含超微氧化亚钴颗粒Beta分子筛的合成及其催化乙苯氧化性能（英文）

杂原子分子筛是指在硅铝分子筛或磷铝酸盐分子筛中含有骨架内或骨架外某种原子或其化合物的分子筛.这些杂原子可以是某些主族元素(如硼、锗、镓)或有变价特性的过渡金属元素(如钛、铁、钴、镍)等.将杂原子或其化合物通过浸渍、离子交换、水热晶化等方式引入沸石分子筛骨架中形成杂原子分子筛,往往可以改变沸石分子筛的骨架结构和理化性能,并赋予沸石分子筛新的催化反应性能.自1983年钛硅分子筛TS-1被发现能够高效催化烯烃环氧化以来,许多杂原子分子筛因其在催化烷烃类及芳烃类氧化、醛酮选择氧化及烯烃类环氧化等领域表现出的优良性能得到了广泛关注.目前,合成含不同杂原子的分子筛已成为分子筛材料开发的一个重要内容.分子筛的微孔孔道结构赋予了被引入其中作为催化中心的杂原子对反应物/产物分子独特的择形选择性;同时,分子筛骨架与杂原子之间往往存在化学键或空间限域作用,使得杂原子在高温高压等反应条件下依然保持高度的分散性,避免由于团聚导致活性降低.钴离子及含钴化合物在烷烃及芳烃类催化氧化反应中表现出很好的活性,能够利用分子氧实现对高碳烷烃及烷基苯的催化氧化.将钴离子及其化合物引入具有合适孔道结构的分子筛,可以提高催化反应的选择性.目前将对含钴分子筛的合成研究主要有后处理法及直接水热法.后处理法包括负载法及离子交换法,用于制备含有钴物种的硅铝分子筛;而直接水热法主要用于制备含有骨架钴的磷酸铝分子筛.目前为止,使用水热法合成含钴的分子筛材料的合成及其催化应用至今鲜有研究报导.这主要是由于传统的分子筛合成体系的高碱性环境会导致钴盐的沉淀,导致其无法被引入分子筛.我们通过优化合成条件,利用含氟体系直接水热法将钴引入Beta分子筛,得到含超微氧化亚钴团簇的Beta沸石分子筛.通过扫描电子显微镜、X射线粉末衍射、紫外-可见漫反射光谱、X射线光电子能谱、透射电子显微镜及H_2程序升温还原等表征手段对合成样品的物理化学性质进行了研究,并与使用浸渍、离子交换得到的含钴Beta沸石及水热合成得到的含钴AlPO-5分子筛的相关性质进行了对比.合成得到的含钴分子筛材料中,钴物种以亚纳米尺度的氧化亚钴颗粒形式存在.我们使用分子氧作为氧源,考察了该含超微氧化亚钴的Beta沸石作为催化剂催化乙苯氧化反应的活性.与浸渍、离子交换制得钴硅分子筛及含有骨架钴的磷酸铝分子筛材料相比,含超微氧化亚钴的Beta分子筛表现出更高的催化活性及对苯乙酮/醛的选择性.     

新型催化材料丝光沸石金属铬覆盖物

新型催化材料的研制一直是催化界努力探索的课题。1990年Davis等利用改进的水热法制备了Y型沸石Cu的覆盖物(Y/Cu),并预言这一新型材料有可能在催化、电化学和光化学等领域发挥重要的作用,但到目前为止,有关其应用方面的研究未见报道。 以往制备金属-沸石分子筛材料大多是采用离子交换法、浸渍法等。固-液、汽-液同晶置换法则将金属原子直接引入沸石阴离子骨架,形成杂原子分子筛。沸石金属覆盖     

硼-硅Pentasil型沸石的晶化相区与导向剂

新型沸石分子筛的开发是国际上分子筛化学界关注的问题之一。我们为了开拓含杂原子骨架结构的沸石分子筛的合成工作,系统地进行了硼硅Pentasil型沸石的研究。     

沸石分子筛的绿色合成路线

沸石分子筛因具有独特的孔道结构、较强的酸性和高的水热稳定性,在吸附分离、催化和离子交换等领域得到了广泛的应用.沸石分子筛的合成方法大多采用水热法,需要使用大量含硅铝的化工产品和有机模板剂,导致沸石分子筛的合成成本较高、效率较低,且环境污染较为严重,因此沸石分子筛高效绿色合成路线的研究具有重大意义.本文主要从沸石分子筛的合成原料绿色化、合成条件绿色化以及合成方法绿色化等三个方面综述了国内外沸石分子筛绿色合成路线的研究新进展,并提出现有沸石分子筛绿色合成路线存在的问题以及将来的发展方向.     

羟基自由基在沸石分子筛合成中的作用

沸石分子筛由于具有独特的形选催化作用及可调的酸性, 已成为化学工业中最重要的固体催化材料. 沸石分子筛的合成主要基于碱性条件下的水热晶化, OH^?被认为起到催化硅铝物种的解聚及聚合作用. 近年来, 研究者发现了羟基自由基加速分子筛的水热晶化机制. 通过利用紫外光照射或芬顿反应等物理或化学方法向分子筛合成体系引入羟基自由基, 可以实现沸石分子筛的加速晶化及高硅沸石分子筛的合成. 理论计算结果表明, 羟基自由基可以促进Si—O—Si 键的断裂和重新生成, 从而显著加快分子筛成核并促进硅原子进入骨架. 本综述介绍了羟基自由基在沸石分子筛晶化方面的最新研究进展, 探讨了羟基自由基的主要作用和优势, 并对沸石分子筛合成的羟基自由基路线发展前景进行了展望.     

羟基自由基在沸石分子筛合成中的作用（英文）

沸石分子筛由于具有独特的形选催化作用及可调的酸性,已成为化学工业中最重要的固体催化材料.沸石分子筛的合成主要基于碱性条件下的水热晶化, OH-被认为起到催化硅铝物种的解聚及聚合作用.近年来,研究者发现了羟基自由基加速分子筛的水热晶化机制.通过利用紫外光照射或芬顿反应等物理或化学方法向分子筛合成体系引入羟基自由基,可以实现沸石分子筛的加速晶化及高硅沸石分子筛的合成.理论计算结果表明,羟基自由基可以促进Si—O—Si键的断裂和重新生成,从而显著加快分子筛成核并促进硅原子进入骨架.本综述介绍了羟基自由基在沸石分子筛晶化方面的最新研究进展,探讨了羟基自由基的主要作用和优势,并对沸石分子筛合成的羟基自由基路线发展前景进行了展望.     

丝光沸石骨架中Fe的XAFS表征

通过水热法合成了骨架含铁的杂原子丝光沸石,采用XRD,FT-IR及TPR等表征技术确认铁进入了分子筛骨架。利用XAFS地分子筛中铁的精细结构和配位环境进行了表征和计算,近边吸收的Fe-K边前跃迁证实铁在分子筛骨架中位于四面体配位环境中,与邻近原子存在共价键作用;铁-氧配位键长为0.188～0.189nm.     

丝光沸石骨架中Fe的XAFS表征

通过水热法合成了骨架含铁的杂原子丝光沸石,采用XRD,FT-IR及TPR等表征技术确认铁进入了分子筛骨架。利用XAFS地分子筛中铁的精细结构和配位环境进行了表征和计算,近边吸收的Fe-K边前跃迁证实铁在分子筛骨架中位于四面体配位环境中,与邻近原子存在共价键作用;铁-氧配位键长为0.188～0.189nm.     

Ce-Beta分子筛的制备及其催化性能（英文）

采用简单、易重现的两步后合成法成功制备了Ce-Beta分子筛.制备过程中,H-Beta分子筛首先经过脱铝处理得到Si-Beta分子筛,然后再以异丙醇铈为前驱体,通过干法浸渍的途径向Si-Beta分子筛引入Ce(IV).利用XRD,FT-IR,UV-Vis和1H MAS NMR等对其结构进行了表征,结果表明,Ce(IV)物种以四配位的形式成功引入Beta分子筛的骨架,Ce原子进入分子筛骨架的机理通过DRIFT光谱得以证实.通过环氧化合物水合制备1,2-二醇反应对所制的Ce-Beta催化剂进行了催化性能评价.     

骨架杂原子对Y型分子筛结构稳定性的影响

采用水热晶化法合成了含骨架杂原子的Y分子筛(BY、TiY、FeY),并对经过离子交换及超稳处理后得到的超稳型USY、USBY、USTiY和USFeY分子筛进行了水热处理和差示扫描量热测定,考察了杂原子B、Ti、Fe对Y分子筛结构稳定性的影响.结果表明;杂原子Ti的引人,明显提高了Y分子筛的热及水热稳定性;而杂原子B、Fe的引入则降低了Y分子筛的热及水热稳定性,特别是FeY分子筛的水热稳定性下降较多.     

SAPO-11/Beta复合分子筛的合成及其异构化性能研究

以Beta分子筛为硅源通过水热合成法合成了SAPO-11/Beta复合分子筛,采用X射线衍射、N2物理吸脱附、扫描电镜、透视电镜-能谱分析、固体核磁及吡啶红外等方法对单分子筛、复合分子筛和机械混合分子筛的物化性质进行了表征.以正十二烷为模型化合物,在固定床反应器上考察了铂负载型分子筛催化剂的异构化性能.结果表明,复合分子筛的物理化学性质明显不同于单分子筛和机械混合分子筛,其呈现核壳结构,SAPO-11和Beta间存在化学作用,使得复合分子筛具有适宜的B酸分布.在正十二烷异构化反应中,复合分子筛催化剂的异构化性能优于单分子筛催化剂和机械混合分子筛催化剂,多支链异构体收率高.     

Ethanol electrooxidation on Pt/ZSM-5 zeolite-C catalyst

The electrooxidation of ethanol on Pt/ZSM-5 zeolite-C catalyst was investigated in sulfuric acid aqueous solution. Because of high stability in general acidic solution, ZSM-5 zeolite particles were selected as the support and the second catalyst. The micrograph and elemental composition of Pt/ZSM-5 zeolite particles were characterized by scanning electron microscopy and energy disperse X-ray spectroscopy. The electrocatalytic properties of Pt/ZSM-5 zeolite-C catalyst for ethanol oxidation have been investigated by cyclic voltammetry. Under the same Pt-loading mass and experimental conditions for ethanol oxidation, Pt/ZSM-5 zeolite-C catalyst shows higher activity than Pt/C catalyst. Additionally, Pt/ZSM-5 zeolite-C catalyst possesses good long-term cycle stability. The results indicate that Pt/ZSM-5 zeolite-C catalyst may have good potential application in direct ethanol fuel cell.     

Different oxidation routes for lattice oxygen recovery of double-perovskite type oxides LaSrFeCoO_6 as oxygen carriers for chemical looping steam methane reforming

Double-perovskite type oxide LaSrFeCoO_6(LSFCO) was used as oxygen carrier for chemical looping steam methane reforming(CL-SMR) due to its unique structure and reactivity. Two different oxidation routes,steam-oxidation and steam-air-stepwise-oxidation, were applied to investigate the recovery behaviors of the lattice oxygen in the oxygen carrier. The characterizations of the oxide were determined by X-ray diffraction(XRD), X-ray photoelectron spectroscopy(XPS), hydrogen temperature-programmed reduction(H_2-TPR) and scanning electron microscopy(SEM). The fresh sample LSFCO exhibits a monocrystalline perovskite structure with cubic symmetry and high crystallinity, except for a little impurity phase due to the antisite defect of Fe/Co disorder. The deconvolution distribution of XPS patterns indicated that Co,and Fe are predominantly in an oxidized state(Fe~(3+) and Fe~(2+)) and(Co~(2+) and Co~(3+)), while O 1s exists at three species of lattice oxygen, chemisorbed oxygen and physical adsorbed oxygen. The double perovskite structure and chemical composition recover to the original state after the steam and air oxidation, while the Co ion cannot incorporate into the double perovskite structure and thus form the CoO just via individual steam oxidation. In comparison to the two different oxidation routes, the sample obtained by steam-oxidation exhibits even higher CH_4 conversion, CO and H_2 selectivity and stronger hydrogen generation capacity.     

多级孔无铝Beta分子筛的合成与表征

研究了氟介质条件下,合成参数对前驱体黏度和无铝Beta分子筛晶化过程的影响.X射线衍射结果表明,高水硅比可降低前驱体的黏度,但抑制分子筛的晶化.当合成体系中加入成核促进剂(二氧化锗)和晶化促进剂(高氯酸根或磷酸根)后,即使水硅摩尔比高达20~30,在150℃水热合成4 d,仍可获得高结晶性、微米级球形或多面体形无铝Beta分子筛.热重和能谱分析结果表明,极少量高氯酸根和磷酸根可进入分子筛孔道,并影响模板剂四乙基铵根离子的热分解过程.氮气吸附-脱附、扫描电子显微镜、透射电子显微镜和选区电子衍射分析结果表明,所得无铝Beta分子筛具有多级孔结构,介孔尺寸在3.4~3.8 nm之间,由纳米晶体或纳米棒堆积而成.     

Stabilization of Extra-Large-Pore Zeolite by Boron Substitution for the Production of Commercially Applicable Catalysts

Stable extra-large-pore zeolites are desirable for industrial purposes due to their ability to accommodate bulky reactants and diffusion through channels. Although there are several extra-large pore zeolites reported, stable ones are rare. Thus, their stabilization is a feasible strategy for industrial applications. Here, an extra-large-pore zeolite EWT with boron substitution is presented, and the resulting zeolite B-RZM-3 increased the thermal stability from 600 °C in its silica form to 850 °C. The crystal structure, determined by combining continuous rotation electron diffraction (cRED) and powder X-ray diffraction (PXRD), shows that B atoms preferentially substitute the interrupted (HO)T(OT)₃ (Q³) sites and are partially converted into 3-coordination to relax framework deformation upon heating. After Al-reinsertion post-treatment, Al-B-RZM-3 shows higher ethylbenzene selectivity and ethylene conversion rate per mol acid site than commercial ZSM-5 and Beta zeolite in benzene alkylation reaction. Synthesizing extra-large-pore zeolite in borosilicate form is a potential approach to stabilize interrupted zeolites for commercial applications.     

Au/SBA-15 的制备及其催化 CO 氧化反应性能

 以 SBA-15 为载体, 采用沉积沉淀法制备了纳米 Au 催化剂, 研究了不同预处理条件对 Au 在载体表面状态的影响, 考察了催化剂样品催化 CO 氧化性能. 以高分辨率透射电子显微镜、N2 吸附、X 射线衍射、紫外-可见漫反射吸收谱、X 射线光电子能谱和电感耦合等离子体发射光谱等手段对催化剂的结构和表面性质进行了表征. 结果表明, 经还原焙烧处理后的 Au/SBA-15 催化剂热稳定性较好, Au 在 SBA-15 孔道表面呈高分散状态, 样品在 CO 氧化反应中表现出优异的低温催化活性和高温稳定性, 同时具有优异的抗烧结性能和良好的循环稳定性.     

杂原子Sn-β分子筛的脱铝补位两步法制备、表征及其催化环己酮Baeyer-Villiger氧化性能

采用酸处理Al-β脱铝以产生T"空位",再高温焙烧插入Sn,即脱铝补位两步法制备了杂原子Sn-β分子筛.考察了β沸石中T"空位"数量、母体硅铝比和焙烧温度等因素对Sn-β分子筛形成与性能的影响,并利用X射线衍射、红外光谱、紫外-可见光谱、扫描电镜、X射线荧光光谱和电感耦合等离子体原子发射光谱等手段及环己酮Baeyer-Villiger(B-V)氧化反应,对催化剂进行了表征和评价.结果表明,脱铝补位两步法可以制备Sn-β分子筛,且Sn以四配位形式存在于分子筛骨架中,在对环己酮B-V氧化反应中表现出较高的催化活性.     

Mechanism of homogeneously and heterogeneously catalysed Meerwein-Ponndorf-Verley-Oppenauer reactions for the racemisation of secondary alcohols

The mechanism of hydrogen transfer from alcohols to ketones, catalysed by lanthanide(III) isopropoxides or zeolite Beta has been studied. For the lanthanide catalysed reactions, (S)-1-phenyl-(1-(2)H(1))ethanol and acetophenone were used as case studies to determine the reaction pathway for the hydrogen transfer. Upon complete racemisation all deuterium was present at the 1-position, indicating that the reaction exclusively takes place via a carbon-to-carbon hydrogen transfer. Zeolite Beta with different Si/Al ratios was applied in the racemisation of (S)-1-phenylethanol. In this case the racemisation does not proceed via an oxidation/reduction pathway but via elimination of the hydroxy group and its re-addition. This mechanism, however, is not characteristic for all racemisation reactions with zeolite Beta. When 4-tert-butyl cyclohexanone is reduced with this catalyst, a classical MPV reaction takes place exclusively. This demonstrates that zeolite Beta has a substrate dependent reaction pathway.     

Pt@Au/Al2O3核壳纳米粒子的制备和表征及其在催化氧化甲苯中的应用

Customizing core-shell nanostructures is considered to be an efficient approach to improve the catalytic activity of metal nanoparticles. Various physiochemical and green methods have been developed for the synthesis of core-shell structures. In this study, a novel liquid-phase hydrogen reduction method was employed to form core-shell Pt@Au nanoparticles with intimate contact between the Pt and Au particles, without the use of any protective or structure-directing agents. The Pt@Au core-shell nanoparticles were prepared by depositing Au metal onto the Pt core; AuCl⁴⁻ was reduced to Au(0) by H₂ in the presence of Pt nanoparticles. The obtained Pt@Au core-shell structured nanoparticles were characterized by transmission electron microscopy (TEM), energy-dispersive X-ray spectroscopy (EDX), high-resolution TEM, fast Fourier transform, powder X-ray diffraction (PXRD), X-ray photoelectron spectroscopy (XPS), Fourier transform infrared spectroscopy (FTIR), and H₂-temperature programmed reduction (H₂-TPR) analyses. The EDX mapping results for the nanoparticles, as obtained from their scanning transmission electron microscopy images in the high-angle annular dark-field mode, revealed a Pt core with Au particles grown on its surface. Fourier transform measurements were carried out on the high-resolution structure to characterize the Pt@Au nanoparticles. The lattice plane at the center of the nanoparticles corresponded to Pt, while the edge of the particles corresponded to Au. With an increase in the Au content, the intensity of the peak corresponding to Pt in the FTIR spectrum decreased slowly, indicating that the Pt nanoparticles were surrounded by Au nanoparticles, and thus confirming the core-shell structure of the nanoparticles. The XRD results showed that the peak corresponding to Pt shifted gradually toward the Au peak with an increase in the Au content, indicating that the Au particles grew on the Pt seeds; this trend was consistent with the FTIR results. Hence, it can be stated that the Pt@Au core-shell structure was successfully prepared using the liquid-phase hydrogen reduction method. The catalytic activity of the nanoparticles for the oxidation of toluene was evaluated using a fixed-bed reactor under atmospheric pressure. The XPS and H₂-TPR results showed that the Pt₁@Au₁/Al₂O₃ catalyst had the best toluene oxidation activity owing to its lowest reduction temperature, lowest Au 4d & 4f and Pt 4d & 4f binding energies, and highest Au⁰/Au^δ+ and Pt⁰/Pt²⁺ proportions. The Pt₁@Au₂Al₂O₃ catalyst showed high stability under dry and humid conditions. The good catalytic performance and high selectivity of Pt@Au/Al₂O₃ for toluene oxidation could be attributed to the high concentration of adsorbed oxygen species, good low-temperature reducibility, and strong interaction.     

负载型金催化剂催化乙醇选择氧化反应

选择不同氧化物(Al2O3,SiO2,TiO2,MgO)和H-ZSM-5分子筛作为载体,以尿素为沉淀剂,采用沉积-沉淀法制备了一系列负载型金催化剂.采用X射线衍射、电感耦合等离子体发射光谱、程序升温还原、NH3程序升温脱附和透射电镜等技术对催化剂样品进行了表征,并测定了催化剂对乙醇选择氧化反应的催化性能.选择Au/Al2O3催化剂,考察了金负载量、反应条件(温度、压力、时间)和添加剂对乙醇选择氧化反应的影响.结果表明,所制备的Au/Al2O3催化剂的金负载率较高,金粒子较小(3～4 nm)且分布均匀.载体对金催化剂催化乙醇氧化反应有显著影响,主要产物为乙醛、乙酸乙酯和缩醛.以TiO2为载体时,乙醇转化率较高.以Al2O3为载体时,乙酸乙酯选择性较高;少量碱性添加剂可抑制缩醛的生成,并可提高乙醇转化率和乙酸乙酯选择性.在优化的条件下,乙醇转化率可达4.7%,乙酸乙酯选择性可达93.5%.