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1.
在活性炭负载金属钌(Ru/C)催化剂上实现了5-羟甲基糠醛的高效选择氧化.以甲苯为反应溶剂,在383 K和2.0 MPa O2的反应条件下,2,5-呋喃二甲醛(DFF)收率高达95.8%.与活性炭负载的具有相似粒径的Pt,Rh,Pd,Au等其它贵金属催化剂相比,Ru/C具有更加优良的活性和DFF选择性.同时Ru/C催化剂结构稳定,具有良好的重复使用性能.在相似的反应条件下,采用水代替甲苯作为溶剂,同时添加少量水滑石固体碱,可便捷地将主要产物从DFF调变为5-甲酰基-2-呋喃甲酸或2,5-呋喃二甲酸,显示出Ru/C催化剂在控制5-羟甲基糠醛选择氧化反应产物方面的优异性能.  相似文献   

2.
采用高温煅烧法、 原位生长法和光还原法分三步制备出双功能复合光催化剂g-C3N4/CdS/Ni. 材料中CdS的引入可以增强光生电子和空穴的分离效率, Ni可以进一步提高光致产氢速率. 在以三乙醇胺(TEOA)为电子给体的水溶液中对所制备的材料进行了催化产氢性能测试, 并对材料中CdS的含量进行了优化. 结果表明, 25% (质量分数)CdS负载量的复合材料催化产氢性能最佳, 其催化产氢速率为4134.5 μmol·g-1·h-1, 是 g-C3N4/Ni催化产氢速率的115倍. 且Ni是一种良好的质子催化剂. 在此基础上, 以5-羟甲基糠醛(HMF)替代TEOA作为体系的电子给体, 其可以被选择性地催化氧化为增值化学品2, 5-二甲酰基呋喃(DFF). 当体系中HMF的转化率为82.3%, DFF的选择性为69.4%时, DFF的产率(57.2%)达到最高, 体系中H2的产量为 51.8 μmol/g. g-C3N4/CdS/Ni复合材料可以在同一体系中进行催化光致产氢和HMF的选择性氧化.  相似文献   

3.
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.  相似文献   

4.
本研究将铁、锰、铜和金刚烷胺缩水杨醛衍生的席夫碱配体组成的原位催化剂用于催化5-羟甲基糠醛(5-Hydroxymethylfurfural,简称HMF)选择性氧化制备5-甲酰基呋喃-2-羧酸(5-formyl-2-furancarboxylic acid,简称FFCA)。通过核磁共振(NMR)、红外(FT-IR)和单晶衍射对配体和配合物进行了表征,并对氧化反应时间、反应温度、MnCl2·4H2O与配体物质的量比、氧化剂和催化剂用量等反应条件进行优化,在最优化条件下,HMF转化率为100%,并且可以获得收率为52.1%的FFCA。根据反应结果对Mn金属配合物催化的HMF氧化反应过程进行了分析。  相似文献   

5.
2, 5-呋喃二甲酸二甲酯(DMFDCA)这一生物质衍生的增值化学品是石油基聚合物单体对苯二甲酸(TPA)的理想替代品。本研究采用一步共热解法合成了两种廉价金属修饰的氮掺杂多孔碳催化剂CoMn@NC,并将其用于5-羟甲基糠醛(HMF)在温和条件下的需氧氧化。由Co3Mn2@NC-800催化HMF在50 ℃和常压氧气的条件下反应12 h后,得到产率为85%的DMFDCA。多孔催化剂的高比表面积提高了传质效率。Co纳米粒子(NPs)和呈原子级分散的Mn与掺杂在碳中的氮配位形成M―Nx。富含吡啶氮的碳基体中的缺电子金属位点有利于HMF和氧的活化。氧形成的超氧自由基阴离子的存在确保了半缩醛中间体和5-(羟基甲基)-2-糠酸甲酯(HMMF)的羟甲基的脱氢氧化,从而高选择性得到DMFDCA。该催化剂性能稳定,可适用于各种取代芳醇。该催化体系具有用于生产聚合物单体羧基酯的应用潜力。  相似文献   

6.
Dimethyl furan-2, 5-dicarboxylate (DMFDCA) is a valuable biomass-derived chemical that is an ideal alternative to fossil-derived terephthalic acid as a monomer for polymers. The one-step oxidation of 5-hydroxymethylfurfural (HMF) to DMFDCA is of practical significance. It not only shortens the reaction pathway but also avoids the separation process of intermediates; thus, reducing cost. In this work, non-noble bimetallic catalysts supported on N-doped porous carbon (CoMn@NC) were synthesized via a one-step co-pyrolysis procedure using different pyrolysis temperatures and proportions of metal precursors and additives. We employed the prepared CoMn@NC catalysts in the aerobic oxidation of HMF under mild reaction conditions to obtain DMFDCA. High-yield DMFDCA was obtained by screening the prepared catalysts and optimizing the reaction conditions, including the strength and amount of the base, as well as the reaction temperature. The optimized yield of DMFDCA was 85% over the Co3Mn2@NC-800 catalyst after 12 h at 50 ℃ using ambient-pressure oxygen. The physicochemical properties of the catalysts were determined using a variety of characterization techniques, the factors affecting the performance of each catalyst were investigated, and the relationship between the physicochemical properties and performance of the prepared catalysts was elucidated. A porous structure with a high surface area had a positive effect on mass transfer efficiency. Cobalt nanoparticles (NPs) and atomically dispersed Mn were coordinated to N-doped carbon to form M―Nx (where M = Co or Mn). Based on the Mott-Schottky effect, there was significant electron transfer between each metal and the N-doped carbon, additionally, the metal NPs supplied electrons to the carbon atoms. The electron-deficient metal site in the pyridinic N-rich carbon was beneficial for the activation of HMF and oxygen. The activation of oxygen produced reactive oxygen species (such as superoxide radical anions) to ensure high selectivity to DMFDCA through dehydrogenative oxidation of the hemiacetal intermediate and hydroxymethyl group of 5-hydroxymethyl-2-methyl-furoate. The existence of disordered and defective carbons increased the number of active sites. Subsequently, we performed a series of control experiments. Based on our current experimental results and previous studies, we propose a simple mechanism for the aerobic oxidation of HMF to DMFDCA. The catalyst was stable, its performance decreased slightly after two cycles, and it was tolerant to SCN ions and resistant against N or S poisoning. Furthermore, the use of this catalytic system can be expanded to various substituted aromatic alcohols, such as benzyl alcohols with different substituents, furfuryl alcohol, and heterocyclic alcohols. Simultaneously, the product type was further extended from methyl esters to ethyl esters with a high yield when the substrate reacted with ethanol. In conclusion, this catalytic system can be applied in the production of carboxylic esters for polymers.  相似文献   

7.
以不同晶型的MnO2为催化剂进行5-羟甲基糠醛(HMF)氧化反应,并将催化活性较高的α-MnO2与Fe3O4复合制备磁性MnO2-Fe3O4复合氧化物,采用X射线衍射(XRD)、扫描电镜(SEM)、X射线光电子能谱(XPS)、NH3/CO2程序升温脱附(NH3/CO2-TPD)及吡啶吸附红外光谱(Py-FTIR)对催化...  相似文献   

8.
5-羟甲基糠醛(HMF)是一种具有重要应用价值的原材料和中间体,以果糖脱水合成HMF具有实现生物质转化利用的重大意义。本文综述了近三年来果糖制备HMF过程的两大关键因素:催化剂和反应介质的重要进展。固体酸(特别是杂多酸及其盐)、离子液体(ILs)中添加卤化物或ILs作为催化剂是近几年来研究的热点,固体酸的优点是可多次重复使用且易于分离,而ILs中果糖的降解条件较温和,副反应较少。目前,用于果糖转化HMF的反应溶剂优、缺点并存。最后对该反应存在的问题和今后的研究进行了总结和展望。  相似文献   

9.
5-羟甲基糠醛(HMF)是一种具有重要应用价值的原材料和中间体,以果糖脱水合成HMF具有实现生物质转化利用的重大意义。本文综述了近三年来果糖制备HMF过程的两大关键因素:催化剂和反应介质的重要进展。固体酸(特别是杂多酸及其盐)、离子液体(ILs)中添加卤化物或ILs作为催化剂是近几年来研究的热点,固体酸的优点是可多次重复使用且易于分离,而ILs中果糖的降解条件较温和,副反应较少。目前,用于果糖转化HMF的反应溶剂优、缺点并存。最后对该反应存在的问题和今后的研究进行了总结和展望。  相似文献   

10.
离子液体催化制备5-羟甲基糠醛的研究进展   总被引:1,自引:0,他引:1  
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。  相似文献   

11.
An eco-friendly and economical route for the oxidation 5-hydroxymethylfurfural (HMF) to 2,5-furandicarboxylic acid (FDCA) with atmospheric dioxygen as the sole oxidant under acid-, base-, metal-and external initiator-free conditions in minimal solvent was reported.  相似文献   

12.
《中国化学快报》2019,30(12):2304-2308
An eco-friendly and economical route for the oxidation of 5-hydroxymethylfurfural (HMF) to 2,5-furandicarboxylic acid (FDCA) with atmospheric dioxygen as the sole oxidant under acid-, base-, metal-, and external initiator-free conditions in minimal solvent was reported. In the present reaction, the 1,2-diethoxyethylane has a dual role: reaction medium and free-radical initiator. The FDCA easily crystallizes during the reaction and was simple purified via recrystallization to provide the pure FDCA.  相似文献   

13.
2,5-Furandicarboxylic(FDCA) is a potential substitute for petroleum-derived terephthalic acid, and aerobic oxidation of5-hydroxymethylfurfural(HMF) provides an efficient route to synthesis of FDCA. On an activated carbon supported ruthenium(Ru/C) catalyst(with 5 wt% Ru loading), HMF was readily oxidized to FDCA in a high yield of 97.3% at 383 K and 1.0 MPa O_2 in the presence of Mg(OH)_2 as base additive. Ru/C was superior to Pt/C and Pd/C and also other supported Ru catalysts with similar sizes of metal nanoparticles(1–2 nm). The Ru/C catalysts were stable and recyclable, and their efficiency in the formation of FDCA increased with Ru loadings examined in the range of 0.5 wt%–5.0 wt%. Based on the kinetic studies including the effects of reaction time, reaction temperature, O_2 pressure, on the oxidation of HMF to FDCA on Ru/C, it was confirmed that the oxidation of HMF to FDCA proceeds involving the primary oxidation of HMF to 2,5-diformylfuran(DFF) intermediate, and its sequential oxidation to 5-formyl-2-furancarboxylic acid(FFCA) and ultimately to FDCA, in which the oxidation of FFCA to FDCA is the rate-determining step and dictates the overall formation rate of FDCA. This study provides directions towards efficient synthesis of FDCA from HMF, for example, by designing novel catalysts more efficient for the involved oxidation step of FFCA to FDCA.  相似文献   

14.
A heterogeneous catalyst was prepared by immobilizing Zirconyl Schiff base complex on the modified MCM-41 and used in the conversion of fructose to HMF. A higher HMF yield was obtained when fructose as raw material under optimal reaction conditions.  相似文献   

15.
田涛  刘英  张勋高 《催化学报》2015,(8):1358-1364
采用均匀沉积-沉淀法制备了氧化铜修饰羟基磷灰石负载金催化剂(Au/CuO-HAP),并用原子吸收光谱、N2吸附脱附、X射线粉末衍射、透射电镜和X射线光电子能谱等方法对催化剂结构和形貌进行了表征.考察了催化剂对醇类液相需氧氧化的催化性能.与单金属Au/HAP或CuO-HAP相比较,双金属Au/CuO-HAP对苯甲醇氧化的催化活性和苯甲醛的选择性有显著提高,120 oC反应1.5 h,苯甲醇的转化率和苯甲醛的选择性分别达到99.7%和98.4%.在Au/CuO-HAP的催化下,其它类型的芳香醇均可高选择性转化为相应的醛或酮. Au/CuO-HAP催化剂有很好的稳定性和可回收性,4次回收后,其催化活性没有明显变化.  相似文献   

16.
Ternary Pt–Te–Ru catalysts with different atomic ratios were synthesized by reducing the precursor with formic acid. The physical and electrochemical characterization of the Pt3TeRu0.25/C catalyst was performed by transmission electron microscopy (TEM), X-ray diffraction, energy-dispersive X-ray spectroscopy equipped with TEM (TEM-EDX), X-ray photoelectron spectrometer, ethanol oxidation, and CO stripping. In TEM images, the Pt3TeRu0.25/C nanoparticles with an average particle size of around 2.9 nm were well dispersed on the carbon support. The Pt3TeRu0.25/C catalyst was superior to the Pt3Te/C catalyst in respect of catalytic activity, durability, and CO tolerance. The positive effect of the Ru presence in the Pt3TeRu0.25/C catalyst was ascribed to the interactions of Ru or Ru oxides.  相似文献   

17.
徐峥  胡志勇  翟丽军  牛宇岚 《化学研究》2007,18(2):35-37,43
利用等体积浸渍法制备了V2O5/C催化剂,并应用于乙二醛的液相氧化反应,采用XRD、TEM手段对催化剂进行了物化性质表征.结果表明,V2O5/C对乙二醛的氧化表现出较高的催化活性和乙醛酸选择性,反应10h,乙二醛的转化率达29.2%,乙醛酸得率13.6%.与贵金属Pd-Bi/C催化剂相比,V2O5/C催化剂的稳定性和重复使用效果都比较好.  相似文献   

18.
Sulfonic acid-functionalized heterogeneous catalysts have been evaluated in the catalytic dehydration of C(,monosaccharides into 5-hydroxymethylfurfural(HMF) using dimethyl sulfoxide(DMSO)as solvent.Sulfonic commercial resin Amberlyst-70 was the most active catalyst,which was ascribed to its higher concentration of sulfonic acid sites as compared with the other catalysts,and it gave 93 mol%yield of HMF from fructose in 1 h.With glucose as the starting material,which is a much more difficult reaction,the reaction conditions(time,temperature,and catalyst loading) were optimized for Amberlyst-70 by a response surface methodology,which gave a maximum HMF yield of 33 mol%at 147 °C with 23 wt%catalyst loading based on glucose and 24 h reaction time.DMSO promotes the dehydration of glucose into anhydroglucose,which acts as a reservoir of the substrate to facilitate the production of HMF by reducing side reactions.Catalyst reuse without a regeneration treatment showed a gradual but not very significant decay in catalytic activity.  相似文献   

19.
邵方君  姚子豪  高怡静  周强  包志康  庄桂林  钟兴  伍川  魏中哲  王建国 《催化学报》2021,42(7):1185-1194,中插50-中插65
饱和及不饱和N-杂环化合物是非常重要的药物中间体.由于它们在催化剂表面的吸附/脱附能力不同,设计具有合适电子结构和几何结构的催化剂用于饱和与不饱和N-杂环化合物的可逆转化具有很大挑战性.目前,负载型纳米金属催化剂通常被用于饱和N-杂环化合物的加氢反应或者不饱和杂环化合物的脱氢反应.然而反应过程中N-杂环化合物与纳米金属的强配位作用,不仅影响其他反应底物与活性位点的接触,而且导致催化剂的循环稳定性较差.在之前的研究中,钌(Ru)催化剂被用于喹啉化合物的选择加氢反应,但反应条件苛刻,循环稳定性差,不能实现杂环化合物的可逆转化.本文在Ru纳米颗粒的晶格中引入杂原子,诱导催化剂表现出不同的几何结构和电子性质,从而调节反应势垒和底物在催化剂表面的脱附能力以优化反应性能.本文以活性炭(AC)为载体,制备了Ru2P,RuO2,RuS2和Ru四种负载型催化剂,以喹啉和四氢喹啉为模型反应物,考察其催化性能.研究发现,Ru2P/AC可在温和条件下同时实现喹啉的加氢反应和四氢喹啉的无受体脱氢反应,且催化剂经过8次循环使用后,其转化率仍高达95%,选择性达到99%,远优于Ru/AC.密度泛函理论计算结果表明,Ru2P中的P原子使得两个相邻的Ru-Ru原子的间距从2.61?增加到2.9?.同时P对催化剂几何结构的变化使反应底物在催化剂表面的吸附行为发生改变,即喹啉和四氢喹啉分子都更容易在Ru2P的表面发生脱附,从而有利于反应进行.通过差分电荷分析,P原子掺杂会将Ru从零价状态调整为缺电子状态.随着P原子掺杂到Ru金属中,反应物表面的电荷大幅度下降,提高了加氢反应和脱氢反应中产物的扩散能力.进一步计算反应路径结果表明,Ru2P实现了N-杂环化合物可逆加氢/脱氢过程中反应与扩散之间的平衡,从而在加氢和脱氢反应中均表现出优异的催化性能.通过浸渍、热解制备的Ru2P/AC对一系列N-杂环化合物的加氢和脱氢反应均表现出优异的催化性能.这主要归因于P原子的掺入稀释了Ru-Ru团簇,引起的几何效应和电子效应的协同作用实现了N-杂环化合物加氢/脱氢过程反应与扩散的平衡,从而提高了可逆反应的催化性能.本文通过原子掺杂调控催化活性的本征结构,从而优化出具有平衡反应和产物扩散的优异催化剂.该合成策略具有直接通用的特点,易于拓展到其它复杂的反应体系当中.  相似文献   

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