芳烃催化加氢反应机理的研究进展

对萘、菲、蒽及芘根据不同计算方法所得的反应活性位进行总结,对苯在金属表面的催化加氢机理-芳烃交换机理进行概括,对菲在MoS₂/Al₂O₃催化剂表面生成二氢菲的基元反应步骤和在Ni-MoS₂/Al₂O₃催化剂表面加氢生成四氢菲的过程进行总结,还给出了蒽的催化加氢反应网络图,分析了在不同催化条件下蒽是否有中环断裂情况的发生,给出了芘在RaneyNickel（W-7）催化剂表面生成二氢芘、四氢芘和六氢芘的催化加氢机理反应图,以及根据能量最低理论,判断芘发生加氢反应的优先位置情况,分别计算了芘加氢生成二氢芘、四氢芘、六氢芘和十氢芘可能存在的加氢路径。并总结了蒽、菲等多环芳烃发生催化加氢反应的规律。加深对多环芳烃催化加氢机理的研究将更好地指导重质油轻质化的进行,因此对多环芳烃催化加氢机理的研究具有重要意义。     

铑催化剂催化烯烃不对称加氢反应研究进展

不对称催化氢化反应具有完美的原子经济性和清洁高效等特点,是最受青睐的不对称合成方法之一。C=C、C=O、C=N的不对称加氢反应仍主要依赖过渡金属催化剂。过渡金属催化剂,尤其是铑催化剂,催化碳碳双键的不对称加氢反应仍是一个不断发展的领域。本文对近年来利用铑催化剂催化烯烃进行不对称氢化反应的研究进展进行了综述,着重介绍了铑-双膦配体催化体系催化烯烃不对称加氢反应的催化机理,以及铑催化剂在烯胺、不饱和羧酸及衍生物、烯醇酯和非官能团烯烃不对称氢化中的应用,并通过对现有文献的总结指出了今后铑催化剂催化烯烃氢化反应的研究重点,即:①铑-单膦配体催化烯烃不对称氢化反应的作用机理须待提出;②非官能化底物不对称催化氢化反应的手性配体亟待拓宽。     

Catalytic Processes Involving Dihydrogen Complexes and Other Sigma-bond Complexes

The discovery of dihydrogen complexes, L_nM(H₂), pointed to direct transfer of hydrogen from coordinated H₂ ligands to substrates as an operable pathway in catalysis both in homogeneous and heterogeneous systems. Sigma complexes, L_nM(η²-H–X) (X=H, Si, C, etc), are indeed relevant in hydrogenation as well as silane alcoholysis and methane conversion.     

间苯二甲胺合成工艺研究

以间苯二甲腈为原料,雷尼镍为催化剂,进行催化加氢制间苯二甲胺,探讨了各种因素对反应结果的影响,即:间苯二甲腈原料纯度、催化剂、反应助剂、反应温度、反应压力及反应溶剂等对催化加氢反应的影响。提出间苯二甲腈催化加氢制间苯二甲胺工艺的最佳控制条件。指出对原料间苯二甲腈的纯化及催化剂的研究是今后间苯二甲腈催化加氢制备间苯二甲胺实现工业化的研究重点。     

Coal liquefaction model: microscopic examination of solids from metal halide catalysed coal hydrogenation experiments

Coal undergoes changes during the hydrogenation process which depend on the balance between carbonization and hydrogenation reactions, which in turn depend on various experimental conditions, i.e. hydrogen availability, heating rate etc. If carbonization conditions prevail, semicoke is formed, whereas liquid hydrocarbons are formed under hydrogenation conditions. This model is applicable to hydrogenation reactions carried out under a wide range of experimental conditions.     

Different Hemi-Salen/Salan Ligand Containing Binuclear Boron-Fluoride Complexes: Synthesis,Spectroscopy, Fluorescence Properties,and Catalysis

A family of hemi-salen (L₁H–L₆H) and hemi-salan (L_1aH–L_2aH) ligands-based N,O-chelated binuclear boron-fluoride [L_n(BF₂)₂] (n = L₁–L₆ or L_1a–L_2a) complexes have been prepared and characterized by a variety of spectroscopic techniques (¹H, ¹³C and ¹⁹F NMR, FT-IR, UV-Vis, LC-MS, and fluorescence spectra) and elemental analysis. All of the binuclear boron-fluoride complexes exhibit strong absorption bands due to S₀→S₁ transitions and strong fluorescence properties were observed at room temperature in the solution. The binuclear boron complexes containing two naphthyl groups are significantly red-shifted in comparison with the other binuclear boron-fluoride complexes. After the structures are characterized, these hemi-salen and salan ligand-based N, O-chelated binuclear boron-fluoride complexes were utilized to the transfer hydrogenation of the different acetophenone derivatives conversion to 1-phenylethanol derivatives as catalysts.     

CO2催化氢化制清洁能源的研究进展及趋势

CO₂的过量排放引发了严重的温室效应,采用CO₂氢化技术在实现CO₂减排的同时又可生成高价值的产物,因此受到研究人员的广泛关注。近年来,关于CO₂氢化的研究逐渐增多,但是综合探讨多种催化技术的相关综述较少。本文将较为新型的CO₂氢化技术大致分为光催化、电催化、生物催化以及等离子体催化4种。主要从催化剂的角度,对以上4种新型CO₂氢化技术的研究现状和最新进展进行了归纳,并简要介绍了其反应机理。同时,基于研究现状的分析,指出了4种氢化技术的进一步研究方向和需要解决的相关问题,并对CO₂氢化技术的发展作出了展望。     

Hydrogenation of cyclohexene and benzene over an amorphous pd-zr alloy

Amorphous Pd-Zr alloys, produced by a rapid solidification technique, were studied to determine their catalytic activity for the hydrogenation of cyclohexene and benzene. The activity of the amorphous alloy without pretreatment by air was lower than that of the corresponding crystalline alloy, but it was gradually increased with the pretreatment. The surface area and the hydrogen adsorption activity of the alloys were simultaneously increased with the pretreatment. It is found from X-ray diffraction pattern and SEM observation that palladium, which is an active species for hydrogenation in the amorphous alloys, is highly dispersed on the granulated ZrO₂ surface by the pretreatment.     

On the mechanism of the copper‐catalysed hydro‐genation; a reinterpretation of published data

The copper‐catalysed hydrogenation of triglyceride oils differs from the nickel‐catalysed reaction in that copper catalysts only hydrogenate double bonds in methylene interrupted polyunsaturated fatty acid moieties. Accordingly, the copper‐catalysed reaction stops when the triglycerides present in the reaction mixture are only monounsaturated fatty acids and polyunsaturated fatty acids in which the double bonds are separated by more than one methylene group. Copper catalysts thus exhibit a very high oleic acid selectivity. This observation has been explained in the literature by assuming that copper catalysts can only catalyse the hydrogenation of conjugated polyenes and that they are also capable of catalysing the conjugation of methylene interrupted polyenes. Accordingly, the hydrogenation of linolenic acid and linoleic acid moieties starts with their conjugation which is then followed by hydrogen addition to these conjugated acids. For both reactions (conjugation and hydrogenation) the literature assumes the Horiuti‐Polanyi mechanism stipulating the addition of a hydrogen atom to a double bond as the first step. Reinterpretation of the literature data now leads to the hypothesis that the first step in the conjugation mechanism could well be the abstraction of a hydrogen atom from an allylic methylene group rather than the addition of a hydrogen atom to a doubly bonded carbon atom. A conjugated double bond system then results from the addition of a hydrogen atom to the allylic radical formed by the foregoing hydrogen abstraction.     

Effects of Lewis acid catalysts on the hydrogenation and cracking of two-ring aromatic and hydroaromatic structures related to coal

Little is known about the hydrogenation of fused aromatic nuclei during the liquefaction of coal under the influence of Lewis acid catalysts. This study was conducted to establish the effects of catalyst acidity on the activity and selectivity of Lewis acid catalysts, the sources of hydrogen involved in hydrogenation and cracking, and the relations between reactant structure and reactivity. Two-ring aromatic and hydroaromatic compounds were used to simulate some of the structural units present in coal. The catalysts examined were ZnCl₂ and AlCl₃. ZnCl₂ is less active than AlCl₃ for both hydrogenation and cracking but it does not promote the formation of tars via Scholl condensation: Methyl or hydroxyl substitution of the reactants greatly enhances their reactivity towards hydrogenation and cracking. The source of hydrogen consumed during hydrogenation depends on the choice of catalyst. In the presence of AlCl₃, Scholl condensation of aromatic nuclei serves as the principal source of hydrogen. Molecular hydrogen is used exclusively, though, when hydrogenation is catalysed by ZnCl₂. The formation of reaction products and the trends in reactant reactivity can be interpreted on the basis of carbonium ion mechanisms. The results of this study provide a basis for assessing the extent of hydrogenation occurring during the liquefaction of coal using ZnCl₂ or AlCl₃.     

Hydrogenation of natural rubber latex in the presence of OsHCl(CO)(O2)(PCy3)2

Hydrogenation is an important method of chemical modification, which improves the physical, chemical, and thermal properties of diene elastomers. Natural rubber latex (NRL) can be quantitatively hydrogenated to provide a strictly alternating ethylene–propylene copolymer using a homogeneous osmium catalyst OsHCl(CO)(O₂)(PCy₃)₂. A detailed kinetic investigation was carried out by monitoring the amount of hydrogen consumption during the reaction using a gas‐uptake apparatus. The kinetic results of NRL hydrogenation indicated that this system had a second‐order dependence of the hydrogenation rate on hydrogen pressure and then decreased toward a zero‐order dependence for hydrogen pressures above 13.8 bar. The hydrogenation was also observed to be first‐order with respect to catalyst concentration and inverse first‐order on rubber concentration due to impurities present in the rubber latex. Additions of a controlled amount of acid demonstrated a beneficial effect on the hydrogenation rate of NRL. The temperature dependence of the hydrogenation rate was investigated and an apparent activation energy (over the range of 120–160°C) was calculated as 57.6 kJ/mol. Mechanistic aspects of this catalytic process are discussed on the basis of kinetic results. © 2006 Wiley Periodicals, Inc. J Appl Polym Sci 100: 640–655, 2006     

Asymmetric Hydrogenation Catalyzed by (S,S)‐R‐BisPast;‐Rh and (R,R)‐R‐MiniPHOS Complexes: Scope,Limitations, and Mechanism

A new class of chiral C₂‐symmetric bis(trialkyl)phosphine ligands has been prepared and used in Rh(I)‐catalyzed asymmetric hydrogenation reactions. The ligands, 1,2‐bis(alkylmethylphosphino)ethanes 1a‐g (abbreviated as BisP*, alkyl = t‐butyl, 1‐adamantyl, 1‐methylcyclohexyl, 1,1‐diethylpropyl, cyclopentyl, cyclohexyl, isopropyl) and 1,2‐bis(alkylmethylphosphino)methanes 2a‐d (abbreviated as MiniPHOS, alkyl = t‐butyl, cyclohexyl, isopropyl, phenyl) are prepared by a simple synthetic approach based on the air‐stable phosphine–boranes. These new ligands give the corresponding Rh(I) complexes, which are effective catalytic precursors for the asymmetric hydrogenation of a representative series of dehydroamino acids and itaconic acid derivatives. Enantioselectivities observed in these hydrogenations are universally high and in many cases exceed 99%. X‐Ray characterization of four precatalysts, study of the pressure effects, deuteration experiments, and characterization of the wide series of intermediates in the catalytic cycle are used for the discussion of the possible correlation between the structure of the catalysts and the outcome of the catalytic asymmetric hydrogenation.     

手性修饰催化剂在多相不对称氢化中的研究进展

手性修饰金属催化剂是最具发展潜力的多相不对称催化剂之一。本文综述了近年来三个具有代表性的多相不对称氢化反应体系的研究进展,即酒石酸修饰镍催化剂催化β-酮酯不对称加氢体系、金鸡纳生物碱修饰铂催化剂催化α-酮酯不对称加氢体系以及金鸡纳生物碱修饰钯催化剂催化C=C和C=N双键不对称加氢体系。概述了催化体系的影响因素,探讨了酒石酸及金鸡纳生物碱修饰型催化剂的手性识别机理模型。指出开发高效催化剂,修正或提出手性识别机理模型仍是今后多相不对称催化氢化反应研究的方向。     

旋光纯伊布利特合成工艺研究

分别采用催化还原法、转氢化法和催化氢化法三种方法对潜手性酮进行不对称还原．最后用LiAlH4对酰胺进行还原,合成了旋光纯伊布利特。产物结构通过FT-IR,1^H NMR和13^C NMR确证。     

Selective hydrogenation of nitriles to imines over a multifunctional heterogeneous Pt catalyst

Imines and their derivatives are versatile synthetic intermediates for the industrial preparation of both bulk and fine chemicals and for pharmaceuticals, but preparing these compounds efficiently through direct hydrogenation of nitriles are hindered by overhydrogenation to secondary amines. Here we report a highly efficient multifunctional catalyst system for selective hydrogenation coupling of nitriles to secondary imines using a heterogeneous Pt catalyst that was deposited on a nickel‐based metal‐organic framework (MOF) containing DABCO. The catalyst showed excellent synergy in promoting the hydrogenation of a variety of nitriles, giving significantly improved activity and selectivity (up to >99% yield) even under atmospheric pressure of H₂. It is suggested that the Lewis base (DABCO) sites on the Ni‐MOF inhibit further hydrogenation of the imines. The influence of H₂ pressure, reactant concentration, stirring speed, and reaction temperature was investigated. The kinetics and mechanism of hydrogenation of benzonitrile (BN) by the Pt/Ni‐MOF catalyst has been studied. The reaction showed a first‐order dependence on both BN concentration and H₂ pressure. A kinetic model was proposed based on the mechanism of nitriles hydrogenation and compared with experimental observations. © 2014 American Institute of Chemical Engineers AIChE J, 60: 3565–3576, 2014     

Ruthenium Phenylindenyl Complex as an Efficient Transfer Hydrogenation Catalyst

An efficient and green protocol for the transfer hydrogenation of carbonyl and imine compounds is presented. The transformations are catalysed by the inexpensive and easily synthesised complex [RuCl(PPh₃)(3‐phenylindenyl)]. Its catalytic activity was compared to that of the most commonly encountered ruthenium complexes in transfer hydrogenation reactions involving several protypical substrates.     

Formation of a new catalyst (Saechol) for coal hydrogenation on the surface of molybdenum alloys by catechol treatment

For the hydrogenation of Japanese Taiheiyo coal, a new catalyst, Saechol, formed on the surfaces of blades made from molybdenum-containing alloys such as SUS316, SCM3 and SKH9 showed significant activity. The activity survived in the flame but was lost easily by washing in 6N hydrochloric acid. The activity was easily regenerated. Several procedures for generation of activity are reported.     

载体酸性对Pt/USY菲加氢制烷基金刚烷的影响

以Pt为活性组分、经不同浓度草酸铝处理的USY分子筛为载体,制备了Pt/USY催化剂,并用于菲一步加氢饱和反应和加氢异构反应体系。由于金属活性位点Pt上易发生加氢反应,USY载体酸性位点上易发生异构反应和裂解反应,实验分别考察了Pt颗粒、载体的酸强度和酸量对菲转化率和产物分布的影响。结果表明,活性金属Pt颗粒尺寸及分散度直接影响菲加氢饱和产物分布;草酸处理后制备的催化剂Pt/0.05-USY、Pt/0.1-USY较未经酸处理的Pt/USY更利于菲加氢反应。全氢蒽是菲向目标产物烷基金刚烷转化的关键中间产物,异构产物烷基金刚烷生成需在USY分子筛Br?nsted酸位点完成;随着催化剂载体酸量和酸强度的降低,裂解反应程度迅速减弱;菲加氢反应最终产物以加氢饱和反应产物为主;使用Pt/0.1-USY催化剂异构反应产物烷基金刚烷收率为2.3%。     

Catalytic roles of iron and hydrogen sulphide on hydrogenation of coal

Washed Samla coal was hydrogenated in batches, with and without added sulphur in the presence and absence of hydrated iron oxide as a catalyst, for 3 h at 400 °C under 21.6 MPa hydrogen pressure. Further, hydrogenation of the same coal was studied with varying amounts of hydrated iron oxide in the presence of tar oil as vehicle, keeping the quantity of added sulphur unaltered, at 450 °C under 24.5 MPa pressure for 1.5 h. Comparative roles of iron and H₂S in the catalytic hydrogenation of coal are suggested from the experimental results.     

δ-癸内酯的合成研究

以环戊酮、正戊醛为原料,经羟醛缩合、氢化和氧化等三步反应合成了δ-癸内酯,在羟醛缩合中,采用了相转移催化技术;在催化加氢反应中,选用了几种离子交换树脂载钯催化剂来代替通常使用的５％Ｐｄ-Ｃ催化剂,最后以６５．５％的总产率合成了δ-癸内酯。