Metathesis of 1-butene and 2-butene to propene over Re2O7 supported on macro-mesoporous γ-alumina prepared via a dual template method

Macro-mesoporous γ-alumina support(MMA) was prepared by a sol-gel route in aqueous medium using pseudo-boehmite as aluminum source and polystyrene microspheres and Pluronic P123 as hard and soft dual templates,respectively.MMA had a BET specific surface area of about 259 m2 g-1,total pore volume of about 1.61 cm3 g-1,macropore diameter of about 102 nm,and mesopore diameter of about 14 nm.Re2O7/MMA and conventional Re2O7/Al2O3 were prepared by a incipient-wetness impregnation method,and their catalytic performances in the metathesis of 1-butene and 2-butene were tested in a fixed-bed tubular reactor.The result showed that Re2O7/MMA possessed higher activity and far longer working life-span than conventional Re2O7/Al2O3.     

胶溶法制备改性氧化铝的结构及织构特点

对胶溶法制备的镧和聚乙二醇(PEG)改性的氧化铝载体进行了深入研究.     

Role of support nature （γ-Al2O3 and SiO2-Al2O3） on the performances of rhenium oxide catalysts in the metathesis of ethylene and 2-pentene

The metathesis of ethylene and 2-pentene was studied as an alternative route for propylene production over Re2O7/γ-Al2O3 and Re2O7/SiO2-Al2O3 catalysts. Both NH3 temperature-programmed desorption (NH3-TPD) and H2 temperature-programmed reduction (H2-TPR) results showed that Re2O7/SiO2-Al2O3 exhibited stronger acidity and weaker metal-support interaction than Re2O7/γ-Al2O3. At 35 60℃, isomerization free metathesis was observed only over Re2O7/γ-Al2O3, suggesting that the formation of metal-carbene metathesis active sites required only weak acidity. Our results suggest that on the Re2O7/SiO2-Al2O3, hydrido-rhenium species ([Re]-H) were formed in addition to the metathesis active sites, resulting in the isomerization of the initial 1-butene product into 2-butenes. A subsequent secondary metathesis reaction between these 2-butenes and the excess ethylene could explain the enhanced yields of propylene observed. The results demonstrate the potential for high yield of propylene from alternative feedstocks.     

负载Ni金属有序介孔氧化铝催化剂的制备及表征

采用原位合成法和传统浸渍法以价格低廉的硝酸铝作为铝源, 聚乙二醇1540为模板剂, 硝酸镍为镍源, 制备出负载Ni金属有序介孔氧化铝催化剂, 并采用BET、TEM、XRD、TG多种测试技术对合成催化剂的物理化学性质和结构特征进行了表征. 实验结果表明, 两种方法均能制备出比表面积大(＞210 m2·g-1)、孔径分布窄(4 nm左右)的负载Ni金属介孔氧化铝催化剂. 与浸渍法相比, 原位合成法所制备的负载Ni金属有序介孔氧化铝镍离子与载体具有更强的相互作用力, 且孔结构具有一定的有序性.     

Effect of Re and Al 2 O 3 Promotion on the Working Stability of Cobalt Catalysts for the Fischer–Tropsch Synthesis

The results of the working stability studies of cobalt catalysts based on SiO2 and Al2O3 promoted with Re and Al2O3 in the synthesis of hydrocarbons from CO and H2 in continuous tests for 200–300 h are presented. The prepared catalysts were characterized by transmission electron spectroscopy, temperature-programmed reduction with hydrogen, temperature-programmed desorption of CO, and X-ray fluorescence spectroscopy and tested at a temperature 200°C, a pressure of 0.1 MPa, and a GHSV of 100 h–1. It was determined that a cobalt–silica catalyst promoted with Al2O3 had the highest activity. It was established that the addition of Al2O3 to a cobalt–silica catalyst increased the conversion of CO and selectivity for C5+ hydrocarbons and inhibited the agglomeration of Co particles under the action of a reaction atmosphere in the Fischer–Tropsch synthesis. It was found that the initial conversion of CO increased by a factor of 2 upon the introduction of 0.1 wt % rhenium into the Co/γ-Al2O3 catalyst; however, the rate of its deactivation increased in this case due to an almost twofold increase in the size of cobalt particles in the course of synthesis after operation for 300 h.     

Preparation of phosphorus-modified PITQ-13 catalysts and their performance in 1-butene catalytic cracking

A series of phosphorus-modified PITQ-13 catalysts was prepared by wet impregnation of NH4H2PO4 solution into an HITQ-13 parent. The catalysts were characterized using XRD, N2 adsorption, MAS NMR and NH3-TPD. Their catalytic performance in 1-butene catalytic cracking was evaluated in a fixed fluidized bed reactor. The results showed that the crystallinity, surface area and pore volume of P-modified PITQ-13 catalysts decreased with the increasing amounts of P. The number of weak acid sites increased, whereas that of strong acidity decreased. The selectivity to propylene in 1-butene cracking reactions increased because of the decrease in strong acidity. The yield of propylene achieved 41.6% over PITQ-13-2 catalyst with a P content of 1.0 wt%, which was 5.1% greater than that achieved over HITQ-13 catalyst.     

双功能催化剂催化CO2加氢制低碳烯烃反应中In2O3的尺寸效应

CO2催化加氢转化成高附加值化学品如低碳烯烃(C2=–C4=)等是减少碳排放的有效途径之一.采用金属氧化物/分子筛双功能催化剂可以实现CO2加氢直接高选择性合成C2+碳氢化合物.通常认为,金属氧化物组分可以活化CO2转化为甲醇等含氧中间体,该中间体在分子筛孔道内进一步转化为各种烃.氧化铟(In2O3)/SAPO-34双功能催化剂由于具有出色的催化CO2加氢制低碳烯烃反应性能而备受关注,然而,仍需进一步提升催化剂的催化性能以推动该反应的工业应用.目前,氧化物的结构与双功能催化剂性能之间的关系还不明确,这不利于其催化性能的改善.现有关于金属氧化物纳米粒子的尺寸(特别是小于23 nm)效应及其对双功能催化CO2加氢反应的活性和产物分布的影响的报道较少,对此深入理解将有利于设计更高性能的催化剂.本文采用沉淀法,通过控制焙烧温度得到了一系列尺寸为7～28 nm的立方相In2O3,通过多种表征手段探究了In2O3的尺寸对其结构与表面化学性质的影响.结果表明,随着In2O3晶粒尺寸的减小,其氧空位数目、CO2、H2与NH3吸附量以及Lewis较强酸性位比例均逐渐增加.在350oC,3 Mpa,9000 mL·gcat–1·h–1和H2/CO2比为3的反应条件下,研究了In2O3/SAPO-34双功能催化剂中In2O3粒径对其催化CO2加氢制低碳烯烃反应性能的影响.结果表明,随着双功能催化剂中In2O3尺寸的增大,低碳烯烃(尤其是丙烯)选择性、收率及烯烃与烷烃比例均先升高后降低,在尺寸为19 nm的In2O3上达到最大值,分别为76.9％、12.3 mmol goxide–1 h–1和4.8.较小尺寸的In2O3虽然具有较大的比表面积和更多的氧空位,并为CO2和H2的活化提供了更多的活性位,但小于19 nm的颗粒更容易烧结;In2O3的尺寸还会影响其与SAPO-34的协同效应,进而影响双功能催化剂的催化活性.此外,相对于其它尺寸的In2O3,19 nm的In2O3更有利于甲醇中间体的生成.因而19 nm In2O3耦合SAPO-34的双功能催化剂性能最好,其催化CO2转化率最高,为14.1％.综上,适中尺寸的In2O3能够促进In2O3/SAPO-34上CO2加氢制低碳烯烃反应.这些结果为通过平衡结构稳定性和催化性能来设计更有效的催化CO2转化的复合催化剂提供了理论指导.     

A Re(CO)5 fragment bonded to a polyhedral oligomeric hydroxysilsesquioxane as a model which gives further evidence to the existence of an unexpected Re(CO)5 surface species

Reaction of Re(CO)5O3SCF3 with (c-C6H11)7Si8O12O-Li+ at 273 K under a CO atmosphere affords the [Re(CO)5OR] (R = (c-C6H11)7Si8O12) derivative (1). 1 is the first example of a rhenium pentacarbonyl bearing an OR ligand (R = alkyl, aryl, or silyl) stable enough to be characterized, and it represents also the first molecular model of the surface [Re(CO)5OSi] species formed by reductive carbonylation of silica-supported [Re(CO)3OH]4. At room temperature, 1 loses one carbonyl ligand and dimerizes to afford {Re(CO)4[(mu-O)O12Si8(c-C6H11)7]}2 (2), which has been characterized by X-ray diffraction and is the first reported example of a rhenium tetracarbonyl mu-oxo-bridged dimer of the type [Re(CO)4(mu-OR)]2.     

Mild and efficient Re(VII)-catalyzed synthesis of 1,1-dihydroperoxides

Re2O7 in CH3CN is a remarkably efficient and mild catalyst for the peroxyacetalization of ketones, aldehydes, or acetals by H2O2 to generate 1,1-dihydroperoxides. Me3SiOReO3 and methyl rhenium trioxide (MTO) are also effective catalysts under these reaction conditions.     

金属羰基络合物制备的Pt-Re/Al_2O_3催化剂的性能 Ⅰ.不同方法制备的Pt-Re/Al_2O_3催化剂上正庚烷的转化

考察了由[Pt_3(CO)_6]_5[NEt_4]_2与Re_2(CO)_(10)共浸或分浸制备的一系列催化剂在接近工业运转的压力下的正庚烷转化反应。以羰基金属原子簇化合物作为前身物制备的Pt-Re/Al_2O_3催化剂的活性、芳构化选择性和稳定性等明显地优于常规的以H_2PtCl_6与HReO_4溶液共浸制备的催化剂。常规Pt-Re/Al_2O_3催化剂的活性和稳定性比Pt/Al_2O_3好,但芳构化选择性降低,若引入Re_2(CO)_(10),则其催化活性、芳构化选择性和稳定性均显著提高。不同方法制备的Pt-Re/Al_2O_3催化剂的活性和稳定性的变化趋势为Pt_5Re_2>Pt_5 Re_2>Pt Re_2>PtRe,表明Pt,Re之间存在相互作用程度的差异。     

氮、磷、碳化物比较研究初探

环保法规的日益严格使得研究者越来越重视新型加氢脱硫、脱氮催化剂的开发。国内外学者在对负载型Mo—Co、Mo—Ni和W—Ni等传统硫化物催化剂进行不断改进的同时，新型催化材料尤其是具有贵金属性质的过渡金属间充化合物一氮化物、碳化物和磷化物的研究也受到很大的关注。人们在探索不同的载体或者是不同的助剂对单金属间充化合物-氮化物、碳化物或磷化物催化剂活性组分的表面状态和结构以及其深度加氢脱硫脱氮性能的影响，而对同一载体负载的氮、磷、碳化物催化剂缺乏横向的比较。本研究制备了以γ-Al2O3为载体的负载型氮化钼、磷化钼和碳化钼催化剂，比较了它们的孔结构、比表面积，并初步分析了钼的质量分数为19％，氮化、磷化和碳化温度均为650℃时三类催化剂的二苯并噻吩加氢脱硫性能。     

Preparation of phosphorus-modified PITQ-13 catalysts and their performance in 1-butene catalytic cracking

A series of phosphorus-modified PITQ-13 catalysts was prepared by wet impregnation of NH₄H₂PO₄ solution into an HITQ-13 parent. The catalysts were characterized using XRD, N₂ adsorption, MAS NMR and NH₃-TPD. Their catalytic performance in 1-butene catalytic cracking was evaluated in a fixed fluidized bed reactor. The results showed that the crystallinity, surface area and pore volume of P-modified PITQ-13 catalysts decreased with the increasing amounts of P. The number of weak acid sites increased, whereas that of strong acidity decreased. The selectivity to propylene in 1-butene cracking reactions increased because of the decrease in strong acidity. The yield of propylene achieved 41.6% over PITQ-13-2 catalyst with a P content of 1.0 wt%, which was 5.1% greater than that achieved over HITQ-13 catalyst.     

溶胶-凝胶法制备钯催化剂的织构与性能

采用溶胶-凝胶法制备了Pd/Al2O3催化剂，用LLS(激光光散射)、XRD和BET等技术考察了溶液pH值对所成胶体粒子流体力学半径、相应催化剂产品孔径分布及热稳定性的影响.研究发现，由pH=4.1的胶体制备的催化剂具有良好的热稳定性和CO、C3H6的氧化活性.氧化镧添加剂可抑制Al2O3载体在高温下由γ相向α相的转化，同时也促进了催化剂上Pd粒子的生长. La2O3可提高新鲜Pd催化剂的氧化活性，但对老化后催化剂活性的提高无促进作用.     

An easily accessible Re-based catalyst for the selective conversion of methanol: evidence for an unprecedented active site structure through combined operando techniques

Heterogeneous Re/SiO(2) catalysts prepared using a one pot sol-gel synthesis were found to display high activity in the direct, selective methanol conversion to methylal, which is correlated to an unprecedented rhenium oxide structure.     

Processes of synthesis of 1-butene from 2-butene by the positional isomerization on sulfocation exchangers

Obtaining of individual 1-butene and 2-butenes from the butane-butene fractions can be processed sufficiently effectively by combining positional isomerization of alkenes on the sulfocation exchanger catalysts and careful rectification. At 50–60°C is reached the equilibrium with the ratio of the sum of 2-butenes to 1-butene ～20:1. The relatively high-boiling 2-butenes are enough completely separated by rectification of 1-butene, and isobutane from the harmful impurities (butadiene and isobutene). The reverse isomerization of the purified 2-butene into 1-butene with the continuous distillation of the latter makes it possible to obtain pure 1-butene with a very low prime cost.     

以无机铝盐为前驱体用溶胶凝胶法合成中孔氧化铝

以水合硝酸铝(Al(NO3)3·9H2O)为前驱体, 通过乙醇介质中环氧丙烷的开环反应促使形成了透明的块状氧化铝凝胶. 凝胶在常压下干燥并于700 ℃焙烧后得到中孔无定型氧化铝. 通过改变环氧丙烷的加入量实现了氧化铝孔径和孔体积等宏观结构性能的调节. 用扫描电镜(SEM)、傅立叶变换红外光谱(FI-IR)和差热分析(DTA)等方法对样品进行了表征. 由于合成中存在环氧丙烷开环产物作为液体模板剂的造孔作用, 在氧化铝凝胶中造成了孔分布曲线具有双峰分布的墨水瓶状孔. 反应过程中pH值的测定和红外光谱的表征结果都证明环氧丙烷是一种很好的质子消耗剂, 其开环促使铝离子水解聚合并形成凝胶网络结构. 同时根据表征结果对环氧丙烷参与的溶胶凝胶氧化铝的合成机理进行了探讨.     

Electrochemical synthesis, structural characterization, and decomposition of rhenium oxoethoxide, Re4O4(OEt)12. Ligand influence on the structure and bonding in the high-valent tetranuclear planar rhenium alkoxide clusters

Anodic oxidation of rhenium in ethanol in the presence of LiCl as a conductive additive results with high yield in formation of a new oxoethoxide cluster, Re(4)O(4)(OEt)(12). The structure of the planar centrosymmetric metal-oxygen core of this molecule is composed of four edge-sharing Re(V)O(6) octahedra. Eight electrons are available for the formation of metal-metal bonds indicated by five relatively short Re-Re distances within the Re 4-rhombus, a "planar butterfly" type cluster. The theoretical calculations are indicating relatively low contribution of metal-metal bonding in the stability of the core. The stability of the +V-oxidation state, unusual for rhenium alkoxides can be at least partially attributed to the size effects in the packing of ligands. The X-ray powder study indicates that treatment of Re(4)O(4)(OEt)(12). in ambient atmosphere rapidly transforms it into a mixed-valence derivative Re(4)O(6)(OEt)(10) with a structure related to the earlier investigated cluster Re(4)O(6)(O(i)Pr)(10). Thermal decomposition of the latter rhenium oxoethoxide results in reduction to rhenium metal at as low temperatures as 380 degrees C, producing aggregates of metal nanoparticles with the average size of 3 nm.     

高效钼基催化剂上正丁烯自歧化生成乙烯和己烯（英文）

烯烃歧化反应(又称烯烃复分解反应)是两分子烯烃通过碳-碳键断裂重排生成新烯烃分子的反应,自1964年Phillips公司的Banks等发现以来,引起了研究者的广泛关注,且在均相催化体系的发展尤为迅速;与此同时,多相烯烃歧化催化剂因其在分离简单、可循环再生利用方面的优势而在工业界崭露锋芒.多相烯烃歧化催化剂通常由活性金属组分(Re,Mo,W)分散到大比表面积的多孔载体制备而成.多相催化剂上烯烃歧化反应主要集中在乙烯和2-丁烯反歧化制丙烯反应,其中WO_3/SiO_2催化剂先后应用于Phillips公司的Triolefin Process和ABB Lummus公司的OCT工艺,低温Re系催化剂被法国石油研究院应用到Meta-4歧化工艺.同时丙烯歧化也是研究最多的反应,多数情况下被用作探针反应来研究催化剂的性能.烯烃歧化反应可以根据市场需求灵活调变产物分布,为碳四烃类的高效转化利用提供很好的途径.受国内拉动内需的政策及下游应用行业强劲需求的影响,中国液化石油气的产量逐年递增.2014年我国液化气产量约为2550万吨,其中仅有39%左右用于碳四深加工,大部分当做燃料直接烧掉.从组成来看,液化气中烯烃含量在40%-50%,可以转化为高附加值的乙烯和丙烯进一步利用.本文重点开发了一条从1-丁烯出发生产乙烯/己烯的反应路线及对应的催化剂.首先从热力学角度分析了碳四歧化反应网络中各反应路径发生的难易程度.在此基础上,以Mo/Al_2O_3为催化剂考察了Mo负载量和反应条件对产物分布的影响-.在优化的6Mo/Al_2O_3催化剂上,80°C,1.0 MPa和丁烯空速3 h1的条件下,产物中乙烯和己烯的摩尔选择性超过85%,并且在48 h内保持良好的反应稳定性.为了进一步探究催化剂结构与反应性能的关系,系统考察了催化剂载体差异对Mo物种状态和反应性能的影响.借助N2吸附,NH_3-TPD,Py-IR,H_2-TPR,UV-Vis和HRTEM等表征手段,发现催化剂反应活性与其酸密度直接相关.催化剂酸量越大,丁烯转化率越高,但副反应越多;载体适宜的酸量和较大的比表面积更有利于钼物种的分散和四配位钼物种的形成,促进目标1-丁烯自歧化制乙烯/己烯反应的发生.     

Rhenium/rhenium oxide nanoparticles production using femtosecond pulsed laser ablation in liquid

In this study, rhenium/rhenium oxide nanoparticles (Re / ReO₃ NPs) have been produced for the first time in ultrapure water by using Femtosecond Pulsed Laser Ablation in Liquid (fsPLAL) method. X-Ray Diffraction (XRD) measurements and results obtained for NPs show the existence of well-crystallized peaks and preferred phases. Re NPs have hexagonal structure while ReO₃ NPs have the perovskite-like cubic crystal structures. The Re / ReO₃ ratio is also determined to be 53 / 47 with ~ 20 nm crystallite size, while pure ReO₃ crystallite sizes were measured to be ~ 25 nm. The TEM results have shown that the produced particles have a spherical shape, and particle sizes changes between ~ 20 nm and ~ 60 nm. The crystallite size is similar due to XRD results. Obtained nanoparticles exhibit promising applications for photonic devices with broad bandgap values which have measured to be 4.71 eV for Re / ReO₃ NPs mixture and 4.36 eV for pure ReO₃ NPs.     

Polystyrene‐Supported (Catecholato)oxorhenium Complexes: Catalysts for Alcohol Oxidation with DMSO and for Deoxygenation of Epoxides to Alkenes with Triphenylphosphine

Polymer‐supported catalysts offer practical advantages for organic synthesis, such as improved product isolation, ease of catalyst recycling, and compatibility with parallel solution‐phase techniques. We have developed the (carboxypolystyrene‐catecholato)rhenium catalyst 2 derived from tyramine (=4‐(2‐aminoethyl)phenol), which is effective for alcohol oxidation with dimethylsulfoxide (DMSO) and for epoxide deoxygenation with triphenylphosphine. The supported [Re(catecholato)]catalyst 2 is air‐ and moisture‐stable and can be recovered and used repeatedly without decreasing activity. The procedures work with non‐halogenated solvents (toluene). DMSO for Re‐catalyzed alcohol oxidation is inexpensive and safer for transport and storage than commonly used peroxide reagents. The oxidation procedure was best suited for aliphatic alcohols, and the mild conditions were compatible with unprotected functional groups, such as those of alkenes, phenols, nitro compounds, and ketones (see Tables 1 and 2). Selective oxidation of secondary alcohols in the presence of primary alcohols was possible, and with longer reaction time, primary alcohols were converted to aldehydes without overoxidation. Epoxides (oxirans) were catalytically deoxygenated to alkenes with this catalyst and Ph₃P (see Table 3). Alkyloxiranes were converted to the alkenes with retention of configuration, while partial isomerization was observed in the deoxygenation of cis‐stilbene oxide ( cis‐1,2‐diphenyloxirane). These studies indicate that supported [Re(catecholato)] complexes are effective catalysts for O‐atom‐transfer reactions, and are well suited for applications in organic synthesis.