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Life and death of a single catalytic cracking particle

机译:单个催化裂化颗粒的生与死

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摘要

Fluid catalytic cracking (FCC) particles account for 40 to 45% of worldwide gasoline production. The hierarchical complex particle pore structure allows access of long-chain feedstock molecules into active catalyst domains where they are cracked into smaller, more valuable hydrocarbon products (for example, gasoline). In this process, metal deposition and intrusion is a major cause for irreversible catalyst deactivation and shifts in product distribution. We used x-ray nanotomography of industrial FCC particles at differing degrees of deactivation to quantify changes in single-particle macroporosity and pore connectivity, correlated to iron and nickel deposition. Our study reveals that these metals are incorporated almost exclusively in near-surface regions, severely limiting macropore accessibility as metal concentrations increase. Because macropore channels are “highways” of the pore network, blocking them prevents feedstock molecules from reaching the catalytically active domains. Consequently, metal deposition reduces conversion with time on stream because the internal pore volume, although itself unobstructed, becomes largely inaccessible.
机译:流化催化裂化(FCC)颗粒占全球汽油产量的40%至45%。分层的复杂颗粒孔结构允许长链原料分子进入活性催化剂区域,在该区域中,它们裂化为更小,更有价值的烃产品(例如汽油)。在此过程中,金属沉积和侵入是导致不可逆的催化剂失活和产品分布变化的主要原因。我们使用了工业FCC颗粒在不同程度的失活程度下的X射线纳米断层照相术,以量化与铁和镍沉积相关的单颗粒大孔隙度和孔连通性的变化。我们的研究表明,这些金属几乎全部掺入近表面区域,随着金属浓度的增加,严重限制了大孔的可及性。由于大孔通道是孔隙网络的“高速通道”,因此将其阻塞会阻止原料分子到达催化活性域。因此,金属沉积降低了随时间流逝的转化率,因为内部孔体积尽管本身不受阻碍,但在很大程度上变得难以接近。

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