稀土三元催化剂催化二氧化碳/环氧丙烷/环氧环己烷的三元共聚合研究

在稀土三元催化剂(三氯乙酸稀土配合物/二乙基锌/甘油)催化下实现了二氧化碳、环氧丙烷及环氧环己烷的三元共聚合.该催化剂对二氧化碳与环氧环己烷共聚的催化活性比对二氧化碳与环氧丙烷共聚的高.增加反应单体中环氧环己烷的比例可提高共聚物中环己撑碳酸酯的含量,大幅度改善共聚物的耐热性.     

醋酸锌催化二氧化碳和环氧化合物共聚研究

以醋酸锌为催化剂,在无溶剂条件下实现了二氧化碳和环氧环己烷共聚,研究了反应温度、反应压力和反应时间对共聚的影响.并在优化条件(120℃、5 MPa和24 h)下,用醋酸锌催化了二氧化碳、环氧环己烷和第三单体(环氧丙烷或烯丙基缩水甘油醚)三元共聚,研究了单体物质的量之比对聚合结果的影响.研究结果表明,第三单体的种类和用量对聚合反应结果影响显著,环氧丙烷或烯丙基缩水甘油醚的引入降低了二氧化碳和环氧环己烷二元共聚物的玻璃化转变温度.     

二氧化碳与环氧化合物的三元共聚反应

用二氧化碳与环氧化合物共聚合反应制备脂肪族聚碳酸酯,是近几年化学利用二氧化碳研究的重要课题之一.其中最受关注的是二氧化碳与环氧丙烷共聚制备聚碳酸丙烯酯(PPC)和二氧化碳与环氧环己烷共聚制备聚碳酸环己烯酯(PCHC).但是,PPC和PCHC的热性能和力学性能欠佳,限制了它们的规模化生产与应用.利用二氧化碳与环氧化合物进行三元共聚是改善二氧化碳共聚物材料热性能和力学性能的有效途径之一,本文对此项研究的新进展进行了综述.     

二氧化碳与环氧化合物共聚催化剂研究进展

二氧化碳是一种廉价、低毒、资源丰富的可用于有机合成的理想原料。由二氧化碳和环氧化合物共聚合成的脂肪族聚碳酸酯具有生物可降解性。自1969年井上祥平等发现二氧化碳和环氧化合物通过共聚反应合成脂肪族聚碳酸酯以来,利用二氧化碳制备高分子材料一直备受人们注目。该过程的关键是寻找具有高选择性的高效催化剂,三十余年来通过各国科学家的不懈努力已取得了不少成果,本文对其研究的最新进展进行了综述。     

聚碳酸亚环己酯及其制备技术研究进展

二氧化碳既(CO₂)是令人头疼的温室气体,更是有价值的碳资源,因此二氧化碳的固定和利用具有重要的理论与现实意义。以二氧化碳和环氧环己烷为原料合成的聚碳酸亚环己酯(PCHC)是一种新型的脂环类可生物降解聚酯材料,相比传统的二氧化碳-环氧烷聚合物,其机械和耐热性能更为优良,有望拓展脂肪类聚碳酸酯的使用范围。本文对PCHC的基本性能及潜在应用领域、合成工艺路线以及交替共聚反应催化剂的发展进行了综述,以期为优质PCHC材料的高效制备提供参考。     

脂肪族聚碳酸酯共聚物的研究进展

脂肪族聚碳酸酯共聚物是一类可完全生物降解的新型材料,自1969年井上祥平等首次通过二氧化碳与环氧化合物反应合成脂肪族聚碳酸酯以来,人们在将二氧化碳固定为全降解聚合物这一研究领域取得了大量研究成果.本文综述了用于二氧化碳和环氧化合物共聚合成脂肪族聚碳酸酯的各类催化剂及反应机理,讨论了脂肪族聚碳酸酯结构/性能关系,并简要介绍了其在不同领域的应用.     

二氧化碳与环氧化物共聚催化剂研究进展

二氧化碳是主要的温室气体,也是最丰富的C1资源.利用二氧化碳与环氧化物共聚生成可生物降解的聚碳酸酯是目前研究的热点之一.就目前的研究情况而言,二氧化碳与环氧化物共聚反应存在的主要问题是催化效率低、催化剂成本高、反应条件苛刻、共聚物产率较低以及催化剂分离复杂等.我们分类综述了二氧化碳与环氧化物共聚的新型催化体系,并探讨了各类催化体系的优缺点,对二氧化碳的资源化利用具有重要的应用价值.     

二氧化碳与环氧化合物直接制备聚碳酸酯

综述了近几年来发展的用于二氧化碳与环氧化合物直接催化合成聚碳酸酯的各类催化剂,并详细讨论了其催化反应机理.利用二氧化碳与环氧化合物来合成聚碳酸酯,对于高分子合成化学、碳资源利用和环境保护都具有重大意义.它是发展聚碳酸酯生产的一个具有很大潜力的方面.     

高效Ni/Zn催化剂体系固定CO2与环氧化合物的环加成反应

在1.5-MPa CO₂,100℃下NiCl₂/bipy/Zn/TBAB催化剂体系能够高效、无溶剂地催化固定二氧化碳和环氧化合物的环加成制备环状碳酸酯的反应,得到了很高的催化收率和转化频率.并且在该催化剂体系中第一次得到了全顺式的环氧环己烷的碳酸酯.     

二氧化碳与环氧化合物合成环状碳酸酯的研究进展

二氧化碳作为温室气体和储量大、无毒且可循环利用的碳资源,其化学利用受到了人们的广泛关注. 二氧化碳与环氧化合物通过环加成反应制备环状碳酸酯是二氧化碳化学法利用最为有效的途径之一. 本文综述了近年来该反应的研究进展,讨论了催化剂作用下的反应机理.     

Copolymerization of Cyclohexene Oxide and CO(2) with a Chromium Diamine-bis(phenolate) Catalyst

A diamine-bis(phenolate) chromium(III) complex, {CrCl[O(2)NN'](BuBu)}(2) catalyzes the copolymerization of cyclohexene oxide with carbon dioxide. The synthesis of this metal complex is straightforward, and it can be obtained in high yields. This catalyst incorporates a tripodal amine-bis(phenolate) ligand, which differs from the salen or salan ligands typically used with Cr and Co complexes that have been employed as catalysts for the synthesis of such polycarbonates. The catalyst reported herein yields low molecular weight polymers with narrow polydispersities. Structural and spectroscopic details of this complex along with its copolymerization activity for cyclohexene oxide and carbon dioxide are presented.     

Heterodinuclear Zn(II), Mg(II) or Co(III) with Na(I) Catalysts for Carbon Dioxide and Cyclohexene Oxide Ring Opening Copolymerizations

A series heterodinuclear catalysts, operating without co-catalyst, show good performances for the ring opening copolymerization (ROCOP) of cyclohexene oxide and carbon dioxide. The complexes feature a macrocyclic ligand designed to coordinate metals such as Zn(II), Mg(II) or Co(III), in a Schiff base ‘pocket’, and Na(I) in a modified crown-ether binding ‘pocket’. The 11 new catalysts are used to explore the influences of the metal combinations and ligand backbones over catalytic activity and selectivity. The highest performance catalyst features the Co(III)Na(I) combination, [N,N′-bis(3,3’-triethylene glycol salicylidene)-1,2-ethylenediamino cobalt(III) di(acetate)]sodium ( 7 ), and it shows both excellent activity and selectivity at 1 bar carbon dioxide pressure (TOF=1590 h⁻¹, >99 % polymer selectivity, 1 : 10: 4000, 100 °C), as well as high activity at higher carbon dioxide pressure (TOF=4343 h⁻¹, 20 bar, 1 : 10 : 25000). Its rate law shows a first order dependence on both catalyst and cyclohexene oxide concentrations and a zeroth order for carbon dioxide pressure, over the range 10–40 bar. These new catalysts eliminate any need for ionic or Lewis base co-catalyst and instead exploit the coordination of earth-abundant and inexpensive Na(I) adjacent to a second metal to deliver efficient catalysis. They highlight the potential for well-designed ancillary ligands and inexpensive Group 1 metals to deliver high performance heterodinuclear catalysts for carbon dioxide copolymerizations and, in future, these catalysts may also show promise in other alternating copolymerization and carbon dioxide utilizations.     

Alternating copolymerization of carbon dioxide and epoxide by manganese porphyrin: The first example of polycarbonate synthesis from 1-atm carbon dioxide

The first successful example of the formation of polycarbonate from 1-atm carbon dioxide and epoxide was demonstrated by the alternating copolymerization of carbon dioxide and epoxide with manganese porphyrin as a catalyst. The copolymerization of carbon dioxide and cyclohexene oxide with (porphinato)manganese acetate proceeded under the 1-atm pressure of carbon dioxide to give a copolymer with an alternating sequence. © 2003 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 41: 3549–3555, 2003     

Mechanistic investigation and reaction kinetics of the low-pressure copolymerization of cyclohexene oxide and carbon dioxide catalyzed by a dizinc complex

The reaction kinetics of the copolymerization of carbon dioxide and cyclohexene oxide to produce poly(cyclohexene carbonate), catalyzed by a dizinc acetate complex, is studied by in situ attenuated total reflectance infrared (ATR-IR) and proton nuclear magnetic resonance ((1)H NMR) spectroscopy. A parameter study, including reactant and catalyst concentration and carbon dioxide pressure, reveals zero reaction order in carbon dioxide concentration, for pressures between 1 and 40 bar and temperatures up to 80 °C, and a first-order dependence on catalyst concentration and concentration of cyclohexene oxide. The activation energies for the formation of poly(cyclohexene carbonate) and the cyclic side product cyclohexene carbonate are calculated, by determining the rate coefficients over a temperature range between 65 and 90 °C and using Arrhenius plots, to be 96.8 ± 1.6 kJ mol(-1) (23.1 kcal mol(-1)) and 137.5 ± 6.4 kJ mol(-1) (32.9 kcal mol(-1)), respectively. Gel permeation chromatography (GPC), (1)H NMR spectroscopy, and matrix-assisted laser desorption/ionization time-of-flight (MALDI-ToF) mass spectrometry are employed to study the poly(cyclohexene carbonate) produced, and reveal bimodal molecular weight distributions, with narrow polydispersity indices (≤1.2). In all cases, two molecular weight distributions are observed, the higher value being approximately double the molecular weight of the lower value; this finding is seemingly independent of copolymerization conversion or reaction parameters. The copolymer characterization data and additional experiments in which chain transfer agents are added to copolymerization experiments indicate that rapid chain transfer reactions occur and allow an explanation for the observed bimodal molecular weight distributions. The spectroscopic and kinetic analyses enable a mechanism to be proposed for both the copolymerization reaction and possible side reactions; a dinuclear copolymerization active site is implicated.     

高聚物负载双金属催化剂催化二氧化碳-氧化环己烯的共聚反应

由CO2 氧化环己烯 (CHO)配位催化共聚制得高Tg 的脂肪族聚碳酸亚环己基酯 ,并用IR、NMR和DSC等进行了表征 ,用TG对聚合物的热稳定性进行分析 .加入环氧丙烷 (PO)三元共聚并分析PO/CHO摩尔比对Tg 的影响 .加入异氰酸苯酯有提高产物特性粘数的作用     

Asymmetric amplification in asymmetric alternating copolymerization of cyclohexene oxide and carbon dioxide

Asymmetric amplification in the copolymerization of cyclohexene oxide and carbon dioxide was demonstrated using chiral zinc complexes, prepared from diethylzinc, diphenyl(pyrrolidin-2-yl)methanol, and ethanol.     

Copolymerization of CO2 and cyclohexene oxide

Generation of high value polymers from carbon dioxide is of general technological interest given that CO2 is both inexpensive and relatively easy to handle on an industrial scale. Previous work on the use of CO2 as a comonomer has focused primarily on development of new catalysts, and the effects of conventional process variables such as temperature and concentration on the polymerization outcome have not been examined in great detail. Recently, we, as well as Darensbourg and colleagues, have shown that one can generate zinc-based catalysts for the polymerization of CO2 and cyclohexene oxide which produce over 400 grams of polymer per gram of metal. In this paper, we use a product of the reaction between zinc oxide and the fluorinated half-ester of maleic anhydride to generate copolymers of CO2 and cyclohexene oxide where CO2 is both reactant and sole solvent. In general, we found that the outcome of the polymerization depends greatly on the proximity to the ceiling temperature and the critical cyclohexene oxide concentration, and also on the phase behavior of the cyclohexene oxide-CO2 binary.     

二氧化碳-氧化环己烯的共聚反应

由CO2 -氧化环己烯 (CHO)配位催化共聚制得高Tg 的脂肪族聚环己基撑碳酸酯 ,并用IR、NMR和DSC等进行了表征 ,用TG对聚合物的热稳定性进行了分析。加入异氰酸苯酯有提高产物特性粘数的作用。     

Differences in Reactivity of Epoxides in the Copolymerisation with Carbon Dioxide by Zinc-Based Catalysts: Propylene Oxide versus Cyclohexene Oxide

The homogeneous dinuclear zinc catalyst going back to the work of Williams et al. is to date the most active catalyst for the copolymerisation of cyclohexene oxide and CO₂ at one atmosphere of carbon dioxide. However, this catalyst shows no copolymer formation in the copolymerisation reaction of propylene oxide and carbon dioxide, instead only cyclic carbonate is found. This behaviour is known for many zinc‐based catalysts, although the reasons are still unidentified. Within our studies, we focus on the parameters that are responsible for this typical behaviour. A deactivation of the catalyst due to a reaction with propylene oxide turns out to be negligible. Furthermore, the catalyst still shows poly(cyclohexene carbonate) formation in the presence of cyclic propylene carbonate, but the catalyst activity is dramatically reduced. In terpolymerisation reactions of CO₂ with different ratios of cyclohexene oxide to propylene oxide, no incorporation of propylene oxide can be detected, which can only be explained by a very fast back‐biting reaction. Kinetic investigations indicate a complex reaction network, which can be manifested by theoretical investigations. DFT calculations show that the ring strains of both epoxides are comparable and the kinetic barriers for the chain propagation even favour the poly(propylene carbonate) over the poly(cyclohexene carbonate) formation. Therefore, the crucial step in the copolymerisation of propylene oxide and carbon dioxide is the back‐biting reaction in the case of the studied zinc catalyst. The depolymerisation is several orders of magnitude faster for poly(propylene carbonate) than for poly(cyclohexene carbonate).     

(Tetramethyltetraazaannulene)chromium chloride: a highly active catalyst for the alternating copolymerization of epoxides and carbon dioxide

A tetramethyltetraazaannulene complex incorporating a chromium(III) metal center has been shown to be highly active toward the copolymerization of cyclohexene oxide and carbon dioxide to afford poly(cyclohexene carbonate) in the presence of [PPN]N3 [PPN+=bis(triphenylphosphoranylidene)ammonium] as a cocatalyst. An asymptotical rate increase was observed, leveling at 2 equiv of cocatalyst with a maximum turnover frequency of 1300 h(-1) at 80 degrees C. A benefit of this new catalyst system over that of the previously studied less-active (salen)CrX system is that the (tmtaa)CrCl catalyst has a much lower propensity toward the formation of a cyclic carbonate byproduct throughout the copolymerization reaction.