164 resultados para Cuo : HZSM-5


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The acid properties of Mo/HMCM-22 catalyst, which is the precursor form of the working catalyst for methane aromatization reaction, and the synergic effect between Mo species and acid sites were studied and characterized by various characterization techniques. It is concluded that Bronsted and Lewis acidities of HMCM-22 are modified due to the introduction of molybdenum. We suggest a monomer of Mo species is formed by the exchange of Mo species with the Bronsted acid sites. On the other hand, coordinate unsaturated sites (CUS) are suggested to be responsible for the formation of newly detected Lewis acid sites. Computer modelling is established and coupling with experimental results, it is then speculated that the effective activation of methane is properly accomplished on Mo species accommodated in the 12 MR supercages of MCM-22 zeolite whereas the Bronsted acid sites in the same channel system play a key role for the formation of benzene. A much more pronounced volcano-typed reactivity curve of the Mo/HMCM-22 catalysts, as compared with that of the Mo/HZSM-5, with respect to Mo loading is found and this can be well understood due to the unique channel structure of MCM-22 zeolite and synergic effect between Mo species and acid sites.

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Some heterogeneous catalysts, cupric oxide supported on different supports, were prepared and employed to catalyze the cyclopropanation of styrene and 2,5-dimethyl-2,4-hexadiene with ethyl diazoacetate (EDA). The catalytic performance for cyclopropanation strongly depends on the nature of the support. A novel catalyst, CUO/TiO2-Al2O3, in which Al2O3 is modified with a monolayer TiO2, is found to be most active and selective for the cyclopropanation reaction. The yields of 93 and 94% cyclopropanes are obtained for styrene and 2,5-dimethyl-2,4-hexadiene at 40 degreesC as the substrates, respectively. The activity and selectivity in cyclopropanes are optimized with a monolayer dispersion of cupric oxide on the corresponding supports. (C) 2002 Elsevier Science B.V. All rights reserved.

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使用复杂晶体化学键理论计算了La0 .5R0 .5Ba2 Cu3O7(R =Pr,Nd ,Sm ,Eu ,Gd ,Dy ,Y ,Ho,Er,Tm ,Yb ,Lu) (La-R12 3) ,Pr0 .5R0 .5Ba2 Cu3O7(R =La ,Nd ,Sm ,Eu ,Gd ,Dy ,Ho ,Y ,Er,Tm ,Yb ,Lu) (Pr -R12 3)以及RBa2 Cu3O7(R =La ,Pr,Nd ,Sm ,Eu ,Gd ,Dy ,Ho ,Y ,Er,Tm) (R12 3)中Cu—O键的键共价性 ,结果表明Pr-R12 3,La-R12 3,以及R12 3都应具有超导性 ,而实验结果是La0 .5Pr0 .5Ba2 Cu3O7,R0 .5Pr0 .5Ba2 Cu3O7(R =La,Nd ,Sm ,Eu ,Gd)无超导性 .产生这种矛盾的原因尚不明确 ,需要做进一步的研究.

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Mixed oxides Ln(2)CuO(4+/-lambda)(Ln = La, Pr, Nd, Sm, Gd) with K2NiF4 structure were prepared. Their crystal structures were studied with XRD and IR spectra. Meanwhile, the average valence of Cu ions and nonstoichiometric oxygen (lambda) were determined through chemical analyses. Catalysis of the above-mentioned mixed oxides in the phenol hydroxylation was investigated. Results show that the catalysis of these mixed oxides has close relation with their structures and composition. Substitution of A site atom in Ln(2)CuO(4+/-lambda) has a great influence on their catalysis in the phenol hydroxylation.

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活性炭是一种十重要的吸附剂和催化剂载体.它属于微晶结构,主要在低衍射角处产生一个比较大的弥散峰,因而人们尚不能够获得关于活性炭的清晰的空间结构特征.一般认为,活性炭的含氧量是影响其化学性质的一个重要因素.而含氧量和含氧基团分布与活化方式有关.遗憾的是,也还不能通过活化方式控制含氧量和含氧基团分布.目前,关于这些基团的组成和分布在催化剂制备的某些关键步骤中和催化反应中的行为都还知道得很少.本工作选取了4种市售国产活性炭:椰壳炭、山楂核炭、山桃核炭和煤质炭.实验表明,当活性炭本身做催化剂时,含氧基团起到了活性中心作用;在制备负载催化剂的浸渍阶段,含氧基团起着成核中心作用,含氧基团的分布可以影响金属离子的分散度.1 实验部分1.l 反应性能评价以等体积浸渍法制备担载量6.25%质量分数硝酸铜/活性炭催化剂.首先室温下真空干燥24h,然后烘箱中65℃下烘4h,再120℃下烘6℃.性能评价在连续流动微型反应装置上进行.石英反应管内径8mm,催化剂用量500mg(20~35目).反应前催化剂在He气中200℃下处理0.5h,然后350℃下热分解1h.反应气NO浓度1.5%摩尔分数(配在He气中),F/W=50mL/...

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The compound BaCuO2.5 Was obtained using BaO2 and CuO as starting materials, and its various properties were investigated. It belongs to the orthorhombic system with a = 8.55 angstrom, b = 10.56 angstrom, and c = 7.62 angstrom. The p-type semiconductor Ba

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Bulk metallic glasses of Nd65Al10Fe25-xCox (x=0,5,10) have been prepared in the form of 3 mm diam rods. Results of differential scanning calrimetry, dynamic mechanical thermal analysis (DMTA), and x-ray diffraction are presented for these alloys. It is shown that the glass transition and crystallization have been observed by DMTA. The reduced glass transition temperature of these glasses, defined as the ratio between the glass transition temperature T-g and the melting temperature T-l is in the range from 0.55 to 0.62. All these glasses have a large supercooled liquid region (SLR), ranging from 80 to 130 K. The high value of reduced glass transition temperature and wide SLR agree with their good glass formation ability.

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We present numerical simulations of thermosolutal convection for directional solidification of Al-3.5 wt% Ni and Al-7 wt% Si. Numerical results predict that fragmentation of dendrite arms resulting from dissolution could be favored in Al-7 wt% Si, but not in Al-3.5 wt% Ni. Corresponding experiments are in qualitative agreement with the numerical predictions. Distinguishing the two fragmentation mechanisms, namely dissolution and remelting, is critical during experiments on earth, when fluid flow is dominant. (C) 2007 COSPAR. Published by Elsevier Ltd. All rights reserved.

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本文在Heisenberg关于速度脉动能量传递函数假设的基础上,提出标量脉动“能量”传递函数的相应形式.讨论了具有常值横向平均速度梯度与标量梯度的均匀湍流流场中关于大波数情形的标量脉动“能”谱性质。

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本文研究了以PMBP-苯萃取稀土和钍、铀、钛、锆的萃取行为。测定了La、Ce、Pr、Nd、Sm、Gd、Dy、Yb、Y、U(Ⅵ)、Ti、Th和Zr的pH_(1/2)值,计算了它们的萃取平衡常数。并介绍了近十年来作者将此萃取剂应用于铀、钍、稀土、鋰、钢铁合金及岩石中痕量稀土、钍和钙的分离和测定方面的工作。实践证明,PMOP合成简便、价格低廉、萃取能力较强,是比TTA更为优越的萃取剂。