限域于SBA-15孔道内的活性相聚集形态

针对Pd/SBA-15和MoO3/SBA-15两类催化剂样品,使用N2物理吸附手段对比研究了限域于介孔SBA-15分子筛孔道内活性相Pd与MoO3的聚集形态.结果表明,金属Pd以颗粒状形态分布在SBA-15分子筛孔道内,氧化物MoO3则以层状形态存在.并用高分辨透射电镜验证了此分析结果.     

含钨SBA-15介孔分子筛催化剂的表面酸性和羟基分布

分别以浸渍法和水热晶化法制备了SBA-15介孔分子筛孔中插入氧化钨和碳化钨的催化剂,采用NH3-TPD测定了表面酸性和总酸量,并采用FT-IR研究了它们的表面羟基分布情况.NH3-TPD结果表明,浸渍法制备的含氧化钨的SBA-15介孔分子筛催化剂表面只有SBA-15介孔分子筛的弱酸位,而含碳化钨的SBA-15介孔分子筛催化剂表面还出现了W2C的强酸位.水热晶化法制备的含氧化钨的SBA-15介孔分子筛催化剂表面SBA-15介孔分子筛的弱酸位随W含量的增大略有增强, W含量较高时还出现了钨物种的强酸位;含碳化钨的SBA-15介孔分子筛催化剂表面除了SBA-15介孔分子筛的弱酸位外, W含量较低时有W2C的强酸位, W含量较高时有W2C和WC两种强酸位.傅里叶变换红外光谱结果表明,浸渍法和水热晶化法制备的含氧化钨和碳化钨的SBA-15介孔分子筛催化剂除表面自由硅羟基外,还存在着α, β和γ三种不同类型的氢键羟基,并且氢键羟基和催化剂的制备方法以及催化剂的W含量都有一定的关系.     

W-SBA-15介孔分子筛的直接合成及其对环己烯环氧化反应的催化性能

 分别以Na2WO4和H2WO4为钨源,以正硅酸四乙酯为硅源直接合成了W-SBA-15介孔分子筛样品,并用小角XRD,N2吸附,FT-IR,UV-Vis,SEM和XRF等手段对合成的分子筛进行了表征. 结果表明,只用P123(EO20PO70EO20)为模板剂时,分子筛中钨的含量只是投料量的一半; 而以P123和十六烷基三甲基溴化铵为混合模板剂时,钨能有效地掺杂到SBA-15分子筛中. 当原料中的Si/W摩尔比为40时,W-SBA-15分子筛中的钨物种以高度分散状态存在,且以H2WO4为钨源比以Na2WO4为钨源更易将钨掺杂到SBA-15介孔分子筛中. W-SBA-15分子筛催化剂对环己烯环氧化反应具有较高的催化活性.     

SBA-15负载钒氧化物催化剂上甲烷选择氧化反应

对SBA-15负载的钒、钼、钨氧化物催化的甲烷选择氧化反应性能进行了比较,发现VO_x/SBA-15催化剂优于MoOx/SBA-15和WOx/SBA-15催化剂.针对钒氧化物催化剂,考察了不同钒源、不同载体以及少量P元素的添加对催化性能的影响,结果表明以SBA-15为载体的催化剂的性能好于MCM-41和Cab-O-Sil为载体的催化剂;与V₂O₅,VO(C₂O₄)相比,NH₄VO₃是制备性能良好的VO_x/SBA-15的钒源;在VO_x/SBA-15中,添加少量P元素后,HCHO的选择性有一定程度的提高.XRD,N₂物理吸附、UN-Raman和H₂-TPR表征结果表明,负载量低于3 wt%时,钒组分可能主要以高分散的单核的VO_x物种存在,我们推测该物种对甲烷选择氧化制甲醛起关键作用.     

SBA-15介孔分子筛担载的钒基氧化物催化剂对乙烷选择氧化性能

用等体积浸渍法制备了SBA-15担载的钒基(V/SBA-15)和钾修饰的钒基氧化物(K-V/SBA-15)催化剂, 使用氮气吸附、小角X射线衍射(XRD)、紫外-可见漫反射光谱(UV-Vis DRS)和紫外激光拉曼光谱对这些催化剂的结构进行表征, 并评价了这些催化剂对乙烷选择氧化的活性与选择性. 实验结果表明介孔结构SBA-15对乙烷选择氧化的活性优于常规的SiO2; 对于SBA-15担载的V/SBA-15和K-V/SBA-15催化剂, 极低钒担载量(nV:nSi≤0.1:100)时隔离的四配位钒氧化物是乙烷选择氧化生成醛类化合物的活性物种, 高钒担载量(nV:nSi≥2.5:100)时聚合的和微晶态的钒氧化物是乙烷氧化脱氢或深度氧化的活性物种.     

低浓度液体酸介质中快速合成SBA-15分子筛

通过在低浓度无机液体酸介质中添加少量磷钼酸(HPMo), 成功地合成了高度有序的SBA-15介孔分子筛. N₂吸附-脱附、XRD、TEM和水热稳定性实验等检测结果表明: 用这种方法不仅可以大幅度降低合成SBA-15分子筛所需液体酸的用量和缩短晶化时间, 同时反应产物SBA-15在100 ℃的水中处理72 h后仍然保持六方有序的介孔结构.     

CuO/SBA-15催化剂上巴豆醛选择性加氢

通过γ-氨丙基三甲氧基硅烷(APTS)偶联与Cu2 离子络合两步法将CuO负载到介孔分子筛SBA-15上,制得CuO/SBA-15催化剂,考察了催化剂的巴豆醛选择性加氢反应性能.通过X射线粉末衍射、氮气吸脱附和程序升温还原(TPR)技术对催化剂进行了表征.结果表明,SBA-15分子筛负载CuO后保持原有的介孔结构,但是孔容和比面表积随着CuO负载量的增大而下降.TPR结果表明CuO/SBA-15系列催化剂有三种CuO物种:高分散CuO、晶相CuO和进入SBA-15分子筛骨架的Cu2 .高分散CuO物种对巴豆醛加氢反应的催化活性最高,晶相CuO物种次之,而进入SBA-15分子筛骨架的Cu2 物种几乎没有活性.     

铝修饰改性对SBA-15分子筛性质及催化剂性能的影响

分别采用调变pH值合成法和后处理嫁接法制备了铝修饰改性的SBA-15分子筛,通过XRD、Al核磁、N₂吸附脱附、NH₃-TPD等方法对改性分子筛的理化性质进行了分析表征,考察了不同的Al修饰改性方法对分子筛性质和加氢裂化催化剂性能的影响。结果表明,调变pH值合成法能够有效地对SBA-15进行Al改性,得到的Al-SBA-15分子筛具有高度有序的六方孔道结构,较好的水热稳定性。Al的引入提高了SBA-15的表面酸性,并使其在加氢裂化反应中表现出较好的中油选择性。     

介孔Ni-β-Mo2C/SBA-16催化剂在CH4/CO2重整制合成气反应中的催化性能

采用等体积浸渍将双金属活性组分负载到介孔分子筛SBA-16上,通过热分解制备了负载型催化剂Ni--Mo2C/SBA-16.N2吸附-脱附、X射线粉末衍射和透射电镜等结果表明,引入活性组分后,样品依然保持原有的有序介孔结构,活性组分高度分散于载体上,没有团聚.在CH4/CO2重整制合成气反应中,Ni--Mo2C/SBA-16催化剂具有较高的CH4和CO2转化率,以及CO和H2选择性,有明显的抗积炭作用.     

磺酸基功能化的有序SBA-15-SO3H介孔分子筛的合成及其在苯酚叔丁基化反应中的应用

通过一步法合成了SBA-15-SO3H介孔分子筛,用XRD,TEM,低温N2吸附和吡啶吸附红外光谱等方法进行了表征,并研究了其在苯酚叔丁基化反应中的催化性能.结果表明,SBA-15-SO3H保持了母体SBA-15高度有序的六方介孔结构,具有较强的酸性和热稳定性,且在苯酚叔丁基化反应中表现较好的催化活性和2,4-二叔丁基苯酚选择性.     

Immobilization and activation of 2,6-bis(imino)pyridyl Fe, Cr and V precatalysts using a MgCl2/AlRn(OEt)3−n support: Effects on polyethylene molecular weight and molecular weight distribution

Ethylene polymerizations carried out with various bis(imino)pyridyl iron, chromium and vanadium complexes immobilized on a MgCl₂/AlR_n(OEt)_3−n support gave relatively broad polyethylene molecular weight distributions in the case of iron, but high molecular weight and a very narrow molecular weight distribution with vanadium, indicative of a single active species. The narrow MWD was confirmed by melt rheometry. Similar results were obtained after reaction of the bis(imino)pyridyl complex LVCl₃ (6) with MeLi or AlEt₃, where alkylation of the pyridine ring gives a complex L′VCl₂ (7). In the case of chromium, a bimodal distribution was obtained, with evidence of incomplete catalyst immobilization. The polyethylene molecular weights obtained with the iron complexes were strongly dependent on the substituents in the bis(imino)pyridyl ligand, and were somewhat higher than have been obtained in homogeneous polymerization. In contrast, the molecular weights obtained with the bis(imino)pyridyl chromium and vanadium complexes were much higher that those previously obtained under homogeneous conditions. In all cases, the activities of the immobilized catalysts were higher than those found in homogeneous polymerization.     

Spectroscopic characterization and electrocatalytical activity of tetrapyridylporphyrins intercalated into hydrated vanadium(V) oxide

The intercalation ofmeso-tetrapyridylporphyrins into hydrated vanadium(V) pentoxide has been studied using X-ray diffraction; FTIR, electronic and Mössbauer spectroscopy; cyclic voltammetry and spectroelectrochemistry. The intercalation compound containing iron tetrapyridylporphyrin exhibits pronounced electrocatalytical activity in the reduction of molecular dioxygen, reflecting an enhanced reactivity of the catalyst in a confined medium.     

Is vanadium a more versatile target in the activity of primordial life forms than hitherto anticipated?

The two predominant forms of vanadium occurring in the geo-, aqua- and biosphere, soluble vanadate(V) and insoluble oxovanadium(IV) (vanadyl), are subject to bacterial activity and transformation. Bacteria belonging to genera such as Shewanella, Pseudomonas and Geobacter can use vanadate as a primary electron acceptor in dissimilation or respiration, an important issue in the context of biomineralisation and soil detoxification. Azotobacter, which can employ vanadium as an essential element in nitrogen fixation, secretes a vanadophore which enables the uptake of vanadium(V). Siderophores secreted by other bacteria competitively (to ferric iron) take up vanadyl and thus interfere with iron supply, resulting in bacteriostasis. The halo-alkaliphilic Thioalkalivibrio nitratireducens possibly uses vanadium as a constituent of an alternative, molybdopterin-free nitrate reductase. Marine macro-algae can generate a variety of halogenated organic compounds by use of vanadate-dependent haloperoxidases, and a molecular vanadium compound, amavadin, from Amanita mushrooms has turned out to be an efficient catalyst in oxidation reactions. The present account is a focused and critical review of the current knowledge of the interplay of bacteria and other primitive forms of life (cyanobacteria, algae, fungi and lichens) with vanadium, with the aim to provide perspectives for applications and further investigations.     

Comparative dimerization of 1-butene with a variety of metal catalysts, and the investigation of a new catalyst for C=H bond activation

Catalytic dimerization of 1-butene by a variety of catalysts is carried out, and the products are analyzed by gas chromatography and mass spectrometry. Catalysts based on cobalt and iron can produce highly linear dimers, with the cobalt-based dimers exceeding 97 % linearity. Catalysts based on vanadium and aluminum prefer to make branched dimers, which are most often methyl-heptenes in the case of vanadium and almost exclusively 2-ethyl-1-butene in the case of aluminum. The vanadium catalyst also produces substantial amounts of dienes and alkanes, suggesting a competing hydrogenation/dehydrogenation pathway that appears to involve vinyl Cbond;H bond activation. Nickel catalysts are generally less selective than those based on iron or cobalt for making linear dimers, but they can make dimers with 60 % linearity. The major by-products for the nickel systems are trisubstituted internal olefins. An important side reaction that must be considered for dimerization reactions is 1-butene isomerization to 2-butene, which makes recycling the butene difficult for a linear dimerization process. Aluminum, iron, and vanadium systems promote very little isomerization, but nickel and cobalt systems tend to isomerize the undimerized substrate heavily.     

Preparation and characterization of vanadium(IV) oxide supported on SBA-15 and its catalytic performance in benzene hydroxylation to phenol using molecular oxygen

Preparation of dispersed transition metal oxides catalyst with low oxidation state still remains a challenging task in heterogeneous catalysis.In this study,vanadium oxides supported on zeolite SBA-15 have been prepared under hydrothermal condition using V 2 O 5 and oxalic acid as sources of vanadium and reductant,respectively.The structures of samples,especially the oxidation state of vanadium,and the surface distribution of vanadium oxide species,have been thoroughly characterized using various techniques,including N 2-physisorption,X-ray diffraction(XRD),transmission electron microscopy(TEM),X-ray photoelectron spectroscopy(XPS),UV-visible spectra(UV-Vis) and UV-visible-near infrared spectra(UV-Vis-NIR).It is found that the majority of supported vanadium was in the form of vanadium(IV) oxide species with the low valence of vanadium.By adjusting hydrothermal treatment time,the surface distribution of vanadium(IV) oxide species can be tuned from vanadium(IV) oxide cluster to crystallites.These materials have been tested in the hydroxylation of benzene to phenol in liquid-phase with molecular oxygen in the absence of reductant.The catalyst exhibits high selectivity for phenol(61%) at benzene conversion of 4.6%,which is a relatively good result in comparison with other studies employing molecular oxygen as the oxidant.     

Effect of the Vanadium Content in V2O5/SiO2 Catalysts on Their Activity and Selectivity in the Partial Oxidation of Methane

The effect of the vanadium content on the catalytic characteristics of samples of V₂O₅/SiO₂, prepared by molecular layering, was investigated. It was shown that in the region of relatively small vanadium contents in the catalyst its surface concentration does not affect the selectivity of the process. The obtained relation between the initial selectivity and the relative reactivity of formaldehyde and the surface density of oxide-vanadium groups in the deposited catalyst is discussed.     

添加钒对Pd/Al2O3-TiO2 催化剂上醇醛催化氧化性能及表面特性的影响

采用浸渍法分别制备了Pd/Al₂O₃-TiO₂、V/Al₂O₃-TiO₂和不同钒含量的V-Pd/Al₂O₃-TiO₂催化剂,并对乙醇、乙醛的完全催化氧化性能进行了测试。结果表明,添加适量的钒组分(1%~3%)能够有效地提高催化剂的深度氧化活性。采用XRD、NH₃-TPD、N₂吸附等技术分析研究催化剂的表面特性与催化活性之间的关系,发现Pd/Al₂O₃-TiO₂催化剂添加适量钒组分后,调变了催化剂的表面酸性、比表面积和孔容,使得V组分和Pd组分与载体之间产生较强的相互作用,双金属组分的协同效应提高了催化剂对乙醇、乙醛的深度氧化活性。     

Effect of Manganese Incorporation Manner on an Iron-Based Catalyst for Fischer-Tropsch Synthesis

A systematic study was undertaken to investigate the effects of the manganese incorpo- ration manner on the textural properties,bulk and surface phase compositions,reduction/carburization behaviors,and surface basicity of an iron-based Fischer-Tropsch synthesis(FTS)catalyst.The cata- lyst samples were characterized by N_2 physisorption,X-ray photoelectron spectroscopy(XPS),H_2(or CO)temperature-programmed reduction(TPR),CO_2 temperature-programmed desorption(TPD),and M(?)ssbauer spectroscopy.The FTS performance of the catalysts was studied in a slurry-phase continuously stirred tank reactor(CSTR).The characterization results indicated that the manganese promoter incor- porated by using the coprecipitation method could improve the dispersion of iron oxide,and decrease the size of the iron oxide crystallite.The manganese incorporated with the impregnation method is enriched on the catalyst's surface.The manganese promoter added with the impregnation method suppresses the reduction and carburization of the catalyst in H_2,CO,and syngas because of the excessive enrichment of manganese on the catalyst surface.The catalyst added manganese using the coprecipitation method has the highest CO conversion(51.9%)and the lowest selectivity for heavy hydrocarbons(C_(12 )).     

掺杂Fe作为第二种金属组分的V-HMS催化剂的苯羟基化反应

采用浸渍法在V-HMS中引入第二种金属组分(Fe、Al、Cu、Ni、Co、Mo、Cr)以提高催化剂在H2O2为氧化剂的苯羟基化反应中的催化性能.筛选发现,Fe在所研究的金属组分中最为有效.进一步采用共合成法制备了一系列FexVy-HMS催化剂.采用粉末X射线衍射、N2物理吸附、透射电子显微镜、NH3程序升温脱附、H2程序升温还原等手段对催化剂的结构和性质进行表征,结果表明,HMS仍保持介孔结构,Fe的加入在催化剂中产生了新的酸性位和更强的氧化还原性.在苯羟基化反应中,钒物种是反应活性物种,铁物种起助剂作用,其中Fe0.04V0.06-HMS具有最高的催化活性,苯酚收率由不含Fe的Fe0.00V0.06-HMS的13.1%提高到18.1%.提出了Fe、V参与反应过程的可能机理.     

Theoretical and Experimental Study on Reaction Coupling： Dehydrogenation of Ethylbenzene in the Presence of Carbon Dioxide

Dehydrogenation of ethylbenzene (EB) to styrene (ST) in the presence of CO2, in which EB dehydrogenation is coupled with the reverse water-gas shift (RWGS), was investigated extensively through both theoretical analysis and experimental characterization. The reaction coupling proved to be superior to the single dehydrogenation in several respects. Thermodynamic analysis suggests that equilibrium conversion of EB can be improved greatly by reaction coupling due to the simultaneous elimination of the hydrogen produced from dehydrogenation. Catalytic tests proved that iron and vanadium supported on activated carbon or Al2O3 with certain promoters are potential catalysts for this coupling process. The catalysts of iron and vanadium are different in the reaction mechanism, although ST yield is always associated with CO2 conversion over various catalysts. The two-step pathway plays an important role in the coupling process over Fe/Al2O3, while the one-step pathway dominates the reaction over V/Al2O3. Coke deposition and deep reduction of active components are the major causes of catalyst deactivation. CO2 can alleviate the catalyst deactivation effectively through preserving the active species at high valence in the coupling process, though it can not suppress the coke deposition.