不同催化体系下腈的水合反应研究进展

腈可用于构建新的碳-碳、碳-杂原子键,所得产物丰富多样.酰胺基团广泛存在于医药、农药和天然产物中,此外,酰胺还是有机合成反应中重要的中间体.在目前报道的酰胺类化合物的合成方法中,腈的水合反应已成为学术界和工业界最广泛使用的获得初级酰胺类化合物的方法之一.早期腈的水合反应中通常涉及强酸、强碱的使用,但在该类反应体系下,往...     

甲苯类化合物的选择性氧化

综述了以O2为清洁氧源甲苯类化合物的气相和液相选择性氧化.甲苯类化合物的气相选择性氧化中主要介绍了金属氧化物、分子筛和负载型催化剂并对影响催化剂活性和选择性的因素进行了分析;甲苯类化合物的液相选择性氧化中重点介绍了MC (mid-century)催化体系及其反应机理方面的研究进展,并特别介绍了仿生催化在甲苯类化合物催化氧化中的应用.对各催化氧化体系的应用前景进行了展望.     

甲苯类化合物的选择性氧化

综述了以O2为清洁氧源甲苯类化合物的气相和液相选择性氧化.甲苯类化合物的气相选择性氧化中主要介绍了金属氧化物、分子筛和负载型催化剂并对影响催化剂活性和选择性的因素进行了分析;甲苯类化合物的液相选择性氧化中重点介绍了MC (mid-century)催化体系及其反应机理方面的研究进展,并特别介绍了仿生催化在甲苯类化合物催化氧化中的应用.对各催化氧化体系的应用前景进行了展望.     

有机碲氧化物催化合成α,β-不饱和腈,腈酯和腈酰胺

本文报道了应用双对-甲氧苯基氧化碲(BMPTO)催化合成α,β-不饱和腈,腈酯和腈酰胺的简便方法。收率73～97％。反应具有较好的立体选择性,所有产物经熔点、IR、~1H NMR证实为E-型异构体。     

甲苯类化合物的选择性氧化

综述了以O2为清洁氧源甲苯类化合物的气相和液相选择性氧化。甲苯类化合物的气相选择性氧化中主要介绍了金属氧化物、分子筛和负载型催化剂并对影响催化剂活性和选择性的因素进行了分析;甲苯类化合物的液相选择性氧化中重点介绍了MC(mid-century)催化体系及其反应机理方面的研究进展,并特别介绍了仿生催化在甲苯类化合物催化氧化中的应用。对各催化氧化体系的应用前景进行了展望。     

含三元环腈的生物转化反应与应用*

腈的对映选择性生物转化反应是合成高光学活性羧酸及其酰胺衍生物的有力手段。 本文介绍了在红球菌AJ270催化下,一系列含三元环结构的腈,包括环丙腈、环氧丙腈和氮杂环丙腈的生物转化反应。提出了腈水合酶和酰胺水解酶酶活中心的假设,即腈水合酶可能位于比较疏散的立体空间环境中,而酰胺水解酶则处于相对深埋的位置且空间大小有限。另外本文还探讨了腈的生物催化反应在天然产物及生物活性分子合成中的应用。     

有机合成中腈的去对称化生物转化反应研究进展

腈的化学水合和水解具有反应条件苛刻、低选择性等缺点,与之相反,腈的去对称化生物转化反应具有反应条件温和、高效、高选择性以及理论产率可达100%的优点,已成为合成对映体纯多官能化羧酸和酰胺的最有效方法之一.将分别从前手性戊二腈、前手性丙二腈、内消旋环状二腈以及其他类底物出发,简单综述腈类化合物的去对称化生物转化反应及其在有机合成中的应用进展,并对各类反应的条件、选择性以及规律机制进行讨论和总结.     

微波辐射I2／Al2O3催化合成腈类化合物

微波辐射下,I2/Al2O3催化芳香醛和盐酸羟氨的无溶剂反应.一锅法合成了腈类化合物,产率80%～99%.     

亚砜及亚磺酰胺类配体催化不对称反应的新进展

亚砜及亚磺酰胺类化合物作为手性配体催化不对称反应是目前研究最为活跃的领域之一,苯环骨架以及链状骨架的亚砜及亚磺酰胺类手性配体相继成功地用于不对称反应中.主要综述了近年来含亚砜及亚磺酰胺类的手性配体催化不对称反应的研究进展.     

Lewis碱催化的α-胺基腈及氰醇的烯丙基官能团化反应研究及应用

对我们研究小组近几年在Lewis碱催化具有α-位氢的α-胺基腈类及氰醇类化合物与Morita-Baylis-Hillman(MBH)加合物立体选择性的烯丙基化反应方面取得的初步成果进行了小结.通过与MBH加合物的烯丙基取代反应,有效地构建了具有α-位季碳结构单元的多官能团腈类衍生物,而且基于此发展了一类非金属催化的烯烃分子内氰官能团化反应,构建了β-位有季碳结构单元的官能团化的腈类化合物.此外对影响反应的可能因素也做了讨论,提出了可能的反应机理.     

气相氨氧化2-甲基吡嗪制备2-氰基吡嗪研究进展

综述了近年来国内外有关氮氧化2-甲基吡嗪合成2-氰基吡嗪反应的研究进展,讨论了催化剂及各种反应条件对活性的影响,分析了反应历程和机理。含钒和含钼氧化物催化剂具有较好的催化活性,原料中适量的氧气和氮气有利于反应活性的提高,2-甲基吡嗪转化率和2-氰基吡嗪选择性随着温度提高而增加,但温度过高使选择性降低,一般选取350～430℃。     

STUDY OF MnOx-PROMOTED Cu/|?-Al2O3 CATALYSTS FOR HYDROGENATION OF CARBON MONOXIDE

|?-Alumina-supported copper-manganese oxide was prepared by impregnation and used for carbon monoxide hydrogenation. The Cu-MnOx/Al2O3 catalysts exhibit high catalytic activity in CO hydrogenation, showing markedly enhanced catalytic activities due to the synergistic interaction between the copper and manganese oxide. The results of XRD indicated that the addition of manganese enhances the dispersion of CuO, retards the reduction of CuO and enhances the ability of H2-adsorption, which contribute to the activity of DME synthesis from syngas.     

In situ Raman studies during sulfidation, and operando Raman-GC during ammoxidation reaction using nickel-containing catalysts: a valuable tool to identify the transformations of catalytic species

Ni-containing catalysts are investigated under reaction conditions for two different cases, during sulfidation, with Ni-Mo based catalysts, and during ammoxidation reaction, with the Ni-Nb catalysts. It is shown how Raman spectroscopy can follow some of the transformations of these catalysts upon different treatments. For the NiMo/Al(2)O(3)-SiO(2) system it was possible to identify some of the sulfided Mo species formed during the sulfidation of the oxide precursors, while for the bulk Ni-Nb oxide catalysts the simultaneous reaction-Raman results strongly suggest that the incipient interaction between niobium and nickel oxides at low Nb/Ni atomic ratios is directly related to catalytic activity, and that a larger size well-defined NiNb(2)O(6) mixed oxide phase is not active for this reaction. Moreover, the promotion by niobium doping appears to be limited to a moderate niobium loading. It was found that in situ and operando Raman are valuable techniques that allowed the identification of active Mo-S and Ni-Nb species under reaction conditions, and that are not stable under air atmospheres.     

An anomalous hydration/dehydration sequence for the mild generation of a nitrile oxide

A nitrile oxide containing a carbamoyl group is readily generated upon the treatment of 2-methyl-4-nitro-3-isoxazolin-5(2H)-one with water under mild reaction conditions, even in the absence of special reagents. The obtained nitrile oxide undergoes cycloaddition with dipolarophiles, alkynes and alkenes, to afford the corresponding isoxazol(in)es, which are useful intermediates in the synthesis of polyfunctionalized compounds. A plausible mechanism underlying the formation of the nitrile oxide is proposed, which involves an anomalous hydration/dehydration sequence. DFT calculations were also performed to support this mechanism.     

Structure and oxidation state of silica-supported manganese oxide catalysts and reactivity for acetone oxidation with ozone

Silica-supported manganese oxide catalysts with loadings of 3, 10, 15, and 20 wt % (as MnO2) were characterized with use of X-ray absorption spectroscopy and X-ray diffraction (XRD). The edge positions in the X-ray absorption spectra indicated that the oxidation state for the manganese decreased with increasing metal oxide loading from a value close to that of Mn2O3 (+3) to a value close to that of Mn3O4 (+2(2)/3). The XRD was consistent with these results as the diffractograms for the supported catalysts of higher manganese oxide loading matched those of a Mn3O4 reference. The reactivity of the silica-supported manganese oxide catalysts in acetone oxidation with ozone as an oxidant was studied over the temperature range of 300 to 600 K. Both oxygen and ozone produced mainly CO2 as the product of oxidation, but in the case of ozone the reaction temperature and activation energy were significantly reduced. The effect of metal oxide loading was investigated, and the activity for acetone oxidation was greater for a 10 wt % MnOx/SiO2 catalyst sample compared to a 3 wt % MnOx/SiO2 sample.     

Preparation,Solid‐state Characteristics,and Catalytic Properties of Promoted Vanadium Phosphate Materials

The syntheses of transition metal promoted (M = Co, Cr, Fe, Mo) supported vanadium phosphate (VPO) catalysts (TiO₂ (anatase), γ‐Al₂O₃) and their characterization by N₂‐adsorption, X‐ray diffractometry (XRD), FTIR‐spectroscopy and determination of V‐valence state is reported. The catalytic properties were checked in the heterogeneous catalytic ammoxidation of 2, 6‐dichlorotoluene to the corresponding nitrile. The catalyst samples were prepared by synthesis of the precursor compound VOHPO₄ · 0.5 H₂O, impregnation using various metal salt solutions and mixing with the support materials. The characterization revealed increased surface areas for all the promoted samples in comparison to the basic materials. XRD showed the formation of (VO)₂P₂O₇ after calcinations as well as patterns of support materials (anatase, γ‐Al₂O₃). The formation of crystalline proportions of mixed oxides were not observed. The catalytic ammoxidation runs revealed a significant effect of the promoter metals on the catalytic properties by an increase of yield by ca. 20 % compared to bulk VPO. Almost complete conversion of 2, 6‐dichlorotoluene and 81 % yield of nitrile were observed using a 25 %VPCoO/γ‐Al₂O₃ catalyst.     

Screening of MgO——and Ce02-Based Catalysts for Carbon Dioxide Oxidative Coupling of Methane to C2＋ Hydrocarbons

The catalyst screening tests for carbon dioxide oxidative coupling of methane (CO2-OCM)have been investigated over ternary and binary metal oxide catalysts.The catalysts are prepared by doping MgO-and CeO2-based solids with oxides from alkali(Li2O),alkaline earth (CaO),and transition metal groups (WO3 or MnO).The presence of the peroxide (O2^2-)active sites on the Li2O2,revealed by Raman spectroscopy,may be the key factor in the enhanced performance of some of the Li2O/MgO catalysts.The high reducibility of the CeO2 catalyst,an important factor in the CO2-OCM catalyst activity,may be enhanced by the presence of manganese oxide species. The manganese oxide species increases oxygen mobitity and oxygen vacancies in the CeO2 catalyst.raman and Fourier Transform Infra Red (FT-IR)spectroscopies revealed the presence of lattice vibrations of metal-oxygen bondings and active sites in which the peaks carresponding to the buld crystalline structures of Li2O,CaO,WO2 and MnO are detected.The performance of 5%MnO/15?O/CeO2 catalyst is the most potential among the CeO2-based catalysts,although lower than the 2%Li2O/MgO catalyst.The 2%Li2O/MgO catalyst showed the most promising C2 hydrocarbons selectivity and yield at 98.0%and 5.7%,respectively.     

Screening of MgO- and CeO_2-Based Catalysts for Carbon Dioxide Oxidative Coupling of Methane to C_(2+) Hydrocarbons

The catalyst screening tests for carbon dioxide oxidative coupling of methane (CO2-OCM) have been investigated over ternary and binary metal oxide catalysts. The catalysts are prepared by doping MgO- and CeO2-based solids with oxides from alkali (Li2O), alkaline earth (CaO), and transition metal groups (WO3 or MnO). The presence of the peroxide (O2-2) active sites on the Li2O2, revealed by Raman spectroscopy, may be the key factor in the enhanced performance of some of the Li2O/MgO catalysts. The high reducibility of the CeO2 catalyst, an important factor in the CO2-OCM catalyst activity, may     

焙烧温度对Fe-Mn催化剂结构和F-T合成性能影响

研究了焙烧温度对Fischer-Tropsch(F-T)合成Fe-Mn催化剂的织构性质、还原行为以及在还原和反应过程中结构变化的影响；在H2/CO=2.0、260 ℃、2.5 MPa和1 000 h－1条件下在固定床反应器上考察了焙烧温度对Fe-Mn催化剂F-T合成反应活性、烃产物选择性和运行稳定性的影响。XRD和TPR结果表明，随着焙烧温度的升高，催化剂中α-Fe2O3晶粒增大，催化剂比表面积降低，促进Mn3+渗入α-Fe2O3晶格中，形成了铁锰固溶体物相，使得催化剂难于还原，当焙烧温度升高到700 ℃时，催化剂中的α-Mn2O3相完全消失。催化剂F-T合成反应评价表明，在不降低催化剂活性的同时，焙烧温度的升高可显著地提高催化剂的反应运行稳定性，并促使烃产物分布向高碳数方向偏移；600 ℃焙烧的Fe-Mn催化剂运行200 h，总体活性高，失活速率较低，对低碳烯烃和中间馏分油段产物选择性好。     

Characterization and Activity of Cu‐MnOx/γ‐Al2O3 Catalyst for Hydrogenation of Carbon Dioxide

The effect of manganese on the dispersion, reduction behavior and active states of surface of supported copper oxide catalysts have been investigated by XRD, temperature‐programmed reduction and XPS. The activity of methanol synthesis from CO₂/H₂ was also investigated. The catalytic activity over CuO‐MnO_x/γ‐Al₂O₃ catalyst for CO₂ hydrogenation is higher than that of CuO/γ‐Al₂O₃. The adding of manganese is beneficial in enhancing the dispersion of the supported copper oxide and make the TPR peak of the CuO‐MnK_x/γ‐Al₂O₃ catalyst different from the individual supported copper and manganese oxide catalysts, which indicates that there exists strong interaction between the copper and manganese oxide. For the CuO/γ‐Al₂O₃ catalyst there are two reducible copper oxide species; α and β peaks are attributed to the reduction of highly dispersed copper oxide species and bulk CuO species, respectively. For the CuO‐MnO_x/γ‐Al₂O₃ catalyst, four reduction peaks are observed, α peak is attributed to the dispersed copper oxide species; β peak is ascribed to the bulk CuO; γ peak is attributed to the reduction of high dispersed CuO interacting with manganese; δ peak may be the reduction of the manganese oxide interacting with copper oxide. XPS results show that Cu⁺ mostly existed on the working surface of the Cu‐Mn/γ‐Al₂O₃ catalysts. The activity was promoted by Cu with positive charge which was formed by means of long path exchange function between Cu? O? Mn. These results indicate that there is synergistic interaction between the copper and manganese oxide, which is responsible for the high activity of CO₂ hydrogenation.