人工固碳技术—热催化还原CO_(2)催化剂的研究进展北大核心CSCD

选择性加氢在功能材料合成和化学产品提纯等化工领域中有非常重要的应用,并且近年来为减少温室效应的影响,将CO_(2)催化选择性加氢转化成其他有应用价值的物质成为研究热点之一。其中热催化是应用较为广泛、易得到多种目标产物并且获得产品收率较高的方法。目前,利用CO_(2)多相热催化加氢制得甲烷、甲醇、轻烯烃等多种高价值的燃料和化学品已取得了一定进展,但仍存在一些难点问题,其中制备高效催化剂是催化加氢反应的关键问题之一。一直以来,研究人员致力于解决催化剂的活性和选择性问题,通过助剂掺杂和加入功能性载体对催化剂进行改性。针对这些问题,本文简要介绍了CO_(2)催化加氢的研究背景,总结了近5年来热催化CO_(2)加氢制得甲烷、甲醇、轻烯烃产品过程中使用催化剂的种类及对加氢反应的影响,期望为CO_(2)多相催化加氢中新型催化剂的开发提供参考。     

室温催化分解空气中臭氧污染物

臭氧污染是我国目前面临的突出环境问题,臭氧及其室内反应形成的二次污染物危害着人体健康。室温催化分解是避免空气臭氧污染的有效方法,本文首先总结了碳、沸石、贵金属与过渡金属氧化物等材料的臭氧催化分解性能;然后聚焦锰氧化物,比较分析了不同锰氧化物的臭氧催化活性,阐述了锰氧化物催化分解臭氧机理的研究进展。水蒸气导致的失活是当前臭氧催化剂研发面临的主要挑战,对臭氧催化分解与失活机理的深入认识是指导高效抗湿臭氧催化材料研发的关键。     

双自由基CF2与O3的反应机理

主要用作致冷剂和发泡剂的氯氟烃（CFCs）是破坏臭氧层的主要物质之一．对氯氟烃类化合物及其降解产物（包括光解、光氧化、化学反应产物等）在大气中行为问题的研究是大气化学研究的重要内容．前人[1-3]从理论和实验两方面研究了自由基与臭氧的反应机制，但是氯氟烃光解过程中     

甲烷选择催化还原NO研究进展

 近十年来,甲烷选择催化还原NOx已引起各国环境研究工作者的关注．综述了近年来甲烷选择催化还原NOx方面的研究进展,着重分析了用于该反应的催化剂的研究状况,探讨了目前比较公认的甲烷选择催化还原NOx的反应机理（NO2机理）,详细介绍了目前催化剂用于提高甲烷DeNOx反应活性的方法;并展望了甲烷选择催化还原NOx今后的研究方向．     

三苯甲烷类染料在催化动力学分析中的应用及研究进展

三苯甲烷类染料是目前催化动力学分析中一类重要的有机试剂.文中综述了近年来,三苯甲烷类染料在催化动力学分析方面(包括催化滴定)的应用及发展趋势.引用文献94篇.     

水相或无溶剂绿色催化合成双吲哚基甲烷研究进展

评价绿色催化合成方法的主要标准包括催化剂、试剂或溶剂、反应条件和后处理等。随着绿色化学的不断发展,水相催化或无溶剂合成表现出明显的优势,在催化双吲哚基甲烷衍生物的合成方面更是受到广泛的关注。但是目前尚无针对吲哚基甲烷催化反应过程以及是否使用试剂或溶剂等相关问题的综述报道。因此,对近十年来水相或无溶剂催化合成吲哚基甲烷的反应方法进行了综述,其目的是为指导和设计更为绿色、洁净的合成吲哚基甲烷新方法和思路,尤其在水相和无溶剂催化方面。     

非均相催化臭氧氧化反应机制

臭氧催化氧化作为高级氧化技术是目前水处理领域研究的热点,其中非均相臭氧催化氧化技术因其氧化能力强、降低臭氧投加量特别是能显著提高有机物矿化率等优点而备受关注。非均相催化臭氧氧化领域不断研究新的催化剂,但是其反应过程及机制更加复杂。催化臭氧氧化的性能很大程度上取决于催化剂及其表面性质。污染物在催化剂表面形成络合物,或者臭氧在催化剂表面分解产生不同的含氧物种如表面氧原子、过氧化物和羟基自由基等。本文评述了非均相臭氧催化氧化反应中存在的多种机理,主要是自由基理论、氧空位理论、表面原子氧理论、表面络合物理论和臭氧直接氧化理论。催化剂表面的羟基基团是主要的催化活性中心,本文探讨了表面羟基基团催化反应机制,得出催化剂表面性质决定其表面活性位点的特性及含量,对诱导臭氧分解产生含氧活性物种起了关键作用;概述了催化剂改性后的结构形态、比表面积及其性能和作用机制;并讨论了非均相臭氧催化氧化反应催化剂未来的发展趋势,为催化臭氧氧化污水处理技术提供了理论参考。     

Fe的分散程度对煤焦催化加氢气化的影响

在加压固定床反应器上研究了Fe催化剂在不同比表面积煤焦中分散性对催化加氢气化性能的影响,利用XRD、BET、H₂-TPR、FT-IR、TEM、拉曼光谱对煤焦及催化剂进行了分析表征。结果表明,煤焦活性位点和石墨化程度并非影响催化气化反应的唯一因素,而催化剂的分散性对反应影响更大。煤焦的比表面积越大,Fe催化剂在煤焦表面的分散更均匀,催化剂活性组分平均晶粒粒径越小,并可以促进煤催化加氢气化中间相产物Fe₃C的生成,甲烷收率越高。对于比表面积较高的900-char,在氢气压力为2 MPa,温度为750 ℃,Fe负载量为5%（质量分数）时,催化加氢气化甲烷收率可达53%。在900-char上考察了Fe催化剂负载量对催化加氢气化的影响,甲烷收率呈先增加后降低的趋势,Fe负载量存在饱和点。     

Pd/Amberlyst-45催化剂催化水相中苯酚选择性加氢制环己酮(英文)

环己酮是重要的有机化工原料和工业溶剂,是制造尼龙、己内酰胺和己二酸的主要中间体,环己酮的绿色生产工艺受到人们关注.目前全世界环己酮年产量接近900万吨,但环己酮生产仍主要以环己烷为原料,采用富氧空气氧化为环己基过氧化氢,再在铬酸叔丁酯催化剂作用下分解为环己醇和环己酮的混合物,然后经一系列蒸馏精制后得到环己酮、工艺复杂、能耗高,而且设备腐蚀、环境污染及安全问题严重.因此,大量工作正致力于新工艺和新催化剂研究,其中光催化氧化、分子筛催化氧化和金属氧化物催化氧化等都有相关报道,同时还有学者开发了其它环己酮制备新方法,如环己烯水合法、苯加氢法、环己醇氧化法和苯酚加氢法等.苯酚直接选择性加氢合成环己酮研究具有重要意义.苯酚加氢通常有两种工艺,气相加氢和液相加氢,由于液相加氢具有无需将反应物汽化、能耗较低和催化剂反应活性高等优势而受到广泛关注.但是目前大量文献报道的苯酚加氢过程仍需要高温条件且较易产生环己醇和环己烷等副产物,大部分催化反应需在有机溶剂中进行,因此如何提高环己酮选择性,减小环境影响成为近年来的热门课题.在过去数年中,人们筛选了大量催化剂,其中Pd催化剂具有较高活性和目的产物选择性,因为其对羰基表现出较低的催化活性.研究还发现,催化剂载体对苯酚加氢产物分布有重要影响,酸性载体或酸性助剂的加入均能提高苯酚转化率和环己酮选择性,可能的原因是催化剂表面可与苯酚羟基形成O-H…π强相互作用,使苯酚分子更容易吸附在载体表面,而一旦苯酚经催化加氢生成环己酮,由于失去羟基与载体表面相互作用,环己酮更容易从载体表面脱附,从而避免过度加氢生成环己醇,同时酸性位点可以增强Pd的电子密度,提高催化加氢活性.另外,通过添加助剂也可有效改善催化剂性能.然而,到目前为止,通过单一的一种催化剂仍然很难同时实现苯酚的高转化率和环己酮的高选择性.因此,开发新催化剂和简便的生产工艺对环己酮高效高质量生产具有重要意义.本文使用一种多孔、不易溶解的酸性离子交换树脂Amberlyst-45(A-45)为载体,采用简单的浸渍工艺制备了一系列不同Pd负载量的Pd/A-45催化剂,详细考察了催化剂在水相中对苯酚选择性加氢制环己酮的催化活性和选择性,包括反应温度、催化剂用量、反应时间和Pd负载量等对反应活性的影响及催化剂重复使用情况,并且与传统的SiO_2,ZnO,MgO,Al_2O_3和活性炭负载的Pd催化剂进行对比.研究发现,Pd/A-45催化剂在温和反应条件(40-100℃,0.2-1 MPa)下具有极高的催化活性和选择性,在适宜的反应条件下苯酚转化率达到100%,环己酮选择性高于89%.进一步分析由不同活性金属负载量制备的不同粒径Pd/A-45催化剂的活性规律发现,苯酚加氢生成环己酮是一个结构敏感型反应,其中Pd颗粒尺寸为12-14 nm时更有利于环己酮生成.     

光热催化甲烷干重整研究进展

随着工业化的推进,化石能源的消耗产生大量温室气体,其中CH₄和CO₂占据温室气体排放的98%以上。将CH₄和CO₂转化为高附加值化学品具有重要的意义,一直受到工业界和学术界广泛关注。传统的热催化甲烷干重整(DRM)可实现将CH₄和CO₂转化为合成气,但该反应过程受热力学限制,需要很高的能量输入,并且由于反应温度较高,催化剂易发生积碳而失活。绿色环保的光催化技术可以使甲烷干重整反应在温和条件下进行,但是存在太阳光利用率和反应转化率较低等问题。最近光热协同催化受到学术界广泛关注。许多研究结果表明,在相对温和的条件下,光热催化DRM可以获得良好的催化效果,可有效实现太阳能转化为化学能。本文简要介绍近期光热催化甲烷干重整反应的研究进展,总结不同金属催化剂在光热催化甲烷干重整中的应用,同时提出了光热催化甲烷干重整存在的一些挑战及展望。     

Pt/Al2O3和Pt-Cu/Al2O3催化CCl4氢化脱氯反应

制备了Al2O3负载Pt单金属催化剂和负载Pt-Cu双金属催化剂,比较了二者不同还原温度对其催化CCl4氢化脱氯反应性能的影响。 单金属Pt催化剂上主要生成CHCl3,而双金属Pt-Cu催化剂上产物随催化剂制备时的还原温度不同而异,当催化剂经400 ℃用H2还原后产物主要为CHCl3,而当催化剂经800 ℃用H2还原后产物主要为CCl2CCl2。 由于CCl4氢化反应是强放热反应,催化剂表面局部过热使得在反应中生成的C2等产物聚合结焦,覆盖了催化剂的活性中心,导致催化剂失活。 因此,通过加入甲醇作为稀释剂以带走部分反应热可提高催化剂的稳定性。 同时也降低了CHCl3的选择性,提高了CCl2CCl2的选择性。     

Low-temperature destruction of carbon tetrachloride over lanthanide oxide-based catalysts: from destructive adsorption to a catalytic reaction cycle

The catalytic destruction of carbon tetrachloride in the presence of steam, CCl(4) + 2 H(2)O-->4 HCl + CO(2), was investigated at 200-350 degrees C over a series of lanthanide (La, Ce, Pr and Nd) and alkaline-earth metal (Mg, Ca, Sr and Ba) oxide-based catalysts with kinetic experiments, Raman spectroscopy, X-ray photoelectron spectroscopy, IR spectroscopy, X-ray diffraction, and DFT calculations. This new catalytic reaction was achieved by combining destructive adsorption of CCl(4) on a basic oxide surface and concurrent dechlorination of the resulting partially chlorinated solid by steam. The combination of the two noncatalytic reactions into a catalytic cycle provided a rare opportunity in heterogeneous catalysis for studying the nature and extent of surface participation in the overall reaction chemistry. The reaction is proposed to proceed over a terminal lattice oxygen site with stepwise donation of chlorine atoms from the hydrocarbon to the surface and formation of the gas-phase intermediate COCl(2), which is readily readsorbed at the catalyst surface to form CO(2). In a second step, the active catalyst surface is regenerated by steam with formation of gas-phase HCl. Depending on the reaction conditions, the catalytic material was found to transform dynamically from the metal oxide state to the metal oxide chloride or metal chloride state due to the bulk diffusion of oxygen and chlorine atoms. A catalyst obtained from a 10 wt % La(2)O(3)/Al(2)O(3) precursor exhibited the highest destruction rate: 0.289 g CCl(4) h(-1) g(-1) catalyst at 350 degrees C, which is higher than that of any other reported catalyst system.     

Chloroform infrared multiphoton dissociation in the presence of O2 and NO2

The infrared multiphoton dissociation (IRMPD) of CDCl3 in the presence of O2 and NO2 as acceptor gases has been studied. We have worked with both pure CDCl3 and mixtures with CHCl3. The reaction mechanism following IRMPD of CDCl3 is discussed in detail. CCl2O, CCl4 and DCl were found to be the main products. With added O2, the observed CDCl3 dissociation was larger than with nonoxygenated acceptor gases. The reaction mechanism probably involves a catalytic cycle initiated by the oxidation of CCl3. With the aim of discriminating the different CDCl3 dissociation mechanisms, the IRMPD of CDCl3 in the presence of NO2 was first studied. In order to make evident the CDCl3 dissociation produced by the catalytic cycle, we then studied the IRMPD of CDCl3 in mixtures with CHCl3 with O2 as the acceptor gas. In this case, the dissociation mechanism subsequent to IRMPD is evidenced in the competence between the two isotopic species.     

Hydrogen/chlorine exchange reactions of gaseous carbanions

Gas-phase reactions of three typical carbanions CH(2)NO(2)(-), CH(2)CN(-), and CH(2)S(O)CH(3)(-) with the chloromethanes CH(2)Cl(2), CHCl(3), and CCl(4), examined by tandem mass spectrometry, show a novel hydrogen/chlorine exchange reaction. For example, reaction between the nitromethyl anion CH(2)NO(2)(-) and carbon tetrachloride CCl(4) forms the ion CHClNO(2)(-). The suggested reaction mechanism involves nucleophilic attack by CH(2)NO(2)(-) at the chlorine of CCl(4) followed by proton transfer within the resulting complex [CH(2)ClNO(2) + CCl(3)(-)] to form CHClNO(2)(-) and CHCl(3). Two other carbanions CH(2)CN(-) and CH(2)S(O)CH(3)(-) also undergo the novel hydrogen/chlorine exchange reactions with CCl(4) but to a much smaller extent, their higher nucleophilicities favoring competitive nucleophilic attack reactions. Proton abstraction is the exclusive pathway in the reactions of these carbanions with CHCl(3). While CH(2)CN(-) and CH(2)S(O)CH(3)(-) promote mainly proton abstraction and nucleophilic displacement in reactions with CH(2)Cl(2), CH(2)NO(2)(-) does not react.     

Dimerization and double proton transfer-induced tautomerism of 4(3H)-pyrimidinone in solution studied by IR spectroscopy and quantum chemical calculations

The tautomerism and dimerization of 4(3H)-pyrimidinone (4(3H)Pyr) in carbon tetrachloride (CCl4) and chloroform (CHCl3) solutions were investigated using IR spectroscopy and quantum chemical calculations. The observed IR spectra in the NH and OH stretching regions clearly revealed the predominance of the keto tautomer in both solvent systems. The enol form only exists in a very small proportion in the CCl4 solution. The tautomeric constant for the two monomers KT[OH/NH] = 0.012 and DeltaE = 2.62 kcal/mol were estimated at 25 degrees C. This result was supported by the self-consistent reaction field/polarizable continuum (SCRF/PCM) calculation at the MP4(full, SDQ)/aug-cc-pVDZ level, which predicted DeltaE = 3.06 kcal/mol in CCl4. In the C=O stretching region, two bands were observed, suggesting the coexistence of two keto structures at equilibrium. The calculated IR spectra indicated that the bands at 1711 and 1675 cm(-1) arise from the keto monomer and keto-keto (KK) ring dimer, respectively. At elevated temperature, the populations of both the keto and enol monomers increased for the CCl4 solution. The present study revealed that the keto <--> enol tautomerization does not occur in the isolated monomer molecule. The double proton transfer (DPT) reaction in the KK ring dimer presumably plays a substantial role in the population increase of the enol monomer. To our knowledge, this may be the first observation of the tautomerization in a model base pair via the temperature-induced ground-state DPT reaction under a nonpolar liquid environment reported so far. This tautomerism can serve as a mimic circumstance for the spontaneous mutations induced by proton transfer in the DNA base pairs.     

多氯甲烷与双环[2,2,1]-2,5-庚二烯光敏化离子自由基加成反应

以芳胺为光敏剂, 研究了多氯甲烷与双环[2,2,1]-2,5-庚二烯离子自由基加成反应, 在所研究的体系中只得到3,5-加成物, 说明该反应具有高度的区域选择性. 结合多氯甲烷对光敏剂N, N, N', N'-四甲基联苯二胺光物理性质的影响, 提出了反应经过离子自由基复俣物中间体的反应机理.     

Palladium-catalyzed addition of arylboronic acids to aldehydes

[reaction: see text] Arylboronic acids react with aldehydes in the presence of a base and a catalytic amount of a palladium(0) complex with chloroform, affording the corresponding secondary alcohols in good yields. General palladium complexes have no catalytic activity without chloroform. Chloroform is essential for this reaction, and palladium complex that was prepared from Pd(PPh3)4 with CHCl3 showed good catalytic acitivity as well.     

Polymer-Supported Lewis Acid Catalysts. III. Diphenylaminomethylpolystyrene-Titanium Tetrachloride Complex

A polymer pearl carrier, diphenylaminomethylpolystyrene, was synthesized by the reaction of chloromethylated polystyrene beads (4% DVB) with diphenylamine and was combined with titanium tetrachloride in chloroform to form a very stable complex containing 24.38% Cl (equivalent to 1.72 mmol TiCl₄/g complex beads). The complex showed good catalytic activity in organic reactions such as esterification, acetalation, and ketal formation. The catalyst can be reused at least eight times without losing its activity.     

Scope, kinetics, and mechanistic aspects of aerobic oxidations catalyzed by ruthenium supported on alumina

The Ru/Al(2)O(3) catalyst was prepared by modification of the preparation of Ru(OH)(3).n H(2)O. The present Ru/Al(2)O(3) catalyst has high catalytic activities for the oxidations of activated, nonactivated, and heterocyclic alcohols, diols, and amines at 1 atm of molecular oxygen. Furthermore, the catalyst could be reused seven times without a loss of catalytic activity and selectivity for the oxidation of benzyl alcohol. A catalytic reaction mechanism involving a ruthenium alcoholate species and beta-hydride elimination from the alcoholate has been proposed. The reaction rate has a first-order dependence on the amount of catalyst, a fractional order on the concentration of benzyl alcohol, and a zero order on the pressure of molecular oxygen. These results and kinetic isotope effects indicate that beta-elimination from the ruthenium alcoholate species is a rate-determining step.     

碳纳米管/FeS类Fenton催化剂的制备及催化性能

以浮动催化热分解法制备碳纳米管(CNTs), 采用氧化-还原-硫化的方法制备了CNTs/FeS催化剂, 采用X射线衍射(XRD)、 透射电子显微镜(TEM)和热重(TG)分析等技术对催化剂进行了结构表征. 将CNTs/FeS作为类Fenton催化剂用于水中环丙沙星的去除, 研究了降解过程中H₂O₂浓度、 CNTs/FeS催化剂的投加量、 环丙沙星浓度及pH等因素对催化降解性能的影响. 结果表明, CNTs/FeS类Fenton催化反应在H₂O₂浓度为20 mmol/L和CNTs/FeS催化剂的投加量为10 mg的条件下具有最优的降解效果, 其催化反应过程符合一级动力学方程, 且具有更加宽泛的pH适应范围(pH=3~8), 同时, CNTs/FeS类Fenton催化剂在使用寿命方面也具有一定的优势.