机械球磨固相化学反应制备AlH3及其放氢性能

以LiAlH4和AlCl3为原料, 采用机械球磨固相化学反应方法制备了铝氢化合物, 通过X射线衍射(XRD)、热分析(TG-DSC)和质谱(MS)分析等方法对反应产物进行分析和表征, 研究了不同球磨时间(4、8、15和20 h)对LiAlH4+AlCl体系的固相反应转变规律﹑合成产物和放氢性能的影响. 研究结果表明, 随球磨时间的增加, 球磨固相反应按3LiAlH4+AlCl3→4AlH3+3LiCl方向进行, 形成了非晶态铝氢化合物AlH3, 球磨20 h时反应基本完全. 球磨产物的放氢动力学特性随球磨时间增加而改善, 其放氢起始温度均低于100 ℃, 最大放氢量达到2.6%-3.6%(H2)(w), 接近反应体系的理论储氢量4.85%(H2)(w). 球磨过程中反应产物形成LiCl·H2O以及少量AlH3发生分解是影响球磨产物最大放氢量的主要因素.     

异丁烷脱氢催化剂V-O-Al水热-流体干燥法合成

负载型 V2 O5催化剂被广泛应用于烃的氧化、低碳烃的氧化脱氢及 NOx的 NH3 还原等催化反应[1～ 3 ] .对于低碳烃脱氢 ,Cr2 O3 和 Pt体系研究较多 ,而 V2 O5体系则鲜有报道[4 ,5] .水热合成方法是合成各种分子筛的常用方法 ,同时也被广泛用于合成多种无机功能材料 (如纳米材料 ,     

K2O-Fe2O3系催化剂的穆斯堡尔谱研究

利用穆斯堡尔谱在K2 O Fe2 O3催化剂中检出了α Fe2 O3(大晶粒及微晶 )、KFeO2 、K1 XFe11O17、α FeOOH和γ FeOOH等物相 ,它们的相对含量取决于催化剂的含钾量及煅烧温度 ,相对含量的改变导致样品的穆斯堡尔谱图出现了复杂的变化 .与XRD相比 ,穆斯堡尔谱可对钾与氧化铁的相互作用进行更有效的表征 ,穆斯堡尔谱和TPR研究都表明钾可延缓催化剂中Fe(III)的被还原 .     

硫化镉晶体结构形态对乙醇光催化脱氢活性的影响

有关醇类水溶液光催化贮能脱氢反应研究大多集中在提高半导体TiO₂和CdS表面修饰组分的光催化活性^[1～3]及考察TiO₂半导体晶体结构与光催化性能的关系上^[4,5],CdS半导体晶体结构形态对光催化性能的影响尚未见报道.本文在这方面进行了一些有益的研究.     

Ga-N共同掺杂CoP催化氨硼烷制氢机理的理论研究

本文通过密度泛函理论(DFT),计算研究了金属原子Ga和非金属原子N共同掺杂磷化钴(Co P)作为催化剂催化氨硼烷(NH₃BH₃)的脱氢过程．在这里,我们设计了四条可行的反应路径,并且计算了每条路径中间体过渡态的能量．通过研究结果得出结论,路径Ⅱ为最优反应路径．这将为金属和非金属共同掺杂Co P催化NH₃BH₃脱氢反应提供一定的理论基础．     

Surface Engineering of Titania Boosts Electroassisted Propane Dehydrogenation at Low Temperature

Electric field catalysis using surface proton conduction, in which proton hopping and collision on the reactant are promoted by external electricity, is a promising approach to break the thermodynamic equilibrium limitation in endothermic propane dehydrogenation (PDH). This study proposes a catalyst design concept for more efficient electroassisted PDH at low temperature. Sm was doped into the anatase TiO₂ surface to increase surface proton density by charge compensation. Pt−In alloy was deposited on the Sm-doped TiO₂ for more favorable proton collision and selective propylene formation. The catalytic activity in electroassisted PDH drastically increased by doping an appropriate amount of Sm (1 mol % to Ti) where the highest propylene yield of 19.3 % was obtained at 300 °C where the thermodynamic equilibrium yield was only 0.5 %. Results show that surface proton enrichment boosts alkane dehydrogenation at low temperature.     

Controlling Metal-Oxide Reducibility for Efficient C−H Bond Activation in Hydrocarbons

Knowing the structure of catalytically active species/phases and providing methods for their purposeful generation are two prerequisites for the design of catalysts with desired performance. Herein, we introduce a simple method for precise preparation of supported/bulk catalysts. It utilizes the ability of metal oxides to dissolve and to simultaneously precipitate during their treatment in an aqueous ammonia solution. Applying this method for a conventional VO_x−Al₂O₃ catalyst, the concentration of coordinatively unsaturated Al sites was tuned simply by changing the pH value of the solution. These sites affect the strength of V−O−Al bonds of isolated VO_x species and thus the reducibility of the latter. This method is also applicable for controlling the reducibility of bulk catalysts as demonstrated for a CeO₂−ZrO₂−Al₂O₃ system. The application potential of the developed catalysts was confirmed in the oxidative dehydrogenation of ethylbenzene to styrene with CO₂ and in the non-oxidative propane dehydrogenation to propene. Our approach is extendable to the preparation of any metal oxide catalysts dissolvable in an ammonia solution.     

Selective Oxidative Dehydrogenation of Ethane and Propane over Copper-Containing Mordenite: Insights into Reaction Mechanism and Product Protection

Copper(II)-containing mordenite (CuMOR) is capable of activation of C−H bonds in C₁-C₃ alkanes, albeit there are remarkable differences between the functionalization of ethane and propane compared to methane. The reaction of ethane and propane with CuMOR results in the formation of ethylene and propylene, while the reaction of methane predominantly yields methanol and dimethyl ether. By combining in situ FTIR and MAS NMR spectroscopies as well as time-resolved Cu K-edge X-ray absorption spectroscopy, the reaction mechanism was derived, which differs significantly for each alkane. The formation of ethylene and propylene proceeds via oxidative dehydrogenation of the corresponding alkanes with selectivity above 95 % for ethane and above 85 % for propane. The formation of stable π-complexes of olefins with Cu^I sites, formed upon reduction of Cu^II-oxo species, protects olefins from further oxidation and/or oligomerization. This is different from methane, the activation of which proceeds via oxidative hydroxylation leading to the formation of surface methoxy species bonded to the zeolite framework. Our findings constitute one of the major steps in the direct conversion of alkanes to important commodities and open a novel research direction aiming at the selective synthesis of olefins.