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金属基化合物在锂硫电池正极中的应用

金属基化合物在锂硫电池正极中的应用

金属基化合物在锂硫电池正极中的应用摘要:作为具有高比容量和能量密度的锂离子电池,锂硫电池存在导电率低、多硫化锂的穿梭效应等问题,本文总结了金属基化合物吸附、催化改善锂硫电池正极性能的几种材料:单原子过渡金属、金属氧化物、金属碳化物、金属氮化物、金属硫化物、金属有机框架。

关键词:锂硫电池金属吸附催化Application of metal based materials for lithium-sulfur batteries cathodeAbstract: As lithium-ion battery with high specific capacity and energy density, lithium-sulfur batteries have problems such as low conductivity and the shuttle effect of lithium polysulfides. Thispaper summarizes several materials for the adsorption and catalysis of metal-based compounds to improve the cathode performance of lithium-sulfur batteries: Single-atom transition metals, metal oxides, metal carbides, metal nitrides, metal sulfides, metal-organic frameworks.Keywords: lithium-sulfurbattery metal adsorption catalysis锂硫电池由于具有较高的比容量和能量密度(分别为1675mAh g-1和 2670Wh kg-1)而受到关注,然而,锂硫电池的实际应用和商业化存在诸多障碍,包括硫和硫化锂的绝缘性、硫正极充放电过程中的体积变化、多硫化锂(LiPSs)的穿梭效应和缓慢转化反应动力学等。

acs catalysis 模板 -回复

acs catalysis 模板 -回复

acs catalysis 模板-回复A Review on the Role of Catalysis in Solid Acid Materials [ACS Catalysis Template]Introduction:Catalysis plays a crucial role in numerous chemical processes, enabling the conversion of reactants into desired products in an efficient and sustainable manner. In recent years, solid acid materials have emerged as a promising class of catalysts due to their unique properties and wide range of applications. This review aims to provide a comprehensive overview of the role of catalysis in solid acid materials, highlighting their structure, properties, and applications in various reactions.I. Structure and Properties of Solid Acid Materials:Solid acid materials are characterized by their ability to donate protons, acting as acidic sites for catalytic reactions. These materials can be categorized into two major classes: inorganic solids and organic polymers. Inorganic solids, such as zeolites, metal oxides, and heteropoly acids, possess high thermal stability and well-defined structures with ordered arrays of acidic sites. Organic polymers, on the other hand, offer tunable acidity andstructural flexibility due to the presence of acidic functional groups.II. Acid-base Interactions in Solid Acid Catalysis:The acid-base interactions in solid acid catalysis play a crucial role in determining the catalytic activity and selectivity of these materials. Proton transfer from the solid acid catalyst to the reactant molecule occurs through various mechanisms such asBrønsted, Lewis, and redox processes. The strength and type of acid-base interactions can be modulated by altering the catalyst's structure, composition, and surface properties, thereby influencing the reaction kinetics and product formation.III. Applications of Solid Acid Catalysis:Solid acid materials find widespread applications in various catalytic reactions, including hydrocarbon conversion, petrochemical processes, biomass conversion, and fine chemical synthesis. In hydrocarbon conversion, solid acid catalysts are used for the isomerization, alkylation, cracking, and reforming of hydrocarbons to obtain value-added products. Acid-catalyzed petrochemical processes, such as the production of ethylene and propylene, heavily rely on solid acid catalysts for the transformation of hydrocarbon feedstocks. Biomass conversionreactions, including cellulose hydrolysis and glucose dehydration, also benefit from the use of solid acid materials, enabling the production of biofuels and platform chemicals. Additionally, solid acid catalysts play a significant role in fine chemical synthesis, supporting reactions such as esterification, acylation, and condensation.IV. Recent Advances in Solid Acid Catalysis:Recent advancements in the field of solid acid catalysis have focused on enhancing catalyst performance through the design and development of novel materials. This includes the synthesis of hierarchical structures, doping with metal species, and engineering of acid sites for improved catalytic activity and stability. Furthermore, the integration of solid acid catalysts with other catalytic systems, such as metal nanoparticles and enzymes, has shown promising results in achieving synergistic effects and enhancing overall catalytic performance.V. Challenges and Future Perspectives:Despite the significant progress made in the field of solid acid catalysis, several challenges remain. The development of robust and reusable catalysts with high stability and selectivity is essentialfor practical applications. Additionally, understanding the intricate mechanisms of acid-base interactions in solid acid materials is crucial for efficient catalyst design and optimization. Future research efforts should focus on addressing these challenges, exploring new synthetic approaches, and utilizing advanced characterization techniques to unravel the catalytic behavior of solid acid materials.Conclusion:Solid acid materials have emerged as promising catalysts due to their unique acid-base properties and structural characteristics. Understanding the acid-base interactions in these materials is vital for unraveling their catalytic behavior and designing efficient catalysts for various applications. With recent advancements in materials synthesis and characterization techniques, the field of solid acid catalysis holds great potential for addressing current and future challenges in the field of sustainable chemistry.。

近十年金属有机化合物固定化酶研究进展及展望

近十年金属有机化合物固定化酶研究进展及展望

近十年金属有机化合物固定化酶研究进展及展望摘要:金属有机骨架材料(MOFs)凭借其较高的比表面积和孔体积、可设计和调控的孔径及结构,以及化学和热稳定性等特点,克服了传统固定化酶载体的孔径尺寸不可控、制备成本高、酶浸出、产物稳定性差等不足,近年来成为一类新型酶固定化载体。

首先,本文分类总结了MOFs固定化酶的特点和近几年发展进展。

文章最后展望了MOFs固定化酶未来发展前景,关键字:金属有机骨架材料,生物酶,固定化,研究进展,应用现状金属有机骨架材料(Metal Organic Frameworks,MOFs)凭借自身独特的性质如特定的主-客体相互作用及限域效应,极大提高了酶的负载率以及限制酶分子的流失,甚至极端环境下仍能维持酶的活性,近年来成为固定化酶载体的研究热点。

不同于传统载体,MOFs材料是由有机配体和金属离子在溶液中发生自组装而形成的一类具有周期性孔结构的结晶杂化材料。

由于其物理和化学性质的独特性,加上其化学和结构灵活多样的可调配性,使得MOFs材料在生物酶的固定领域具有巨大的应用价值[1, 2]。

1.MOFs固定化酶的方法常见MOFs固定酶的方法主要包括以下4种,即表面吸附、共价结合、孔道包埋和原位合成,见表1。

其中,表面吸附的温和操作条件使其成为保持酶构象和活性的理想选择;酶表面上丰富的氨基与MOFs的羧酸基团以共价偶联结合生成肽键则可以防止酶从MOFs中浸出;酶进入介孔MOFs的孔道或空腔完成包埋可以实现高酶负荷和低酶浸出;原位合成的优势在于克服了酶尺寸限制对固定在MOFs上的应用,并且即使在恶劣条件下也能表现出色的稳定性。

表1 利用MOFs载体固定酶的4种主要合成策略及其比较方法方法优势劣势原位合成制备条件温和,酶活性不受影响;快速合成条件限于水溶液;MOFs种类较少表面吸附操作简单;绿色化学酶与载体作用力弱,易流失;耗时;强静电相互作用可能影响蛋白质构象,从而导致酶活性下降共价键法酶与载体之间作用力强操作复杂;化学试剂引入可能对酶活性有影响孔道包埋酶负载率高且不易流失对MOFs孔径(大多限于介孔)、酶尺寸、形状都有要求1.MOFs固定化酶的特点MOFs用于酶的固定化具有4个显著的特点,即可重复使用性、高选择性和催化活性、高稳定性和水耐受性。

金属氧化物催化剂在多相催化中的重要性、特点和应用

金属氧化物催化剂在多相催化中的重要性、特点和应用

ABSTRACT
This short review paper aims at assembling the present state of the art of the multiuses of metal oxides in heterogeneous catalysis, concerning liquid and gaseous phases of the reactant mixtures on solid catalysts. It includes the description of the main types of metal oxide catalysts, of their various preparation procedures and of the main reactions catalysed by them (acid-base type, selective and total oxidations, bi-functional catalysis, photocatalysis, biomass treatments, environmental catalysis and some of the numerous industrial applications). Challenges and prospectives are also discussed.
Chinese Journal of Catalysis 40 (2019) 1627–1636
催化学报 2019年 第40卷 第11期 |
at
journal homepage: /locate/chnjc
Keywords: Heterogeneous catalysis Metal oxide catalyst Preparation procedure Acid-base reaction Selective and total oxidation reaction Photocatalysis Environmental catalysis Industrial process

中英文催化剂的制备与表征(catalysis and physical properties)

中英文催化剂的制备与表征(catalysis and physical properties)

Introduction to this subject
➢ Preparation, characterization and application of a catalyst is crucial to innovate a novel catalyst.是发明一个新催化剂的关键。
➢ Catalyst is usually not the same with other chemicals, especially pure chemicals.催化剂一般与其他化学品一样,特别是纯化学品。
Definition of Catalyst
➢ Ostwald (德国)的观点 催化剂是一种能够改变化学反应的速度,而它本身又不 参与最终产物的 物质。 (流行)
➢ IUPAC定义: 催化剂能够加速反应速率而不改变反应的标准Gibbs自 有焓变化。
➢ 国内新近定义 催化时加速反应速度、控制反应方向或产物构成,而不 影响化学平衡的一类作用。起这种作用的物质称为催化 剂,它不在主反应的化 学计量式中反映出来,即在反应 中不被消耗。
Ideal surface is not perfect
理想的表面是不完美的
扭结
阶梯空位
阶梯位
台阶吸附的原子 台阶空位
球的堆积模型表示不完美表面
Heterogeneous Catalyst
* Metals (Transition metals, IB metals);金属
Fe Co Ni Ru Rh Cu Ag Au Pd Os Ir Pt
Mechanism for heterogeneous Catalysis
Heterogeneous Catalysis
➢ Heterogeneous mechanism is difficult to investigated in the laboratory. Disappearance of reactants and appearance of products are easily followed, but important features such as the rates and energetic of adsorption, structure of active sites, the nature of active intermediates, require separate experimentation using a constantly changing arsenal of techniques. 非均相机理的实验室研究非常困难。反应物的消耗和产物的生成比 较容易追踪,但许多重要的因素比如速度和吸附能,活性位结构、 活性中间体特点等需要通过大量的单因素实验来得出。

原位限域生长策略制备有序介孔碳负载的超小MoO_(3)纳米颗粒

原位限域生长策略制备有序介孔碳负载的超小MoO_(3)纳米颗粒

Vol.42 2021年5月No.51589~1597 CHEMICAL JOURNAL OF CHINESE UNIVERSITIES高等学校化学学报原位限域生长策略制备有序介孔碳负载的超小MoO3纳米颗粒王常耀,王帅,段林林,朱晓航,张兴淼,李伟(复旦大学化学系,上海200433)摘要采用原位限域生长策略制备了一系列有序介孔碳负载的超小MoO3纳米颗粒复合物(OMC-US-MoO3).其中,有序介孔碳被用作基质来原位限域MoO3纳米晶的生长.依此方法制备的MoO3纳米晶具有超小的晶粒尺寸(<5nm),并在介孔碳骨架内具有良好的分散度.制得的OMC-US-MoO3复合物具有可调的比表面积(428~796m2/g)、孔容(0.27~0.62cm3/g)、MoO3质量分数(4%~27%)和孔径(4.6~5.7nm).当MoO3纳米晶的质量分数为7%时,所得样品OMC-US-MoO3-7具有最大的孔径、最小的孔壁厚度和最规整的介观结构.该样品作为催化剂时,表现出优异的环辛烯选择性氧化性能.关键词有序介孔碳;氧化钼纳米晶;纳米材料;限域生长中图分类号O611.4文献标志码AIn situ Confinement Growth Strategy for Ordered Mesoporous CarbonSupport Ultrasmall MoO3NanoparticlesWANG Changyao,WANG Shuai,DUAN Linlin,ZHU Xiaohang,ZHANG Xingmiao,LI Wei*(Department of Chemistry,Fudan University,Shanghai200433,China)Abstract Ultrasmall particle sizes and excellent dispersity of the MoO3active species on support majorly dominate their catalytic performances.Herein,a series of ordered mesoporous carbon support ultrasmall mo⁃lybdena nanoparticles(OMC-US-MoO3)composites was synthesized through an in situ confinement growth strategy.Ordered mesoporous carbon was used as the matrix to in situ confine the growth of MoO3nanocrystals. The obtained MoO3nanocrystals show ultrasmall particle sizes(<5nm)and excellent dispersity on the meso-porous carbon frameworks.The obtained OMC-US-MoO3exhibits tunable specific surface areas(428―796 m2/g),pore volumes(0.27―0.62cm3/g),MoO3contents(4%―27%,mass fraction)and uniform pore sizes (4.6―5.7nm).As a typical example,the obtained sample with7%MoO3(denoted as OMC-US-MoO3-7)shows the largest pore size,smallest thickness of pore wall and most regular mesostructures.When being used as a catalyst,the OMC-US-MoO3-7exhibits an excellent catalytic activity for selective oxidation of cyclooctene with a high stability.Keywords Ordered mesoporous carbon;MoO3nanocrystal;Nanomaterials;Confinement growthdoi:10.7503/cjcu20200303收稿日期:2020-05-28.网络出版日期:2020-09-24.基金项目:国家自然科学基金(批准号:21975050)、国家重点研发计划纳米科技重点专项(批准号:2016YFA0204000, 2018YFE0201701)和中国博士后科学基金(批准号:2019M651342)资助.联系人简介:李伟,男,博士,教授,主要从事介孔材料的合成及应用研究.E-mail:*******************.cn1590Vol.42高等学校化学学报Epoxides,an important industrial chemicals,has been widely used in the fields of food additives,phar⁃maceutical intermediates,etc.[1,2].Catalytic epoxidation of olefin is one of the essential route to produce epo-xides,which oxygenation of carbon-carbon double bond to form cyclic epoxide groups.The kind of catalyst plays a key role on the epoxidation reaction.Among all catalysts,precious metal of gold based one illustrates high activity for olefin epoxidations[3,4].However,gold is limited resource and very expensive,even though it shows high conversion efficiency.Molybdenum oxide(MoO3),as one of the low cost,non-toxic and environ⁃mentally benign transition metal oxides,is widely used as heterogeneous catalysis for Friedel-Crafts alkyla⁃tion[5],hydrogenation reaction[6,7],epoxidation reaction[8,9],hydrogen evolution reaction[10],electrochemical energy storage for lithium-ion batteries[11,12],and gas sensors[13,14],etc..Gratifyingly,MoO3has been reported by several groups which have high activity for epoxidation of olefins in recent years[15,16].It is obvious that the size and morphology of MoO3active species are critical factors that affect their prop⁃erties for application[17~20].However,the synthesis and reaction process often easily causes serious sintering,migration and agglomeration of the MoO3nanoparticles,leading to the degradation of catalytic activity.Sup⁃ports are necessary for the immobilization of active species.Carbon has been widely used as an outstanding matrix to control the size and dispersity of supported metal oxides attributing to its advantages of intrinsical chemical inertness,high thermal stability,non-toxic and wide-sources[21~23].Molybdena supported carbon have been reported and show excellent performance as the catalyst for cyclooctene epoxidation[24,25].Recently,Chen group[26]fabricatedγ-Fe2O3@C@MoO3core-shell structured nanoparticles as a magnetically recyclable catalyst for the epoxidation reaction of olefins.The coated carbon layer play an efficient role for the stabiliza⁃tion of magnetic core.Biradar group[8]also reported a carbon microspheres-supported molybdena nanoparticles catalyst which also show outstanding effect for the epoxidation of olefins.However,above-mentioned catalysts are less porosity.Porous supports,especially,mesoporous carbon have been reported on many catalytic areas because of its large surface area,pore volume and pore size,which can not only improve the load capacity but also enlarge the reaction progress,where the diffusion process may be the rate-limiting step[26~28].Up to now,it is still urgent to fabricate mesoporous carbon supported MoO3catalyst with ultrasmall particle size and excel⁃lent dispersity.Herein,we construct an ordered mesoporous carbon support ultrasmall MoO3nanoparticles(OMC-US-MoO3)composites via an in situ confinement growth strategy.In this strategy,the ordered mesoporous carbon works as a matrix to in situ confine the growth of MoO3nanocrystals.The obtained MoO3nanocrystals show ultrasmall particle size(<5nm)and excellent dispersity on the mesoporous carbon frameworks.The content (mass fraction)of MoO3can be tuned from4%to27%.The obtained OMC-US-MoO3shows tunable specific surface areas(428―796m2/g),pore volumes(0.27―0.62cm3/g)and uniform pore size(4.6―5.7nm).As a typical example,the obtained sample with7%MoO3(denoted as OMC-US-MoO3-7)shows largest pore size,smallest thickness of pore wall and most regular mesostructures.When being used as a catalyst,the OMC-US-MoO3-7exhibits an excellent catalytic activity for selective oxidation of cyclooctene with a high stability.1Experimental1.1Chemicals and MaterialsPluronic F127(EO106PO70EO106,M w=12600)was purchased from Aldrich.All others chemicals were obtained from Aladdin company and used directly.Deionized water was used in all experiments.1.2Synthesis of Ordered Mesoporous Carbon Support Ultrasmall Molybdena NanoparticlesIn detail synthesis procedure,1.0g of Pluronic F127powders was added into10.0g of ethanol solution and stirred to a homogeneous clear solution at40℃.Afterwards,5.0g of20%(mass fraction)preformedNo.5王常耀等:原位限域生长策略制备有序介孔碳负载的超小MoO 3纳米颗粒phenolic resins ethanol solution and 1.0mL of peroxomolybdenum precursor solution were added into the ho⁃mogeneous system (5—200mg/mL ).The preformed phenolic resins was synthesized based on the reported method [27,28].Peroxomolybdenum precursor solution [29]was prepared by dissolving different contents of molyb⁃denum trioxide into 10.0mL of 30%hydrogen peroxide.The mixture solution was poured into dishes after 2h and then the dishes were heat treated at 40and 100℃for 8and 20h ,respectively ,forming the as -made com⁃posites consisting of Pluronic F127,phenolic resins ,and Mo species (denoted as as -made sample ).Then ,the calcination of as -made sample was implemented in a tubular furnace under N 2atmosphere.The temperature program was set from 25℃to 350℃with a ramp of 1℃/min ,maintenance for 3h ,and then to 600℃with 1℃/min ,maintenance for 2h.The obtained sample after pyrolysis was named as ordered mesoporous carbon support ultrasmall molybdena nanoparticles (OMC -US -MoO 3-x ),wherein x represent the actual mass fraction of MoO 3.1.3Activity Test The selective oxidation reaction of cyclooctene was carried out in the round -bottom flask (50mL ).In which ,40.0mmol of cyclooctene ,40.0mmol of 5.5mol/L TBHP in decane ,10mg of OMC -US -MoO 3-7cata⁃lyst (0.0048mmol/L of MoO 3),6.0g of 1,2-dichloroethane as solvent ,and 15.0mmol of chlorobenzene as internal standard.The reaction temperature is 80℃.At different time intervals ,conversion was calculated by sampling.The samples were analyzed on an Agilent 7890A gas chromatograph equipped with a HP -5column and products were confirmed by GC -MS.TOF values (mol of reacted cyclooctene per mol of catalyst and hour )was calculated at about half conversion of the reaction.The catalyst was reused after washing by water and drying.The test condition was kept same to the first time on the cyclic test.2Results and Discussion2.1Synthesis and CharacterizaitonThe developed in situ confinement growth strategy is employed to the preparation of ordered mesoporous carbon support ultrasmall molybdena nanoparticles (OMC -US -MoO 3)composites (Fig.1).In the synthesis sys⁃tem ,Pluronic F127is used as the structure -directing agent (soft -template ),preformed phenolic resins is used as carbon resource ,peroxomolybdenum solution is used as precursor ,and ethanol/H 2O is used as co -solvent ,respectively.The as -made sample and product OMC -US -MoO 3composites can be obtained after heat -treatment at 100and 600℃,respectively.The mass content of MoO 3in the OMC -US -MoO 3composites can be well tuned through adjusting the amount of peroxomolybdenum precursor in the synthesis system.TGA curves (Fig.2)show that the mass fractions of MoO 3species in the OMC -US -MoO 3composites areFig.1Illustration of the construction of OMC ⁃US ⁃MoO 3composites via the in situ confinementgrowth strategy Fig.2TGA curves of the OMC ⁃US ⁃MoO 3composites with different MoO 3contents obtained afterpyrolysis at 600℃,respectivelyMass fraction of MoO 3(%):a .4;b .7;c .10;d .16;e .27.1591Vol.42高等学校化学学报4%,7%,10%,16%and 27%(Table 1),respectively ,when adjusting the amount of molybdenum precursors in the synthesis system.The mass loss below 100℃is caused by the volatilization of adsorbed water in the composites.A slight mass increasement can be detected between 100and 300℃,demonstrating the existence of trace amount of MoO 2and abundant MoO 3in the composites.The mass increasement can be attributed to the oxidation of the trace amount MoO 2.Subsequently ,the huge mass loss above 300℃can be observed attribu -ting to the remove of carbon species in the composites.The mass loss between 100and 600℃is approximate to the mass fraction of MoO 3species in the composites.The SAXS patterns [Fig.3(A )]of OMC -US -MoO 3-4and OMC -US -MoO 3-7composites show two scatteringdiffraction peaks at 0.391and 0.782nm −1,and 0.412and 0.824nm ‒1,respectively ,indexing to the (100)and (200)reflections of a hexagonal mesosturtures with space group P 6mm .With the increasement of MoO 3content ,the q values of the (100)diffraction peaks shift to 0.532,0.617,and 0.678nm −1,for samples OMC -US -MoO 3-10,OMC -US -MoO 3-16,and OMC -US -MoO 3-27,respectively.The corresponding cell parame⁃ters of five composites are calculated to be about 18.5,17.6,13.6,11.7,and 10.7nm with the increased MoO 3content ,respectively.WAXRD patterns [Fig.3(B )]of five composites all show no diffraction peaks of MoO 3phase ,suggesting the ultrasmall particle size of MoO 3nanocrystals in the frameworks.This result demonstrates that the ordered mesoporous carbon frameworks can confine the size of MoO 3nanocrystals to an ultrasmall size even at a high MoO 3content effectively.Nitrogen adsorption -desorption isotherms of five OMC -US -MoO 3composites obtained after calcined at 600℃in N 2all display representative type -Ⅳcurves with H2hysteresis loops [Fig.4(A )],in agreement with the previously reported ordered mesoporous materials [30~32].Sharp capillary condensation steps in the relative pressure (p /p 0)of 0.41―0.70are observed for five composites ,demonstrating the narrow pore size distribu⁃tion.The Brunauer -Emmett -Teller (BET )surface area and pore volume of five composites are calculated and listed on Table 1.The surface area and pore volume decrease with the increased MoO 3content ,which can be attributed to the partial destroy and disappear of pore structures.The average pore sizes of five composites are also calculated and listed on Table 1from their pore size distribution curve [Fig.4(B )]derived from the adsorption branch based on BJH model.The average pore sizes are 4.7,5.7,5.5,5.4,and 4.6nm ,Table 1Structural and textural parameters for OMC -US -MoO 3with different content Sample No.12345MoO 3content (%,mass fraction )47101627S BET /(m 2·g -1)796693652574428V /(cm 3·g -1)0.620.540.490.410.27D /nm 4.75.75.55.4 4.6Fig.3SAXS(A)and WA ⁃XRD(B)patterns of the OMC ⁃US ⁃MoO 3composites with differentMoO 3contents obtained after pyrolysis at 600℃Mass fraction of MoO 3(%):a .4;b .7;c.10;d .16;e .27.1592No.5王常耀等:原位限域生长策略制备有序介孔碳负载的超小MoO 3纳米颗粒respectively.According to the cell parameters results ,the pore walls of five composites are calculated to be 14.1,11.9,8.1,6.3,and 6.1nm ,respectively.SEM images (Fig.5)show that OMC -US -MoO 3-4and OMC -US -MoO 3-7composites own the most regular mesostructures.Notably ,the regular [100]and [110]directions can be clear observed from the SEM images of OMC -US -MoO 3-7composites [Fig.5(B )and (F )].In addition ,the mesopores are opened and no obvious big metal nanoparticles can be observed from the surface.With further increasement of MoO 3content ,the reg⁃ular mesostructures is partial destroyed.TEM images of OMC -US -MoO 3-7composites [Fig.6(A )—(C )]taken along the [100]and [110]directions manifest a well -defined 2D hexagonal mesostructures in agreement with the result of the SAXS pattern [Fig.2(A )].The lattice spacing is measured to be 0.35nm from the HRTEM image [Fig.6(D )],attributing to the (040)crystalline planes of α-MoO 3[33].The average size of MoO 3nano⁃crystals is estimated to be (4.1±1.0)nm from the size statistics diagram.The survey spectrum of the OMC -US -MoO 3-7composites shows the presence of only Mo ,O and C elements [Fig.7(A )].The high -resolution Mo 3d core level XPS spectra [Fig.7(B )]show four peaks at 230.5,232.7,233.6,and 235.9eV ,demon⁃strating the co -existence of Mo 4+and Mo 6+species [34~36].The ratio of Mo 4+/Mo 6+is calculated to be about 13%.Only a few Mo 4+signals can be detected from the spectrum ,in agreement with the TGAresults.Fig.4N 2adsorption⁃desorption isotherms(A)and pore size distributions(B)of the OMC⁃US⁃MoO 3composites with different MoO 3contents obtained after pyrolysis at 600℃Mass fraction of MoO 3(%):a .4;b .7;c.10;d .16;e .27.Fig.5SEM images of OMC⁃US⁃MoO 3composites with different MoO 3contents obtained afterpyrolysis at 600℃Mass fraction of MoO 3(%):(A)4;(B)7;(C)10;(D)16;(E)27.1593Vol.42高等学校化学学报2.2Formation Mechanism Studies Based on the above results ,we propose that the in situ confinement growth strategy show significant impact on the formation of final OMC -US -MoO 3composites.The obtained MoO 3nanocrystals show ultrasmall particle size (<5nm )and excellent dispersity on the mesoporous carbon frameworks.This structure can be retained even the mass fraction of MoO 3is increased to 27%.However ,the regular mesostructures can be partial destroyed with the increased MoO 3mass content.According to the results that no large MoO 3nanocrys⁃tals can be detected from samples obtained after pyrolysis at 600℃,the unregular mesostructures can be attributed to the uncontrollable origin co -assembly process.2.3Selective Oxidation of Cyclooctene The selective oxidation reaction of cyclooctene with high catalytic performance and stability is still highly desired.However ,the stability of active nanoparticles in catalytic reaction is a major challenge ,especially for active nanoparticles with ultra -small size.For our case ,the OMC -US -MoO 3-7composites show most regular mesostructures ,largest pore sizes ,appropriate hole wall size ,MoO 3content and dispersity.So ,the obtained OMC -US -MoO 3-7composites catalyst is selected as the catalyst for cyclooctene epoxidation.The reactions were carried out using 1,2-dichloroethane as solvent in flask with chlorobenzene as internal standard at 80℃.The OMC -US -MoO 3-7composites catalyst shows a high TOF value of 2163h ‒1which is calculated on the basis of the experimental data at 2h.Meanwhile ,a high conversion (100%)of cyclooctene ,and selectivity (>99%)to 1,2-epoxycyclooctane at 8h can also be parison with the reported heterogeneous Mo -based catalyst using similar conditions was shown in Table 2.The present OMC -US -MoO 3-7catalystshowsFig.7Survey XPS spectrum(A)and high⁃resolution XPS spectra of Mo 3d (B)for OMC⁃US⁃MoO 3⁃7composites obtained after pyrolysis at 600℃Fig.6TEM images of OMC⁃US⁃MoO 3⁃7composites obtained after pyrolysis at 600℃Viewed along the hexagonal (A )and columnar (B ,C )directions and HRTEM image (D )of a representative MoO 3nanoparticle.1594No.5王常耀等:原位限域生长策略制备有序介孔碳负载的超小MoO 3纳米颗粒a higher TOF value than MoO 3/C [8],MoO 3/SiO 2[37],Mo -MOFs [9],Mo -MCM -41[38],Mo -SBA -15[38],[Pipera⁃zinCH 2{MoO 2(Salen )}]n [39],and MNP 30-Si -inic -Mo [40]as previous reported.It should be noted that cyclooc⁃tene still gave about 18%conversion [Fig.8(A )]in the absence of catalyst owing to the presence of strong TBHP oxidants ,which is consistent with previous reports [41,42].Further ,two other substrates ,cyclohexene and styrene were also tested under the same conditions to test the versatility of OMC -US -MoO 3-7as an epoxida⁃tion catalyst.Surprisingly ,the conversion of cyclohexene to 1,2-epoxyclohexane can reach 54%in 8h.Inaddition ,the conversion of styrene to styrene oxide can reach 95%in 36h ,respectively (Fig.S1,see the Sup⁃porting Information of this paper ).Beside the efficient conversion of catalyst and high TOF values ,the stability of catalyst is also very impor⁃tant ,especially for heterogeneous catalysis.Here ,the hot filtration test was used to assess the presence of active Mo species in solution.When the reaction lasted for 2h ,we removed the catalyst by hot filtration and let the mother liquid for reacting another 6h.The results showed that there was only a slight increase in con⁃version [Fig.8(A )],which is proof of a heterogeneous catalysis.For the recycling study ,cyclooctene epoxida⁃tion was performed maintaining the same reaction conditions except using the recovered catalyst.It can be clearly found that obvious changes are undetected for catalytic performance after five runs [Fig.8(B )].It indi⁃cates that ultrasmall MoO 3nanoparticles supported on ordered mesoporous carbon is highly stable and can be reused ,demonstrates its potential for industrial applications.The high conversion ,selectively ,and the TOF value for the cyclooctene epoxidation reaction can be attributed to the unique structure of the OMC -US -MoO 3-7composites.The high surface area ,volume ,andTable 2Calculating TOF value for epoxidation of cyclooctene and comparing with other catalysts *Catalyst OMC -US -MoO 3-7MoO 3/C MoO 3/SiO 2Mo -MOFs Mo -MCM -41Mo -SBA -15[PiperazinCH 2{MoO 2(Salen )}]n MNP 30-Si -inic -MoTime/h 2267331224Conv.(%)5280909397999546Epoxide sel.(%)>9910010099959398100TOF/h -1216353[8]72[35]270[9]22[36]40[36]16[37]2[38]*.TOF values(mol of reacted cyclooctene per mol of catalyst and hour)were calculated at abouthalf conversion of the reaction.Fig.8Time course plots of cyclooctene epoxidation(A)and reusability(B)by using OMC⁃US⁃MoO 3⁃7com⁃posites as catalystReaction conditions :40.0mmol of cyclooctene ,40.0mmol of 5.5mol/L TBHP in decane ,10mg of OMC -US -MoO 3-7catalyst (0.0048mmol/L of MoO 3),6.0g of 1,2-dichloroethane as solvent ,and 15.0mmol of chlorobenzene as internalstandard.The reaction temperature is 80℃.15951596Vol.42高等学校化学学报uniform mesopores can not only enrichment the reaction substrate but also in favor to the diffusion of sub⁃strates.The ultrasmall MoO3nanocrystals size and its excellent dispersity in the frameworks can expose more active sites.All these features are beneficial to the rapid conversion of substrate molecular with high selective⁃ly and conversion.3ConclusionsIn summary,an in situ confinement growth strategy was developed to the construction of ordered mesopo⁃rous carbon support ultrasmall molybdena nanoparticles(OMC-US-MoO3)composites.Ordered mesoporous carbon was used as an effective matrix to in situ confine the growth of MoO3nanocrystals.The obtained MoO3 nanocrystals show ultrasmall particle size(<5nm)and excellent dispersity on the mesoporous carbon frame⁃works.In addition,a serious of OMC-US-MoO3composite can be obtained with controllable specific surface areas(428―796m2/g),pore volumes(0.27―0.62cm3/g),MoO3contents(4%―27%,mass fraction)and uniform pore size(4.6―5.7nm).The mesostructures can be retained even the MoO3content as high as27%. 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硫酸氧化锆催化正庚烷异构化

硫酸氧化锆催化正庚烷异构化

摘要过渡金属氧化物作为固体酸多相催化剂在催化研究中占有重要的地位。

氧化锆由于具有酸性和碱性表面活性中心,作为催化剂和催化剂载体受到广泛关注。

硫酸氧化锆因其具有超强酸性,在正庚烷异构化反应上有着很好的催化活性。

然而硫酸氧化锆却存在着比表面不高,硫组易流失等问题,限制其在工业中的应用。

通过掺杂金属元素的方法可以提高氧化锆的稳定性,增强酸性和相关的反应性能。

本论文致力于用溶胶-凝胶法制备掺铝介孔硫酸氧化锆,并通过引入助剂等,力争获得在正庚烷异构化反应中具有高催化性能的硫酸氧化锆催化剂。

本论文主要开展了以下几个方面的工作。

1.通过溶胶-凝胶法制备掺铝介孔硫酸氧化锆催化剂,并考察不同铝含量对催化剂性能的影响。

2.在铝含量为5%的情况下考察不同焙烧温度对催化剂性能的影响,寻找最佳的焙烧温度。

3.在催化剂中掺入稀土元素,考察稀土元素的影响。

4.通过红外,XRD等表征技术研究催化剂的结构。

关键词:氧化锆;介孔;溶胶-凝胶;硫酸化;正庚烷异构化AbstractTransition-metal oxides play an important role in catalysis as solid acid catalyst.Among them,zirconia has been paid much attention and has been used as acidic catalyst and catalyst support because of the presence of acidic and basic surface active center.As a strong acidic catalyst .SO42-/ZrO2 exhibit unique catalytic performance on n-heptane isomerization.However,SO42-/ZrO2 has main disadvantages of loss of sulfur species and relative low surface area,which limits its industrial process.Doping other metal species can improve the stability of zirconia to enhance the performance of the acid and related reactions.In this thesis ,the research work was mainly focused on the preparation of Al-SO42-/ZrO2with intracystalline mesopore by sol-gel method and the exploration of catalysis with high performance over n-heptane isomerization through lead into assistant.The major work may be summarized as the follows:1.composing Al-SO42-/ZrO2 with intracystalline mesopore by sol-gel method and considering the effect of the proportion of Al on the performance of catalyst.2.considering the effect of different calcination temperature on the performance of catalyst when the content of aluminium was 5%.3.leading rare earth into catalyst and observe the change of the performance of catalyst.4.Characterization by XRD,IR Techniques.Key words:zirconia ;mesoporous ;sol-gel ;sulfated ;n-heptane isomerization目录第1章概述 (1)1.1 氧化锆的研究及应用进展 (1)1.2 正庚烷异构化反应简介 (4)第2章实验部分 (12)2.1 实验所用试剂及仪器 (12)2.2 实验方法 (12)2.3 表征方法 (14)第3章制备条件对催化剂结构及性能的影响 (15)3.1 催化剂的表征 (16)3.2正庚烷临氢异构化反应测试结果 (18)结论 (22)参考文献 (23)致谢 .............................................................................................. 错误!未定义书签。

钯炭还原硝基

钯炭还原硝基

Applied Catalysis A:General 476(2014)103–112Contents lists available at ScienceDirectApplied Catalysis A:Generalj o u r n a l h o m e p a g e :w w w.e l s e v i e r.c o m /l o c a t e /a p c a taInfluence of preparation method and palladium content on Pd/C catalysts activity in the liquid phase hydrogenation of nitrobenzene to anilineMária Turákováa ,Milan Králik b ,∗,Peter Lehock ´y b ,L ’ubomír Pikna c ,Miroslava Smrˇc ovác ,Dagmar Remeteiovác ,Alexander Hudák caDepartment of Organic Technology,Faculty of Chemical and Food Technology,Slovak University of Technology in Bratislava,Radlinského 9,81237Bratislava,Slovak Republic bResearch Institute of Chemical Technology,VUCHT a.s.,Nobelova 34,83603Bratislava,Slovak Republic cDepartment of Chemistry,Faculty of Metallurgy,The Technical University of Koˇs ice,Letná9,04200Koˇs ice,Slovak Republica r t i c l ei n f oArticle history:Received 7October 2013Received in revised form 13February 2014Accepted 14February 2014Available online 23February 2014Keywords:Liquid phase hydrogenation Nitrobenzene PalladiumCatalyst activity Leachinga b s t r a c tTwo sets of Pd/C catalysts with 1–10wt.%Pd content supported on active carbon were prepared by a conventional formaldehyde method.One set was prepared using H 2[PdCl 4]complex and other one with Na 2[PdCl 4].In spite of different metal loadings,average crystallite size of palladium particles estimated by XRD and TEM analyses was virtually the same in all the cases,from 3to 5nm.Catalysts were tested for nitrobenzene hydrogenation in a stirred autoclave with the presence of methanol as a solvent,at 5MPa and 50◦C.Ratio of Pd to nitrobenzene substrate was in every reaction mixture the same:15.4mg of palladium per mol of nitrobenzene.Specific initial catalyst activity (initial reaction rate)for catalysts with 1–4wt.%Pd content for both sets of catalysts was comparable.It means that palladium complex used for the preparation had no-effect on catalyst activity.With palladium content higher than 4wt.%a significant drop in the catalytic activity and increase in amount of the leached palladium were observed,which should be prescribed for the formation of agglomerates of palladium crystallites (revealed by TEM)and consequent decrease in concentration of catalytic sites.Because of a decrease in catalytic activity,the reaction times were longer,which caused a higher metal leaching.©2014Elsevier B.V.All rights reserved.1.IntroductionThe hydrogenation of aromatic nitro compounds with hetero-geneous catalysts is a classical procedure for the production of the corresponding aniline derivatives [1–3].The hydrogenation of sim-ple aromatic nitroarenes poses few problems and is carried out catalytically on very large scales in a continuous arrangement either in the gas(vapour)phase or in the liquid phase [4].This article focuses on estimating catalytic activity and stability of Pd/C catalysts in a liquid phase hydrogenation of nitrobenzene to aniline in a batch mode.We decided to use this reaction accord-ing to its technological relevance.Results from these experiments will be implemented in a more sophisticated hydrogenation of 4-nitrodiphenylamine and 4-nitrosodiphenylamine mixture to 4-aminodiphenylamine that is used as an intermediate for rubber∗Corresponding author.Tel.:+421918609502;fax:+421244258558.E-mail addresses:mkralik@vucht.sk ,milan.kralik@stuba.sk (M.Králik).antioxidants production.We would like to point out that the choice of palladium precursors,catalyst preparation method and solvent was influenced by its potential use at industrial scale.For a good economy,palladium precursors and solvent must have low prices and preparation method must be simple.Due to higher mass transport resistance in liquid systems gas/vapour-solid catalytic reactors are preferred for large-scale technologies.Catalyst deactivation by leaching is another disadvan-tage of the liquid phase hydrogenation.Especially in a slurry-phase hydrogenation processes [5–7],the loss of metal by formation of soluble complex compounds may occur.Considering metal stability,avoiding hydrogen-starving conditions and keeping the metal crystallites in a well-reduced,metallic state are of major importance [6,8].Hydrogenation in the liquid phase is used when reactants and/or relevant products have high boiling points and/or are temperature sensitive,also utilization of reaction heat is more comfortable from the liquid phase due to a higher value of the par-tial heat transfer coefficient in the liquid phase in comparison with the gas phase./10.1016/j.apcata.2014.02.0250926-860X/©2014Elsevier B.V.All rights reserved.104M.Turákováet al./Applied Catalysis A:General 476(2014)103–112Scheme 1.Basic reaction routes in the hydrogenation of nitrobenzene.Adapted from [16].Hydrogenation of nitrobenzene to aniline belongs to the oldest studied reactions,while the first industrial process was reduction with iron and water [9]and later catalytic routes appeared [10,11].This hydrogenation still keeps great importance both from theo-retical [12–16]and industrial aspects [17,18].Generally,for the hydrogenation of nitrobenzene,the reaction routes depicted in Scheme 1are considered.In comparison with the original reaction route proposed by Haber [19],this scheme indicates a direct formation of N-phenylhydroxylamine (PHA)from nitrobenzene (NB),transfor-mation of PHA to NB and aniline (AN)and basic condensation reaction (lower part of Scheme 1).A direct formation of PHA was observed by Gelder et al.[15]and Richner et al.[16],whereas latter proved the existence of nitrosobenzene (NSB)on the surface of a gold catalyst.For catalytic hydrogenation of nitrobenzene a wide set of metal catalysts are used,whereas copper for the vapour/gas phase hydro-genation is preferred [20]or combination of copper with other metals [21].Nickel is also frequently used for the hydrogenation of nitrobenzene both for the gas phase [22]as well as for the liquid phase [23].For the liquid phase hydrogenation,catalysts comprising precious metals as palladium,platinum,ruthenium and combination with other metals are used the most frequently [24].The potentiality of palladium catalysts together with our experi-ence from the past [25]inspired us to test them.The advantage of palladium catalysts lies in its high activity and that they do not attack or even disrupt aromatic ring [26].But when a higher mass transfer resistance occur in the reaction system,palladium cata-lysts in the hydrogenation of nitro compounds are deactivated by the transformation of palladium metal into complex,according to the simplified Scheme 2.When the activity of hydrogen increases and activity of nitro compound or nitroso compound decreases,Pd 2+can be again reduced to Pd 0[27].The outlined process of deactivation has been properly described by Bird et al.[6,8]and Janssen et al.[28,29].From the mentioned facts,leaching of a precious metal can beminimizedScheme 2.Representation of metal palladium transformation into complex during nitrobenzene hydrogenation.by either improving the availability of hydrogen in the liquid phase reaction medium or by optimizing the “catalyst side”of the pro-cess.The former can be achieved by using a special reactor design,e.g.a loop reactor,using special stirring device or increasing hydro-gen partial pressure in the reactor.For modifying or adapting the “catalyst side”of the process two approaches are possible:to use smaller quantities of catalyst for the reaction or to decrease the precious metal loading of the catalyst (e.g.3wt.%of precious metal instead of 5wt.%)[7].All these actions lead to a higher availability of hydrogen at the catalytically active metal particles,for example on a carbon support.Thus,stabilization of the metal in its metallic or hydridic form is achieved and leaching is avoided sustaining the catalytic activity of the supported palladium.It is well known that both,the size distribution of the metal crys-tallites and the type of support can have a strong influence on the performance of a heterogeneous catalyst [30].Use of wide range of supports for hydrogenation applications has been reported,e.g.carbon based materials,(bio)polymers [31,32]or metal oxides [33].Active carbon is often preferred because of its low cost,high surface area,chemical inertness,particularly in strong basic and acid envi-ronments and because of easy metal recovery by burning off the carbon [34].Charcoal supports are able to adsorb large amounts of water and for safety reasons are handled with 50%and more water content (dry Pd/C catalysts are strongly pyrophoric).Even minor changes in the preparation conditions can signifi-cantly influence a delicate balance of conflicting demands:a high activity,a high selectivity and a long lifetime [35].Choices of pal-ladium precursor,catalyst support,method of precursor reduction etc.are crucial factors.A high activity of supported catalyst often calls for a large active surface area and,thus,for high microporosity of a support used for preparation of a catalyst as well as for small particles in order to achieve high dispersion of the active phase.Because small particles,especially small metal particles tend to sinter already at relatively low temperatures,these are generally applied onto a pre-existing support material which itself is ther-mally and chemically stable and maintains a high specific surface area up to high temperatures [36].All these facts,together with an urge to be close to potential industrial applications,motivated us to prepare and check palladium catalysts supported on carbon with various contents of metal (0.9–10wt.%)and using the common formaldehyde procedure [37,38]and Na 2PdCl 4and H 2PdCl 4as pre-cursors.It is worth to note that formaldehyde procedure ensures no adsorbed hydrogen and therefore these catalysts under wet state are not pyrophoric.The aim of the presented research has been to compare influ-ence of the palladium precursor and the content of palladium in a catalyst on their activity in the hydrogenation of nitrobenzene.M.Turákováet al./Applied Catalysis A:General476(2014)103–1121052.Experimental2.1.Preparation of catalystsActivated carbon(C NORRIT SX PLUS)with specific surface area 1100m2g−1(declared by the producer)was used as a carrying agent.Palladium chloride from Aldrich(∼60wt.%Pd)was dissolved either in the solution of NaCl,or HCl,while10%excess was applied with respect to formation[PdCl4]2−complex.Activated carbon was mixed in sodium carbonate solution(78g l−1)and appropri-ate amount of the palladium complex was added dropwise.Then the reaction mixture was heated to95◦C and formaldehyde solu-tion(30wt.%)was added dropwise.The amount of formaldehyde was infive-fold excess with respect to the reaction[39,40]:Pd(OH)2+H2CO+Na2CO3=Pd0+NaOH+NaHCO3+H2+CO2(1)The mixture was held for1h at95◦C and mild mixing;the pre-cipitate was separated byfiltration,washed with sodium carbonate solution(0.2wt.%)and dried to approximately60%wetness.Cata-lysts containing0.9–10%were prepared.2.2.Catalyst characterizationThe content of wetness was determined using IR oven METTLER LP16(Mettler Toledo,USA).Catalysts were dried at105◦C until a stable weight was achieved.Exact content of Pd in prepared dry catalysts was measured by ICP-OES method at SPECTROBLUE ICP-OES(Spectro,Germany) spectrometer.Sample was decomposed in a mixture of concen-trated sulphuric and nitric acid before each measurement.Particle size distribution was measured by CILAS930Liquid (Cilas,France)device in a range of0.2–500␮m and results were distributed in histogram with70classes.Samples were treated with and without ultrasound where water served as liquid medium without any dispersing agent.BET surface area was obtained on a high-speed gas sorption ana-lyzer model NOVA1000e(Quantachrome Instruments,USA)with sorption gas N2.Specific surface area and porosity were evalu-ated by QuantachromeNovaWim program using BET method for multi-point(S a(M))and single-point analysis(S a(B)),HK method for micropores and BJH method for mesopores.Before measure-ment,all the samples were under vacuum at the temperature200◦C for10h.Samples were measured in the range of relative pressures p/p0= 0.0025–0.998 .Average palladium crystallite size was estimated from X-ray powder diffraction(XRPD)patterns recorded on Panalytical X’Pert Pro(PANalytical,USA)with Co K␣radiation source( =1.78901˚A) and scan range0–120◦2Âat40kV and30mA.The basic Scherrer’equation[41]was applied for the calculation,for which FWHM(full width at half maximum)and position of peaks were calculated from a peakfitting by PseudoVoight function using the Origin SW.The microstructure was observed by the scanning electron microscope TESLA BS300equipped with digital unit TESCAN.TEM images were observed by Jeol2000FX(Jeol,UK)device with200kV acceleration tension.Samples were dispersed using ultrasound in methanol.2.3.Catalytic tests–nitrobenzene hydrogenationReactions were carried out in a300ml stirred autoclave(Parr Instrument Company,USA)with a mechanical stirrer and hydrogen inlet above a level of liquid.A typical reaction mixture contained 10g of nitrobenzene,100ml of methanol and a catalyst.Amount of catalyst depended on palladium content and wetness.Ratio of Pd to nitrobenzene substrate was in every reaction mixture the same (molar ratio of Pd to nitrobenzene was1.45×10−4that corresponds to0.05g of the dry2.5wt.%Pd/C catalyst per10g of nitrobenzene). Afterfilling the reactor vessel with the cold solution of nitroben-zene in methanol(−15◦C)and proper amount of the catalyst the reactor vessel wasfixed to a head of reactor and the reactor was 3timesflushed with hydrogen to achieve virtually pure hydrogen atmosphere.Catalytic experiments were carried out at temperature 50◦C and starting hydrogen pressure6MPa.Decrease in the pres-sure was monitored.After drop of hydrogen pressure in the reactor to4MPa,reactor was quickly pressurized back to6MPa.During the reaction one pressurization of reactor was necessary to perform. Tests were held until zero hydrogen consumption was achieved.After completing the reaction,reaction mixture was cooled,fil-tered and analyzed.2.4.Deactivation testsPalladium deactivation tests were carried out in the same device as catalytic tests.Three versions of tests were carried out.Reactor wasfilled with0.5g of4Pd/C-H catalyst,100ml of methanol and 10g of nitrobenzene.In thefirst run mixture was kept at50◦C in a N2atmosphere(0.5MPa)at700rpm agitation rate for2h.During second run reaction mixture was kept in H2atmosphere instead, at the same conditions for1h.In the third run reaction mixture undergone same conditions and time as in thefirst run and then as in second run.After completing reaction,reaction mixture was analyzed for its composition and amount of leached palladium.2.5.Analysis of reaction products and leached palladiumAnalysis of the reaction mixture was performed by using the gas chromatograph Shimadzu GC-2010with capillary column DB-624 (Shimadzu,Japan),length30m,inner diameter0.53mm andfilm thickness3␮m)andflame ionization detector.Contents of reaction species were determined using calibration curves.An amount of leached palladium to solution was measured by GFAAS(HR-CS AAS)method on analyzer ContrAA700(Ana-lytik Jena,Germany)using the primary resonance line of Pd at 244.791nm.The content of Pd in the reaction mixture samples was determined by a calibration curve.3.Results and discussionTwo parallel series of Pd/C catalysts with1–10wt.%content were prepared by conventional method using hydrochloric acid or sodium chloride instead.Exact content of palladium and wetness of the used catalysts are in Table1.3.1.Particle size distributionAn average particle size estimated without ultrasound was 50␮m in case of active carbon and all measured catalysts as well. Compared to the analysis performed by utilization of ultrasound the average particle size was32␮m what indicates disrupting the agglomerated material.Palladium loading has not influenced size distribution probably due to its low content.50%of all particles had size below45␮m and90%of all particles below110␮m.Results are listed in Table2.3.2.SEMSEM images of support and catalysts containing3and10wt.% of palladium prepared from H2PdCl4and Na2PdCl4precursors are shown in Fig.1.With a higher amount of palladium bigger crys-tallites appeared on the surface and had more sintered structure.106M.Turákováet al./Applied Catalysis A:General476(2014)103–112Table1Dry matter(Dry mat.)in wet catalysts and palladium content in the dry matter.H2PdCl4Dry mat.[wt.%]Pd[wt.%]Na2PdCl4Dry mat.[wt.%]Pd[wt.%] 1Pd/C-H40.30.91Pd/C-Na41.60.82Pd/C-H45.3 1.62Pd/C-Na41.8 1.63Pd/C-H44.5 2.43Pd/C-Na41.5 2.44Pd/C-H41.9 3.24Pd/C-Na42.3 3.25Pd/C-H43.1 3.95Pd/C-Na41.8 3.97Pd/C-H42.77.57Pd/C-Na43.77.510Pd/C-H43.79.910Pd/C-Na44.49.9Table2Particle size distribution.Without ultrasound With ultrasoundd50[␮m]d90[␮m]dpriem[␮m]d50[␮m]d90[␮m]dpriem[␮m]C NORIT XS PLUS40.8103.349.424.562.530.24Pd/C-H42.4109.751.826.866.432.510Pd/C-H44.6105.351.727.766.532.84Pd/C-Na42.5111.152.328.672.535.010Pd/C-Na40.196.048.329.264.333.2Catalysts prepared from Na2PdCl4developed better crystalline and organized structure in comparison with H2PdCl4.The difference is visible especially in the case of10Pd/C-H and10Pd/C-Na.3.3.Textural propertiesSamples of C NORIT and Pd/C were described as microporous by the HK method.This method was also used for evaluation of volume of micropores under2nm.From adsorption/desorption curves,the surface area as well as volume of mesopores was obtained by the BJH method.The decrease in a specific surface area S a(M),espe-cially in surface area of micropores that constitute majority of catalyst surface,has been observed.Average pore diameter differs in a range of 3.65–3.80 nm.According to XRPD and TEM mea-surements(estimated average crystallite size of all the catalysts was about5nm)we can declare that palladium crystallitesfill the pores and thus cause decrease in catalyst surface area.This decrease was proportional to the applied amount of Pd%.However,obtained values of specific surface areas within the limit of the content of Pd in the catalyst sample from0.9%to3.9%do not differ significantly. The average pore diameters are listed in the last column of Table3.3.4.X-ray diffraction analysisXRPD patterns of the prepared catalysts with0.9;1.6;2.4;3.2;3.9and9.9wt.%.Pd loadings in a range of40–60◦2Âare presentedin Fig.1.Activated carbon(Norit)–left above and below,4Pd/C-H–middle above,10Pd/C-H–right above,4Pd/C-Na–middle below,10Pd/C-Na–right below.M.Turákováet al./Applied Catalysis A:General476(2014)103–112107 Table3Specific surface areas for single point S a(B)and multipoint S a(M)analysis,volumes of micropores and mesopores and average pore diameter.Sample S a(B)[m2g−1]p/p0=0.27S a(M)[m2g−1]Micro-poresvolume[cm3g−1](HK)Meso-poresvolume[cm3g−1](BJH)A/D aAverage porediameter[nm]Overall p/p00.05–0.3Micro-pores Meso-pores(BJH)A/D aC Norit844(935b)890605155/2290.3860.42/0.46 3.60 1Pd/C-Na835807540159/2230.3800.39/0.43 3.65 5Pd/C-Na805775508149/2170.3690.41/0.45 3.83 1Pd/C-H808784528162/2200.3860.40/0.43 3.73 5Pd/C-H779749502164/2260.3660.42/0.46 3.80a A/D–values determined from adsorption and desorption curves.b Conditions of p/p0=0.1,when the sample correspond to a maximum surface area.Fig.2.The average size of palladium crystallites was estimated from XRPD measurements using the Scherrer[41]equation taking into account.The FWHM of diffraction peak typical for plane palladium nanocrystals(111)according to its highest intensity was used for calculations.Position of this characteristic peak was approximately at47◦2Âthat is characteristic for patterns using Co K␣radiation source[42].In order to obtain reliable characteristics(FWHM,Â),it was necessary to treat Pd/C diffraction data as a two-peak function. With a higher Pd amount it is visible how intensity of a broad peak typical for active carbon at51◦2Âdiminishes in comparison to the Pd peak and therefore uncertainty of the crystallite size value is lower.Neither palladium content,nor type of precursor has influenced formation of Pd crystallites.In Fig.3it is documented that XRPD pat-terns of catalysts with same Pd loading,but prepared with different precursors are almost identical,without any significant differences. As seen from Table4,an average crystallite size of all the cata-lysts was about5nm.We observed similar tendency as Sanap et al.[43]that even with the increased loading the average crystallite size remains constant thus indicating for homogeneousparticleFig.2.XRPD patterns of catalysts prepared with H2PdCl4(left)and Na2PdCl4(right)in a range of40–60◦2Â:(a)active carbon NORIT SX PLUS and Pd/C catalysts with(b) 0.9%;(c)1.6%;(d)2.4%;(e)3.2%;(f)3.9%and(g)9.9%metal loadings.108M.Turákováet al./Applied Catalysis A:General 476(2014)103–112parison of XRD patterns of catalysts prepared with Na 2PdCl 4and H 2PdCl 4with 1.9(left)and 3.2%Pd (right)content.Fig.4.TEM scans for 1Pd/C-H,4Pd/C-H and 10Pd/C-H catalysts.distribution over the whole surface with no concentrated growth on existing nucleating centres.3.5.TEMThe metal dispersion was characterized by TEM analysis and from the obtained pictures also average Pd crystallite size was esti-mated.As it is documented by Fig.4in a case of catalysts with a lower palladium loading (1–4wt.%),palladium particles are uni-formly and separately dispersed on a catalyst surface,only their surface density increased.In the case of 10Pd/C catalysts,second layer of palladium appeared on a surface what caused decrease in accessibility of previously existing catalyst centres (see evaluation of catalyst activity).Similar to our results,White et al.had reported differences in metal dispersion caused by different metal loadings as well [44].In average about 200metal particles were measured asequivalent circle and involved into the calculation of metal particle size.Fig.5depicts a typical histogram for the 5Pd/C-H sample.From Table 4,difference between palladium crystallites esti-mated by XRD and TEM measurements is visible,especially for catalysts with the higher metal loading (7Pd/C and 10Pd/C).Differences are caused by formation of palladium crystallite agglomerates on previously existed layer,thus according to XRD measurements estimated size is smaller (crystallite size)than in case of TEM analysis (grain size)[45].Similar differences were observed and reported by Marrodan et al.as well [31],who were preparing resin supported palladium catalysts.3.6.Catalytic testsAll the catalysts were prepared in two parallel series and sub-jected to catalytic tests.Table 4Average size of palladium crystallites estimated from XRPD patterns (d XRPD )and TEM measurements (d TEM )(for catalysts with palladium content lower than 2wt.%in dry matter,the estimation from XRPD pattern was not reliable).H 2PdCl 4d XRPD [nm]d TEM [nm]Na 2PdCl 4d XRPD [nm]d TEM [nm]1Pd/C-H 4.2 5.01Pd/C-Na 5.252Pd/C-H 4.8 5.52Pd/C-Na 4.28.53Pd/C-H 3.743Pd/C-Na 2.864Pd/C-H 4.054Pd/C-Na 3.145Pd/C-H 3.645Pd/C-Na 3.557Pd/C-H 3.557Pd/C-Na 3.7410Pd/C-H2.7510Pd/C-Na3.55Average3.84.73.75.7M.Turákováet al./Applied Catalysis A:General476(2014)103–112109Fig.5.Typical histogram for the sample5Pd/C-H.In comparison with majority of laboratory catalytic tests for liq-uid phase hydrogenation,which are carried out at temperature close to laboratory one and pressure usually not exceeding1MPa, we carried out the tests under more severe conditions,at hydrogen pressure4–6MPa and temperature50◦C.We can note that similar temperature(50◦C)was used as a standard temperature for evaluation of Pd/C catalyst activity by Bond and Acres[46].According to their research the highest reaction rate of liquid phase hydrogenation of nitrobenzene in methanol was achieved at50◦C.At higher temperature the vapor pressure of the solvent methanol also increases,and hence progres-sively reduces the partial pressure of hydrogen.The reason for use of significantly higher pressures is an attempt to achieve more similar conditions to industrial hydrogenation processes and to eliminate deactivation which is very typical for processes with a low pressure of hydrogen[24–26].A practical advantage is that under high pressure of hydrogen and a mild temperature(323K)a virtually100%selectivity to AN should be obtained at the total conversion of NB.This was also proved in our case.Analysis of the reaction mixtures gave the amount of side products lower than0.3%.Therefore,it was possible to apply stoichiometry(2):NO2+ 3 H2NH2+ 2 H2O(2)To estimate catalysts activity(TOF as mol AN h−1mol Pd−1) we performed a series of experiments.Molar ratio of Pd to nitrobenzene substrate was in every reaction mixture the same (1.4×10−4:1)to avoid influence of palladium content and to be able to focus on other catalysts properties effect on its behaviour, such as crystallite size,distribution,etc.From the monitoring of pressure changes in the reaction system,the curves expressing the relative consumption of hydrogen were constructed.Initial reaction rate and reaction rate in time of50%and90%rela-tive hydrogen consumption were calculated.As it can be seen from Fig.6,activity of catalysts with1–4wt.%Pd loading was constant. Only4Pd/C-Na catalyst slightly differs with highest activity.Using catalysts with a higher Pd content caused a drop of reac-tion rate in comparison with lower Pd loading catalysts.This can be explained by decreasing of accessibility of catalytic centres,caused by forming of layered structure(see TEM analysis,Fig.5).Active particles in thefirst layer are covered with the second layer,and the next ones(formation of agglomerates).Consequently the specific metal palladium activity decreased.Obtained results correspond with the catalyst characterization results.The XRPD analysis revealed no difference in crystallite size and XRPD patterns andno significant differences in reaction rate Fig.6.Dependencies of TOF on Pd content at time t=0(a),in time of50%relativehydrogen consumption(b)and at time of90%relative hydrogen consumption(c). (Data in Fig.7are average values ofreaction rate from two parallel reactions). Fig.7.Dependency of the reaction Gibbs energy for the reaction(6)and(7),lines denoted by H2PdCl4and Na2PdCl4respectively.(Calculated using the program HFC Chemistry for the infinite diluted aqueous solutions,Pd(OH)2as a solid and CO2asa gas).between catalysts prepared using Na2PdCl4or H2PdCl4precursors were detected.This can be prescribed to a similar properties of hydrated Pd(OH)2as thefirst step in the preparation of palladium catalysts.For the preparation route starting from dihydrogen tetra-chloropalladium is:H2PdCl4(aq)+2Na2CO3(aq)→Pd(OH)2(s)+4NaCl(aq)+2CO2(g)(3) And from disodium tetrachloropalladate:Na2PdCl4(aq)+Na2CO3(aq)+H2O→Pd(OH)2(s)+4NaCl(aq)+CO2(g)(4) Fig.7shows a dependence of the Gibbs energies for the reactions (3)and(4).Lower values for the reaction(3)imply the higher driv-ing force for this reaction and one should expect that this affects the structure of the formed hydrated Pd(OH)2.However this prob-ably has no significant effect,when tetrachloropalladium is added dropwise to the hot stirred suspension of carbon in the solution of disodiumcarbonate.According to Rylander[47]a support can influence catalyst resistance to poisoning by extraneous contaminants and by-products of the reaction(e.g.benzene).To clarify the influence of active carbon on catalyst activity experiments with highly loaded。

吲哚基修饰的链状化合物的合成及其对阴离子的选择键合_郭鹏

吲哚基修饰的链状化合物的合成及其对阴离子的选择键合_郭鹏

第39卷第2期河北工业大学学报2010年4月V ol.39No.2JOURNAL OF HEBEI UNIVERSITY OF TECHNOLOGY April2010文章编号:1007-2373(2010)02-0023-04吲哚基修饰的链状化合物的合成及其对阴离子的选择键合郭鹏1,段中余1,黎刚1,陈娅斐2(1.河北工业大学化工学院,天津300130;2.河北工业大学理学院,天津300401)摘要从香兰素(4-羟基-3-甲氧基苯甲醛)和一缩二乙二醇出发,合成了一种吲哚基修饰的开链冠醚1,并用核磁、红外和元素分析对其结构进行了表征.进而采用紫外光谱分析的方法研究了该主体化合物对F、Br、HSO4,C l,I was evaluated by Uv-vis spectrum.The result obtained indicates that this linear compound displays extraordinary selectivity for fluoride ion.Key words open-chain crown ether;indole group;anion selectivity;fluoride ion;spectrometric titration0引言化学传感器由于其在化学、生物、药物分析以及环境监测方面的广泛应用已引起了人们越来越多的关注[1-2].由于氟离子水合焓很高,所以氟离子是最难识别的目标阴离子之一,同时氟离子传感器研究也一直是阴离子复合物化学中的研究热点[3-7].设计特异性检验氟离子的受体化合物对食品、药品管理和环境保护相关指标检测具有重要的实际意义.开链冠醚比之一般冠醚具有易于合成,产率高,原料易得,成本低,低毒或无毒,具有良好的构象揉曲性等优点,已成为当今冠醚化学中十分活跃的研究领域之一[8].因此,结合开链冠醚的优势,本文设计合成了一种新型的、以二吲哚苯甲烷为端基的链状化合物1,其特殊的结构可以有效络合F的检测方法,有广泛的应用前景.1实验部分1.1仪器与试剂香兰素(4-羟基-3-甲氧基苯甲醛)、对甲苯磺酰氯(TsCl)、吲哚购自天津市福晨化学试剂厂,分析纯;四氢呋喃(THF)、N,N-二甲基甲酰胺(DMF)、无水乙醇、KHSO4均为天津市化学试剂三厂产品,分析纯;各种阴离子的四丁基胺化物购自中国上海青浦试剂厂;没有特殊说明,均未经处理直接使用.元素分析采用Perkin-Elmer240型元素分析仪;红外光谱在Bruker Vector22型红外光谱仪上测得(KBr 压片);核磁共振1H谱采用BRUKER AC-P300型核磁共振仪测得;熔点用XRC-1型显微熔点仪测定;紫外收稿日期:2009-05-07基金项目:河北省科学技术研究与发展计划(07215133);河北工业大学博士科研启动基金作者简介:郭鹏(1979-),男(汉族),讲师.24河北工业大学学报第39卷可见光谱由Shimadzu UV-2401PC紫外可见光谱仪测定.1.2合成1.2.1化合物32-TsCH2CH2O/cm):1662,1593,1508,1456,1417,1338,1267,1137,1095,1031,931,869,744.元素分析计算值(C52H46O5N4):C77.40,H5.75,O9.91,N6.94,实验值:C77.45,H 5.78,O9.87,N6.91.1.3紫外光谱实验配制一系列含有相同浓度主体1的DMF溶液(2.5×10、Cl、I(四丁基季胺盐;离子浓度2.5×10、Br、HSO425郭鹏,等:吲哚基修饰的链状化合物的合成及其对阴离子的选择键合第2期光谱曲线无明显变化.而有趣的是,当加入F能够有效键合以形成稳定的配合物.为定量研究主体化合物1对氟离子的键合能力,本文测定了化合物1随着不同浓度氟离子的加入其紫外光谱的变化,如图2b ).随着F以1∶1配位,将520nm处的吸收强度数据通过非线性最小二乘法拟合,得到了其表观键合常数F,紫外光谱均无明显变化.我们有理由认为,F.较之其它阴离子,F离子易于与吲哚基团上的NH部分形成稳定的氢键[10].3结论本文设计合成了一种新型的链状化合物,并对其结构进行了必要的表征,进而通过紫外—可见光谱分析的方法考察了其对阴离子的识别作用.重要的是,通过定性和定量的比较,发现该链状化合物对F具有重要的实际应用价值.这一研究结果不仅提供了一种新的化学传感器,同时使在离子识别基础上的可视离子识别成为可能.通常来说,开链冠醚可以选择性键合阳离子,而在柔性的多醚链末端引入吲哚基团后,使其有望识别离子对,对该化合物识别离子对以及识别的机理研究还在进行中.a )分别加入F,Br ,HSO 42M )加入的情况图225℃时链状化合物1的DMF (2.5×104M in DMF )in the presence of various anions at 25℃The nonlinear least-squares analysis (inset )of the differential absorbance (A )to caculate the complex stability constants (Ks )3004005006000.60.50.40.30.20.10.0F None,Cl ,HSO 4/nm/nm 4M )的DMF 溶液中加入各种阴离子(2.5×10(粉色)、1+Cl (浅黄色)、1+I (浅黄色)Fig.3Visible observed from samples of 1and various anions.Left to right:1(light yellow ),1+F(light yellow )、1+Br (light yellow )、1+HSO 430河北工业大学学报第39卷3结论对不同复合金属氧化物在尿素与PG合成PC反应中的催化性能进行了研究,结果表明共沉淀法制备的MgO-Al2O3的催化剂活性最高;MgO-Al2O3的最佳制备条件为:以硝酸镁和硝酸铝为前驱体,Mg/Al摩尔比3∶1,沉淀剂氢氧化钠和碳酸钠的摩尔比3∶1,采用正加法,焙烧温度400℃,老化温度70℃.以最佳条件下制备的MgO-Al2O3为催化剂,PC收率为81.0%;CO2-TPD和BET分析表明催化剂的比表面是影响其活性的主要因素,XRD和TG-DTA分析表明400℃时制备MgO-Al2O3的前驱体可完全分解.参考文献:[1]Su Wei-Yang,Speranza George Phillip.A process for preparing alkylene carbonate[P].EP0443758A1,1991-2-11.[2]Doya Masaharu,Ohkawa Takashi,Kanbara Yutaka,et al.A process for producing alkylene carbonate[P].EP0581131A2,1993-7-15.[3]孙予罕,魏伟,李奇飚,等.一种合成碳酸丙烯酯或碳酸乙烯酯的方法[P].CN1421431A.2002.[4]Qibiao Li,Wenyu Zhang,Ning Zhao,et al.Synthesis of cyclic carbonate from urea and diols over metal oxides[J].Catalysis Today,2006,115:111-116.[5]Zhao Xianqiang,Zhang Yan,Wang Yanji.Synthesis of Propylene Carbonate from Urea and1,2-Propylene Glycol over Zinc Acetate Catalyst[J].Industrial and Engineering Chemistry Research,2004,43(15):4038-4042.[6]贾志光,赵新强,安华良,等.Pb/SiO2催化剂上尿素与1,2-丙二醇合成碳酸丙烯酯[J].石油化工,2006,35(10):927-931.[7]崔一强,安华良,赵新强,等.MgO催化尿素与1,2-丙二醇合成碳酸丙烯酯反应研究[J].河北工业大学学报,2007,36(4):11-15.[责任编辑田丰]参考文献:[1]Huang Kewei,Yang Hong,Zhou Zhiguo,et al.Multisignal chemosensor for Cr3+and its application in bioimaging[J].Org Lett,2008,10(12):2557-2560.[2]Constantin T P,Silva G L,Robertson K L,et al.Synthesis of new fluorogenic cyanine dyes and incorporation into RNA fluoromodules[J].OrgLett,2008,10(8):1561-1564.[3]Hudnall T W,Chiu C W,Gabba(上接第25页)。

电催化剂英语

电催化剂英语

电催化剂英语Electrochemical Catalysts: Revolutionizing Energy Conversion and StorageElectrochemical catalysts have emerged as a critical component in the global pursuit of sustainable energy solutions. These remarkable materials have the ability to accelerate chemical reactions, enabling more efficient and cost-effective energy conversion and storage technologies. From fuel cells to metal-air batteries, electrochemical catalysts have the potential to transform the way we harness and utilize energy, paving the way for a cleaner and more sustainable future.At the heart of electrochemical catalysis lies the intricate interplay between the catalyst's structure, composition, and the electrochemical reactions it facilitates. Catalysts can be designed to target specific reactions, optimizing their performance and selectivity. This tailored approach allows for the development of highly efficient systems that can overcome the limitations of traditional energy technologies.One of the primary applications of electrochemical catalysts is in fuelcells. Fuel cells are electrochemical devices that convert the chemical energy of fuels, such as hydrogen or methanol, directly into electrical energy. The efficiency of fuel cells is largely dependent on the performance of the catalysts used in the electrochemical reactions. Platinum-based catalysts have been widely used in fuel cell technology, but their high cost and limited availability have driven the search for alternative, more cost-effective catalysts.Researchers have explored a wide range of non-precious metal catalysts, such as transition metal oxides, nitrides, and sulfides, as well as carbon-based materials, to address the cost and scarcity issues associated with platinum. These alternative catalysts have shown promising performance, often matching or even exceeding the activity and durability of their platinum-based counterparts. The development of these cost-effective and earth-abundant catalysts has the potential to significantly improve the commercialization and widespread adoption of fuel cell technology.Another crucial application of electrochemical catalysts is in metal-air batteries, which have gained attention due to their high energy density and potential for low-cost energy storage. In these batteries, the electrochemical reactions at the air cathode are catalyzed by specific materials, enabling efficient oxygen reduction and oxygen evolution. The performance of these catalysts directly impacts the battery's energy efficiency, cycle life, and overall viability as anenergy storage solution.Researchers have explored a variety of catalyst materials for metal-air batteries, including transition metal oxides, perovskites, and carbon-based materials. These catalysts have shown improved activity, stability, and selectivity, addressing the challenges associated with traditional metal-air battery technologies. The development of advanced electrochemical catalysts has the potential to unlock the full potential of metal-air batteries, making them a more attractive option for large-scale energy storage applications.Beyond fuel cells and metal-air batteries, electrochemical catalysts play a crucial role in other energy conversion and storage technologies, such as water electrolysis and metal-ion batteries. In water electrolysis, catalysts are used to facilitate the splitting of water molecules into hydrogen and oxygen, enabling the production of clean hydrogen fuel. Similarly, in metal-ion batteries, electrochemical catalysts can enhance the efficiency of the redox reactions, leading to improved energy density and cycle life.The versatility of electrochemical catalysts extends beyond energy applications. These materials also find use in environmental remediation, such as the electrochemical treatment of wastewater and the removal of pollutants. Catalysts can be designed to selectively target and degrade various contaminants, making themvaluable tools in the quest for sustainable and eco-friendly solutions.The development of advanced electrochemical catalysts is an ongoing and dynamic field of research, with scientists and engineers continuously exploring new materials, structures, and synthesis methods to enhance their performance and cost-effectiveness. Computational modeling and machine learning techniques have played a crucial role in accelerating the discovery and optimization of novel catalyst materials, enabling rapid progress in this field.As the global demand for clean and efficient energy solutions continues to grow, the importance of electrochemical catalysts cannot be overstated. These remarkable materials hold the key to unlocking the full potential of energy conversion and storage technologies, paving the way for a more sustainable and environmentally-conscious future. Through continued research and innovation, electrochemical catalysts will undoubtedly play a pivotal role in shaping the energy landscape of tomorrow.。

金属氧化物的英语

金属氧化物的英语

金属氧化物的英语Metals are an integral part of our lives, and we use them for various purposes. From construction to electronics, we rely on these elements to enhance our daily routine. Nevertheless, metals may react with oxygen present in air or water, leading to corrosion and damage. Therefore, scientists have developed metal oxides known to possess uniqueproperties such as corrosion resistance, thermal stability, optical transparency, and electrical conductivity. In this article, we will discuss metal oxides and their importance in various industries.Step 1: What are Metal Oxides?Metal oxides are compounds formed from the reaction between metals and oxygen. They are often solid, inorganic substances with high melting and boiling points. Examples of metal oxides include rust (iron oxide), alumina (aluminum oxide), and copper oxide.Step 2: Properties of Metal OxidesMetal oxides possess unique properties that make them useful in different applications. Some of these properties include:- Corrosion resistance: Metal oxides are known to resist corrosion, making them suitable for use in pipes, tanks, and other metal structures.- Thermal stability: Metal oxides can withstand high temperatures, making them ideal for use in furnace linings and insulation.- Optical transparency: Some metal oxides possessoptical transparency, which makes them suitable for use in glass and ceramics.- Electrical conductivity: Some metal oxides possess high electrical conductivity, which makes them suitable for use in electronic devices.Step 3: Uses of Metal OxidesMetal oxides have a wide range of uses in various industries. Below are some examples:- Construction: Metal oxides such as alumina and titanium dioxide are used to make cement, which is useful in construction.- Electronics: Metal oxides such as indium tin oxide (ITO) and zinc oxide are used to make transparent conductive films, which are used in LCD displays, touch screens, and solar cells.- Catalysis: Metal oxides such as cerium oxide and zirconia are used as catalysts in the chemical industry.- Energy storage: Metal oxides such as lithium cobalt oxide and lithium iron phosphate are used in rechargeable batteries.- Healthcare: Metal oxides such as titanium dioxide and zinc oxide are used in sunscreens and cosmetics.In conclusion, metal oxides have proven to be useful in various industries due to their unique properties. The advances in research and development in metal oxides have led to the creation of new applications in emerging technologies such as energy storage and catalysis. We can only imagine the future possibilities of metal oxides as scientists continue to discover new properties and applications for these valuable compounds.。

金属氧化物 红外光谱

金属氧化物 红外光谱

金属氧化物红外光谱Metal oxides are a class of compounds that have gained significant attention due to their unique properties and wide range of applications. Among them, metal oxide nanoparticles have attracted considerable interest in recent years, particularly in the field of infrared (IR) spectroscopy. IR spectroscopy is a powerful analytical technique used to study the vibrational modes of molecules and materials, providing valuable information about their chemical composition and structure. In this context, metal oxide nanoparticles have shown great potential as novel materials for enhancing the sensitivity and selectivity of IR spectroscopy.One of the key advantages of metal oxide nanoparticles in IR spectroscopy is their ability to exhibit strong and tunable surface plasmon resonances. Surface plasmons are collective oscillations of conduction electrons at the surface of a material, and they can strongly interact with incident electromagnetic radiation, such as IR light. Metaloxide nanoparticles, with their unique size and shape-dependent plasmonic properties, offer a versatile platform for tailoring the absorption and scattering of IR light. This enables the enhancement of the IR signals of analytes, leading to improved sensitivity and detection limits in various applications, including environmental monitoring, biomedical diagnostics, and chemical sensing.Moreover, metal oxide nanoparticles can also act as efficient catalysts in IR-driven reactions. The localized surface plasmons of these nanoparticles can generate intense electric fields at their surfaces, which can promote the activation of molecules and facilitate chemical reactions under IR irradiation. This has opened up new possibilities for the development of energy-efficient and environmentally friendly catalytic processes. For instance, metal oxide nanoparticles have been employed as catalysts for the selective oxidation of organic compounds, photocatalytic water splitting, and CO2 reduction. The combination of metal oxide nanoparticles and IR spectroscopy offers a synergistic approach for studying and optimizing these catalytic processes, enabling betterunderstanding of the reaction mechanisms and improving the overall efficiency.In addition to their plasmonic and catalytic properties, metal oxide nanoparticles also exhibit unique optical and thermal properties that make them attractive for IR spectroscopy. For example, some metal oxide nanoparticles, such as titanium dioxide (TiO2) and zinc oxide (ZnO), are known for their high refractive indices and strong absorption in the UV-visible range. These properties can be exploited to enhance the light-matter interaction and improve the sensitivity of IR spectroscopy. Furthermore, metal oxide nanoparticles have high thermal conductivity, which enables efficient heat dissipation during laser-induced heating in IR spectroscopy experiments. This is particularly important for preventing thermal damage to the samples and ensuring accurate measurements.Despite the numerous advantages of metal oxide nanoparticles in IR spectroscopy, there are also some challenges that need to be addressed. One of the main challenges is the synthesis and control of the size, shape,and composition of these nanoparticles. The properties of metal oxide nanoparticles strongly depend on these parameters, and slight variations can significantly affect their plasmonic and catalytic performance. Therefore, it is crucial to develop reliable and scalable synthesis methods that can produce metal oxide nanoparticles with well-defined properties. Additionally, the stability and long-term performance of metal oxide nanoparticles in different environments need to be carefully evaluated to ensure their practical applicability.In conclusion, metal oxide nanoparticles have emerged as promising materials for enhancing the sensitivity and selectivity of IR spectroscopy. Their unique plasmonic, catalytic, optical, and thermal properties make them highly attractive for a wide range of applications, from chemical sensing to catalysis. However, further research is still needed to address the challenges associated with their synthesis, stability, and scalability. With continued advancements in nanotechnology and materials science, metal oxide nanoparticles hold great potential forrevolutionizing the field of IR spectroscopy and opening up new opportunities for analytical and catalytic applications.。

2,4-二羟基苯甲酸辅助合成不同形貌二氧化铈及其在NH3-SCR中的应用

2,4-二羟基苯甲酸辅助合成不同形貌二氧化铈及其在NH3-SCR中的应用

2,4-二羟基苯甲酸辅助合成不同形貌二氧化铈及其在NH3-SCR中的应用苏航;徐蔓;周诗健;杨福;孔岩【摘要】使用2,4-二羟基苯甲酸(DHBA)辅助控制合成出具有不同形貌(棒状与片状)的碱式碳酸铈.在水热阶段,碱式碳酸铈的形貌可以通过DHBA的量进行调控.当DHBA为3.5 mmol时,得到棒状碱式碳酸铈,然而增加DHBA的量至5.0 mmol时,可形成片状碱式碳酸铈.棒状与片状fcc-CeO2(面心立方二氧化铈)可成功地通过相应的焙烧处理获得.所得二氧化铈均有较大的比表面积(>60 m2· g-1),然而与片状二氧化铈相比,棒状二氧化铈有更高的氧化还原能力与更多的酸量.棒状二氧化铈用于NH3-SCR时有着更好的催化活性.%Different morphologies (rod-like and sheet-like) of CeOHCO3 were controllably synthesized by using 2,4-dihydroxybenzonic acid (DHBA) as auxiliary.During the hydrothermal process,the morphologies of CeOHCO3 were controlled by adding different amount of DHBA.When the amount of DHBA was 3.5 mmol,rod-like CeOHCO3 was synthesized,while by increasing the amount of DHBA to 5.0 mmol,the sheet-like CeOHCO3 was relatively generated.Then the rod-like and sheet-like fcc-CeO2 (face-centered cubic-CeO2) were successfully obtained by the subsequent calcination procedure.The resulted CeO2 affords large surface area (>60 m2· g-1),while the rod-like CeO2 exhibits higher redox ability and more acid amount compared to those of sheet-like CeO2.In addition,the rod-like CeO2 exhibits better catalytic activity in NH3-SCR.【期刊名称】《无机化学学报》【年(卷),期】2018(034)008【总页数】9页(P1538-1546)【关键词】二氧化铈;2.4-二羟基苯甲酸;纳米结构;水热合成;NH3-SCR【作者】苏航;徐蔓;周诗健;杨福;孔岩【作者单位】南京工业大学化工学院,材料化学工程国家重点实验室,南京 210009;南京工业大学化工学院,材料化学工程国家重点实验室,南京 210009;南京工业大学化工学院,材料化学工程国家重点实验室,南京 210009;南京工业大学化工学院,材料化学工程国家重点实验室,南京 210009;南京工业大学化工学院,材料化学工程国家重点实验室,南京 210009【正文语种】中文【中图分类】O643.36;TB340 IntroductionIn recentdecades,metaloxideshave been intensely applied in the fields of catalysis[1-2],sensor[3-4],lithium-ion battery[5-6],etc.Particularly,metal oxides with controlled shapes have positive effect in heterogeneous catalysis system.Some related properties,such as the specific architecture and high surface area have important influence on the anchoring of the active sites and controlling the diffusion of reactants.With the well-defined morphologies,the researchers can not only adjust the requiredphysicochemical properties but also improve the catalytic performance[7].Therefore,it is of great significance to explore facile and controllable routes for designing the desired structures.As well known,nitrogen oxides remain the major pollution source in the air,which could result in the formation of photochemical smog,ozone depletion and acid rain[8].These situations are directly harmful to ecological environment and human health.In order to address this dilemma,some effective approaches are expected.Fortunately,selective catalytic reduction of NO with NH3has been regarded as one of the considerable technologies for the abatement of NO(NH3-SCR),and the process can be described by the following equation:Besides,as one of the metal oxides,ceria(CeO2)has been continually focused owing to the highly oxygen storage capacity,enhanced metal dispersion and facile stabilization of the support[9-10].Meantime,CeO2can also serve as an outstanding component in the field of selective catalytic reduction of NO with NH3[11].However,the CeO2-based materials have been significantly demonstrated that the morphologies are closely associated with the physicochemical properties.Typically,for the pure CeO2,hollow ceria nanosphere with multiple shells exhibited distinguishable photocatalytic activity in water oxidation[12].With regard to the hybrid CeO2-based materials,core-shell Pd@CeO2 nanostructures were found to exhibit excellent catalytic activity in NOreduction[13].Recently,in the system of NH3-SCR,Li et al.reported that thenovel MnOx-CeO2nanosphere showed superior activity than the non-structured MnOx-CeO2catalyst[14].Hybrid multi-shell hollow structured CeO2-MnOxwas designed and found that this material displayed excellent catalytic activity compared to the traditional CeO2-MnOxnanoparticles or single-shell hollow spheres[15].Although great efforts have been achieved,there is still room for controllable synthesis of CeO2with specific morphologies and apply to NH3-SCR.To control the morphology of CeO2,some efficient methods,such as hydrothermal[16],polyol method[17],template method[18]and colloidal solution combustion[19]have been adopted.While,in consideration of the tunable reaction parameters,such as different temperatures and additives,the hydrothermal method could be considered as a promising route.Notably,benzoic acid compoundshavebeen achieved toprepare various polymers,pharmaceuticals and metal-organic framework particles (MOFs).Especially,Fan et al.[20]reported CuFe2O4@HKUST-1 heterostructureswith MOFs shell were constructed by 1,3,5-benzenetricarboxylic acid.Korpany et al.[21]explored a series of benzoic acid derivatives to fabricate surface functionalized iron oxide nanoparticles.Plentiful functional materials have opened a doorto discoverthe relationship between benzoic acid derivatives and nanomaterials.Therefore,choosing the appropriate method as wellas the suitable benzoic acid compounds play an important role in the synthesis of desirable nanoparticles.Whereas,to the best of our knowledge,it is still lack the research in controlling synthesis of nanocrystallines including CeO2byusing benzoic acid derivatives.Herein,the rod-like and sheet-like CeO2were successfully synthesized with the assistant of 2,4-dihydroxybenzonic acid.The selected 2,4-dihydroxybenzonic acid could be completely dissolved in the reaction system to form a homogeneous solution.Timedependentand temperature-dependentexperiments were carried out to study the growth mechanism of the CeO2.Besides,the physicochemical properties of the CeO2were investigated.In addition,the catalytic activity of the as-prepared CeO2was evaluated in the system of NH3-SCR.1 ExperimentalThe rod-like CeO2was synthesized via the hydrothermalmethod and the calcination procedure.Typically,2 mmol of Ce(NO3)3·6H2O and 3.5 mmol of 2,4-dihydroxybenzoic acid (DHBA)were dissolved in the mixed solution of 15.0 mL ethanol and 30.0 mL deionized water.Then 5.0 mL of sodium acetate solution (0.5 mol·L-1)was added dropwise into the mixed solution with stirring.The obtained homogeneous solution was transferred into a Teflon-lined autoclave and heated at 180℃for 24 h in an electricoven.Moreover,the autoclave was cooled to room temperature,the precipitate wascentrifuged and washed with deionized water for four times and dried at 60℃for 6 h.Then the precursor(Ce-Pre-1)was calcined in air atmosphere at 500℃with a heat ramp rate of 2℃·min-1for 4 h,and the calcined products were named as Ce-Cal-1.Instead,the sheet-like CeO2was obtained according to the similar process of rod-like CeO2by increasing the amount of DHBA to 5 mmol,and thehydrothermal products and the calcined products were labeled as Ce-Pre-2 and Ce-Cal-2,respectively.Time-dependent experiments for the precursors of Ce-Cal-1 and Ce-Cal-2 were carried out at different hydrothermal intervals of 3,6,10 and 21 h without changing other reaction parameters.The temperaturedependent experiments of Ce-Cal-2 were performed at 120,140 and 160℃,respectively. X-ray diffraction patterns (XRD)was used for characterizing the phase purity with a monochromatic Cu Kα radiation source (λ =0.154 178 nm)and operated at 40 kV and 100 mA in the range of 10°~80°.Field-emission scanning electron microscopy(FESEM)was performed on a Hitachi S4800 Field-Emission Scanning Electron Microscope and operated at 5 kV.High-resolution transmission electron microscopy(HRTEM)images were recorded on an EM-2010 EX microscope with the accelerating voltage at 200 kV.The N2adsorption-desorption isothermswere carried out in the relative pressure (P/P0)range from 0.01 to 0.99,and the surface area of samples were calculated by Brunauer-Emmet-Teller equation(BET).Temperature-programmed reduction under H2environment(H2-TPR)was carried out on a TP-5000 instrument.50 mg CeO2was pretreated under He-O2stream at 500℃for 1 h.After cooling down to room temperature,the catalyst was purged with 30 mL·min-1of He for 30 min to remove the excess O2.Then the flow of 5%H2-He was introduced into the sample with a flow rate of 30 mL·min-1and the temperature was raised to 950℃ at a rate of 10℃·min-1.The acidity of the CeO2was measured by NH3temperature programmed desorption (NH3-TPD)in the same instrument as the H2-TPR.Prior to TPDexperiment,100 mg CeO2was pretreated at 300℃for 30 min and cooling to 50℃under argon flow.The sample was exposed to a flow of 2.500 g·L-1NH3/Ar(50 mL·min-1)at 100 ℃for 1 h,followed by argo n purging for another 1 h.Then,the temperature was raised to 950℃in argon flow at the rate of 10℃·min-1.Thermogravimetry and differential scanning calorimetry (TG-DSC) was measured by a NETZSCH STA 409 instrument with a heating rate of 10℃·min-1under nitrogen atmosphere.Fourier transform infrared (FT-IR)spectra of the samples were obtained in the range of 4 000~500 cm-1with powders dispersed in KBr on Bruker VECTOR22 resolution.The catalytic conversion of NO was measured via a fixed-bed reactor with 0.2 g pure CeO2 (40~60 mesh)as catalyst.The feed gas contained 500 mg·L-1 NH3,500 mg·L-1NO,5%(V/V)O2,5%(V/V)H2O,with N2as the balance gas.The total flow rate of the feed gas was 200 mL·min-1,corresponding to a space velocity of 60 L·g-1·h-1.The concentration of NO was detected by an onlin e Thermo fisher IS10 FTIR spectrometer equipped with a 2 m path-length gas cell(250 mL).The NO conversion can be calculated by NO conversion=(cNO,in-cNO,out)/cNO,in×100%.2 Results and discussionFig.1(a)and Fig.1(e)show the X-ray diffraction patterns(XRD)of Ce-Cal-1 and Ce-Cal-2.The diffraction peaks atca.28.5°,32.9°,47.3°,56.2°,59.1°,69.4°,76.5°,78.7°are well indexed to the facecentered cubic CeO2(fcc-CeO2,PDF No.34-0394),implying the samples are not amorphous.Fig.1(b)depicts the typical rod-morphology of Ce-Cal-1 with the average width of 100~300 nm and the average length of 500nm~1.5 μm.The TEM image in Fig.1(c)also reveals the rod-like profile of CeO2.Fig.1(d)presents the corresponding HRTEM image of Ce-Cal-1.As shown in Fig.1(d),the lattice fringe spacing of 0.27 and 0.31 nm correspond to (200)and(111)diffraction planes of CeO2,respectively.On the other hand,Ce-Cal-2 displays the sheet morphology with the thickness below 80 nm and the length can reach to 700 nm(Fig.1(f)and Fig.1(g)).Theobvious lattice fringe spacing of 0.31 nm in Fig.1(h)matches well with(111)diffraction plane of CeO2.In addition,the SAED profiles manifest the typical single crystal,and some defects of the resulted CeO2could be discovered(marked as green rectangles).Therefore,the rod-like and sheet-like CeO2are successfully synthesized in this case.Fig.1 XRD patterns(a,e),SEM images(b,f),TEM images(c,g),HRTEMimages(d,h)with the corresponding SAED(inset)of Ce-Cal-1 and Ce-Cal-2,respectivelyFig.2 N2adsorption-desorption isotherms(a,b),H2-TPR(c)and NH3-TPD profiles(d)of Ce-Cal-1 and Ce-Cal-2The N2adsorption-desorption isotherms of CeO2 were measured and shown in Fig.2(a)and Fig.2(b).The BET surface areas of the Ce-Cal-1 and Ce-Cal-2 are calculated as about 61 m2·g-1and 68 m2·g-1,respectively.Temperature-programmed reduction under H2environment (H2-TPR)was tested to detect the redox property of the resultedCeO2(Fig.2(c)).Both the samples manifest the similar reduction peak positions,which are in good agreement with the pure ceria in other reports[22-23].To be specific,the α1 peak at the lower temperaturebetween 250~600 ℃ could be attributed to the reduction of the absorbed surface oxygen species and the surface oxygen species of CeO2.The α2 peak in the range of 750~800 ℃ could be ascribed to the reduction of bulk oxygen.The H2 consumption amount of Ce-Cal-1 at α1 is higher than that of Ce-Cal-2,which could be attributable to the abundant surface oxygen species in Ce-Cal-1(Table 1).Meantime,some differences of the bulk oxygen are also presented(α2),which may be connected with the different structures.Temperature-programmed desorption experiments of NH3(NH3-TPD)were examined to understand the acidity strength,and the results are presented in Fig.2(d).The desorbed β1 peak presents at the lower temperature of 300~570 ℃,corresponding to the desorption of physisorbed NH3and NH3at the weak acid sites[24].While the desorbed β2 peak ranging between 570 and 940℃is assigned to NH3 absorbed at the strong acid sites[25].The desorbed peak positions of the acid sites are analogous with each other;however,the NH3amount of β1 and β2 in Ce-Cal-1 are higher than those in Ce-Cal-2,indicating that the Ce-Cal-1 could possess of more acid sites.Moreover,the acid amount of the strong acid sites in both Ce-Cal-1 and Ce-Cal-2 are higher than those in the weak acid sites.Therefore,the H2consumption and NH3desorption amount of Ce-Cal-1 are higher than those of Ce-Cal-2,possibly associating with the diverse shapes and differentexposed crystalline facets[26-27].Distinguishable physicochemical properties of the as-prepared rod-like and sheet-like CeO2can be discovered.To reveal the crystal phase and morphology evolution for the precursors ofCe-Cal-1 and Ce-Cal-2,time-dependentexperimentswere investigated.As displayed for the precursors of Ce-Cal-1(Fig.3(a)),the diffraction peaks of the samples can be well indexed to pure orthorhombic phase of CeOHCO3(PDF No.41-0013).However,with regard to the precursors of Ce-Cal-2(Fig.3(b)),the resulted precursors show the gradual phase transformation behaviors from orthorhombic phase (initial period)to hexagonal phase(final period).As expected,those products can be completely transformed into hexagonal phase of CeOHCO3(PDF No.32-0189)with the longer reaction time(21 and 24 h).It is noticeable that the mixed phases of orthorhombicand hexagonalareinvolved in the intermediate stages.Besides,representative SEM images of the precursors at different reaction intervals were examined.For the precursors of Ce-Cal-1,the SEM images display the simplex rod-like morphology from Fig.3(c)to Fig.3(g)without obvious morphology transformation.However,as depicted from Fig.3(h)to Fig.3(l),the product affords rod-like structure at initial 3 h,and then the rod particles partially dissolve and accompany with the presence of some apparently granular particles(6 and 10 h).Finally,more sheet-like particles emerge as the dominant state (21 and 24 h).It should be noted that when the reaction system is absence of DHBA,the hydrothermal product presents the pure phase of CeO2with irregular morphology (Fig.4).Those results indicate that the CeOHCO3with specific morphology fails to be obtained in this condition.Table 1 Quantitative analysis of H2-TPR and NH3-TPDa,bH2consumptionand NH3amount are calculated from the corresponding peakarea,respectively.NH3-TPD H2consumption/a.u.a NH3amount/a.u.b α1 α2 β1 β2 β1+β2 Ce-Cal-1 1 090 946 8 187 9 385 17 572 Ce-Cal-2 849 864 5 999 7 941 13 940 H2-TPR Catalyst α1+α2 2 036 1 713Fig.3 XRD patterns of the precursors Ce-Cal-1(a)and Ce-Cal-2(b)at different hydrothermal intervals;SEM images for the precursors of Ce-Cal-1(c~g)and Ce-Cal-2(h~l)at different reaction intervals of 3,6,10,21 and 24h,respectivelyFig.4 XRD pattern(a)and SEM image(b)of the hydrothermal product synthesized without DHBATemperature-dependentexperimentsbased on Ce-Cal-2 were carried out and the SEM images are shown in Fig.5.The sample obtained at120℃exhibits the rod-like structure with the average width of 300~500 nm and the length below 3 μm.Moreover,those particles present the highly decentralized state withoutsignificantaggregation.However,as the temperature up to 140 and 160℃,the products exhibit the rod-like morphology with the state of aggregation.Obviously,the typical sheet-like morphology ofthe productcan be observed asthe temperature reaching to 180℃(Ce-Pre-2).This phenomenon indicates that a morphology reconstruction process could be triggered with the high temperature. Fig.5 SEM images of the hydrothermal products at 120℃(a,b),140℃(c)and 160℃(d)For investigating the inorganic species of Ce-Pre-1 and Ce-Pre-2,FT-IR was recorded and the results are displayed in Fig.6(a).The Ce-Pre-1 is taken asan example to illustrate.The peak at ca.3 461 cm-1 could be due to the stretching vibration of O-H groups in the adsorbed water,and the bending mode of O-H at ca.1 638 cm-1could also be observed.The band at ca.1 561 cm-1should be attributable to the asymmetric stretching of CO2.Another sharp peak at ca.1 420 cm-1 may be assigned to the stretching vibration of CO32-.Besides,in the region of 700~900 cm-1,the bands at ca.861 and ca.724 cm-1are correspondingly attributed to the deformation of CO32-and asymmetric vibration of CO2species,respectively.The peak at ca.594 cm-1could be ascribed to the Ce-O stretching band[28].Some of the characteristic peaks including the stretching vibration and bending mode of O-H,the asymmetric stretching of CO2and the stretching band of Ce-O in Ce-Pre-2 are similar to Ce-Pre-1,indicating the same component of the two samples(CeOHCO3).However,some difference can be found in the range of 1 400~1 500 cm-1and 700~900 cm-1,which could be due to the different crystal phases and morphologies of the CeOHCO3.In addition,the thermostability of Ce-Pre-1 and Ce-Pre-2 were analyzed by thermogravimetry and differential scanning calorimetry(TGDSC).As can be seen from Fig.6(b)and Fig.6(c),the curves manifest the weight loss between 240 and 300℃with the major exothermic peak.The weight loss of Ce-Pre-1 and Ce-Pre-2 are approximately 21.8%and 21.2%,respectively,which are close to the theoretical decomposition value of CeOHCO3to CeO2(20.7%). Fig.6 FT-IR spectra(a),TG-DSC curves(b,c)of Ce-Pre-1 and Ce-Pre-2Fig.7 Illustration for the possible morphology evolution process for the Ce-Cal-1 and Ce-Cal-2Based on the above-mentioned characterization and analysis,we tentatively propose that the DHBA could decompose into carbon species(CO32-).The OH-could also be produced by the hydrolysis of CO32-,CH3COO-under the hydrothermal condition.Thus,Ce3+could combine with OH-and CO32-to generate small granules with high surface energy.Meantime,the sustaining nucleation could be favorable to the growth of rod-like orthorhombic phase of CeOHCO3.It is noticeable that the rod-like CeOHCO3could exist as the stable product with 3.5 mmol of DHBA(Fig.7,Route 1).While theprocessofdissolution and recrystallization could be triggered with 5.0 mmol of DHBA,and rod-like CeOHCO3could dissolve and reconstruct to form the sheet-like hexagonal phase of CeOHCO3ultimately(Fig.7,Route 2).As reported,the defects of the crystals could induce the dissolution and recrystallization process for the formation of CeO2 with nanosheet morphologies[29-30].However,in consideration of the different experiment conditions,the high content of the DHBA and high hydrothermal temperature could also play the important roles in this process.Furthermore,the as-prepared CeO2could preserve the rod-like and sheet-like morphologies after calcination.In this work,Ce-Cal-1 and Ce-Cal-2 are used as catalysts for eliminating NO with NH3.As shown in Fig.8,both of the samples present the similar trend of NO conversion from 100 to 400℃.With increasing the temperature to 350℃,Ce-Cal-1 shows the higher conversion about 69.2% compared with Ce-Cal-2(50.9%).According to the results of H2-TPR and NH3-TPD,this phenomenon could be due to that Ce-Cal-1 possesses of the higher redoxability and more acid amount.The obtained CeO2particles exhibit structuredependent catalytic activity for the catalytic reduction ofNO.Besides,both the NO conversion of Ce-Cal-1 and Ce-Cal-2 are higher than the reported pure CeO2,indicating high catalytic activity of Ce-Cal-1[31].On the account of the catalytic results,the rod-like CeO2 could be viewed as the optimized structure for the reaction.Fig.8 NO conversion of the Ce-Cal-1 and Ce-Cal-23 ConclusionsIn summary,the rod-like and sheet-like CeOHCO3 were successfully synthesized with the assistant of 2,4-dihydroxybenzonic acid.The rod-like orthorhombic phase of CeOHCO3was proposed as the stable product via the nucleation growth process,and the dissolution and recrystallization accompanied with the morphology evolution and phase transformation were supposed to the generation ofsheet-like hexagonalphase of CeOHCO3.The highly dispersed rod-like CeOHCO3 could be obtained under the low hydrothermal temperature,while the state of aggregation and the transformation of morphology could be triggered by the high temperature.The obtained CeO2presented distinguishablestructure-dependentproperties,and the rod-like CeO2exhibited higher redox ability and moreacid amount.Moreover,the rod-like CeO2 manifested the better catalytic activity in NH3-SCR.Furthermore,it is proposed that more benzoic acid compounds can be expected to fabricate metal oxides with desirable morphologies.References:【相关文献】[1]Mitsudome T,Yamamoto M,Maeno Z,et al.J.Am.Chem.Soc.,2015,137(42):13452-13455[2]Yen H,Seo Y,Kaliaguine S,et al.Angew.Chem.Int.Ed.,2012,51(48):12032-12035[3]Li Y,Luo W,Qin N,et al.Angew.Chem.Int.Ed.,2014,53(34):9035-9040[4]PENG Juan(彭娟),LI Ye(李晔),JI Peng-Yu(季鹏宇),et al.Chinese J.Inorg.Chem.(无机化学学报),2012,28(6):1251-1258[5]Bai J,Li X,Liu G,et al.Adv.Funct.Mater.,2014,24(20):3012-3020[6]Cai D P,Wang D D,Huang H,et al.J.Mater.Chem.A,2015,3(21):11430-11436[7]Florea I,Feral-Martin C,Majimel J,et al.Cryst.Growth Des.,2013,13(3):1110-1121[8]Qi G S,Yang R T,Chang R.Appl.Catal.B:Environ.,2004,51(2):93-106[9]Sayle D C,Maicaneanu S A,Watson G W.J.Am.Chem.Soc.,2002,124(38):11429-11439[10]Premkumar T,Govindarajan S,Coles A E,et al.J.Phys.Chem.B,2005,109(13):6126-6129[11]Tang C J,Zhang H L,Dong L.Catal.Sci.Technol.,2016,6(5):1248-1264[12]Qi J,Zhao K,Li G,et al.Nanoscale,2014,6(8):4072-4077[13]Wang X,Zhang Y,Song S,et al.Angew.Chem.Int.Ed.,2016,55(14):4542-4546[14]Li L,Sun B,Sun J,et mun.,2017,100:98-102[15]Ma K,Zou W,Zhang L,et al.RSC Adv.,2017,7(10):5989-5999[16]WEI Zhong-Bin(位忠斌),CUI Yu-Qian(崔育倩),GUO Pei-Zhi(郭培志),et al.ChineseJ.Inorg.Chem.(无机化学学报),2011,27(7):1399-1404[17]Ho C,Yu J C,Kwong T,et al.Chem.Mater.,2005,17(17):4514-4522[18]YUE Lin(乐琳),ZHANG Xiao-Ming(张晓鸣).Chinese J.Inorg.Chem.(无机化学学报),2008,24(5):715-722[19]Voskanyan A A,Chan K Y,Li C Y V.Chem.Mater.,2016,28(8):2768-2775[20]Fan S,Dong W,Huang X,et al.ACS Catal.,2017,7(1):243-249[21]Korpany K V,Majewski D D,Chiu C T,et ngmuir,2017,33(12):3000-3013[22]Liu W,Feng L,Zhang C,et al.J.Mater.Chem.A,2013,1(23):6942-6948[23]Zhang L,Li L,Cao Y,et al.Catal.Sci.Technol.,2015,5(4):2188-2196[24]Yao X,Zhang L,Li L,et al.Appl.Cata.B:Environ.,2014,150:315-329[25]Zhang D,Zhang L,Shi L,et al.Nanoscale,2013,5(3):1127-1136[26]Aneggi E,Wiater D,de Leitenburg C,et al.ACS Catal.,2014,4(1):172-181[27]Sayle T X T,Cantoni M,Bhatta U M,et al.Chem.Mater.,2012,24(10):1811-1821[28]Sun C W,Sun J,Xiao G L,et al.J.Phys.Chem.B,2006,110(27):13445-13452[29]Li C R,Sun Q T,Lu N P,et al.J.Cryst.Growth,2012,343(1):95-100[30]Gong J,Meng F,Yang X,et al.J.Alloys Compd.,2016,689:606-616[31]Yao X,Ma K,Zou W,et al.Chin.J.Catal.,2017,38(1):146-159。

诺贝尔化学奖简介原文及翻译

诺贝尔化学奖简介原文及翻译

1. Phase-Switching CatalysisBy simply adding or removing carbon dioxide,chemists in Scotland devised a neat trick forreversibly shuttling a homogeneous catalystbetween the organic and aqueous phases in abiphasic solvent system (C&EN, Jan. 26, page 11;Angew. Chem. Int. Ed. 2009, 48, 1472). Thephase-switchable catalyst designed by Simon L.Desset and David J. Cole-Hamilton of theUniversity of St. Andrews adds flexibility to theoften complicated techniques required to isolateproducts and recycle catalysts duringhomogeneous reactions. The secret to theswitchability is a weakly basic amidine group,–N=C(CH 3)N(CH 3)2, that the researchers added tothe phenyl rings of triphenylphosphine. Therhodium catalyst made with the modifiedphosphine ligand is soluble in organic solvent. On bubbling CO 2 into an aqueous-organic reaction system containing the catalyst, the CO 2 reacts with water to form carbonic acid (H 2CO 3). The transient acid protonates the amidine groups and renders the catalyst water-soluble. Subsequently bubbling N 2 into the biphasic system drives off CO 2 and shifts the equilibrium of the catalyst-carbonic acid complex, leading thecatalyst to deprotonate and making it water-insoluble again. After a reaction iscompleted in either organic solvent or water, the researchers separate the product and catalyst into different phases, remove the product, and then shuttle the catalyst back into the original phase for the next reaction cycle. Building switchability into basic chemicals in this manner could facilitate greener and less-energy-intensive industrial chemical processes.能够转相的催化反应通过简单的添加或除去二氧化碳,苏格兰的科学家发明了一种在两相系统中来回转运匀相催化剂的灵巧的把戏。

氧化亚铜还原糖检索表

氧化亚铜还原糖检索表

氧化亚铜还原糖检索表1. 引言氧化亚铜是一种重要的还原剂,在化学实验和工业生产中被广泛应用。

糖是一类重要的有机化合物,广泛存在于自然界中,具有重要的生理功能和工业应用价值。

本文将介绍氧化亚铜在糖的还原反应中的应用,并提供一个检索表,以帮助读者更好地了解这一领域。

2. 氧化亚铜的基本性质氧化亚铜,化学式为Cu2O,是一种红色固体。

它具有良好的还原性能,在还原反应中起到重要的作用。

氧化亚铜可溶于酸和氨水,但不溶于水。

它的溶解度随温度的升高而增加。

3. 糖的还原反应糖是一类碳水化合物,由碳、氢、氧元素组成。

在一些特定条件下,糖可以发生还原反应,将氧化亚铜还原为金属铜。

这种反应常用于糖的定性和定量分析中。

4. 氧化亚铜还原糖的机理氧化亚铜还原糖的机理是一个复杂的过程。

一般来说,糖分子中的羟基与氧化亚铜发生反应,产生相应的醛基和酮基。

这些产物进一步与氧化亚铜反应,最终生成金属铜和相应的酸。

5. 氧化亚铜还原糖的应用氧化亚铜还原糖的应用广泛。

在化学实验中,氧化亚铜常用于糖的定性和定量分析。

通过观察反应产物的颜色变化或测量反应过程中产生的气体体积,可以确定糖的类型和含量。

在工业生产中,氧化亚铜还可用作催化剂,促进糖的转化和反应。

6. 氧化亚铜还原糖检索表下面是一个氧化亚铜还原糖检索表,列出了常见的糖和它们与氧化亚铜的反应情况。

糖反应情况葡萄糖还原为金属铜果糖还原为金属铜麦芽糖还原为金属铜蔗糖不发生反应乳糖不发生反应糖反应情况玉米糖还原为金属铜7. 结论氧化亚铜是一种重要的还原剂,在糖的还原反应中发挥着重要作用。

通过检索表,我们可以了解不同糖与氧化亚铜的反应情况,为糖的定性和定量分析提供参考。

同时,氧化亚铜还可用于工业生产中的糖转化和反应。

希望本文对读者在研究和应用氧化亚铜还原糖方面提供帮助。

参考文献:1.Smith, A.B. et al. (2010). The use of cuprous oxide as a reagentfor the determination of reducing sugars. Journal of the American Chemical Society, 132(15), 5427-5433.2.Zhang, H. et al. (2015). Catalytic conversion of sugars tochemicals by metal oxides. Catalysis Science & Technology, 5(3), 1470-1481.。

催化基础知识普及、探讨帖之五:催化期刊及投稿

催化基础知识普及、探讨帖之五:催化期刊及投稿

催化基础知识普及、探讨帖之五:催化期刊及投稿催化基础知识普及、探讨帖之五:催化期刊及投稿催化知识普及、探讨系列帖第 5 帖——催化期刊及投稿此帖主题相信大家平时了解的比较多,恐怕也是大家最为关心的问题之一。

小木虫论文投稿专版关于此方面的介绍比较多也比较详细,且我们催化专版也有几个帖子专门进行了探讨和讨论,而我对这方面了解比较少(主要是没发过什么文章,哈哈),此帖内容主要是对网络上的一些投稿知识进行汇总(加入了少的可怜的自己对催化期刊的认识及投稿经验)。

目的还是办此系列帖的主旨:介绍催化相关基础知识、抛砖引玉、相互学习、分享经验及教训。

催化是一门跨学科、跨专业的科学,按理论上讲化学类,甚至物理等类的期刊都可以收录催化相关的文章,因此本贴并不打算介绍诸如《科学》《自然》《德国应用化学》、、、JACS 等等这些高等次的通用型期刊,此帖只局限于催化专业期刊。

简而言之:只介绍含有“催化”两字的相关期刊。

具体介绍各个催化期刊之前,有必要对现今几大出版社或数据库简要介绍一下(一般催化期刊都是这四个出版社或数据库名下的):(1)Elsevier Science 出版社Elsevier 出版的期刊是世界公认的高品位学术期刊,且大多数为核心期刊,被世界上许多著名的二次文献数据库所收录。

SDOS 目前收录1700 多种数字化期刊,该数据库涵盖了食品、数学、物理、化学、生命科学、商业及经济管理、计算机科学、工程技术、能源科学、环境科学、材料科学和社会科学等众多学科。

该数据库不仅涵盖了以上各个学科的研究成果,还提供了简便易用的智能检索程序。

通过Science Direct Onsite(SDOS)中国集团的数据库支持,用户可以使用Elsevier Science 为其特别定制的科学、技术方面的学术期刊并共享资源。

目前 (截止到 2005 年 11 月 16 日)该数据库已有期刊种数1,734,期刊期数145,078 ,文章篇数2,576,316,最早年份为1995 年。

工业催化 英语

工业催化 英语

工业催化英语Industrial CatalysisThe field of industrial catalysis has played a pivotal role in the development and advancement of modern society. Catalysts, which are substances that facilitate chemical reactions without being consumed themselves, have become indispensable in a wide rangeof industries, from the production of fuels and chemicals to the development of new materials and pharmaceuticals. In this essay, we will explore the fundamental principles of industrial catalysis, its applications, and the significant impact it has had on the world around us.At the heart of industrial catalysis lies the concept of reaction kinetics. Catalysts work by providing an alternative pathway for a chemical reaction, one that has a lower activation energy than the original reaction. This means that the reaction can occur more easily and at a faster rate, ultimately increasing the efficiency and productivity of the industrial process. Catalysts can be classified into two broad categories: homogeneous catalysts, which are soluble in the reaction mixture, and heterogeneous catalysts, which are in a different phase (typically solid) from the reactants.Homogeneous catalysts are often used in the production of fine chemicals, pharmaceuticals, and specialty materials. These catalysts can be highly selective, meaning they can promote the formation of a specific product while minimizing the formation of unwanted byproducts. Examples of homogeneous catalysts include transition metal complexes, organometallic compounds, and enzymatic catalysts. These catalysts are typically employed in reactions that involve organic solvents or aqueous solutions, and their performance can be fine-tuned by modifying the ligands or the metal center.On the other hand, heterogeneous catalysts are widely used in large-scale industrial processes, such as the production of fuels, petrochemicals, and bulk chemicals. These catalysts are typically in the form of solids, such as metals, metal oxides, or supported catalysts, and they interact with the reactants at the surface. Heterogeneous catalysts offer several advantages, including ease of separation from the reaction mixture, reusability, and the ability to withstand harsh reaction conditions. Examples of heterogeneous catalysts include zeolites, supported metal catalysts, and metal-organic frameworks (MOFs).One of the most significant applications of industrial catalysis is in the production of fuels and energy-related materials. Catalysts play a crucial role in the refining of crude oil, the conversion of natural gasto liquid fuels, and the production of biofuels. For instance, catalysts are used in the process of catalytic cracking, where large hydrocarbon molecules are broken down into smaller, more valuable components, such as gasoline and diesel fuel. Additionally, catalysts are essential in the production of hydrogen, a clean and renewable energy source, through processes like steam reforming and water-gas shift reactions.Beyond the energy sector, industrial catalysis has had a profound impact on the chemical industry. Catalysts are used in the production of a wide range of chemicals, from basic commodities like ammonia and sulfuric acid to more specialized products like fine chemicals, polymers, and pharmaceuticals. For example, the Haber-Bosch process, which uses a heterogeneous iron-based catalyst, is responsible for the production of ammonia, a key ingredient in fertilizers that have revolutionized global food production.In the field of materials science, catalysts have played a crucial role in the development of new and advanced materials. Catalysts are used in the synthesis of polymers, ceramics, and composites, enabling the creation of materials with tailored properties for specific applications. For instance, catalysts are used in the production of high-performance plastics, such as polyethylene and polypropylene, which have become ubiquitous in modern life.The impact of industrial catalysis extends beyond the realm of chemistry and materials science. Catalysts are also employed in the environmental and biomedical fields. In the environmental sector, catalysts are used in the treatment of air and water pollutants, as well as in the production of clean energy sources. Catalytic converters in automobiles, for example, use precious metal catalysts to reduce the emission of harmful pollutants. In the biomedical field, enzymes, which are a type of biological catalyst, play a crucial role in the development of new drugs and the treatment of various diseases.The future of industrial catalysis is bright, with ongoing research and development aimed at addressing the challenges of sustainability, efficiency, and environmental impact. Researchers are exploring the use of renewable and sustainable feedstocks, the development of more selective and energy-efficient catalysts, and the integration of catalytic processes with emerging technologies, such as artificial intelligence and machine learning.In conclusion, industrial catalysis is a field that has profoundly shaped the world we live in. From the production of fuels and chemicals to the development of new materials and the treatment of environmental and biomedical challenges, catalysts have been at the forefront of technological advancements. As we continue to face the pressing issues of our time, the importance of industrial catalysis willonly grow, and it will play a crucial role in shaping a more sustainable and prosperous future for all.。

催化作用基础英文版

催化作用基础英文版

催化作用基础英文版Catalysis: A Fundamental ConceptCatalysis is a fundamental concept in chemistry and plays a crucial role in various chemical reactions. It involves the use of a catalyst, a substance that increases the rate of a chemical reaction without being consumed in the process. The word "catalysis" originates from the Greek word "katalysis," which means "dissolution" or "loosening."The concept of catalysis was first introduced by the Swedish chemistJöns Jacob Berzelius in the early 19th century. He observed that certain substances could accelerate chemical reactions without undergoing any permanent changes themselves. This discovery laid the foundation for the study of catalysis and its applications in various fields.Catalysts work by providing an alternative reaction pathway with lower activation energy. Activation energy is the energy required for a chemical reaction to occur. By lowering the activation energy, catalysts enable reactions to proceed at a faster rate. They achieve this by stabilizing the transition state of the reaction, which is an intermediate state between the reactants and the products.There are two types of catalysts: homogeneous catalysts and heterogeneous catalysts. Homogeneous catalysts are in the same phase as the reactants, while heterogeneous catalysts are in a different phase. Homogeneous catalysts are often used in solution-phase reactions, while heterogeneous catalysts are commonly employed in gas-phase or solid-phase reactions.Catalysis finds applications in various industries, including petroleum refining, pharmaceuticals, and environmental protection. In petroleum refining, catalysts are used to convert crude oil into useful products such as gasoline, diesel, and jet fuel. The use of catalysts in this process increases the efficiency of the refining process and reduces the environmental impact.In the pharmaceutical industry, catalysts are employed in the synthesis of drugs. They enable the production of complex molecules with high selectivity and efficiency. Catalysts also play a crucial role in environmental protection. For example, catalytic converters in automobiles convert harmful pollutants into less harmful substances, reducing air pollution.Catalysis is not limited to industrial applications; it also occurs in biological systems. Enzymes, which are biological catalysts, are essential for various biochemical reactions in living organisms. They enable reactions to occur under mild conditions, such as body temperature, which would otherwise require harsh conditions.The study of catalysis has led to significant advancements in the field of chemistry. Researchers continue to explore new catalysts and develop more efficient catalytic processes. The development of sustainable and environmentally friendly catalysts is also a focus of current research.In conclusion, catalysis is a fundamental concept in chemistry that involves the use of catalysts to increase the rate of chemical reactions. It has applications in various industries and plays a crucial role in environmental protection. The study of catalysis has led to significant advancements in chemistry and continues to be an active area of research.。

固体酸催化假紫罗兰酮合成紫罗兰酮研究进展

固体酸催化假紫罗兰酮合成紫罗兰酮研究进展

2015年7月第23卷第7期 工业催化INDUSTRIALCATALYSIS July2015Vol.23 No.7综述与展望收稿日期:2014-12-29;修回日期:2015-07-06 基金项目:国家林业公益性行业科研专项(201204811)作者简介:顾胜华,1988年生,男,安徽省定远县人,在读硕士研究生,主要从事天然产物化学与利用的研究工作。

通讯联系人:李湘洲,1965年生,女,湖南省郴州市人,教授,博士研究生导师,研究方向为天然产物化学与利用。

固体酸催化假紫罗兰酮合成紫罗兰酮研究进展顾胜华,李湘洲 ,张盛伟(中南林业科技大学材料科学与工程学院,湖南长沙410004)摘 要:固体酸催化剂可成为制备紫罗兰酮的环境友好型催化剂,综述金属盐、阳离子交换树脂、固体超强酸、分子筛和杂多酸等固体酸在催化假紫罗兰酮环化反应中的应用,固体超强酸是目前的研究热点,存在易失活、不易保存和稳定性不足等问题。

通过对催化剂载体改性、加入其他金属或氧化物形成多组元固体超强酸、引入稀土元素或特定的分子筛改性制备固体超强酸以及引入纳米级金属氧化物制备出纳米型固体超强酸等,这些均可为催化剂提供合适的比表面积、增加酸中心密度、增加酸种类型、增加稳定性和提高机械强度。

关键词:催化化学;固体酸;假紫罗兰酮;环化;紫罗兰酮doi:10.3969/j.issn.1008 1143.2015.07.002中图分类号:O643.36;TQ426.94 文献标识码:A 文章编号:1008 1143(2015)07 0505 04ProgressinsynthesisofiononefrompseudoiononecatalyzedbysolidacidsGuShenghua,LiXiangzhou,ZhangShengwei(CollegeofMaterialsScienceandEngineering,CentralSouthUniversityofForestryandTechnology,Changsha410004,Hunan,China)Abstract:Thesolidacidcatalystscanbeanenvironmentalfriendlycatalystsforthesynthesisofionone.Theapplicationofsolidacidcatalystssuchasmetalsalts,cationexchangeresin,solidsuperacids,molecu larsievesandheteropolyacidsforcyclizationofpseudoiononewasreviewed.Thesolidsuperacidsbecametheresearchhotspots.Thereexistedthedefectsofeasydeactivation,difficultpreservationandinsufficientstability.Themulti componentsolidsuperacidswerepreparedbymodifyingthecatalystsupportsandaddingmetalsormetaloxides.Thesolidsuperacidswereattainedbyintroductionofrareearthelementsormodificationofspecificmolecularsieves.Thenano solidsuperacidswereobtainedbyintroducingnano metaloxides.Thesemeasurescouldprovideappropriatespecificsurfaceareaforthecatalysts,enhanceacidcentredensity,acidtypes,stabilityandmechanicstrength.Keywords:catalyticchemistry;solidacid;pseudoionone;cyclization;iononedoi:10.3969/j.issn.1008 1143.2015.07.002CLCnumber:O643.36;TQ426.94 Documentcode:A ArticleID:1008 1143(2015)07 0505 04 紫罗兰酮属萜类物质,外观为淡黄色油状液体,室温下有特殊香气,是重要的香精香料,广泛应用于化妆品、食品和饮料,同时,可进一步合成其他香料产品及维生素A、β-胡萝卜素、脱落酸等,是重要的医药中间体[1-2]。

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Materials Chemistry and Physics, 18 (1988)
533-552
533
CATALYSIS BY BASIC METAL OXIDES
H. HATTORI
Department of Chemistry, Faculty of Science, Hokkaido University, Sapporo, 060 (Japan)
pressure 2SrO + O2 2BaO + 0 + CO2 2
The metal exposure
oxides
listed in Table
1 scarcely
exhibited
basic properties of
on
to atomosphere. and peroxides
log P vs. l/T plots for the decomposition of alkaline are very oxides Removing earth low elements are shown
dependent on the severity of the heat treatment on metal oxides.
535
-2
-3
T-l
Fig. 1. Equilibrium a 2Sr02e b 2Ba02~ c MgC03eMg0
x
lo3 / K-’
for decomposition. d CaC03e e SrCO e f BaCOz= cao + co2 SrO + CO2 BaO + CC2
INTRODUCTION Acid and base are paired concepts; a number of chemical interactions have been understood in terms of acid-base interaction. In contrast to extensive
studies of solid acid catalysts, less attention has been given to the studies of solid base catalysts. The study of solid base catalysts was first reported by Pines et al. that sodium metal dispersed on Al203 acted as an effective catalyst
for double bond migration to donate electrons, it of alkenes seems [l]. Considering that Na/Al 0 23 in the strong acts as tendency a solid of Na base
natural
GENERATION OF BASIC SITES Generation of basic sites requires highteperature metal oxide surfaces by removing H2, C02, and 02.
pretreatment to reveal
The catalytic activities are
separation
reaction
regeneration to reactor
after
reaction.
3. Noncorrosive
system.
0254-0584/88/$3.50
OElsevier Sequoia/Printed Netherlands inThe
534 Table I. Solid base catalysts. Alkaline earth oxides ( MgO, CaO, SrO, BaO ) Rare earth oxides ( La203, CeO2, Nd203, Y2O3, etc.) Alkaline oxides ( Li20, Na20, K20, Rb20, Cs20, ) Other metal oxides (Th02, Zr02, ZnO, )
Compared have a
the catalysts of advantages are:
homogeneous practical
solid
nuห้องสมุดไป่ตู้ber
The main advantages from
of solid base catalysts mixture.
1. Easy catalyst 2. Easy catalyst
Received
May 15, 1987; accepted
August
31, 1987
ABSTRACT Catalytic properties of basic materials investigated in our laboratories are reviewed. Firstly, the types of metal oxides and the indications of their basic properties are presented. Secondly, the importance of removing H20, CO2 and 02
In addition to the advantages, specific catalytic behavior would be expected of solid base catalyst caused by surface reaction in which geometric factors are important in some cases. Following the discovery of Na/A1203 by Pines et al., certain metal oxides with a single component were found to be solid base catalysts in the absence of such alkali metals as Na and K. The representatives of single-component metal oxides known to act as solid base catalysts are summarized in Table I. In addition to the metal oxides listed in Table I, any metal oxides are in principle solid base catalysts. Metal oxides expose 0 atoms on the surfaces, and 0 atoms attractively interact with H+. Any 0 atoms would be able to abstract H+ from strongly acidic molecules. The metal oxides listed in Table I act as base toward most of the reagents and therefore are called solid bases. Four reasons for recognizing certain metal oxides as solid base catalysts are as follows. (a) Color change of indicators to basic colors. The acid-base indicators adsorbed on the surfaces, exhibit basic colors. Using a series of indicators having different pKBH values, the basic strengths of the solid surfaces can be expressed in H_ scale [2]. (b) Poisoning effects of acidic molecules on the catalytic activity. The catalytic activities are reduced or eliminated when acidic molecules such as H20 and CO2 are present in the reaction mixtures. (c) Similar activities to those of homogeneous catalyzed reactions" in homogeneous systems. The metal oxides catalyze the reactions well known as base-catalyzed reactions in homogeneous systems. (d) Indications of anionic intermediates participating in the reactions. Mechanistic studies of the reactions, product distribution, and spectroscopic observation of adsorbed species over the metal oxides strongly suggest that anionic intermediates are involved in the reactions. catalysts for "base-
catalyst. Numerous alkaline base-catalyzed are used reactions are known homogeneous with systems and in for
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