离子液体中Lewis酸催化葡萄糖和果糖脱水制备5-羟甲基呋喃甲醛

在离子液体中采用不同的Lewis酸催化葡萄糖和果糖脱水制备5-羟甲基呋喃甲醛(5-HMF).结果表明,CrCln和SnCln均可高效催化葡萄糖转化为5-HMF.另外,Lewis酸的酸性越强,其催化果糖转化为5-HMF的产率越高.镧系金属氯化物在反应中表现出较好的催化活性和产物选择性.同时还研究了离子液体结构对催化反应的...     

生物质糖类催化制备液体燃料2,5-二甲基呋喃（英文）

在化石燃料储量不断减少,温室效益趋势加重的情况下,寻求可以替代化石燃料的可再生燃料已经引起了人们的广泛关注.人们普遍认为源于生物质的2,5-二甲基呋喃(DMF)是很有前景的一种可再生液体交通燃料,为此本文作者对近年来生物质制备DMF的方法及途径进行了综述,同时对今后的研究作了展望.     

果糖一步转化制备呋喃基燃料:溶剂效应及离子液体修饰活性金属对产物选择性的决定作用（英文）

在众多生物基化合物中,2,5-二甲基呋喃(DMF)是一种有实用前景的可再生液体生物质燃料,也是一种具有重要价值的化学品,可作为生产对苯二甲酸的原料.2,5-二甲基四氢呋喃(DMTF)是DMF进一步加氢产物,该化合物比DMF更稳定,适合长期保存;由于具有更高的氢碳比,用作生物燃料燃烧时能够释放更多能量.研究生物质资源制备DMF和DMTF对可再生资源制备液体燃料和化学品具有重要意义.从生物质多糖出发制备这两类化合物,中间经历了水解、脱水、加氢、加氢脱氧等多个反应步骤,每一步反应都十分复杂,包含许多副反应途径.此外,由于每一步反应条件的不兼容性,大多数研究集中在分步反应阶段,鲜有文献能够实现从碳水化合物原料直接转化为DMF和DMTF.发展由生物质一锅法多步耦合转化技术制备化学品和燃料,不仅具有科学意义,而且可大大简化反应过程,避免中间产物分离和损失,节省资源和时间,历来受到化学家和工业界的关注.本文利用离子液体对Ru/C催化剂电子性质的修饰作用以及溶剂效应的影响,设计了离子液体/THF双相体系中果糖直接催化转化制备2,5-二甲基呋喃(DMF)和2,5-二甲基四氢呋喃(DMTF)的新路线.该转化过程耦合了果糖脱水制HMF、HMF加氢及加氢脱氧生成DMF和DMTF等多步反应.通常在HMF加氢转化过程中,Ru/C催化剂的高活性易导致HMF深度加氢生成大量开环产物及气体,我们借助离子液体与有机溶剂的不同溶解性,筛选出[BMIm]Cl/THF双相溶剂体系,使极性HMF在离子液体层反应,生成弱极性的DMF和DMTF能及时被THF萃取出来,有效稳定了目标产物.其次,果糖转化为HMF会产生少量水,通常水的存在易导致HMF发生水合等副反应,对下一步的加氢转化是不利因素;然而在本催化体系中,由于[BMIm]Cl能与水以较强的氢键结合形成水合物,对水分子起到了束缚作用,减少了HMF发生水解、水合等副反应的机会.另一方面,离子液体粘度较大,微量水的存在能降低离子液体层粘度,改善传质,从而提高反应速率.在HMF加氢处理过程中,离子液体对DMF和DMTF的生成起了决定作用.当反应体系中不添加离子液体,以THF为溶剂,反应结束后未检测到DMF生成,DMTF的收率仅为2%,但HMF已经完全转化.取气体样品进行GC分析,发现有部分气相产物生成,包括CO2、CH4和C2H6等.液体混合物进行GC-MS检测,发现产物主要包括DHMTF、5-甲基四氢糠醇(MTFA)、四氢糠醇(TFA)、1,2-戊二醇、DMTF、2-己醇和少量戊醇,产物中所有呋喃环结构的双键都发生加氢反应.以上结果表明,没有离子液体的THF中,Ru/C催化的HMF涉氢反应平衡已发生改变.当反应体系中添加0.2 g离子液体[BMIm]Cl进行HMF的加氢时,此时开始有DMF生成,随着[BMIm]Cl量依次增加,DMF以及DMTF的收率也呈上升趋势.1.0 g离子液体获得两种产物最高收率为68%.然而,如果进一步增加[BMIm]Cl的量到2.0 g,呋喃基液体燃料DMF和DMTF的收率却开始下降.综合以上实验结果,我们认为适量的[BMIm]Cl存在有可能会对催化剂物理化学性质造成影响,从而对产物的选择性起了决定性作用.通过对催化剂进行元素分析、XPS、H2-TPR表征以及一系列对比实验证明,离子液体不仅促进果糖脱水转化为HMF,同时在HMF选择性加氢反应中可修饰活性金属电子性质,改变催化路径,是多步串联反应能够耦合的关键因素.在[BMIm]Cl/THF双相溶剂体系中,离子液体的"溶剂笼效应"促进DMF和DMTF高效生成,THF的萃取功能对目标产物的稳定起了关键作用.以上对催化剂和溶剂的合理设计共同促进高产率呋喃基燃料的获得.该研究实现由六碳糖直接选择转化获取DMF和DMTF,为生物质高效催化转化制备生物基能源化学品提供了新思路.     

离子液体催化制备5-羟甲基糠醛的研究进展

本文综述了离子液体催化制备5-羟甲基糠醛的研究进展。运用离子液体作为反应溶剂和催化剂,与常规合成HMF的方法相比,其反应在常压、低温下进行,更易于操作控制;副反应数量明显减少,HMF的产率稳定,可达90%;离子液体催化活性稳定,可重复利用,减少了有机溶剂的使用量;利用离子液体作为媒介,能将反应原料从单一的果糖扩展到葡萄糖和纤维素等廉价原料,降低了生产成本。由此可见,运用离子液体催化制备HMF将是今后研究的重点和发展的必然趋势。     

离子液体中树脂催化转化果糖为5-羟甲基糠醛

开发了以离子液体1-丁基-3-甲基咪唑氯盐([BMIM]Cl)为溶剂, 固体酸离子交换树脂NKC-9为催化剂转化果糖为5-羟甲基糠醛的绿色工艺. 在此催化体系中, 100 ℃下反应10 min时5-HMF的产率达到78.0%, 其反应时间远远小于已有文献报道的长达数小时的反应时间. 在此催化体系中, 果糖起始浓度的增加对5-HMF产率影响不大, 因而此工艺同样适用于处理高浓度的果糖溶液. 离子液体[BMIM]Cl和树脂组成的催化体系可以循环使用, 经过9次重复使用后仍能保持稳定的催化活性.     

CdS基纳米管光催化氧化5-羟甲基糠醛选择性生成2,5-呋喃二甲醛

将生物质转化为高附加值化学品以替代传统化石能源衍生的碳资源不可再生能源已经引起了人们的广泛关注. 本工作制备了内部中空的ZnS@CdS/Ni纳米管催化剂用于光催化氧化5-羟甲基糠醛(HMF). 通过X射线光电子能谱表征了催化剂内部存在ZnS缺陷态使得ZnS能带带隙降低. 光照条件下, 光生空穴能够从CdS迁移至ZnS缺陷态, 抑制了ZnS@CdS内部的载流子复合, 提高了光催化性能. 中空的纳米管表面负载Ni催化剂可以参与质子还原产氢的反应, 而ZnS@CdS内部产生的空穴可以催化氧化HMF选择性生成2,5-呋喃二甲醛(DFF). 光反应1 h后, HMF的转化率达到36%, 产物DFF选择性为99%, 并且催化剂可以重复利用三次而不降低催化效果.     

助溶剂在离子液体催化制备5-羟甲基糠醛中的应用

本文研究了不同助溶剂对酸性离子液体催化制备5-羟甲基糠醛的(HMF)的影响.以果糖为反应原料,二甲基亚砜(DMSO)、二甲基乙酰胺(DMA)、二甲基甲酰胺(DMF)以及乙二醇(EG)四种不同的有机溶剂作为助溶剂,运用酸性离子液体催化制备5-羟甲基糠醛.结果表明:以DMSO作为反应助溶剂,38.5wt%的果糖反应液在催化...     

生物质转化为液体燃料2,5-二甲基呋喃 的途径与机理

随着化石燃料的日益减少,寻找可再生的液体生物质燃料已经引起了越来越广泛的关注。由生物质制备得到的2,5-二甲基呋喃(DMF)具有高能量密度、高沸点、高辛烷值和不溶于水等优点,近年来被认为是一种非常有前景的液体燃料。本文归纳和总结了生物质转化为DMF的化学途径、方法和反应机理以及DMF的燃烧性能,并对今后的研究方向进行了展望。     

酸性离子液体降解纤维素制备5-羟甲基糠醛的研究

以离子液体氯化1-烯丙基-3-甲基咪唑鎓([Amim]Cl)为溶剂,以咪唑类酸功能离子液体[Cnmim]HSO4(n=2,4,6,8)和Cr Cl3·6H2O为复合催化剂,在微波辅助加热条件下降解纤维素制备5-羟甲基糠醛(5-HMF),考察了催化剂加入量、反应温度、催化剂种类、反应时间、加水量等反应条件对纤维素降解反应的影响。结果表明,当[C2mim]HSO4的加入量为0.02g、微晶纤维素(MCC)和Cr Cl3·6H2O的摩尔比为10∶1、反应温度为160℃、反应时间为30min、加水量为50μL时,微晶纤维素转化率为100%,总还原糖收率为87.2%,5-HMF产率最高可达到50%。     

离子液体中磺化无定形炭催化菊糖制备5-羟甲基糠醛

研究了以1-丁基-3-甲基咪唑氯盐([Bmim]Cl)离子液体作溶剂,磺化无定形炭为催化剂催化菊糖脱水制5-羟甲基糠醛(HMF)的反应.考察了溶剂、水量、反应温度、反应时间和催化剂用量对HMF收率的影响.实验结果表明,反应温度为100°C,反应时间60min,R=5(R为水的物质的量与菊糖中所含果糖单位的物质的量的比值),m(催化剂):m(菊糖)=1:3时,HMF的收率可达50%.     

Asymmetric hydrogenation of methyl α-benzamido cinnamate in ionic liquid solvent

The room temperature ionic liquid EMIMOTf was employed as the sole reaction solvent for the asymmetric hydrogenation of methyl α-benzamido cinnamate. Under conditions of 60 psi hydrogen and 50 °C for 24 h, near quantitative conversions were observed using both the achiral DiPFc-Rh catalyst, and the chiral EtDuPHOS-Rh catalysts. Enantiomeric excess of 89% ee was observed for hydrogenations carried out with the chiral catalyst.     

Aqueous biphasic systems composed of ionic liquid and fructose

Liquid–liquid equilibria data of the [Bmim]BF₄ + fructose + water system were determined at 298.15, 308.15, 31815 K. It was found that the liquid–liquid equilibria can be formed over a wide component range and the effect of the temperature on the phase equilibria is obvious within the fructose concentration changing from 3 to 40%. The binodal curves were correlated using a five-parameter equation, and the tie lines were fitted the Othmer–Tobias and Bancroft correlations. Correlation coefficients for the equations exceeded 0.99.     

Influence of ionic liquid content on properties of dense polymer membranes

Pervaporation was used for removal of butan-1-ol from its 5 wt.% of aqueous solution, at which the concentration of Clostridium acetobutylicum starts to decrease. The polydimethylsiloxane (PDMS) membrane containing 0, 10, 20 or 30 wt.% of benzyl-3-butylimidazolium tetrafluoroborate ([BBIM][BF₄]) ionic liquid was used. Differential scanning calorimetry measurements showed that PDMS-[BBIM][BF₄] membranes (though optically homogeneous) contained PDMS and [BBIM][BF₄] phases. Pervaporation selectivity increased and total flux through membranes raised moderately with an increased content of [BBIM][BF₄] in PDMS-[BBIM][BF₄] membranes. Hence, immobilization of a proper ionic liquid in a membrane results in the creation of pervaporation membranes, effective in the removal of alcohol from fermentation broths.     

Analysis by desorption of volatile impurities from an ionic liquid solution in an unmodified gas chromatograph inlet

A procedure for using ionic liquids to determine volatile impurities in compounds or matrices that are soluble in an ionic liquid is described. Using a conventional autosampler a droplet of ionic liquid solution is suspended in the inlet of the gas chromatograph and analytes are desorbed onto a GC column using splitless injection conditions. Results are presented for 1,2-propanediol, nonane, N,N-dimethylacetamide, and mesitylene in two different compounds in the ionic liquids trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide and trihexyltetradecylphosphonium dicyanamide.     

The first one-pot oxidative 1,2-acetoxysulfenylation and 1,2-disulfenylation of Baylis-Hillman alcohols in an ionic liquid

The first example of tandem oxidation and 1,2-acetoxysulfenylation/1,2-disulfenylation of Baylis-Hillman (BH) alcohols to afford 1,2-acetoxysulfides/1,2-dithioethers is reported. The reaction involves oxidation of BH alcohols with IBX in [bmim]Br to give β-ketomethylene compounds in situ followed by CuI-imidazole-catalyzed 1,2-acetoxysulfenylation with an organodisulfide and acetic acid under air to afford vicinal acetoxysulfides in excellent yields with complete regioselectivity. In the absence of the Cu(I) catalyst, 1,2-disulfenylation takes place to give vicinal dithioethers in 81-90% yields.     

Beneficial effect of water as second solvent in ionic liquid biphasic catalytic hydrogenations

When reactions take place in ionic liquids, a solvent is normally used to extract the products after reaction. It is reported here how the presence of the solvent during the reaction already can seriously improve the catalytic performance. Above all, employing water as the added solvent enhanced the catalytic activities significantly, ascribed to the creation of a well mixed ‘emulsion-like’ system. The reductions of methyl 2-acetamidoacrylate with Rh-EtDuPHOS and of 2-cyclohexen-1-one with Wilkinson’s catalyst in bmimPF₆ were thus successfully performed in the presence of water. The complexes were easily recycled and Rh-EtDuPHOS was even no longer air sensitive.     

Controllable synthesis of composites of ZSM-5 and KIT-1 using an ionic liquid as template

ZSM-5/KIT-1 composites were synthesized using an ionic liquid as a template. The structures and morphologies of as-obtained products were characterized using an infrared spectroscopy, X-ray diffractometer, N₂ adsorption/desorption, scanning electron microscopy and transmission electron microscopy. The resultant zeolites show a fully crystalline microporous MFI zeolite framework and a three-dimensional network of short worm-like channels. Mesopores and microspores of 4.2 and 0.8 nm in diameter coexist in the zeolite composites. Moreover, the ratio of ZSM-5 and KIT-1 could be simply adjusted by controlling the pre-crystalline time. We believe that the strategy for fabricating ZSM-5/KIT-1 through a simple method could potentially promote the large-scale production of zeolite composites.     

An imidazolium tosylate salt as efficient and recyclable catalyst for acetylation in an ionic liquid

A novel non-metallic salt, 1-butyl-3-methylimidazolium tosylate ([bmim][OTs]) dissolved in the ambient temperature ionic liquid of 1-butyl-3-methylimidazolium tetrafluoroborate ([bmim][BF₄]), was found to be the efficient catalyst for acetylation with the advantages of good recyclability, avoidance of metal contamination, mild reaction conditions, and wide availability for substrates (alcohols, phenols, and amines), could completely replace organic bases, metal Lewis acids, or metallic triflates to fulfill acetylation by a nucleophilic catalytic mechanism, which was supported by ¹³C NMR analysis. Correspondence: Ye Liu, Shanghai Key Laboratory of Green Chemistry and Chemical Processes, Chemistry Department of East China Normal University, Shanghai 200062, China.