“…In petroleum refineries, catalyst deactivation has been well studied for hydrotreating processes. , The deactivation is largely a result of simultaneous coke and metal deposition and is affected by several factors, including catalyst type, feedstock properties, operating conditions, and reactor design. , The impact of biomass-derived oil and crude intermediates on coprocessing catalyst stability has been reported. − For instance, introducing a lignocellulosic HTLbiocrude into petroleum gas oil showed premature and faster catalyst deactivation . Studies on coprocessing lignocellulosic bio-oils with petroleum distillates showed that the high oxygen content in bio-oil leads to increased coke formation and a gradual sulfur leaching, resulting in catalyst deactivation and process deficiency. , In addition, when coprocessing animal fat with gas oils, the high amounts of inorganic impurities, such as silicon, phosphorus, and alkali and alkaline earth metals, represent a risk of catalyst poisoning as one of the main reasons for catalyst deactivation. , A clear understanding of the deactivation behavior particularly caused by biocrudes is highly desirable and critical to improving hydrotreating catalysts and processes to enable coprocessing renewable feedstocks and to incorporate biogenic carbon in fuels.…”