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Hydrogenation by spillover of hydrogen from metal to acidic support or by reverse spillover of the reactant molecule from the support to the metal

机译:通过从金属溢出到酸性载体的氢化或通过将反应物分子与金属载体的反向溢出来氢化

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For hydrogen spillover to be effective in catalysis, it must lead to a net transport of hydrogen atoms. The first prerequisite for this to happen is a thermodynamic driving force between the point of hydrogen atom creation by H_2 dissociation on the metal particle and the site where the hydrogen is used for hydrogenation. The second prerequisite is a means of transportation of the hydrogen atoms over the support surface. Proof of the existence of spillover came from experiments with reducible supports such as WEO_3. In a metal/WO_3 catalyst both prerequisites are met. The thermodynamic driving force is the reducibility of the support cations, and they provide at the same time the means of transportation by a redox transfer of the hydrogen atom between neighbouring tungsten cations. Scientists have tried to use the same explanation for systems in which the support metal cations cannot be reduced. Thus, hydrogen-deuterium exchange on a metal/SiO_2 catalyst is often quoted as an example of spillover as well. This, however, is a misunderstanding. There is no net hydrogen transport on an ideal metal/SiO_2 system, only hydrogen-deuterium exchange. Exchange between a deuterium atom on the metal surface and a hydrogen atom of a silanol group occurs at the metal-support interface by a bending over of a silanol group towards the metal surface. The diffusion of the deuterium atom over the silica surface, away from the metal particle, takes place by exchange of a Si-OD group with a Si-OH group. This is a water-assisted proton and deuteron jump process. The difference between the two examples is that in the case of the metal/WO_3 system there is a genuine transport of hydrogen atoms away from the metal particles. These hydrogen atoms turn into protons by donating an electron to the support surface cations, and the protons combine with the oxygen anions of the support to hydroxyl surface groups. In the case of the metal/SiO_2 system, however, hydrogen atoms cannot reduce the Si cations. As a result, there can only be exchange between OH and OD groups, but no net transport of hydrogen away from the metal particles. With the need to remove more sulfur-containing and aromatic molecules from diesel fuel, interest in metal catalysts supported on acidic carriers has increased.
机译:对于氢溢出在催化中有效,它必须导致氢原子的净运输。这种情况的第一个先决条件是通过H_2在金属颗粒上的H_2解离和氢气用于氢化的位点之间产生的热力动力驱动力。第二个先决条件是在支撑表面上运输氢原子的方法。溢出的存在证明来自实验,诸如Weo_3的可还原支持。在金属/ WO_3催化剂中,所有先决条件都得到满足。热力学驱动力是支撑阳离子的还原性,它们同时提供通过相邻钨阳离子之间的氢原子的氧化还原转移来运输的方式。科学家们试图使用相同的解释,其中可以减少支撑金属阳离子的系统。因此,通常引用金属/ SiO_2催化剂上的氢氘交换作为溢出的例子。然而,这是一种误解。理想的金属/ SiO_2系统上没有净氢输送,仅氢氘交换。在金属表面上的氘原子和硅烷醇基的氢原子之间的交换在金属支撑界面上发生硅烷醇基朝向金属表面的硅烷醇基。氘原子在二氧化硅表面的扩散,远离金属颗粒,通过与Si-OH基团的交换交换进行Si-OD组。这是一个水辅质子和氘核跳跃过程。两个实例之间的差异是在金属/ WO_3系统的情况下,存在远离金属颗粒的氢原子的真正传输。这些氢原子通过向支撑表面阳离子赋予载体表面阳离子而变成质子,而质子与羟基表面基团的载体的氧阴离子结合。然而,在金属/ SiO_2系统的情况下,氢原子不能减少Si阳离子。结果,只能在OH和OD组之间进行交换,但没有净氢从金属颗粒转运。由于需要去除来自柴油燃料的更多含硫和芳族分子,因此对酸性载体负载的金属催化剂的兴趣增加了。

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