Pt/NbPWO双功能催化剂的制备及氢解碱木质素制备芳香单体

木质素是一种天然芳香族聚合物,约占木质纤维素的30%,是唯一通过裂解C―O醚键和C―C键生产芳香族化学品或液体燃料的可再生芳香族资源。迄今为止,对木质素氢解制备有价值化合物的研究主要集中在相对不稳定的C―O键的裂解上,这限制了木质素氢解的效率。采用水热法和湿浸渍法制备了多功能Pt/NbPWO催化剂。通过破坏碱木质素中的C―O键和C―C键,可以得到产率为18.02%的芳香族单体。该反应不仅可以断裂木质素聚合物中醚键,同时也可以断裂部分关键的C―C键。其氢解机理可能是丰富的Brønsted酸和Lewis酸位点参与了C―C的活化。此外,重点分析载体和Pt物种在Pt/NbPWO催化剂中的协同作用。     

系列甘露糖醛酸寡糖的制备与鉴定

用酸降解法制备了系列甘露糖醛酸寡糖(聚合度2～8),并分析测定了寡糖的结构. 褐藻胶经部分酸水解,于pH=2.85处分级获得聚甘露糖醛酸. 继续用酸降解法降解聚甘露糖醛酸,经凝胶柱层析分离纯化,获得系列甘露糖醛酸寡糖. 用荧光标记糖电泳(FACE)对寡糖进行了分析,并用电喷雾离子化质谱(ESI-MS)、 核磁共振波谱(NMR)及红外光谱(FTIR)进行了结构表征. 本研究用酸降解法制备饱和甘露糖醛酸寡糖,用凝胶柱层析法分离获得系列聚合度的寡糖,为褐藻胶大分子构效关系研究和药物的筛选与发现提供了重要的基础资料.     

原子转移自由基聚合技术制备新型手性配体交换色谱固定相及对手性化合物的拆分

采用原子转移自由基聚合(ATRP)技术, 以溴代硅胶为引发剂, CuCl/2,2'-联吡啶(Bpy)为催化体系, 水为溶剂, N-丙烯酰基-L-脯氨酸为单体, 室温下在硅胶表面进行聚合反应, 制得硅胶接枝聚N-丙烯酰基-L-脯氨酸分子刷. 通过改变ATRP反应体系中单体的量, 制备了3种不同键合量且键合量可控的手性配体交换色谱固定相, 利用元素分析和热重分析对其进行表征. 考察了配体接枝率、 流动相Cu²⁺浓度、 pH值和柱温等对DL-氨基酸和α-羟基酸拆分的影响, 优化了色谱分离条件, 探讨了拆分过程的热力学. 结果表明, 所合成的手性配体交换色谱固定相能够分离9种DL-氨基酸和α-羟基酸, 其中DL-酪氨酸、 DL-色氨酸和DL-苏氨酸3种氨基酸可同时进行拆分, 且拆分过程由熵控制.     

沸石分子筛酸性质表征方法研究进展

沸石分子筛的酸性质决定其酸催化性能,如何准确、定量地区分沸石分子筛上酸类型、密度、强度及分布,对于阐明沸石酸催化性能具有重要的意义。 本文主要总结了近几年来关于沸石分子筛酸性位分布、酸类型、酸强度等重要酸性质的定性和定量分析方法的研究进展。     

磺化甲苯膦酸锆的制备及催化反应研究

首次制得磺化甲苯膦酸锆（ＺＳＴＰ），用Ｘ－衍射、热重量分析、红外光谱、元素分析等进行了表征。并以磺化甲苯膦酸锆为固体酸催化剂对酯化、缩醛、缩酮、醇脱水成醚、成烯等有机反应进行了研究。ＺＳＴＰ催化的反应收率高，操作简便，后处理容易，催化剂可以重复使用和再生。     

鸡蛋壳制备葡萄糖酸钙的研究

葡萄糖酸钙是一种溶解度高,生理宽容性大的钙营养剂和抗过敏药,广泛用作食品添加剂及医药制剂供口服或静脉注射.目前常用的生产方法主要是生物发酵法,其缺点是工艺复杂, 生产周期长且易造成污染.本研究以葡萄糖酸δ内酯作为葡萄糖酸的来源,利用蛋壳中所含高达93%的CaCO3[1]进行中和反应制备葡萄糖酸钙,探索了一条变废为宝,工艺简单,成本低,污染小的葡萄糖酸钙生产路线.     

Beta分子筛中Al的分布和Brφnsted酸的酸性强度

基于量子化学中的密度泛函理论(DFT), 研究了Beta分子筛中骨架Al在9个不同T位的分布和Brφnsted酸的分布及其强度. 计算采用8T 簇模型和B3LYP/6-31G(d,p)方法, 得到了不同T位的Al/Si替代能、(Al, H)/Si替代能和质子亲和势, 以及碱性探针分子NH3在Beta分子筛酸性位的吸附能. 结果表明, 骨架Al和Brφnsted酸优生位于Beta分子筛的T5 和T6 位; 其中酸性最强的位置是Al5-O14-Si9, 最弱的位置是Al7-O3-Si1.     

反相微乳液法制备纳米氧化铝

采用由环己烷、聚乙二醇辛基苯基醚(TritonX-100)、正丁醇与水溶液构成的反相微乳液体系, 合成了纳米Al2O3粉体. 采用X射线衍射、扫描电子显微镜、透射电子显微镜、比表面积分析仪等表征手段, 分别对产物的结构、形貌、比表面积和孔容进行了表征, 该纳米Al2O3比表面积约450 m2·g-1(随反应参数不同发生变化), 均属γ-Al2O3, 粒径均匀, 颗粒直径小于10 nm. 考察了微乳液体系中水与表面活性剂的物质的量之比r0、表面活性剂与助表面活性剂的体积比φ、焙烧温度等关键因素对产物比表面积等物理性质的影响. 结果表明, 当r0=20, φ=0.5, 焙烧温度为500 ℃时, 可以得到大比表面积、高孔容、分散性好及粒径分布均匀的γ-Al2O3粉体.     

氧化石墨烯增强卡拉胶复合膜的制备与性能

在Hummers法基础上制得了氧化石墨烯(GO), 采用流延法制备了氧化石墨烯/κ-卡拉胶(GO/κ-Car)复合膜材料. 结合红外光谱、 扫描电子显微镜及热重分析对其结构进行表征. 探讨了不同条件所得膜的成膜性、 溶解性、 透气性和力学性能, 得到性质稳定GO/κ-Car复合膜的制备条件为15.0 g 3%的κ-Car溶液、0.040 g GO粉末及5.0 g 8%的PVA溶液于75 ℃搅拌混合5 h后, 流延铺平, 于30 ℃烘干6.5 h. GO质量分数为5%的GO/κ-Car复合膜的最大负荷、 拉伸强度及杨氏模量分别是对照组κ-Car膜的1.5倍、 1.5倍和1.6倍. 同时, GO/κ-Car复合膜具有较强的透气性能, 且保留了κ-Car清除羟基自由基的生物性能.     

一种可分散性石墨烯的制备

先通过γ-氨丙基三乙氧基硅烷(KH-550)与氧化石墨反应得到改性氧化石墨, 再经水合肼还原制备了改性石墨烯. 未烘干的改性石墨烯经超声处理后, 可稳定分散于体积比为9∶1的N,N-二甲基甲酰胺/水或丙酮/水的混合溶液中, 而且在N,N-二甲基甲酰胺/水体系中超声得到的改性石墨烯分散液可在乙醇、丙酮中稳定存在. 采用红外光谱、X光电子能谱及X射线衍射分析等手段研究了KH-550改性氧化石墨及石墨烯的结构. 结果表明, KH-550上的氨基与氧化石墨的羧基反应生成了酰胺键, 与环氧基发生了加成反应, 干燥的改性石墨烯层间通过Si-O-Si键连接在一起.     

生物质转化中C―O/C―C键的活化断裂

Sustainable fuels and chemicals are receiving unprecedented attention worldwide in the context of achieving global carbon neutrality. Biomass, as the only natural and sustainable carbon-based source, shows great potential in addressing our current environmental/energy problems and in creating a carbon-neutral society. Lignocellulosic biomass is made up of basic structural units containing C―O/C―C bonds, and the catalytic cleavage of these C―O/C―C bonds is the key for biomass valorization; thus, garnering considerable attention in the past decade. This viewpoint begins with a brief report on the current status of catalytic activation/cleavage of C―O/C―C bonds during biomass conversion, and then goes on to discuss the key challenges experienced and possible strategies that can be implemented using cooperative catalysis. Our goal is not to provide a comprehensive overview of the activation/cleavage of the C―O/C―C bonds in biomass, but rather to highlight the core questions and challenges related to this process and the requirements for future investigations. We selected several representative C―O/C―C bonds in carbohydrates and lignin to discuss their catalytic mechanism in terms of total/selective bond cleavage, and then present our own insights for future studies. Therefore, this article mainly discusses the following two aspects: (1) The activation and cleavage of C―O bonds, which includes total and selective C―O bond cleavage in furan-based fuel precursors and lignin. When aiming to produce liquid fuels, including alkanes and arenes from biomass, the total cleavage of C―O bonds is essential. During the hydrodeoxygenation (HDO) of furan-based fuel precursors, various C―O bonds need to be cleaved, especially the C―O bond of each tetrahydrofuran ring, which has the highest bond energy. When compared with the total HDO of fuel precursors, the removal of the phenolic hydroxyl groups in lignin to produce arenes is more challenging because of the competition between the over-hydrogenation of the benzene rings and the cleavage of phenolic C―O bonds. The selective or partial cleavage of C―O/C―C bonds to form highly functionalized chemicals has recently attracted great interest and is believed to be a dynamic future research avenue. For example, the production of phenol from lignin or lignin-model compounds, through the selective removal of methoxy groups and para-side-chain groups, while preserving the phenolic hydroxyl groups, has been extensively explored in the past few years. (2) The other important aspect of this article is the cleavage of the C―C bonds in carbohydrates and lignin. The cleavage of carbohydrate C―C bonds occurs via retro-aldol condensation, which produces propylene glycol, ethylene glycol, ethanol, and lactic acid. The cleavage of C―C bonds in lignin is challenging because the bond energy of the C―C bonds is generally higher than that of the C―O bonds in lignin. Therefore, in this section, we discuss the cleavage of the strongest 5―5' bond in lignin. Finally, some subjective perspectives and future directions are provided, also highlighting several major challenges in this field.      

生物质转化中C―O/C―C键的活化断裂

生物质作为自然界中唯一可持续的有机碳来源,在解决环境和能源问题、创建一个碳中和的社会方面展现出巨大的潜力。木质生物质是由具有C―O/C―C键的基本结构单元构成的高分子化合物,活化、断裂这些C―O/C―C键是生物质高值化利用的关键,因此在过去十年中受到了广泛的关注。本文首先简要综述了生物质转化中C―O/C―C键催化断裂的现状,主要关注C―O/C―C键断裂的关键挑战和现有策略。我们的目标不是全面概述C―O/C―C键活化断裂的现况,而是提出与C―O/C―C键断裂相关的核心问题并且对未来的研究作出展望。我们选择了碳水化合物和木质素中几种具有代表性的C―O/C―C键来讨论它们在不同情况下协同催化断裂的机理,然后对未来的研究提出自己的见解。     

纤维素及其衍生物催化脱氧转化制化学品

Biomass, as a renewable carbon resource in nature, has been considered as an ideal starting feedstock to produce various valuable chemicals, fuels, and materials, and thus, can help build a sustainable chemical industry. Because cellulose is one of the richest components in lignocellulosic biomass, the efficient transformation of cellulose plays a crucial role in biomass utilization. However, there are many oxygen-containing groups in cellulose, and therefore, the selective removal of particular functional groups from cellulose becomes an essential step in the synthesis of the chemicals or fuels that can meet the requirements set by current chemical industries. In the past decades, several efficient catalytic systems have been developed to selectively split the C―O bonds inside cellulose and its derivatives, thereby producing various valuable chemicals. In this review article, we highlight recent progress made in the selective deoxygenation of cellulose and its derived key platforms such as glucose and 5-hydroxymethyl furfural (HMF) into ethanol, dimethyl furfural (DMF), 1, 6-hexanediol (1, 6-HD), and adipic acid. The selection of these reactions is primarily because these chemicals are of great significance in chemical industries. More importantly, the formation of these chemicals represents the cleavage of different C―O bonds in biomass molecules. For instance, the synthesis of ethanol requires cleaving of only one C―O bond and two C―C bonds of the glucose unit inside cellulose. If two or more C―O bonds in the sugar or sugar acids are cleaved, olefins, oxygen-reduced sugars, and adipic acid will be attained. HMF has a furan ring linked by hydroxyl/carbonyl groups, and hence, either a furanic compound (e.g., DMF) or linear products (e.g., 1, 6-HD and adipic acid) can be synthesized by selective removal of hydroxyl/carbonyl oxygen or ring oxygen atoms. This article focuses on the selective cleavage of particular C―O bonds via heterogeneous catalysis. Efficient catalytic systems using hydrogenolysis and/or deoxydehydration strategies for these transformations are discussed. Moreover, the functions of typical catalysts and reaction mechanisms are presented to obtain insight into the C―O bond cleavage in these biomass molecules. Additionally, other factors such as reaction conditions that also influence the deoxygenation performance are analyzed. We hope that these knowledge gained on the catalytic deoxygenation of cellulose and its derived platforms will promote the rational design of effective strategies or catalysts in the future utilization of lignocellulosic biomass.     

纤维素及其衍生物催化脱氧转化制化学品

纤维素是木质纤维素生物质中最为丰富的组分,将其催化转化制备高附加值化学品在生物质资源化利用中占据极为重要的一席之地。由于纤维素中氧含量过高,需选择性地脱除部分氧原子才可获得满足当前化学工业对各类高值化学品的要求。近年来,针对纤维素以及由其衍生的关键平台分子葡萄糖和5-羟甲基糠醛(HMF)等催化脱氧的研究已引起广泛关注,并取得诸多重要进展。在此,我们总结了具有代表性的多相催化剂体系,讨论了利用氢解或脱水脱氧策略分别将纤维素和葡萄糖等分子中一个或多个C―O键裁剪制备乙醇、烯烃或己二酸等的研究。我们还着重介绍了HMF和其衍生的呋喃化合物选择性剪切C―OH/C＝O键或呋喃环中的C―O―C键分别制备二甲基呋喃和1, 6-己二醇等催化体系。此外,对各多相催化剂的作用机制和特定C―O断键机理也分别进行了探讨,以期深入理解纤维素及其衍生物的催化脱氧反应。     

Ag(111)表面Ag配位结构的分等级组装

表面辅助的金属有机纳米结构因其结构稳定性和潜在应用受到广泛关注。在金属有机纳米结构中,金属原子来源于外部沉积的金属或金属表面原子。外部沉积的金属原子种类多样,取决于目标纳米结构。然而,金属表面原子受限于表面科学常用的金、银和铜单晶金属表面。金属有机纳米结构大多包括Au配位或是Cu配位结构,而只有少量的用表面Ag原子构成。分子金属相互作用的进一步研究有助于预期纳米结构的精确控制形成。至于构建基元,有机分子通过M―C、M―N和M―O键与表面金属原子配位。末端炔反应或者乌尔曼耦合能够实现C―M―C节点的形成。Cu和Au原子能够与含有末端氰基或吡啶基官能团的分子配位形成N―M―N键。另外,表面Ag增原子能够通过Ag―N配位键与酞菁分子配位。然而,M―O配位键的相关研究较少。因此,我们计划使用末端羟基分子与Ag增原子配位形成金属有机配位纳米结构去研究O―Ag节点。我们通过扫描隧道显微镜利用4, 4’-二羟基-1, 1’: 3’, 1’’-三联苯分子(4, 4’-dihydroxy-1, 1’: 3’, 1’’-terphenyl,H3PH)和Ag增原子成功构筑了一系列二维有序纳米结构。在室温下,蒸镀的H3PH分子自组装形成由环氢键连接的密堆积结构。当退火温度提升到330 K,一种新的纳米结构出现了,该结构由O―Ag配位键和氢键共同作用形成。进一步地提升退火温度至420 K,蜂巢结构和共存的二重配位链出现,这两种结构中仅由O―Ag―O键构成。为分析金属分子反应路径和O―Ag―O键的能量势垒,我们对该体系进行密度泛函理论计算。计算结果显示,O―Ag键形成的能量势垒是1.41 eV,小于O―Ag―O节点1.85 eV的能量势垒。这也解释了分等级金属-有机纳米结构形成的原因。我们的实验结果提供了一种利用有机小分子和金属增原子来设计和构筑分等级二维纳米结构的有效方法。     

均相催化剂催化氧气氧化生物质制备甲酸

甲酸是一种重要的化工原料,以可再生生物质为原料,通过催化氧气氧化制备甲酸具有重要意义。对于不溶于水的生物质原料的转化,采用可溶于水的均相催化剂体系证明是有效的。本文总结了均相催化剂体系(包括含钒杂多酸、含钒杂多酸+H₂SO₄、含钒杂多酸基离子液体、NaVO₃+H₂SO₄、VOSO₄、NaVO₃-FeCl₃+H₂SO₄、FeCl₃+H₂SO₄等)在催化氧气氧化生物质(包括生物质模型化合物、纤维素、木材、秸秆和玉米芯等)制备甲酸方面的研究,分析了其转化的过程和机理。最后,指出了目前催化氧化生物质制备甲酸存在的问题和挑战。     

负载Pt-WOx催化剂上甘油选择氢解合成1, 3-丙二醇

Glycerol is a versatile platform compound that is formed in considerable amounts as a by-product of biodiesel production. The catalytic selective hydrogenolysis of glycerol to 1, 3-propanediol (1, 3-PDO) provides a sustainable route for the synthesis of this important diol. In this study, a series of platinum-tungsten oxide (Pt-WO_x) catalysts with different WO_x surface densities dispersed on titanium(Ⅳ) oxide, zirconium(Ⅳ) oxide, and aluminum oxide supports were prepared and evaluated for the glycerol hydrogenolysis to 1, 3-PDO. The highest reaction activity and 1, 3-PDO selectivity were achieved at a WO_x density of approximately 1.5–2.0 W·nm⁻², with all three support materials. Such a strong dependence on the surface density of WO_x revealed the critical role of the dispersed WO_x domains in the hydrogenolysis of glycerol to 1, 3-PDO. The infrared spectra for carbon monoxide adsorption confirmed the electron transfer and strong interaction between the Pt particles and WO_x domains. These phenomena were hypothesized to contribute to the superior selectivity to 1, 3-PDO over 1, 2-PDO of the supported Pt-WO_x catalysts when compared with the corresponding supported Pt catalysts. The realized superior 1, 3-PDO selectivity was consistent with its higher stability on the Pt-WO_x catalysts, as reflected by the lower reaction rate constant of 1, 3-PDO than those of 1, 2-PDO and glycerol obtained in their hydrogenolysis reactions. There existed a volcano-type dependence of the glycerol reaction activity on the hydrogen partial pressure. Such a dependence, together with the measured ratio (1 : 2) of the secondary to the primary C−H bonds in 1, 3-PDO in the presence of deuterium and deuterium oxide (replacing hydrogen and water, respectively), indicated that the glycerol hydrogenolysis proceeds by the kinetically relevant dehydrogenation of glycerol to the glyceraldehyde intermediate, followed by the dehydration and hydrogenation of glyceraldehyde to 1, 3-PDO over the Pt-WO_x catalysts.      

负载Pt-WOx催化剂上甘油选择氢解合成1, 3-丙二醇

甘油是重要的生物质基平台分子,可以从生物柴油生产过程中作为副产物大量获得。本文采用等容浸渍法,在氧化钛、三氧化二铝和氧化锆载体上制备一系列具有不同WO₃表面密度的负载Pt-WO_x催化剂,研究了它们在甘油选择氢解合成1, 3-丙二醇反应中的催化性能。实验结果表明,WO₃的表面密度显著影响这些催化剂的活性和1, 3-丙二醇选择性,它们均在1.5–2.0 W∙nm⁻²表面密度时表现出最优性能,表明分散的WO_x物种是影响Pt-WO_x催化剂性能的关键因素。通过原位红外CO吸附表征等方法发现Pt粒子与WO_x物种之间存在电荷转移和强相互作用,进而提高Pt-WO_x催化剂的甘油氢解转化为1, 3-丙二醇的活性。进一步比较甘油、1, 2-丙二醇和1, 3-丙二醇的氢解反应发现,1, 3-丙二醇的氢解速率常数低于甘油和1, 2-丙二醇,表明在Pt-WO_x催化剂上1, 3-丙二醇具有更高的反应稳定性,这跟Pt-WO_x催化剂具有较高的1, 3-丙二醇选择性相一致。结合氢气分压对甘油氢解活性表现出的火山型影响结果和在D₂/D₂O存在下,观察到的1, 3-丙二醇产物中仲碳与伯碳上的H原子数的比例(~1 : 2),我们推测在甘油氢解合成1, 3-丙二醇反应中,甘油首先在Pt-WO_x催化剂上脱氢生成甘油醛中间体,然后甘油醛进一步脱水和加氢转化为1, 3-丙二醇。     

过渡金属参与C―H键切断模式的理论研究进展

过渡金属催化活化C―H键来构建新共价键因具有原子经济和合成简捷的特点,已成为合成化学中最为有效策略之一。本文中,我们总结了过渡金属参与的C―H键切断的理论研究进展,并系统性提出了C―H键切断的相关模式,包括:C―H键对金属的氧化加成、碱协助的去质子化、σ-复分解、Friedel-Crafts型亲电芳香取代、α-或β-氢消除以及夺氢活化等。理论计算表明,当使用还原性较强的零价金属催化剂时,反应可按照氧化加成模式进行。当使用金属羧酸盐作为催化剂时,通常以协同金属化-去质子化机理模式实现C―H键切断。当使用阳离子金属催化剂,富电子芳烃比缺电子芳烃优先反应时,C―H键切断则会经历碱协助的内部亲电取代模式。σ-复分解是协同金属化-去质子化机理的另一种模式。如果亲电体对芳烃进行加成时,则可按照Friedel-Crafts型亲电芳香取代方式活化C―H键。α-或β-氢消除也是比较常见的活化C―H键模式。此外,夺氢活化可通过自由基过程实现C―H键活化。本文通过对过渡金属参与的C―H键活化模式的论述旨在为实验提供理论指导。