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首页> 外文期刊>The journal of physical chemistry, C. Nanomaterials and interfaces >Parallel Alkane Dehydrogenation Routes on Bronsted Acid and Reaction-Derived Carbonaceous Active Sites in Zeolites
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Parallel Alkane Dehydrogenation Routes on Bronsted Acid and Reaction-Derived Carbonaceous Active Sites in Zeolites

机译:在沸石中的桥接酸和反应衍生的碳质活性位点上并联烷烃脱氢途径

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摘要

Alkane dehydrogenation rates on acidic zeolites measured in the presence of co-fed H-2 during initial contact with reactants solely reflect protolytic reactions at Bronsted acid sites, reflect additional contributions from an extrinsic dehydrogenation while rates measured without co-fed H-2 and at later reaction times function derived from reactants and products. This extrinsic function consists of unsaturated organic residues that catalyze dehydrogenation turnovers by accepting H-atoms from alkanes and recombining them as H-2. Such hydrogen transfer routes are inhibited by alkenes and H-2 products and proceed with activation barriers much lower than for protolytic dehydrogenation at H+ sites, causing them to become more prevalent at lower temper- attires and for zeolites with lower H+ densities. The number, composition, and reactivity of these extrinsic carbonaceous active sites depend on the local concentrations of reactants and products, which vary with alkane and H-2 pressure, bed residence time, and axial mixing. These extrinsic catalytic moieties form within H-2-deficient regions of catalyst beds but can be removed by thermal treatments in H-2, which fully restore zeolite catalysts to their initial state. Carbonaceous deposits do not catalyze alkane cracking reactions; thus, cracking rate constants serve as a reporter of the state of proton sites, and their invariance with product pressure, residence time, and axial mixing confirms that protons remain unoccupied and undisturbed as extrinsic organic residues change in number, composition, and reactivity. The rates of the reverse reaction (alkene hydrogenation) under H-2-rich conditions inhibit the formation and the reactivity of these organic residues, and taken together with formalisms based on nonequilibrium thermodynamics, they confirm that alkane dehydrogenation occurs solely via protolytic routes only at the earliest stages of reaction in the presence of added H-2. These findings provide a coherent retrospective view of the root causes of the literature discord about alkane dehydrogenation turnover rates and activation barriers on acidic zeolites, variously attributed to extraframework Al or radical active sites and to turnovers limited by alkene desorption instead of protolytic steps. Importantly, these findings also prescribe experimental protocols that isolate the kinetic contributions of protolytic dehydrogenation routes, thus ensuring their replication, while suggesting strategies to deposit or remove extrinsic organocatalytic functions that mediate hydrogen transfer reactions.
机译:在与反应物的初始接触期间在与反应物的初始接触期间测量的酸性沸石上测量的酸性沸石仅反映在勃朗斯酸位点的质量反应,反映来自外本脱氢的额外贡献,同时在没有共用H-2的情况下测量的速率。后来反应时间源自反应物和产物。该外本功能由不饱和的有机残基组成,通过接受来自烷烃的H-原子并将其重组为H-2来催化脱氢失误。这种氢转移途径被烯烃和H-2产物抑制,并进行了低于H +位点的质子解脱氢的活化屏障,导致它们在较低的脾气上变得更普遍,并且具有较低的H +密度的沸石。这些外本含碳活性位点的数量,组合物和反应性取决于局部反应物和产物的局部浓度,其与烷烃和H-2压力,床停留时间和轴向混合不同。这些外本催化部分在催化剂床的H-2缺陷区域内形成,但可以通过H-2的热处理除去,该热处理将沸石催化剂完全恢复到它们的初始状态。碳质沉积物不催化烷烃裂化反应;因此,开裂速率常数作为质子位点状态的记者,以及它们与产品压力,停留时间和轴向混合的不变性证实,质子保留未被占用并且不受干扰,因为所外的有机残留物的数量,组合物和反应性变化。富含H-2的条件下的反应(烯烃氢化)的速率抑制了这些有机残基的形成和反应性,并与基于非醌热动力学的形式主义一起,它们证实烷烃脱氢仅通过质子解途径发生在加入的H-2存在下最早反应的阶段。这些发现提供了酸性沸石对烷烃脱氢周转速率和活化屏障的文献不和谐的根本原因的连贯的回顾图,这些结果是酸性沸石上的激活屏障,各种归因于预α或激进活性位点,并通过烯烃解吸而不是质子解渗透的渗透。重要的是,这些发现还规定了分离质子脱氢途径的动力学贡献的实验方案,从而确保其复制,同时建议沉积或去除介导氢转移反应的外在有机催化功能的策略。

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