乙二醇的合成和展望

本文综述了由乙烯、环氧乙烷、合成气等不同原料合成乙二醇的工艺过程、催化体系及反应机理,并展望乙二醇的发展前景。     

漆酚缩甲醛钕聚合物催化合成环己酮乙二醇缩酮

以环己酮和乙二醇为原料,漆酚缩甲醛钕聚合物为催化剂合成了环己酮乙二醇缩酮。实验结果表明：在环己酮100mmol,n(环己酮)：n(乙二醇)=1：1,漆酚缩甲醛钕聚合物3．0g,环己烷7．5mL,回流反应1．0h,目标化合物的收率达74％。     

多缩乙二醇二苯醚与甲醛缩聚合成酚醛型聚合物假冠醚的研究

本文采用苯酚、多缩乙二醇二氯化物、多缩乙二醇等为起始原料,合成了九个多缩乙二醇二苯醚新单体,经甲醛聚合获得一系列聚合物假冠醚,并对它们的溶解性能、络合性能以及催化作用等进行研究。     

高硫合成气法合成甲硫醇研究进展

甲硫醇是生产农药,医药,石油化工产品与合成材料的重要原料,其最主要的应用为合成动物饲料蛋氨酸.硫化氢合成气一步法制备甲硫醇具有原料易得,工艺简单等优点,因此该方法成为合成甲硫醇工艺的研究热点.我们综述了硫化氢合成气合成甲硫醇反应中钼基、钨基和钒基催化剂的研究进展,特别是钼基催化剂体系下载体和助剂对催化剂性能的影响,探索了该工艺的反应路径和反应机理,并对高硫合成气制备甲硫醇工艺的应用前景进行了展望.     

CO2与CH4催化反应合成气研究

CO_2与液化天然气(98%为C_3-C_4烃)催化重整制合成气,八十年代初期在当时的西德已建立了工业生装置.近年来,由于石油资源日趋短缺,促进世界各国重视探讨和研究天然气资源利用的新途径.除甲烷氧化偶联制乙烯,甲烷氧化制甲醇和甲醛等直接转化过程已引起广泛的重视外,研究和开发由甲烷制取合成气的新过程也正日益受到人们的关注,其中利用CO_2与甲烷催化重整制合成气,可将造成温室效应,破坏人类生存环境的CO_2气体转化为宝贵的化工原料,所制得的合成气中CO/H_2=1,特别适合做羰基合成和合成有机含氧化合物的原料,近年来对该反应的研究已引起人们的重视.其反应表示如下:     

甲烷部分氧化制合成气Ni/MgO和Ni-MgO/MgO催化剂的研究

甲烷氧化偶联制乙烷、乙烯以及甲烷选择氧化制甲醇、甲醛等反应 ,因其转化率和收率低 ,故短期内无法实现工业化 .目前 ,工业上应用甲烷蒸汽转化制合成气 ,进而合成氨等化工产品 .甲烷蒸汽转化制的合成气 ,其 H2 /CO≥ 3,不适用于甲醇合成和 F- T合成 .而甲烷部分氧化制的合成气 ,其H2 /CO≤ 2 ,因而最适合用于甲醇合成和 F- T合成 ,故近 1 0年来倍受科学家的关注[1 ,2 ] .在 CH4部分氧化制合成气中 ,钌、铑、钯、铂等贵金属催化剂的活性高、选择性好、稳定性好[1 ] ,但价格昂贵 (负载量以 1 2 %～ 4 0 %为佳 ) ,因而难以实现商品化 .N…     

铜催化一锅法合成吡咯[1,2-a]喹喔啉衍生物

建立了一种简单实用、经济高效的以邻碘苯胺、吡咯甲醛为起始原料,廉价的CuI为催化剂,价廉、易获得的2,2-联吡啶为配体,110℃条件下一锅法合成吡咯[1,2-a]喹喔啉类衍生物的催化体系,得到中等到优良产率.本方法具有催化剂廉价易得、操作简便、合成效率高的优点.     

乙二醇二缩水甘油醚的合成及作为阳离子型紫外光固化稀释剂性能研究

以三氟化硼乙醚络合物为催化剂,以氢氧化钠为成环反应的闭环剂,利用乙二醇和环氧氯丙烷为原料合成了乙二醇二缩水甘油醚.研究了催化剂三氟化硼乙醚络合物用量、环氧氯丙烷和乙二醇摩尔比、氢氧化钠和乙二醇摩尔比,以及成环反应温度这些因素对合成反应的影响.结果表明较好的合成反应条件是:三氟化硼乙醚络合物质量分数为0.40%,环氧氯丙烷和乙二醇较佳摩尔比为2.4:1,氢氧化钠和乙二醇较佳摩尔比为2.2:1,较佳的成环反应温度为30℃.同时,把乙二醇二缩水甘油醚作为稀释剂加入到环氧树脂E-51中,利用三芳基锍鎓六氟锑酸盐作为引发剂,制备了阳离子型紫外光固化涂料,其紫外光固化膜的拉伸强度为46.25MPa,杨氏模量为1487.26MPa,断裂伸长率为6.27%.     

球型乙二醇单苯醚-甲醛负载三乙烯四胺螯合树脂的制备及其对Cu2+的吸附性能

以乙二醇单苯醚、甲醛为原料,采用分散聚合方法制备出乙二醇单苯醚-甲醛聚合物微球;经二甲亚砜氧化,制得醛基化改性微球(PB-CHO);微球(PB-CHO)与三乙烯四胺进行Schiff碱反应及加氢反应,制备出球型乙二醇单苯醚-甲醛负载三乙烯四胺螯合树脂(PB-TETA).对所制备的新型螯合树脂进行了红外光谱、扫描电镜等表征,并研究了PB-TETA对Cu2+的吸附性能.结果表明,在pH值为5时,PB-TETA对Cu2+的最大吸附量为0.16mmol/g;树脂对Cu2+的吸附受液膜扩散控制;吸附动力学符合拟一级动力学模型;等温吸附符合Langmuir吸附模型.     

用无声放电转化甲烷和二氧化碳同时制备合成气与烃

在低温常压条件下,研究了在无声放电反应器中以A型分子筛为催化剂从甲烷和二氧化碳合成烃和合成气,实现了在无声放电反应器中同时合成烃和合成气。实验在原料气流量200－600ml/min、原料气甲烷和二氧化碳摩尔比1／1－3／1及输入功率100－500W的范围内进行。研究结果表明,低原料气流量有利于甲烷和二氧化碳的转化,而高原料气流量有利于烃的生成;原料气甲烷和二氧化碳摩尔比对制得合成气的H2／CO摩尔比的影响最显著;甲烷和二氧化碳转化率及合成气和烃的产率均随输入功率的增加而提高。而所研究的范围内,当原料气流理为200ml/min、甲烷和二氧化碳摩尔比为1／1、输入功率为500S时,甲烷和二氧化碳转化率达到最高值,分别为64％和39％。以此法制备的合成气的H2／CO摩尔可以在很宽的范围内变化,本研究合成气H2／CO摩尔比的变化范围是0.7-3.1。     

合成气直接制C2含氧化合物Rh基催化剂中金属-助剂(载体)界面的构建

由煤、天然气或生物质经合成气直接制取乙醇等C₂含氧化合物可以替代传统的石油和粮食路线，其意义重大。负载型助剂促进的金属Rh是实现该过程最有效的催化剂，其中Rh-助剂（载体）接触界面是发生目标反应的活性位，其面积的大小直接决定了该催化剂的性能，因此，近些年来人们尝试多种物理或化学方法来改进Rh基催化剂的制备过程，以最大化金属-助剂界面。我们简要介绍和评述了涂覆法、形成复合氧化物或合金、强静电吸附法、控制表面反应法和原子层沉积法等的原理、过程以及优缺点。通过结合上述合成方法，可制备出均一分布的、界面活性位结构确定的催化剂。     

非合成气法烯烃、炔烃氢甲酰化研究进展

烯烃、炔烃的氢甲酰化反应是制备醛及其衍生物的重要反应,传统的过渡金属催化合成气(CO/H_2)合成法,因为价格低廉,工艺成熟,在工业上得到了广泛应用.然而合成气的高毒性、高危性限制了它的实验室研究,因此使用非合成气的氢甲酰化反应吸引了化学家的研究兴趣.采用非一氧化碳(CO)为羰基源的新型氢甲酰化研究发展迅速,我们对该领域近20年的发展进行综述,针对合成气替代物甲醛(HCHO),二氧化碳(CO_2),甲酸(HCOOH),(缩)乙醛酸(HOOCCHO)丁醛以及多元醇等优缺点进行了详细的讨论,并对该领域发展方向予以展望.     

C60的加成反应

富勒烯化学是以全碳分子球烯为母体的新兴有机化学领域, 在材料、医学及立体化学合成方法等方面具有广泛的应用和发展前景。本文综述了C₆₀的加成反应, 较全面地展示了富勒烯的化学性质。     

Effect of textural characteristics on the catalytic performance of supported KCoMoS2 in the synthesis of higher alcohols from syngas

The influence of textural characteristics on the catalytic performance of supported KCoMoS₂ catalysts was explored to provide essential information for the design of better catalysts for the synthesis of higher alcohols (C₁–C₅) from syngas. Syngas conversion was carried out over KCoMoS₂ catalysts supported on various mesoporous (alumina and carbon-coated alumina) and microporous (two types of powdered activated carbons) materials. The experimental results show that catalysts supported over microporous materials exhibit higher catalytic activity in HAS from syngas than catalysts based on mesoporous materials.     

Carbon monoxide and hydrogen (syngas) as a C1-building block for selective catalytic methylation

A catalytic reaction using syngas (CO/H₂) as feedstock for the selective β-methylation of alcohols was developed whereby carbon monoxide acts as a C1 source and hydrogen gas as a reducing agent. The overall transformation occurs through an intricate network of metal-catalyzed and base-mediated reactions. The molecular complex [Mn(CO)₂Br[HN(C₂H₄PⁱPr₂)₂]] 1 comprising earth-abundant manganese acts as the metal component in the catalytic system enabling the generation of formaldehyde from syngas in a synthetically useful reaction. This new syngas conversion opens pathways to install methyl branches at sp³ carbon centers utilizing renewable feedstocks and energy for the synthesis of biologically active compounds, fine chemicals, and advanced biofuels.

A broadly applicable catalytic process for the selective β-methylation of alcohols is presented using syngas (CO/H₂) directly as a C1 building block and the shown manganese complex in the presence of a base as the catalytic system.     

大气压下甲烷火花放电制乙炔和合成气

用大气压下火花放电方法和发射光谱原位诊断技术, 对CH₄直接转化制乙炔和间接转化制合成气进行了研究, 并与介质阻挡放电进行了比较。结果表明, 火花放电具有能量效率高的突出优点, 能够高效地将CH₄活化成C原子、H原子和C₂等活泼物种。当CH₄单独进料时, 能得到以C₂H₂为主的烃类产物。当CH₄与CO₂和O₂共进料时, 能得到H₂/CO比值可调的合成气产物。在用火花放电转化CH₄和CO₂制合成气时, 添加O₂能够避免反应器的结炭问题, 反应温度只需225 ℃, 与常规催化法相比具有明显的低温优势。     

Direct and Highly Selective Conversion of Synthesis Gas into Lower Olefins: Design of a Bifunctional Catalyst Combining Methanol Synthesis and Carbon–Carbon Coupling

The direct synthesis of lower (C₂ to C₄) olefins, key building‐block chemicals, from syngas (H₂ /CO), which can be derived from various nonpetroleum carbon resources, is highly attractive, but the selectivity for lower olefins is low because of the limitation of the Anderson–Schulz–Flory distribution. We report that the coupling of methanol‐synthesis and methanol‐to‐olefins reactions with a bifunctional catalyst can realize the direct conversion of syngas to lower olefins with exceptionally high selectivity. We demonstrate that the choice of two active components and the integration manner of the components are crucial to lower olefin selectivity. The combination of a Zr–Zn binary oxide, which alone shows higher selectivity for methanol and dimethyl ether even at 673 K, and SAPO‐34 with decreased acidity offers around 70 % selectivity for C₂–C₄ olefins at about 10 % CO conversion. The micro‐ to nanoscale proximity of the components favors the lower olefin selectivity.     

Polarity Behaviour and Specific Interactions of Imidazolium‐Based Ionic Liquids in Ethylene Glycol

The molecular interactions of the ionic liquids (ILs) 1‐butyl‐3‐methylimidazolium tetrafluoroborate [C₄mim][BF₄], 3‐methyl‐1‐octylimidazolium tetrafluoroborate [C₈mim][BF₄] and 1‐butyl‐3‐methylimidazolium octylsulfate [C₄mim][C₈OSO₃] are investigated in ethylene glycol (EG) over the whole mole fraction range using fluorescence (steady‐state and time‐resolved), Fourier transform infrared and nuclear magnetic resonance (NMR) spectroscopy. The cybotactic region surrounding the pyrene fluorescent probe exhibits peculiar characteristics for different ILs in the EG‐rich region. The extent of solute–solvent interactions is assessed by determining the deviations of experimentally observed vibronic band intensity ratios of peak 1 to peak 3 of pyrene fluorescence (I₁/I₃) from a composite I₁/I₃ value obtained using a preferential solvation model. A distinct vibrational frequency shift for various stretching modes of EG (O? H) or ILs (C? H of ring protons, B? F and S?O of anions) indicates specific interactional preferences of EG toward the IL protons/anion. Splitting of the O? H vibration band of EG at 3000–3700 cm^?1 into three separate bands, and analysis of the changes in location and area of these bands as a function of concentration enable precise determination of the effect of ILs on hydrogen bridges of EG. NMR chemical shifts and their deviations from ideality show multiple hydrogen‐bonding interactions of varying strengths between unlike molecules in the mixtures. A comparison of spectroscopic results with thermodynamic properties shows that the mixing microscopic behaviour of the investigated systems is completely different from the macroscopic behaviour, which is primarily governed by the difference in shape, size and nature of the molecules.     

Study on the method of chemical trapping for formyl intermediates

The method of chemical trapping for formyl intermediates has been studied, with syngas conversion to ethanol over rhodium-based catalysts as the diagnostic reaction concerned, and CH₃I as the trapping reagent. Two species of acetaldehyde, i.e., CH₃CHO and CH₃CDO, were produced in the trapping reaction following CO + 2D₂ reaction. It was shown that the formation of CH₃CHO in the trapping reaction resulted from dehydrogenation of CH₃ from CH₃I to give H, which induced the formation of CH₃CHO in the presence of CO and CH₃ So there may be two pathways for the formation of CH₃CDO in the trapping reaction: one, methylation of DCO adspecies; the other, deuteration of CH₃ CO formed by CO insertion into CH₃ The catalyst surface was purged with Ar following CO + 2D₂ reaction before the trapping reaction was performed. By means of this modified method of chemical trapping for formyl intermediates, CH₃CDO was found to be mainly derived from the methylation of DCO adspecies. Accordingly, it could be concluded that formyl is a C₁ intermediate in the syngas conversion to ethanol over rhodium-based catalysts.