Single-site homogeneous and heterogeneized gold(III) hydrogenation catalysts: mechanistic implications

Au(III)-Schiff base complexes are active hydrogenation catalysts, giving turnover frequencies similar to those of the corresponding complexes of Pd(II), which has the same d8 electronic structure as Au(III). The mechanism of the reaction has been studied in detail by a combination of kinetic experiments and theoretical calculations. It is predicted and tested that the nature of the solvent plays a critical role for the heterolytic cleavage of H2 (controlling step). Taking this into account, and by properly selecting the nature of solid supports (polarity and proton-donating ability), it was possible to strongly increase the activity of the homogeneous Au(III) and Pd(II) catalysts by grafting them onto the surface.     

Efficient addition of alcohols, amines and phenol to unactivated alkenes by Au(III) or Pd(II) stabilized by CuCl2

The nucleophilic addition of alcohols, amines and phenol to unactivated alkenes catalyzed by cationic gold and palladium becomes limited due to the fast reduction into metallic gold under reaction conditions. The presence of CuCl2 retards the reduction of Au(III) and Pd", strongly increasing the turnover number of gold and palladium catalysts. It is shown that new Au(III)-CuCl2 and Pd(II)-CuCl2 catalysts are active and selective for the nucleophilic addition of alcohols, amines and phenol to unactivated alkenes.     

Synthesis of N-(2-pyridyl)indoles via Pd(II)-catalyzed oxidative coupling

Readily available Pd(II) chloride catalysts can catalyze selective and efficient oxidative coupling between N-aryl-2-aminopyridines and internal alkynes to yield N-(2-pyridyl)indoles. This process involves the ortho C-H activation of N-aryl-2-aminopyridines, and CuCl(2) was used as an oxidant. Compared to our previously reported Rh(III)-catalyzed synthesis of this class of product, this method is advantageous with a wider scope of alkynes and cost-effective Pd(II) catalysts. Molecular oxygen can be used as a terminal oxidant.     

汽车尾气净化反应的UBI-QEP法研究

应用单位键指标-二次指数势(UBI-QEP)方法对汽车尾气净化反应中氮氧化物的分解进行了理论分析.结果表明,NOx的分解的可能途径为氮氧化物的直接分解、CO还原助解和氮助解离.在富氧条件下,以CO助解为主.NO的解离存在N2O中间态.Ni与Rh一样,也是优秀的还原NOx催化剂,若能有效克服表面氧的共吸附,Ni-Cu可能是良好的汽车尾气净化催化剂的主体成份.     

The aerobic oxidation of a Pd(II) dimethyl complex leads to selective ethane elimination from a Pd(III) intermediate

Oxidation of the Pd(II) complex (N4)Pd(II)Me(2) (N4 = N,N'-di-tert-butyl-2,11-diaza[3.3](2,6)pyridinophane) with O(2) or ROOH (R = H, tert-butyl, cumyl) produces the Pd(III) species [(N4)Pd(III)Me(2)](+), followed by selective formation of ethane and the monomethyl complex (N4)Pd(II)Me(OH). Cyclic voltammetry studies and use of 5,5-dimethyl-1-pyrroline-N-oxide (DMPO) as a spin trap suggest an inner-sphere mechanism for (N4)Pd(II)Me(2) oxidation by O(2) to generate a Pd(III)-superoxide intermediate. In addition, reaction of (N4)Pd(II)Me(2) with cumene hydroperoxide involves a heterolytic O-O bond cleavage, implying a two-electron oxidation of the Pd(II) precursor and formation of a transient Pd(IV) intermediate. Mechanistic studies of the C-C bond formation steps and crossover experiments are consistent with a nonradical mechanism that involves methyl group transfer and transient formation of a Pd(IV) species. Moreover, the (N4)Pd(II)Me(OH) complex formed upon ethane elimination reacts with weakly acidic C-H bonds of acetone and terminal alkynes, leading to formation of a new Pd(II)-C bond. Overall, this study represents the first example of C-C bond formation upon aerobic oxidation of a Pd(II) dimethyl complex, with implications in the development of Pd catalysts for aerobic oxidative coupling of C-H bonds.     

Synthesis of N-Methyl-2-Thioimidazole Resin and Its Complex Behavior for Noble Metal Ions

The functional group capacity and the percentage of functional group conversion of crosslinked polystyrene resin bearing N-methyl-2-thioimidazole (MTIR) synthesized under optimum conditions are as high as 4.08 mmol/g resin and 96.0%, respectively. The apparent activation energies of sorption of MTIR for Au(III) and Pt(IV) are 13.1 and 13.4 kJ/mol, respectively. The sorption behavior of MTIR for Au(III), Pt(IV), and Pd(II) obeys the Freundlich and Langmuir isotherms. The sorption capacities of MTIR for Au(III), Pt(IV), and Pd(II) are as high as 4.33, 2.12, and 2.33 mmol/g resin, respectively. Au(III), Pt(IV), and Pd(II) adsorbed on MTIR can be eluted quantitatively by the eluant. The resin can be regenerated easily and reused without an obvious decrease in the sorption capacity for Au(III) and Pd(II). The resin has high sorption selectivity for noble metal ions. Au(III) can be separated quantitatively in the presence of high concentrations of Cu²⁺, Fe³⁺, Ni²⁺, and Mn²⁺. The recovery of platinum from the spent industrial catalysts is 98.6% by MTIR. The preconcentration and separation of palladium and platinum from the anode deposits of electrolysis of crude copper have been investigated. The resin may have potential industrial uses.     

Metal-catalyzed cycloetherification reactions of β,γ- and γ,δ-allendiols: chemo-, regio-, and stereocontrol in the synthesis of oxacycles

Versatile routes that lead to a variety of functionalized enantiopure tetrahydrofurans, dihydropyrans, and tetrahydrooxepines are based on chemo-, regio-, and stereocontrolled metal-catalyzed oxycyclization reactions of β,γ- and γ,δ-allendiols, which were readily prepared from (R)-2,3-O-isopropylideneglyceraldehyde. The application of Pd(II), Pt(II), Au(III), or La(III) salts as the catalysts gives controlled access to differently sized oxacycles in enantiopure form. Usually, chemoselective cyclization reactions occurred exclusively by attack of the secondary hydroxy group (except for the oxybromination of phenyl β,γ-allenic diols 3b and 3d) to an allenic carbon atom. Regio- and stereocontrol issues are mainly influenced by the nature of the metal catalysts and substituents.     

CO and C3H8 Total Oxidation over Pd Catalysts Supported on Commercial Ce-Zr Solid Solution: Effects of the Calcination Temperature and Hydrothermal Treatment

A series of Pd catalysts supported on commercial Ce-Zr solid solution(Pd/CZ) calcined at different temperatures(750, 900 and 1050 ℃) was prepared via an incipient wetness impregnation method. The activities of the fresh and hydrothermally aged Pd/CZ catalysts were tested for total oxidation of CO and C₃H₈. For CO oxidation, the activity of either fresh or aged Pd/CZ catalysts decreased with the elevating of calcination temperature of CZ support, with a fresh catalyst calcined at 750 ℃ possessing the highest activity and hydrothermal stability. For C₃H₈ total oxidation, the activity of Pd/CZ catalysts could be improved by increasing the calcination temperature of support. However, the aged Pd/CZ catalysts showed higher activity than corresponding fresh Pd/CZ catalysts. The turnover frequency(TOF) over Pd/CZ catalyst for CO oxidation increased with increasing reduction ability of the catalysts, with a fresh catalyst calcined at 750 ℃ having the highest value(0.27 s^-1). However, the TOF of Pd/CZ catalyst for C₃H₈ total oxidation was mainly affected by the size of Pd particles, and large Pd particles possessed a higher activity, with the highest TOF value(0.96 s^-1) obtained over an aged catalyst calcined at 1050 ℃.     

Synthesis and catalytic application of Pd complex catalysts: Atom‐efficient cross‐coupling of triarylbismuthines with haloarenes and acid chlorides under mild conditions

Palladium‐catalysed cross‐coupling reactions are some of the most frequently used synthetic tools for the construction of new carbon–carbon bonds in organic synthesis. In the work presented, Pd(II) complex catalysts were synthesized from palladium chloride and nitrogen donor ligands as the precursors. Infrared and ¹H NMR spectroscopic analyses showed that the palladium complexes were formed in the bidentate mode to the palladium centre. The resultant Pd(II) complexes were tested as catalysts for the coupling of organobismuth(III) compounds with aryl and acid halides leading to excellent yields with high turnover frequency values. The catalysts were stable under the reaction conditions and no degradation was noticed even at 150°C for one of the catalysts. The reaction proceeds via an aryl palladium complex formed by transmetallation reaction between catalyst and Ar₃Bi. The whole synthetic transformation has high atom economy as all three aryl groups attached to bismuth are efficiently transferred to the electrophilic partner.     

Hydrodechlorination of chlorobenzene over supported metal catalysts

The use of supported Pd catalysts, with low and high metal content, for the hydrodechlorination of chlorobenzene is presented in this article. Application of microwave irradiation during preparation of catalysts resulted in the synthesis of large Pd particles at moderate temperatures. The nature of the support played a key role in the formation of cationic Pd species. The extent of interaction of the Pd species with the support, the nature of metal precursor, particularly the residual chlorine on the surface were found to significantly affect the activity of the catalysts. In the case of bimetallic catalysts also microwave heating resulted in creation of bigger particles of Pd compared to those observed in conventionally heated catalysts. Besides, it minimized alloy formation as a result of which the activity of the catalysts in hydrodechlorination was found to be higher compared to that observed on conventionally prepared catalysts. Contrary to the general observation that low dispersed Pd catalysts are preferable for high stability, by means of the deposition-precipitation method adopted for catalyst preparation it was demonstrated that even highly dispersed (low Pd containing) catalysts can exhibit comparable activity and stability. An analysis of the nature of Pd species and its role in the stability of the catalysts is presented.IICT communication No. 051224     

Catalytic Performance of Carbon Materials Supported Pd Nanoparticles in Selective Hydrogenation of Acetylene

Pd/C catalysts were prepared by deposited Pd nanoparticles (NPs) on different carbon supports including activated carbon (AC), graphite oxide (GO), and reduced graphite oxide (rGO) using sol-immobilization method. Through transmission electron microscopy, powder X-ray di raction, and X-ray photoelectron spectroscopy, the role of the carbon supports for the catalytic performances of Pd/C catalysts was examined in selective hydrogenation of acetylene. The results indicate that Pd/AC exhibited higher activity and selectivity than Pd/GO and Pd/rGO in the gas phase selective hydrogenation of acetylene. Thermal and chemical treatment of AC supports also have some effect on the catalytic performance of Pd/AC catalysts. The differences in the activity and selectivity of various Pd/C catalysts were partly attributed to the metal-support interaction.     

Rapid formation of triarylphosphines by microwave-assisted transition metal-catalyzed C-p cross-coupling reactions

Rapid, direct transition metal-catalyzed C-P(III) cross-coupling reactions were performed by microwave dielectric heating, employing diphenylphosphine and aryl halides/triflates as substrates. Depending on the specific aryl halide/triflate precursor, the highest yields were obtained utilizing heterogeneous or homogeneous Pd or Ni catalysts in DMF or NMP in the presence of KOAc or DABCO as a base. [reaction: see text]     

聚苯胺对钯催化甲酸电氧化反应的促进作用

钯基纳米材料是甲酸电氧化反应的优良催化剂.本工作制备了两个系列钯基催化剂,并考察了聚苯胺对钯上甲酸电氧化反应的助催化作用.一种是以聚苯胺为基底,在其表面电沉积钯纳米粒子,制得nPANI/Pd催化剂(n表示聚合苯胺的循环数);另一种是直接在商业Pd/C催化剂表面电聚合苯胺,制得Pd/C/nPANI催化剂.结果显示,聚苯胺单独存在时对甲酸电氧化反应没有催化活性,但其可对钯上甲酸电氧化反应呈现明显的促进作用,且促进作用与聚苯胺的厚度(聚合循环数)密切相关.在两个系列催化剂中,15PANI/Pd和Pd/C/20PANI显示出最高的催化性能.15PANI/Pd中钯的质量比催化活性是纯钯催化剂的7.5倍; Pd/C/20PANI中钯的质量比催化活性和本征催化活性分别是商业Pd/C催化剂的2.3和3.3倍.钯催化性能的提升与聚苯胺和钯纳米粒子间的电子效应有关.     

金属蒸气法制备聚合物固载双金属催化剂———Pd-Cu催化剂的价态,分散度与活性

利用金属蒸气法制备了三种不同金属重量比的树脂固载及活性炭负载Ｐｄ Ｃｕ双金属催化剂．透射电镜（ＴＥＭ）和Ｘ 射线衍射（ＸＲＤ）测定结果表明催化剂中Ｐｄ Ｃｕ已形成合金．合金粒度极小，平均直径小于５ｎｍ．树脂固载催化剂金属粒度远小于活性炭负载催化剂的金属粒度．Ｘ 射线光电子能谱（ＸＰＳ）结果表明Ｐｄ和Ｃｕ均以零价态存在．在４ 甲基 ３ 戊烯 ２ 酮加氢反应中，树脂固载催化剂的活性和选择性均高于相应的活性炭负载催化剂     

贫燃/富燃循环气氛下原位活化Pd负载钙钛矿催化剂促进NOx还原消除

稀燃发动机通过提高空燃比来改善燃油经济性,减少CO2排放.但由于空燃比较高,稀燃发动机尾气中的NOx无法通过传统的三效催化技术有效消除.为了解决这一问题,适用于稀燃条件的NOx储存还原(NSR)技术得到了开发和应用.传统的NSR催化剂以贵金属Pt作为其氧化还原活性中心.Pt基催化剂具有较高的NOx消除活性,然而热稳定性...     

Development of liquid-liquid extraction and separation method for ruthenium(III) with 2-octylaminopyridine from succinate media: Analysis of catalysts

Ruthenium(III) has been efficiently extracted from 0.05 M sodium succinate at pH 9.5 by 2-octylaminopyridine in xylene and stripped with aqueous 10% (w/v) thiourea solution and determined spectrophotometrically. Various parameters viz., pH, weak acid concentration, reagent concentration, stripping agents, contact time, loading capacity, aq.: org. volume ratio, solvent has been thoroughly investigated for quantitative extraction of ruthenium(III). The utility of method was analyzed by separating the ruthenium(III) from binary mixture along with the base metals like Cu(II), Ag(I), Fe(II), Co(II), Bi(III), Zn(II), Ni(II), Se(IV), Te(IV), Al(III) and Hg(II) as well as platinum group metals (PGMs). Ruthenium(III) was also separated from ternary mixtures like Os(VIII), Pd(II); Pd(II), Pt(IV); Pd(II), Au(III); Pd(II), Cu(II); Fe(II), Cu(II); Ni(II), Cu(II); Co(II), Ni(II); Se(IV), Te(IV); Rh(III), Pd(II); Fe(III), Os(VIII). The stoichiometry 1: 2: 1 (metal: succinate: extractant) of the proposed complex was determined by slope analysis method by plotting graph of logD _[Ru(III)] versus logC _[2-OAP] and logD _[Ru(III)] versus logC _[succinate]. The interference of various cations and anions has been studied in detail and the statistical evaluations of the experimental results are reported. The method was successfully applied for the analysis of ruthenium in various catalysts, synthetic mixtures corresponding to the composition of alloys and minerals.     

高(111)晶面暴露的Pd纳米颗粒的制备与表征及其加氢性能

通过液相氢气还原法,在不同温度下制备出了不同（111）晶面占比的Pd单晶纳米颗粒,用活性炭吸附制备成Pd/C纳米催化剂。通过透射电子显微镜（TEM）、傅里叶变换（FFT）、X射线衍射（XRD）表征证实了低温下制备的Pd纳米颗粒具有较高的（111）晶面占比。氢氧脉冲滴定（H₂-O₂）和H₂-程序升温脱附（H₂-TPD）结果显示,上述催化剂表面吸附氢气量与其Pd（111）晶面占比呈线性关系。此外,该系列Pd/C催化剂具有相似的粒径4.3 nm以及较窄的尺寸分布,相近的孔隙参数和Pd负载量,从而可对比（111）晶面比例差异对其加氢性能的影响。3个探针反应（苯乙烯、环己烯和对硝基甲苯的加氢反应）的实验结果表明,相比于低（111）晶面暴露比例的Pd/C催化剂,含有高（111）晶面暴露比例的Pd/C催化剂显示出更高的加氢活性,且Pd（111）晶面比例与氢气消耗速率呈一定的线性关系,这归因于H₂优先吸附于Pd（111）晶面促进了活性氢原子的形成。基于以上分析,高（111）晶面暴露的Pd基催化剂有利于加氢性能的提高。     

溶剂化金属原子浸渍法制备高分散负载型催化剂——ⅩⅣ.Pd催化剂的表面组成及CO_2甲烷化催化性能

用元素分析、热脱附和H_2还原脱附等方法分析了Pd/γ-Al_2O_3、Pd/MgO、Pd/TiO_2溶剂化金属原子浸渍(SMAI)催化剂的表面组成和孔结构。结果表明Pd颗粒表面覆盖着一些有机碎片,这些碎片主要由C_1和少量C_2,C_3及C_3以上物种组成。SMAI催化剂的比表面积均高于相应纯载体的比表面积。而平均孔径均小于后者,CO_2甲烷化反应中,SMAI催化剂的活性均高于相应的普通浸渍法(CI)催化剂,而活化能却低于后者。在SMAI催化剂上CO_2甲烷化反应机理与Solymosi机理相同。     

Pd/PVP-MWCNTs电极对甲酸氧化的电催化性能

用聚乙烯吡咯烷酮（PVP）修饰的多壁碳纳米管（MWCNTs）作为Pd纳米粒子的载体,制得了Pd/PVP-MWCNTs催化剂并研究了其对甲酸氧化的电催化性能. 红外光谱仪（FTIR）和透射电镜（TEM）观测结果表明,Pd/PVP-MWCNTs催化剂中的Pd纳米粒子平均粒径小、分散性好. 因此,Pd/PVP-MWCNTs催化剂对甲酸电氧化有很好的电催化性能.     

双介孔硅基材料负载Pd催化剂上甲苯氧化性能的研究

催化氧化技术是挥发性有机物(VOCs)减排与控制的主流技术之一,其关键之处在于高效催化材料的研究与开发,负载型贵金属催化材料由于其低温下优越的VOCs催化氧化性能,受到国内外研究者的广泛关注.对于负载型催化剂而言,载体的性质直接影响活性相的分散,反应物和生成物的扩散与吸脱附,是影响负载型催化剂性能的主要因素.近年来,多级孔结构硅基材料由于具有多级的孔道结构、高比表面积和大的孔体积,逐渐成为VOCs催化氧化材料的研究热点.本文采用溶胶凝胶法和浸渍法制备了系列双介孔结构硅基材料负载Pd催化剂(Pd/BMS-x),通过控制合成过程中氨水的用量以调节催化剂的介孔结构分布. X射线衍射(XRD)结果表明,所合成的Pd/BMS-x催化剂在~2.0°的衍射峰,类似于MCM-41的(100)晶面衍射峰,表明所有的样品均具有有序的介孔结构. N2吸脱附实验表明所有样品的比表面积均高于1000m2/g,孔径分布表明Pd/BMS-30样品为单一介孔结构,而Pd/BMS-5~Pd/BMS-20样品具有2.64 nm以及18–45 nm范围内的双介孔结构,且Pd/BMS-15样品介孔分布较为集中. Pd/BMS-x催化剂上甲苯催化氧化性能测试表明,双介孔结构的Pd/BMS-5~Pd/BMS-20催化剂上甲苯催化氧化活性远高于单一介孔结构的Pd/BMS-30催化剂,表明载体结构对催化剂性能有重要影响.其中, Pd/BMS-15催化剂性能最佳(T90为228°C)且具有较强的稳定性,250°C条件下,反应持续60h催化剂未见明显失活. SEM和TEM结果表明, Pd/BMS-15催化剂中Pd高度分散于载体上,平均粒径在~3 nm左右.而Pd/BMS-30催化剂中Pd颗粒间有明显的团聚,平均粒径在8~17 nm之间.分散度测试表明,单一介孔结构的Pd/BMS-30催化剂, Pd分散度仅为27%,而双介孔结构Pd/BMS-5–Pd/BMS-20催化剂介于39%到69%,其中Pd/BMS-15催化剂中Pd分散度高达69%.与常规单一介孔MCM-41和MCM-48负载Pd催化剂相比,在低空速(42000 h–1)条件下, Pd/BMS-15催化剂上甲苯催化氧化性能与Pd/MCM-41和Pd/MCM-48催化剂相当.高空速(70000h–1)条件下, Pd/BMS-15催化剂的活性远高于单一介孔的Pd/MCM-41和Pd/MCM-48催化剂. Pd/BMS-15催化剂独特的双介孔结构,有利于活性相Pd的分散、反应物的扩散和传输,特别是在高空速条件下,有利于反应物与活性相的接触,提高了材料的氧化反应性能.进一步考察了材料的水热稳定性,将11 vol%的水蒸气引入到反应体系中,测试结果表明水蒸气的加入导致Pd/MCM-41和Pd/MCM-48催化剂的甲苯催化氧化性能显著下降,反应500 min后甲苯转化率分别从100%下降到76%和81%,而对于Pd/BMS-15催化剂,水蒸气的引入并未导致其活性明显下降,从而表明Pd/BMS-15催化材料具有较高的水热稳定性.