双金属氧联醇盐催化环硫丙烷的开环聚合

研究了环硫丙烷以铝锌双金属氧联醇盐为催化剂在甲苯中的聚合动力学及分子量分布。结果表明,环硫丙烷的聚合速度对单体浓度是二级关系,对催化剂浓度是半级关系。聚合系统中催化剂存在缔合,认为环硫丙烷以双分子配位增长。测得聚合活化能为12.2±0.5kcal/mol,计算了单体及溶剂的链转移常数。通过淋洗液中加氯化锂的GPC工作研究了分子量及其分布随转化率的变化。     

STEREOCHEMICAL CONTROL IN PROPYLENE POLYMERIZATION CATALYZED BY UNBRIDGED METALLOCENE CATALYSTS*

Two unbridged metallocene catalysts, bis (2, 4, 7-trimethylindenyl)zirconium dichloride (met-I) and bis(2, 4, 6-trimethylindenyl) zirconium dichloride (met-II), which are different in the position o f substituents on the six-membered ringof the indenyl ligands were synthesized. The effect of substituents in the two metallocenes on the propylene polymerizationwas studied in the presence of methylaluminoxane (MAO) and triisobutylaluminium (TIBA). From the analysis ofmicrostructure determined by ~(13)C-NMR, it was demonstrated that the polymers produced by met-II have higher [mmmm]isotactic sequences than that of met-I. Using a mechanism based on model statistical analysis, it was found that chain-endmodel was dominant for met-I. However, met-II obeys the concurrent two-sites model during polymerization, which can beattributed to the existence of "racemic-like" conformer in its system.     

RING-OPENING POLYMERIZATION OF ε-CAPROLACTONE BY LANTHANOCENE CATALYSIS*

Ring-opening polymerization of ε-caprolactone (CL) catalyzed bylanthanocenes, O(C_2H_4C_5H_3CH_3)_2YCl (Cat-YCl) and Me_2Si[(CH_3)_3SiC_5H_3]_2NdCl(Cat-NdCl) has been carried out for the first time. It has been found that both yttroceneand neodymocene are very efficient to catalyze the polymerization of CL, giving high molec-ular weight poly (ε-caprolactone) (PCL ). The effects of [cat] / [ε- CL] molar ratio, polymeriza-tion temperature and time, as well as solvents were investigated and polymerization tem-perature is found to be the most important factor affecting the polymerization. The bulkpolymerization gives higher molecular weight PCL and higher conversion than that in solu-tion polymerization. NaBPh_4 was found to promote the polymerization of ε-caprolactone,and thus to increase both the polymerization conversion and MW of poly (ε- caprolactone ).     

双金属氰化物络合物催化环氧烷烃开环聚合的特征

合成了Co Zn双金属氰化物 (DMC)络合物催化剂 ,以X 射线衍射、元素分析、红外光谱等手段进行了表征 ,考察了该催化体系下环氧丙烷开环聚合的反应特性 ,并初步探讨了聚合反应的机理 .研究发现 ,Co Zn双金属氰化物催化剂具有很高的催化活性 ,适合于中高分子量聚醚的合成 ,但是碱性起始剂起阻聚作用 ;在该催化体系下聚合物分子量可控 ,不饱和度很低 (<0 .0 14meq g) ,分批加料聚合所得到的聚合物分子量分布较窄 (Mn Mw <1.4 ) ,而一步加料聚合所得到的聚合物分子量分布变宽 ;1 3C NMR分析表明聚合物主链具有无规立构分布的特点 ,且链节分布几乎都为头 尾方式 .聚合过程中活性链与非活性链之间可能存在一个交换反应 ;虽然聚合反应有终止 ,但与聚合物链长没有关系 ,聚合物链的终止是可逆的 .     

RING-OPENING POLYMERIZATION OF TRIMETHYLENE CARBONATE BY CALIX[8]ARENE-NEODYMIUM*

Ring-opening polymerization of trimethylene carbonate (TMC) with a rare earth calixarene compound as catalysthas been studied for the first time. The effect of TMC/Nd (molar ratio) and polymerization conditions were investigated indetail. It was found that calix[8]arene-neodymium is a highly effective catalyst for the bulk polymerization of TMC and giveshigh molecular weight (M_v = 60,000) polymer. The optimum conditions of TMC polymerization were found to be asfollows:TMC/Nd (molar ratio) = 2,000, 80℃, 16 h. The polymers were characterized by NMR, GPC and DSC. Studying themechanism by NMR showed that the polymerization of TMC catalyzed by calix[8]arene-neodymium proceeds via a cationicmechanism.     

TS-1催化丙烯环氧化过程中环氧丙烷的开环反应研究

环氧丙烷的开环反应是TS-1催化丙烯环氧化制备环氧丙烷过程的副反应,本文对醇溶剂中开环反应进行了研究,分析了该反应的酸性催化机理,酸性主要来自TS-1与H2O2的相互作用产生的质子酸,醇溶剂能显著增强体系酸性从而加快环氧丙烷的开环反应速度。三种醇按酸性增强程度的顺序为甲醇>异丙醇>仲丁醇。根据反应的Eley-Rideal 机理（吸附态的PO与游离态的醇发生开环反应,表面反应为控制步骤）再考虑各组分在TS-1上的吸附特点提出反应的机理模型。用实验数据进行了回归,得到了令人满意的动力学方程式,实验数据与模型计算值平均偏差小于10％。     

RING OPENING POLYMERIZATION OF PROPYLENE SULFIDE BY RARE EARTH COORDINATION CATALYSTS*

Ring opening polymerization of propylene sulfide using rare earth coordination catalysts has been investigated for the first time. It has been found that trinary rare earth coordination catslysts composed of rare earth compounds of phosphonate, naphthenate or acetylacetonate, trialkyl sluminum and water are effective catalysts for the polymerization of propylene sulfide. The polymerization in toluene is a homogeneous reaction. High molecular weight as high as several million poly(propylene sulfide) with high yield can be prepared by these catalysts. Kinetic studies showed that the polymerization rate is of first order with respect to both monomer concentration and catalyst concentration. The activation energy of the polymerization reaction is 61.4 k fJ/mol. The structure of the polymers so obtained has also been characterized by ~(13)C NMR spectroscopy, X-ray diffraction, gel permeation chromatography and differential scanning calorimetry.     

THE EFFECT OF ETHERS ON ALTERNATING COPOLYMERIZATION OF BUTADIENE AND PROPYLENE CATALYZED BY VANADIUM-ALUMINUM SYSTEM

The effect of five ethers on alternating copolymerization of br(?)adiene and propylene were investigated. It was found that under appropriate conditions, by adding ether into reaction system, the conversion could be increased by 10-20% and the catalytic efficiency doubled at -45℃. The interaction between ether and active center was also studied.     

Fe-Zn双金属氰化物催化环氧丙烷开环聚合的研究

用Fe Zn双金属氰化物 (DMC)催化剂合成了数均分子量 30 0 0～ 12 0 0 0的聚氧化丙烯二元醇 .着重考察了聚合反应的温度、加料方式等对聚合物分子量及分布的影响 ,并初步探讨了Fe Zn双金属氰化物催化环氧丙烷开环聚合的反应特征 .实验发现 ,采用Fe ZnDMC催化剂 ,聚合物分子量可控 ;在较高温度下聚合所得的聚合物分子量分布呈双峰形 ,显示反应体系中至少存在两类活性中心 ,这可能与催化剂中存在两种价态的络合物有关 ,当降低聚合温度时 ,聚合物分子量分布呈单峰形 ,可能是一类活性中心没有引发 ;实验中还发现单体分批加料时聚合物分子量分布较窄 ,而一步加料法所得聚合物分子量分布则很宽     

STUDIES ON THE KINETICS OF PROPYLENE POLYMERIZATION WITH THE COMPLEXTYPE TiCl_3 CATALYST

The active center concentration C_p, the rate constant k_p, and the activation energy of chain propagation E_p in the polymerization of propylene with complex-type TiCl_3-(C_2H_5)_2AlCl catalyst system were studied. The Mn was corrected by (?) value determined by GPC. The values thus obtained for C_p, k_p, and E_p at 50℃were 3.01 mol/mol Ti, 6.27 1/mol·sec, and 5.10 Kcal/mol respectively.The kinetic parameters were compared with those obtained from conventional TiCl_3·AlCl_2 catalyst, showing that the higher activity of the complex-type catalyst over the conventional catalyst is not only due to the higher C_p of the former, but to a greater extent due to the increase of the k_p value.     

PLASMA POLYMERIZATION OF HEXAMETHYLCYCLOTRISILOXANE

In a capacitively coupled RF discharge system with external electrodes ,hexamethyicyclotrisiloxane was polymerized, and the effects of discharge power and plasma gas on polymer deposition rate were studied. The polymer structures and properties were studied by IR spectroscopy, XPS measurement, PGC/MS combined technique, TG analysis and contact angle measuring. The results showed that the polymers prepared in H_2 or O_2 have higher C/Si ratio in comparison with those prepared in inert gases. PGC/MS results revealed the existence of many short carbon chains in the polymer structure .TG analysis suggested that the polymers prepared in the inert gas would possess better thermal stabilities.     

SYNTHESIS, CHARACTERIZATION AND RING-OPENING POLYMERIZATION OF CYCLIC (ARYLENE PHOSPHONATE) OLIGOMERS

INTRODUCTIONThe use of cyclic oligomers as macrocyclic precursors for the preparation of high performance polymers byring-opening polymerization (ROP) has sparked much interest in recent years. It could produce a revolutionarychange in the preparation of advanced composite materials, and is of great importance in the polymerizationprocess yielding polymers such as the reinforced reactive injection model (RRIM) and the resin transfer model(RTM) etc. Within the last 10 years, the synthes…     

THE RING-OPENING POLYMERIZATION OF D,L-LACTIDE WITH ONE COMPONENT RARE EARTH CATALYST

(D, L)-Lactide (LA) was first polymerized with one component of rare earth cata-lysts [Nd(naph)_3, Nd(oct)_3, Nd(O-iPr)3, Nd(AcAc)_3, Y(AcAc)_3, Sm(AcAc)_3, Er(AcAc)_3)]respectively in solution and in melt state. The effects of [Cat]/[LA] molar ratio, solvents,polymerization time, temperature, various rare earth elements and ligands were investi-gated in detail. The results showed that both the conversion of polymerization and themolecular weight (MW) of poly (D, L-Lactide) (PLA) in melt polymerization are higherthan that in solution polymerization, but the polymerization rate in melt was lowr than insolution. The molecular weight distribution (MWD) of PLA is broader with increasing tem-perature. X-ray study indicated that PLA obtained by Nd(AcAc)_3 in melt polymerizationis an amorphous polymer.     

大环碳酸酯的Novozym-435酶促开环聚合

研究了14元环的碳酸丁二酯二聚体在固定化脂肪酶Novozym-435催化下的开环聚合反应制备聚碳酸丁二酯.聚合在常压,75℃的甲苯溶液中进行,反应条件温和.详细探讨了反应条件诸如单体浓度,酶浓度对于聚合的影响.结果显示Novozym-435具有与异辛酸亚锡可比拟的高催化活性,同时可以回收重复使用.聚合动力学研究表明碳酸丁二酯的酶促甲苯溶液开环聚合和环状内酯的酶促甲苯溶液聚合有所不同,没有表现出活性聚合的特征.     

苄醇存在下脂肪叔胺催化内酯开环聚合

为研究脂肪叔胺结构对内酯开环聚合规律的影响,以三乙胺( TEA)、N,N,N′,N′-四甲基乙二胺(TMEDA)、N,N,N′,N″,N″-五甲基二亚乙基三胺(PM DTA)3种不同结构的叔胺催化碳酸三亚甲基酯(TMC)和左旋丙交酯( L-LA)开环聚合.结果显示,在55℃的THF溶液中,以苄醇为引发剂,3种叔胺均能催...     

MECHANISM FOR THE INITIATION OF ACRYLONITRILE POLYMERIZATION BY POLYPROPYLENE-BASED POLYAMIDOXIME-THIOUREA COMBINATION

Polymerization of acrylonitrile (AN) in aqueous nitric acid initiated by polypropylene-based polyamidoxime (PPAO)-thiourea (TU) combination has been investigated. The overall rate of polymerization (R_p) under the conditions of [TU]/[PPAO]<0.5 molar ratio isThe molecular weights of the polymers were found to be inversely proportional to 3/2-power of nitric acid concentration and 1-power of thiourea concentration. In addition, it is independent with the concentrations of monomer and PPAO, and decreases with increasing temperature.On the basis of these experimental results, a coordination-proton transfer mechanism for the initiation was proposed and discussed.     

双金属催化环氧化物聚合动力学研究

研究了双金属氰化络合催化剂DMC催化环氧丙烷聚合的动力学 .用测定反应过程体系压力变化来决定聚合的起始速率 ,发现聚合反应速率正比于催化剂用量C ,单体浓度M的平方 .该实验规律可以从单体参与链引发的动力学特点解释 .考察了温度对聚合反应速率的影响并求得了表观活化能为 5 9 1kJ·mol- 1 ,该值与环氧聚合的卟啉铝、稀土络合物等催化体系接近 .     

KINETICS OF SUSPENDED EMULSION POLYMERIZATION OF METHYL METHACRYLATE*

 The kinetics of suspended emulsion polymerization of methyl methacrylate (MMA), in which water acted as the dispersed phase and the mixture of MMA and cyclohexane as the continuous phase, was investigated. It showed that the initial polymerization rate (R_p0) and steady-state polymerization rate (R_p) were proportional to the mass ratio between water and oil phase, and increased as the polymerization temperature, the potassium persulphate concentration ([I]) and the Tween20 emulsifier concentration ([S]) increased. The relationships between the polymerization rate and [I] and [S] were obtained as follows: R_p0∝[I]^0.71[S]^0.23.The above exponents were close to those obtained from normal MMA emulsion polymerization. It also showed that the average molecular weight of the resulting poly(methylmethacrylate) decreased as the polymerization temperature,[I]and [S] increased. Thus, MMA suspended emulsion polymerization could be considered as a combination of many miniature emulsion polymerizations proceeding in water drops and obeyed the classical kinetics of MMA emulsion polymerization.     

KINETICS OF POLYMERIZATION OF METHYL METHACRYLATE INITIATED BY COPPER POLYPROPYLENE-BASED POLYAMIDOXIME-SODIUM SULFITE SYSTEM*

The aqueous polymerization of methyl methacrylate initiated by copper polypropylene-based polyamidoxime (PPAO-Cu) -sodium sulfite system was investigated. The overall rate of polymerization (R_p) isR_p=9.7 x 10~(12) e~(-21.200/RT) [MMA]~(O.88)[Na_2 SO_3]~(0.50)The length of the induction period (τ) is inversely proportional to the concentration of sodium sultite and independent of the amount of polymer supported copper and the concentration of monomer. It could be expressed as follows:1/τ=1.2x10~(12)e~(-15.600/RT)[Na_2SO_3]=K_τR_iThe polymerization is initiated by a primary radical generated from the redox reaction rather than induced by "coordination-proton transfer" mechanism.     

POLYMERIZATION OF OCTAMETHYLCYCLOTETRASILOXANE WITH HEXAMETHYLDISILAZYL-LITHIUM AS INITIATOR*

 This work focused on the anionic polymerization of octamethylcyclotetrasiloxane (D₄, D = Me₂SiO_2/2) initiated by a new kind of initiator hexamethyldisilazyl-lithium (MM^NLi). ²⁹Si-NMR spectroscopy and gas chromatography (GC) were used to characterize the polymerization products. The process was accelerated by adding a small amount of high activity monomer D₃ and by raising the polymerization temperature. At the end of polymerization more than 95% of the monomer was converted to polymer and only a very small amount ofD₄ and D₅ remained in the polymers.