Catalytic Upgrading of Vacuum Residue Over Metal-Loaded Iraqi Kaolin Using a Fixed-Bed Reactor
Metadatos
Afficher la notice complèteAuteur
Basil Al-Ameri, Osamah; Elmouwahidi, Abdelhakim; Alzuhairi, Mohammed; Bailón García, Esther; Amaro-Gahete, Juan; Carrasco Marín, FranciscoEditorial
MDPI
Materia
Kaolin Catalytic cracking Vacuum residue
Date
2026-04-07Referencia bibliográfica
Al-Ameri, O. B., Elmouwahidi, A., Alzuhairi, M., Bailón-García, E., Amaro-Gahete, J., & Carrasco-Marín, F. (2026). Catalytic upgrading of vacuum residue over metal-loaded Iraqi kaolin using a fixed-bed reactor. Applied Sciences, 16(7), 3597. https://doi.org/10.3390/app16073597
Patrocinador
Consejería de Universidad, Investigación e Innovación and the ERDF Andalusia Program 2021–2027 - (C-EXP-247-UGR23) (PLSQ_2023_00183); MICIU/AEI/10.13039/501100011033, the “European Union NextGenerationEU/PRTR” program - (PID2021-127803OB-I00); “ERDF A way of making Europe” under Projects - (CNS2023-144680)Résumé
The catalytic upgrading of vacuum residue (VR) is constrained by the high cost, diffu
sional limitations, and rapid deactivation of conventional zeolite-based catalysts due to
severe coking. Addressing this, we developed novel, low-cost, and coke-resistant catalysts
utilizing naturally abundant Iraqi kaolin. A composite support comprising 80 wt.% Iraqi
red kaolin and 20 wt.% white kaolin was synthesized via thermal activation at 800 °C and
acid leaching. This support was subsequently impregnated with transition and rare-earth
metals (Ni, Co, Ce) at 3–40 wt.% loadings, and comprehensively characterized using XRD,
BET, SEM-EDX, and XPS. Catalytic performance was evaluated during VR upgrading in
a fixed-bed batch reactor at 450 °C. Among the formulations, the 20 wt.% Ce-loaded cata
lyst (MKRW-800A@Ce20%) exhibited superior efficiency, achieving 80.15% VR conver
sion, 61.04% liquid yield, and minimal coke formation (3.81 g) compared to Ni and Co
counterparts. This enhanced activity is attributed to synergistic effects of improved sur
face acidity, textural accessibility, and the Ce3+/Ce4+ redox couple, which promotes selec
tive cracking while suppressing coke precursors. These findings provide new insights into
the rational design of natural clay-based catalysts, establishing Ce-modified metakaolin
as a viable, sustainable alternative to zeolites for industrial heavy-oil processing.





