利用空间位阻和氢溢流协同作用促进5-羟甲基糠醛选择性加氢制备5-甲基糠醛

化学工业生产中，用氢气为还原剂，通过选择性加氢可以制备多种重要化学品。5-羟甲基糠醛是重要的生物质基平台化合物，而5-甲基糠醛是用途广泛的化学品。由5-羟甲基糠醛加氢得到5-甲基糠醛是一条非常理想的路径，但是选择性活化C-OH非常困难。本文设计并制备了Pt@PVP/Nb₂O₅(PVP: 聚乙烯吡咯烷酮)催化剂，该催化体系巧妙地结合了位阻效应、氢溢流和催化剂界面的电子效应，系统研究了该催化剂对5-羟甲基糠醛选择性加氢制备5-甲基糠醛催化性能，在最优条件下，5-甲基糠醛的选择性可达92%。利用密度泛函理论计算研究了5-羟甲基糠醛选择性加氢制备5-甲基糠醛反应路径。     

利用空间位阻和氢溢流协同作用促进5-羟甲基糠醛选择性加氢制备5-甲基糠醛

Selective hydrogenation is a vital class of reaction. Various unsaturated functional groups in organic compounds, such as aromatic rings, alkynyl (C≡C), carbonyl (C＝O), nitro (-NO₂), and alkenyl (C＝C) groups, are typical targets in selective hydrogenation. Therefore, selectivity is a key indicator of the efficiency of a designed hydrogenation reaction. 5-(Hydroxymethyl)furfural (HMF) is an important platform compound in the context of biomass conversion, and recently, the hydrogenation of HMF to produce fuels and other valuable chemicals has received significant attention. Controlling the selectivity of HMF hydrogenation is paramount because of the different reducible functional groups (C＝O, C-OH, and C＝C) in HMF. Moreover, the exploration of new routes for hydrogenating HMF to valuable chemicals is becoming attractive. 5-Methylfurfural (MF) is also an important organic compound; thus, the selective hydrogenation of HMF to MF is an essential synthetic route. However, this reaction has challenging thermodynamic and kinetic aspects, making it difficult to realize. Herein, we propose a strategy to design a highly efficient catalytic system for selective hydrogenation by exploiting the synergy between steric hindrance and hydrogen spillover. The design and preparation of the Pt@PVP/Nb₂O₅ catalyst (PVP = polyvinyl pyrrolidone; Nb₂O₅ = niobium(V) oxide) were also conducted. Surprisingly, HMF could be converted to MF with 92% selectivity at 100% HMF conversion. The reaction pathway was revealed through the combination of control experiments and density functional theory calculations. Although PVP blocked HMF from accessing the surface of Pt, hydrogen (H₂) could be activated on the surface of Pt due to its small molecular size, and the activated H₂ could migrate to the surface of Nb₂O₅ through a phenomenon called H₂ spillover. The Lewis acidic surface of Nb₂O₅ could not adsorb the C＝O group but could adsorb and activate the C-OH group of HMF; therefore, when HMF was adsorbed on Nb₂O₅, the C-OH groups were hydrogenated by the spilled over H₂ to form MF. The high selectivity of this reaction was realized because of the unique combination of steric effects, hydrogen spillover, and tuning of the electronic states of the Pt and Nb₂O₅ surfaces. This new route for producing MF has great potential for practical application owing to its discovered advantages. We believe that this novel strategy can be used to design catalysts for other selective hydrogenation reactions. Furthermore, this study demonstrates a significant breakthrough in selective hydrogenation, which will be of interest to researchers working on the utilization of biomass, organic synthesis, catalysis, and other related fields.      

CoMn@NC催化5-羟甲基糠醛常压氧化为2, 5-呋喃二甲酸二甲酯

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―N_x (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.     

糠醛渣对气化煤灰熔融特性影响的研究

本研究选择一种典型糠醛渣和两种硅铝比(Si/Al)不同的气化煤,考察配入糠醛渣对两种气化煤灰熔融温度的影响,利用X射线衍射仪(XRD)分析了不同温度下灰渣的矿物质变化规律,采用热力学计算软件FactSage计算了平衡状态下的物相变化。研究结果表明,随着糠醛渣配比的增加,两种气化煤灰的熔融温度均呈现先增加后降低的趋势,其中,高硅铝比的气化煤灰增加趋势更显著。配入糠醛渣后气化灰渣难熔相由钙长石(CaAl₂Si₂O₈)变为白榴石(KAlSi₂O₆),白榴石(KAlSi₂O₆)在1300℃仍以固相形式存在,导致灰熔融温度升高。硅铝比高的气化煤灰的SiO₂相对含量高,其与糠醛渣中的K₂O反应生成更多高熔点的白榴石(KAlSi₂O₆),导致其熔融温度升高趋势更显著。随着糠醛渣配比的继续增加,共气化灰渣中K₂O含量增加,灰渣中形成低熔点的钾...     

非贵金属催化剂在羟甲基糠醛电氧化增值中的应用

羟甲基糠醛是呋喃类化合物,具有价格低廉及来源广泛的优点,可作为平台化合物用于制备其它高附加值产品.传统的热催化氧化增值方法需要高温、高压及贵金属催化剂,造成经济效益的下降.而电氧化方法不需要高温、高压条件;同时,通过对电催化剂的合理设计,非贵金属催化剂表面的羟甲基糠醛选择性转化已经得以实现,从而避免使用大量贵金属.因此,通过电氧化方法对羟甲基糠醛平台化合物进行高附加值转化受到了广泛关注.在羟甲基糠醛氧化的多种产物中,羟基和醛基被全部氧化为羧基的产物——2,5-呋喃二甲酸,被美国能源部列为“最具有价值的12种生物质衍生化学品”之一.鉴于此,本文介绍了羟甲基糠醛电氧化增值生产2,5-呋喃二甲酸的重要研究价值及相关非贵金属电催化剂的最新进展,并对催化羟甲基糠醛电氧化反应的非贵金属催化剂的发展前景进行了展望.     

脱水Ni-Fe类水滑石的制备及其作为环保型催化剂用于生物质糠醛的高选择性缩醛化反应

合成了含硝酸根离子的脱水Ni-Fe类水滑石（Ni-Fe HTLCs）并将其应用于室温下的糠醛缩醛化反应。脱水Ni-Fe HTLCs对糠醛缩醛化反应显示出高选择性并基本实现糠醛的完全转化。作为耐水的路易斯酸和脱水剂,脱水Ni-Fe HTLCs被证明是适用于糠醛缩醛化反应的高效双功能催化剂。通过研究发现,脱除Ni-Fe HTLCs中水分导致颗粒收缩并增强层板间硝酸根离子间的电荷互斥,Ni-Fe HTLCs中弱酸性位点在糠醛缩醛化中发挥重要作用,脱水可改变酸性位点结构并增强其活性。脱水Ni-Fe HTLCs可吸收缩醛化反应中产生的大部分水分,但吸水后Ni-Fe HTLCs的结构并不能完全恢复,这可能是由扩散进入HTLCs层板间的有机分子导致。     

双功能[Sn,Al]-Beta分子筛一步催化葡萄糖生成5-羟甲基糠醛

以部分脱铝的Beta分子筛为母体,采用同晶置换法将Sn植入骨架制备双功能[Sn,Al]-Beta分子筛,并应用于葡萄糖一步催化生成5-羟甲基糠醛(5-HMF)反应中.样品中Sn与Al的含量通过酸洗的浓度和酸洗的时间以及SnCl4处理的时间来控制.由于骨架中有与Al相关为B酸位,和Sn相关的L酸位,[Sn,Al]-Beta可作为一种双功能的固体酸催化剂.优化了[Sn,Al]-Beta催化葡萄糖一步催化生成5-HMF的反应参数,在最优Sn/Al比条件下,葡萄糖转化率为60.0%,5-HMF选择性为62.1%.     

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

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.     

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.