由木质素制备高品位运输燃料初探

木质素是一种绿色可再生的资源,是制备液体运输燃料的理想原料。本文研究了一种由木质素制备液体运输燃料的方法。首先,选用K-OMS-2催化剂进行氧化反应,通过氧化木质素单体模型物获得芳香醛,木质素二聚体模型物(α-O-4结构木质素二聚体)氧化解聚后获得了65%产率的芳香醛;同时尝试氧化碱木素,产物中检测到香草醛、对羟基苯甲醛等化合物;其次,通过芳香醛和丙酮发生Claisen-Schmidt缩合反应增加碳链长度;最后,通过芳烃加氢获得高品位的饱和烷烃燃料。     

木质素降解模型化合物愈创木酚及苯酚原位加氢制备环己醇

以Raney Ni为催化剂,研究了甲醇水相重整制氢与木质素降解模型化合物愈创木酚／苯酚加氢的耦合反应.考察了反应前冷压、反应温度、反应时间、物料配比等条件对木质素降解模型化合物原位加氢反应性能的影响,并对影响机制进行了讨论.结果表明,在反应温度为220 ℃、反应前冷压0 MPa(表压)、物料比水／甲醇／模型化合物为20∶5∶0.8的条件下,反应7 h后愈创木酚转化率与环己醇选择性分别达99.00％和93.74％,反应12 h后苯酚的转化率与环己醇选择性分别达90.50％和99.29％.采用原位加氢反应,木质素降解的酚类模型化合物转化率和选择性明显优于外部供氢反应的转化率和选择性,同时,避免了外部供氢反应存在的氢气制备、储存、传输及加氢条件苛刻等问题,为木质素解聚产物制备化工品提供了新思路与实验基础.     

Ni/SAPO-11催化剂上棕榈油加氢脱氧制异构烃燃料(英)

采用水热法合成了小粒径、具有介孔结构的SAPO-11分子筛.采用浸渍法制备了不同Ni负载量的Ni/SAPO-11催化剂.并采用X射线衍射,扫描电镜,N₂物理吸附-脱附,NH₃程序升温脱附,热重和H₂化学吸附技术对该类催化剂的物理化学性质进行了详细表征.结果表明,SAPO-11较大表面积和介孔结构可分散Ni,使得Ni粒子尺寸较小.在棕榈油加氢脱氧制备液体烃类燃料反应中,液体烷烃产物由相关脂肪酸中间产物的直接加氢脱氧和脱羰-加氢脱氧两种途径产生.Ni/SAPO-11催化剂的弱/中强酸性质及其匹配的金属-酸双功能可显著抑制积炭反应,提高催化剂的寿命,液体烷烃收率高达70%,异构烷烃选择性超过80%.     

α-氰醇立体选择性合成新进展

总结了近十年来立体选择性合成α-氰醇的最新进展, 包括金属配合物催化的醛、酮类底物的立体选择性氢氰化和硅氰化反应, 不含金属的有机小分子催化剂催化的醛、酮类底物的立体选择性硅氰化反应以及生物催化的立体选择性氢氰化反应. 另外对部分反应中涉及的机理也作了介绍.     

二氧化碳多相催化加氢制C2及以上烃类和醇的研究进展

通过可再生能源得到的氢气将二氧化碳转化为高附加值的燃料和化学品,对于缓解全球变暖、改善生态环境和解决化石资源日益枯竭的难题具有重要的意义。通过加氢反应合成碳氢化合物,尤其是C₂₊烃类和含氧化合物愈来愈引起大家的研究兴趣。设计制备兼具二氧化碳活化和碳-碳键耦合的多功能催化剂仍然是一较大的挑战。本文总结了二氧化碳加氢合成长链烷烃、低碳烯烃、高级醇的最新研究进展,探讨了二氧化碳加氢所涉及的相关反应的热力学和动力学、反应机理和反应路径,并对现阶段报道的多相催化剂进行了归纳和分析,最后指出未来在二氧化碳加氢的多相催化过程中所面临的问题和发展方向。     

双功能催化剂Ru2P在N-杂环加氢和无受体脱氢反应中的几何效应和电子效应

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.     

糠醛气相加氢制备糠醇Cu/SiO2催化剂的失活机理研究

采用共沉淀法制备了Cu/SiO₂催化剂，在固定床反应器上评价其糠醛气相催化加氢制备糠醇的反应性能，并采用XRD、H2-TPR、ICP-OES、XPS、TG、Raman、TEM等手段对使用后的Cu/SiO₂催化剂进行表征，研究其在反应中的失活机理。在常压、反应温度140℃、质量空速2.4 h^-1、氢醛比9.7的条件下，反应5 h内糠醛转化率均高于97%；反应6-21 h，糠醛转化率从96%快速下降到32%，说明Cu/SiO₂催化剂在糠醛加氢反应中快速失活，失活的主要原因是活性组分铜的团聚烧结和催化剂表面上积炭覆盖了反应活性位。     

吡啶桥连双功能有机催化剂催化二氧化碳、环氧化物和芳香胺合成3-芳基-2-噁唑烷酮的研究

合成了一类羧基或羟基功能化的有机小分子催化剂,成功用于二氧化碳、环氧化物和芳香胺一锅法制备噁唑烷酮类化合物的制备.该催化体系具有反应条件温和、底物普适性好的优点.控制实验表明整个反应过程经过了三个阶段:环氧化物分别与二氧化碳、芳香胺反应形成环状碳酸酯、氨基醇,最终环状碳酸酯和氨基醇进一步反应形成噁唑烷酮类化合物.     

贵金属催化剂上两步法选择性降解有机溶剂型木质素

使用担载型贵金属催化剂和磷酸在不同温度下通过两步法加氢降解二氧六环木质素. 第一步反应使用Rh/C和浓度为1% (w)的磷酸为催化剂, 在270 ℃和4 MPa氢气气氛下反应后通过气相色谱(GC)和气相色谱-质谱(GC-MS)分析木质素单体和二聚体, 总收率最高可达16.9%. 通过傅里叶变换红外(FTIR)光谱、X射线光电子能谱(XPS)、元素分析(EA)和凝胶渗透色谱(GPC)等方法研究第一步反应产物的变化. 结果发现, 二氧六环木质素中的C－O－C键被打断, 木质素分子量降低, 部分羰基和羧基被脱除. 随着反应温度的上升, 产物的含氧量不断下降, 在270 ℃反应10 h 后氧含量从35% (w)降低至21% (w). 结合不同的表征方法, 提出二氧六环木质素的第一步反应路径. 第二步反应中使用Pd/C和磷酸为催化剂在250 ℃可以将木质素单体、二聚体高选择性地加氢脱氧转化为对应的烃类产物.     

木质素基酚类化合物加氢脱氧制取碳氢燃料

木质素是生物质中碳资源密度最高的组分.木质素到高品质液体燃料的转化主要通过其解聚的单环酚类化合物经加氢脱氧工艺来实现.来源于木质素的酚类化合物的加氢脱氧产物一般为C6~C10之间的碳氢化合物,与现有的商品汽油组分碳数分布一致,是理想的交通替代燃料.酚类化合物的加氢脱氧研究近年来发展迅速,文献报道数量激增.本文对硫化态Mo基催化剂、贵金属催化剂及非硫化非贵金属催化剂作用下单环酚类化合物的加氢脱氧反应特性分别进行了回顾,对典型酚类模型化合物在催化反应机理进行了简述,并对载体材料在加氢脱氧过程中的作用进行了介绍.随后,在此基础上总结了当前酚类化合物加氢脱氧过程中的难点,并对下一步的技术发展方向进行展望.     

PROBING STUDY OF Rh CATALYSTS ON DIFFERENT SUPPORTS IN CO HYDROGENATION

Rh catalysts on SiO₂ and CeO₂ were studied in CO hydrogenation by adding probing molecules during the reaction. The results demonstrate that alkanes were not formed through the oxygen-containing intermediates, e.g. methanol, ethanol or acetaldehyde. Ethanol and acetaldehyde were not produced through the formation of methanol. Acetaldehyde was not formed through ethanol dehydrogenation, however, ethanol was formed through the hydrogenation of acetaldehyde and CeO₂ itself can catalyze the hydrogenation of acetaldehyde.     

Ni/HZSM-5的结构及催化木糖醇水相加氢合成液体烷烃的性能研究

采用浸渍法制备了Ni/HZSM-5双功能催化剂,采用BET、XRD、NH3-TPD、H2-TPR、FTIR和TG等方法表征了催化剂比表面、孔结构、酸性、还原能力及骨架结构等信息,研究了其催化木糖醇水相加氢合成液体烷烃的性能及催化剂失活的原因。结果表明,在优化的金属中心/酸中心的协同作用下,木糖醇可通过水相加氢高选择性地合成C5-C6烷烃;过高的金属中心或酸中心均会导致C-C键断裂形成轻质烷烃,以2%Ni/HZSM-5催化剂上木糖醇水相加氢活性最高,木糖醇C转化率为94%液体烷烃总收率可达90%,这与其具有较大的比表面积、合适的孔径分布、较多的金属活性中心、适中的酸量和强酸量有关。催化剂6次重复使用后活性明显降低,其骨架部分脱铝和表面积碳是其失活的主要原因。     

Silver and palladium nanoparticles-containing products of the low-temperature wave conversion of an energetic material: Catalytic activity in piperylene hydrogenation

The hydrogenation of 1,3-pentadiene into pentenes over the commercial 0.5% Pd/Al₂O₃ catalyst and over a new catalyst containing 1.0% Pd and 3.7% Ag (μ-catalyst) has been investigated. The new catalyst has been prepared via the flameless wave conversion of cyclotrimethylenetrinitramine in a porous composite. The catalytic properties of the new composite in the hydrogenation reaction depend on the hydrogen/1,3-pentadiene ratio and on the catalyst activation temperature. The reaction conditions for selective 1,3-pentadiene hydrogenation have been optimized. The pentenes yield as a function of temperature passes through a maximum at any H₂/C₅H₈ ratio between 1 and 2. The 2-pentene/1-pentene ratio in the reaction products increases as the temperature is raised.     

Hydrogenation of 2- tert -butylphenol over Ni catalyst

The hydrogenation of 2-tert-butylphenol was studied in regard to possibilities of influencing selectivity, namely the ratio ofcis- andtrans-isomers of 2-tert-butylcyclohexanol in the final reaction mixture. The hydrogenation reactions were carried out using the catalyst Ni/Al₂O₃. During the hydrogenations, a higher content of thecis-isomer was attained, when simultaneously the final reaction mixture contained 2-tert-butylcyclohexanone. The content of this intermediate, which primarily hydrogenated to thecis-isomer, increased with a decreased pressure and after the addition of acetic acid into the reaction mixture.     

Catalytic Ethanolysis of Kraft Lignin into High‐Value Small‐Molecular Chemicals over a Nanostructured α‐Molybdenum Carbide Catalyst

We report the complete ethanolysis of Kraft lignin over an α‐MoC_1?x/AC catalyst in pure ethanol at 280 °C to give high‐value chemicals of low molecular weight with a maximum overall yield of the 25 most abundant liquid products (LP25) of 1.64 g per gram of lignin. The LP25 products consisted of C₆–C₁₀ esters, alcohols, arenes, phenols, and benzyl alcohols with an overall heating value of 36.5 MJ kg^?1. C₆ alcohols and C₈ esters predominated and accounted for 82 wt % of the LP25 products. No oligomers or char were formed in the process. With our catalyst, ethanol is the only effective solvent for the reaction. Supercritical ethanol on its own degrades Kraft lignin into a mixture of small molecules and molecular fragments of intermediate size with molecular weights in the range 700–1400, differing in steps of 58 units, which is the weight of the branched‐chain linkage C₃H₆O in lignin. Hydrogen was found to have a negative effect on the formation of the low‐molecular‐weight products.     

Selective Amplification of CO Bond Hydrogenation on Pt/TiO2: Catalytic Reaction and Sum‐Frequency Generation Vibrational Spectroscopy Studies of Crotonaldehyde Hydrogenation

The hydrogenation of crotonaldehyde in the presence of supported platinum nanoparticles was used to determine how the interaction between the metal particles and their support can control catalytic performance. Using gas‐phase catalytic reaction studies and in situ sum‐frequency generation vibrational spectroscopy (SFG) to study Pt/TiO₂ and Pt/SiO₂ catalysts, a unique reaction pathway was identified for Pt/TiO₂, which selectively produces alcohol products. The catalytic and spectroscopic data obtained for the Pt/SiO₂ catalyst shows that SiO₂ has no active role in this reaction. SFG spectra obtained for the Pt/TiO₂ catalyst indicate the presence of a crotyl‐oxy surface intermediate. By adsorption through the aldehyde oxygen atom to an O‐vacancy site on the TiO₂ surface, the C?O bond of crotonaldehyde is activated, by charge transfer, for hydrogenation. This intermediate reacts with spillover H provided by the Pt to produce crotyl alcohol.     

Studies on Tripolycyanamide Formaldehyde Resin-Pd Complex and Its Use in the Synthesis of the Branch of Paclitaxel

A novel method was developed to prepare the branch of paclitaxel using 2,4-dichlorophenylaldehyde as the starting material.The branch was synthesized through condensation, cydoaddltion and catalyzing hydrogenation of dichlorophenyl intermediate. Tripolycyanamide formaldehyde resin-Pd complex as hydrogenation catalyst has been studied. The influence of temperature and N/Pd atomic ratio of the catalyst on the effect of catalytic hydrogenation was investigated and the optimum conditious were found. Because of the mild cyclization reaction condition, convenient asymmetric resolution operation and high yield, the synthetic route was practical.     

Homogeneous hydrogenation of alk-1-enes and alkynes catalyzed by the 1-[Ir(CO)(PhCN)(PPh3)]-7-C6H5-1,7-(σ-C2B10H10) complex

The complex [Ir(σ-carb)(CO)(PhCN)(PPh₃)], where carb = -7-C₆H₅-1,2C₂B₁₀H₁₀, was found to be an effective catalyst for homogeneous hydrogenation of terminal olefins and acetylenes at room temperature and atmospheric or subatmospheric hydrogen pressure. Internal olefins are not hydrogenated, but simple alk-1-enes are readily converted into the corresponding alkanes. Isomerization of the double bond catalyzed by the metal complex occurs at very small extent. Catalytic hydrogenation of olefins having carboxylate substituents on the unsaturated carbon atoms is prevented by the formation of thermally stable chelate hydridoalkyl complexes of the type I$\text{(H)}$(σ-CHRCHR′C(O)OR″) (σ-carb)(CO)(PPh₃)]. Acetylenes are hydrogenated to alkenes. The alk-1-enes formed in the hydrogenation of the alkynes HCCR in turn undergo the more slow reactions either of hydrogenation to alkanes or isomerization to internal olefins which cannot be further hydrogenated. Hydrogenation of alkynes of the type RCCR′ is stereospecifically cis, yielding cis- olefins. Catalyzed cis → trans isomerization reaction of these internal olefins occurs only to a negligeable extent.     

苯甲酸甲酯促进茂金属催化剂催化SBS加氢反应研究

以苯甲酸甲酯为促进剂,用茂金属催化剂制备了活性丁苯嵌段共聚物(SBS)的选择性催化加氢产物,讨论了苯甲酸甲酯、SBS的数均分子量等因素在几种实验条件下对产物加氢度的影响.结果表明,每百克干胶使用0.15～0.3mmol Ti催化条件下,苯甲酸甲酯在特定添加方式下能较大程度地提高茂金属催化剂的活性.在不加入苯甲酸甲酯的情况下,Mn=6.5×104和Mn=5.5×104两种SBS基础胶加氢反应180min时加氢度均97.0%;加入酯以后,反应60～120min时,基础胶的加氢度≥98%;与已报道的研究结果相比,将加氢反应时间缩短了60～120min.在每百克干胶使用0.15～0.3mmolTi催化条件下,数均分子量的大小也对SBS基础胶的加氢度有影响,反应30min时,Mn=5.5×104的加氢度≥97%,Mn=6.5×104的加氢度90%;随着反应时间的延长,这种差距在逐渐缩小;反应180min时,两者已无明显差距,此时两种基础胶的加氢度都≥98%.对影响的加氢度的机理进行了解释.