“…Catalytic hydrocracking of heavy oils to produce commercial-value and high-quality transportation fuels and other petrochemical products has received an increasing level of attention owing to energy demands and tighter environmental regulations. − Prior to this process, hydrodemetallization (HDM) is required to remove metal impurities in the feedstocks, , in which Ni- and V-porphyrin enriched in large asphaltene aggregates (>1 nm in size) are most abundant and problematic, causing detrimental impacts on the downstream catalysts. , Typically extruded alumina-supported catalyst pellets comprising Mo sulfide promoted by Co or Ni are employed for the HDM reaction in industrial plants. ,− However, the alumina-supported HDM catalysts generally undergo two-step deactivation, that is, a slow loss in the activity due to the active sites being covered by the metal deposition followed by a rapid deactivation attributed to the pore plugging arising from the accumulation of the metal sulfides and ultimate pore blockage. − This would lead to serious intraparticle diffusion limitations for the long-time HDM operation. , Hence, there is an urgent need to design appropriate pore structures and geometries of the catalyst pellet for a highly efficient HDM process.…”