在1000—2000之间可调。与通常用三氟化硼或五氯化磷及二元醇制备的四氢呋喃-环氧丙烷共聚醚不同;当环氧丙烷用量低时,收率并不降低;产物的端羟基官能度为2;以伯醇端基为主(约65—70％)。     

四氢呋喃正离子聚合转为烯类单体负离子嵌段共聚合的研究

本文以癸二酰氯-高氯酸银催化剂在低温引发四氢呋喃正离子聚合,用伯胺终止,制得带有双端仲胺基的聚四氢呋喃遥爪聚合物(PTHF-NHR,R为苄基、正丁基、苯基)。当R为苯基时,PTHF-NHR与萘钠的金属化反应接近完全。以PTHF-NHR的胺钠盐引发烯类单体(甲基丙烯酸甲酯、苯乙烯、丙烯腈)负离子嵌段共聚合。当R为苯基、单体为甲基丙烯酸甲酯时,室温反应可得到转化率为100％的ABA型嵌段共聚物,为热塑性弹性体,其抗张强度为157kg/cm~2,扯断伸长率为700％。     

在Bu_2SnO-Bu_3PO_4缩合物的存在下以端羟基聚醚增韧环氧树脂

工业中大量生产的端羟基聚醚 ,由于羟基的反应活性不够 ,不能直接用于增韧胺类固化的环氧树脂 .Bu2 SnO Bu3PO4 缩合物能催化羟基对环氧基的加成反应 .本文研究在Bu2 SnO Bu3PO4 缩合物Sn P6 70 0的存在下以端羟基聚四氢呋喃 (PTMG)增韧芳香胺 4,4′ 二氨基二苯砜 (DDS)固化的环氧树脂 .PTMG首先与环氧树脂反应生成嵌段共聚物 ,在固化时发生微相分离 .分散相的尺寸在有利于增韧的范围内 .PTMG在分子量与浓度适当时 ,能使树脂的断裂韧性大大提高 ;抗弯强度也有显著提高 ,而Tg 和模量略有降低 .     

叶立德活性聚合制备基于聚亚甲基的大分子单体

利用叶立德活性聚合方法制备了两种基于聚亚甲基的大分子单体. 其中一种是以叶立德活性聚合制备的主链链端含有羟基的聚亚甲基(PM-OH)为原料, 通过链端羟基的基团转换, 得到链端含有甲基丙烯酸酯基的大分子单体. 另一种则是以硼烷-四氢呋喃(BH₃-THF)和二乙烯基苯反应得到的三烷基硼中间体为催化剂和引发剂, 然后进行叶立德活性聚合, 再经过二水合氧化三甲胺(TAO)的氧化, 最终得到基于聚亚甲基的一端含有羟基另一端含有苯乙烯基的大分子单体. 通过高温核磁氢谱、傅立叶红外光谱和高温凝胶色谱法表征了这两种大分子单体的链结构和分子量及其分布.     

四氢呋喃开环聚合的研究

本文探讨了以环氧氯丙烷(ECH)为促进剂,用发烟硫酸—高氯酸、乙酸酐—高氯酸为催化剂的四氢呋喃开环聚合。探讨了反应温度和ECH、高氯酸用量对开环聚合的分子量及产率的影响。采用了KOH回流法对原料进行处理,效果显著。     

化学发光免疫分析试剂吖啶酯的合成新路线

设计了一种化学发光免疫分析试剂吖啶酯的合成新路线,以二苯胺为原料合成吖啶-9-羧酸,经酰氯化后与3-(4-羟基苯基)-丙酸-N-羟基琥珀酰亚胺酯反应得4-(2-琥珀酰亚胺基氧羰基乙基)苯基-9-吖啶羧酸酯,最后与氟磺酸甲酯反应即得4-(2-琥珀酰亚胺基氧羰基)苯基-10-甲基吖啶-9-羧酸酯氟磺酸盐(俗称吖啶酯).     

双端正离子活性链的研究——α,ω—二胺基聚丁二醇-聚酯-聚丁二醇三嵌段低聚物的合成

<正> 本实验室前项工作曾证明用脂肪二酰氯与高氯酸银引发四氢呋喃(THF)在0—50℃下聚合可形成没有链终止和链转移反应的活性聚合链.为了减少聚丁二醇醚结晶趋势,又制备了双端活性的THF-环氧丙烷无规共聚醚链.本文则通过THF的开环聚合,将一个非“活性”的聚酯转变成为双端活性链,合成了伯胺端基聚丁二醇-聚酯-聚丁二醇遥爪低聚物,并用以增韧环氧树脂.     

化学酶法合成五嵌段聚合物及其自组装行为的研究

用酶促开环聚合与ATRP方法相结合,制备了聚甲基丙烯酸六氟丁酯-聚己内酯-聚乙二醇-聚己内酯-聚甲基丙烯酸六氟丁酯(PHFMA-b-PCL-b-PEG-b-PCL-b-PHFMA)五嵌段聚合物.首先用Novozym e 435作为催化剂合成了聚己内酯-聚乙二醇-聚己内酯三嵌段聚合物,然后通过端基官能化法合成了大分子引发剂,并用其引发甲基丙烯酸六氟丁酯(HFMA)的ATRP反应,合成了五嵌段聚合物.通过核磁和GPC证明了大分子引发剂和五嵌段共聚物的结构,五嵌段共聚物的GPC分析表明这种合成方法的可行.共聚物胶束的直径和大小通过动态光散射方法和原子力显微镜测试,五嵌段共聚物在水中的的自组装行为也被研究.结果证明胶束是球形,其平均直径为77 nm.聚合物在四氢呋喃中的浓度对聚合物的聚集形貌有很大的影响.     

遥爪型液体聚合物及其多相共聚物的合成与表征——Ⅰ.端羧基乙烯基四氢呋喃-环氧丙烷液体共聚醚的合成

本文探索了端羟基液体聚合物,四氢呋喃-环氧丙烷共聚醚,与顺丁烯二酸酐的酯化反应,得到了端羧基乙烯基液体聚合物。 通过控制反应温度,配料比以及选择适宜的催化剂,使端基转化率达到了100%。 用化学分析、核磁共振以及红外光谱分别对端基转化程度和聚合物结构进行了测定。     

用三氟化硼引发体系制备聚丁二醇

分子量在3000以下特别是1000或2000的聚丁二醇(PTMG)是制备嵌段聚醚聚氨酯及嵌段聚醚聚醋弹性体的重要软段原料。用三氟化硼(BF_3)体系引发制备PTMG巳有报道,但尚难在工业上采用,主要是引发效率低。前已报道,BF_3-环氧氯丙烷(ECH)体系的引发效率比BF_3-环氧乙烷(EO)体系高2.5～6倍,比BF_3-环氧丙烷(PO)体系高2～3倍。本文用BF_3-ECH为引发体系,并用水为分子量调节剂制备分子量1000或2000的PTMG,测     

New synthetic route of polyoxytetramethyleneglycol by use of heteropolyacids as catalyst

Polyoxytetramethyleneglycol (PTMG) can be directly prepared from tetrahydrofuran (THF) and water in the presence of heteropolyacids (HPA), without the hydrolysis step. The reaction is carried out by mixing two liquid phases: the THF phase and a heteropolyacid catalyst phase. In this reaction the molar ratio of water to a heteropolyacid (H₂O/HPA) in the catalyst phase plays an important role in the THF polymerization activity and the molecular weight of PTMG. IR spectrometric studies revealed that THF is coordinated to a heteropolyanion through either a water molecule or a proton in the catalyst phase. The latter type of coordination bings about the activation of THF capable of initiating the ring-opening polymerization even in the presence of water at a lower acid strength. The PTMG prepared by this method has a narrow molecular weight distribution (M?_w/M?_n = 1.5 or less) and a number average molecular weight of 500–2000 which are requisite for the production of polyurethane elastomers. A new polymerization mechanism named “Phase Transfer Polymerization” is proposed for elucidating a narrow molecular weight distribution.     

四氢呋喃与环氧氯丙烷共聚合的研究

<正> 晃玉等曾以BF_3-二元醇(DO)引发四氢呋喃(THF)与环氧氯丙烷(ECH)共聚合,用所得共聚醚制成嵌段聚醚聚氨酯,与用THF均聚醚或THF-环氧丙烷(PO)共聚醚为软段的聚氨酯相比,分别在低温性能及强度上有明显改进.且由于引入氯甲基侧基可作进一步接枝共聚改性。但用BF_3-DO为引发剂很难制得不含环聚体的共聚醚,     

STUDIES ON THE RING-OPENING POLYMERIZATION OF TETRAHYDROFURAN Ⅳ. COPOLYMERIZATION OF TETRAHYDROFURAN AND PROPYLENE OXIDE INITIATED BY FUMING SULFURIC ACID AND PERCHLORIC ACID CATALYST SYSTEM

The yield of copolymerization of tetrahydrofuran and propylene oxide (THF:PO=100:5—15, by wt.) using a binary catalyst of fuming sulfuric acid (21% or 28%) and perchloric acid is around 50—60%, and the loss of THF in the reaction is below 10—15%. The average molecular weight of the product can be controlled in the range of 1000—2000 by varying the binary catalyst system. The present method, which is different from the usual copolymerization initiated by BF_3-diol or SbCl_5-diol system, shows the pecularities i.e. the yield of copolymerization with the low PO feed is not decreased, the hydroxyl functionality is equal to 2, and the end-groups are predominantly primary hydroxyls (around 65—70%).     

Polymerization of 1-methoxy-1-ethynylcyclohexane by transition metal catalysts

The polymerization of 1-methoxy-1-ethynylcyclohexane (MEC) was carried out by various transition metal catalysts. The catalysts MoCl₅, MoCl₄, and WCl₆ gave a relatively low yield of polymer (≤ 16%). The catalytic activity of Mo-based chloride catalyst was greater than that of W-based chloride catalyst. However, catalyst tungsten carbene complex (I) gave a larger molar mass and higher yield in the presence of a Lewis acid such as AlCl₃ than in the absence of a Lewis acid. The activity of the tungsten carbene complex was obviously affected by Lewis acidity. The catalyst PdCl₂ was a very effective catalyst for the present polymerization and gave polymers in a high yield. The structure of the resulting poly(MEC) was identified by various instrumental methods as a conjugated polyene structure having an α-methoxycyclohexyl substituent. The poly(MEC)s were mostly light-brown powders and completely soluble in various organic solvents such as tetrahydrofuran (THF), chloroform (CHCl₃), ethylacetate, n-butylacetate, dimethylformamide, benzene, xylene, dimethylacetamide, 1,4-dioxane, pyridine, and 1-methyl-2-pyrrolidinone. Thermogravimetric analysis showed that the polymer started to lose mass at 125°C and that maximum decomposition occurred at 418°C. The x-ray diffraction diagram shows that poly(MEC) has an amorphous structure. © 1997 John Wiley & Sons, Inc.     

Preparation of poly(oxybutyleneoxymaleoyl) catalyzed by a proton exchanged montmorillonite clay

The polycondensation of tetrahydrofuran with maleic anhydride catalyzed by Maghnite-H+ (Mag-H) was investigated. Maghnite is a montmorillonite sheet silicate clay that is exchanged with protons to produce Maghnite-H [1]. It was found that the polymerization in bulk is initiated by Mag-H in the presence of acetic anhydride at 40 degrees C.The effects of the amounts of Mag-H and acetic anhydride were studied. The polymerization yield increased as the proportions of catalyst and acetic anhydride were increased.     

Cationic polymerization of formaldehyde in liquid carbon dioxide. Part II: A kinetic study of the polymerization

The kinetic behavior on the polymerization of formaldehyde with and without acidic catalyst, in liquid carbon dioxide, in the temperature range of 30 to 50°C. was investigated. In the polymerization without catalyst both the polymer yield and the degree of polymerization increased with reaction time and also with rising temperature. With acidic catalyst, such as acetic acid and dichloroacetic acid, both the polymer yield and the degree of polymerization increased more than that in the polymerization without catalyst. The overall rate of polymerization with and without acidic catalyst was expressed by the first-order rate equation with respect to monomer concentration. From the results it was concluded that the polymerizations belonged to a type of successive polymerization with rapid initiation and no termination. The rate constant and the activation energy of each elementary process of polymerization were estimated on the basis of the results.     

三氟化硼引发四氢呋喃聚合的研究——Ⅱ. 水的影响

<正> 分子量在3000以下的四氢呋喃聚合产物-聚丁二醇(PTMG)是重要的工业原料。前报中我们已证明用BF_3-环氧氯丙烷(ECH)引发四氢呋喃(THF)聚合时引发效率较高,在这一基础上有希望通过在聚合体系中加水以达到控制产物分子量的目的。 文献上对水在BF_3-ECH引发THF聚合反应中作用的研究不多,Kyzaeb等人     

乙炔在钒催化体系下的聚合

本工作采用三乙酰基丙酮钒及二乙酰基氧钒同烷基铝组成的催化体系,研究了乙炔聚合的规律及聚乙炔成膜的条件,并初步研究了聚乙炔膜的链节结构、形态结构及室温电导率。