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Nickel Poisoning of a Cracking Catalyst Unravelled by Single‐Particle X‐ray Fluorescence‐Diffraction‐Absorption Tomography
Author(s) -
Gambino Marianna,
Veselý Martin,
Filez Matthias,
Oord Ramon,
Ferreira Sanchez Dario,
Grolimund Daniel,
Nesterenko Nikolai,
Minoux Delphine,
Maquet Marianne,
Meirer Florian,
Weckhuysen Bert M.
Publication year - 2020
Publication title -
angewandte chemie international edition
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 5.831
H-Index - 550
eISSN - 1521-3773
pISSN - 1433-7851
DOI - 10.1002/anie.201914950
Subject(s) - dehydrogenation , catalysis , fluid catalytic cracking , materials science , coke , nickel , spinel , cracking , zeolite , particle (ecology) , particle size , chemical engineering , analytical chemistry (journal) , metallurgy , chemistry , composite material , organic chemistry , oceanography , engineering , geology
Ni contamination from crude oil in the fluid catalytic cracking (FCC) process is one of the primary sources of catalyst deactivation, thereby promoting dehydrogenation–hydrogenation and speeding up coke growth. Herein, single‐particle X‐ray fluorescence, diffraction and absorption (μXRF‐μXRD‐μXAS) tomography is used in combination with confocal fluorescence microscopy (CFM) after thiophene staining to spatially resolve Ni interaction with catalyst components and study zeolite degradation, including the processes of dealumination and Brønsted acid sites distribution changes. The comparison between a Ni‐lean particle, exposed to hydrotreated feedstock, and a Ni‐rich one, exposed to non‐hydrotreated feedstock, reveals a preferential interaction of Ni, found in co‐localization with Fe, with the γ‐Al 2 O 3 matrix, leading to the formation of spinel‐type hotspots. Although both particles show similar surface zeolite degradation, the Ni‐rich particle displays higher dealumination and a clear Brønsted acidity drop.

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