“…It is known that coke formation is markedly inhibited when the active species are applied as dispersed nanoparticle catalysts [14]. The application of the highly dispersed catalysts in the slurry-phase hydroprocessing of heavy residues favors the rapid uptake of hydrogen and deactivates the intermediate free radical moieties in the liquid phase, thereby suppressing coke formation, increasing total conversion, and enhancing quality of liquid product [50].…”
Section: Unsupported Dispersed Catalystmentioning
confidence: 99%
“…Dispersed catalyst can be classified into either water-soluble or oil-soluble [50]. Oil-soluble dispersed catalyst is generally preferred because it has a better catalyst activity as it can disperse uniformly in oil.…”
With the increasing demand of petroleum-derived products due to the world population and development, upgrading of crude oil with heavier quality and petroleum residues is unavoidable. Hydroprocessing is a preferable process for heavy oil upgrading. The process is operated with the presence of a catalyst, and catalysis plays an important role in the process. An overview regarding the catalyst design such as the catalyst active metal, active phase, support properties, and catalyst structure for heavy oil hydroprocessing is provided. There also include some recent advancements related to catalytic hydroprocessing of heavy oils and residue processes. Further catalyst performance improvement will likely come from catalyst optimization and better catalyst deactivation resistance resulting from metal poisoning and coke formation.
“…It is known that coke formation is markedly inhibited when the active species are applied as dispersed nanoparticle catalysts [14]. The application of the highly dispersed catalysts in the slurry-phase hydroprocessing of heavy residues favors the rapid uptake of hydrogen and deactivates the intermediate free radical moieties in the liquid phase, thereby suppressing coke formation, increasing total conversion, and enhancing quality of liquid product [50].…”
Section: Unsupported Dispersed Catalystmentioning
confidence: 99%
“…Dispersed catalyst can be classified into either water-soluble or oil-soluble [50]. Oil-soluble dispersed catalyst is generally preferred because it has a better catalyst activity as it can disperse uniformly in oil.…”
With the increasing demand of petroleum-derived products due to the world population and development, upgrading of crude oil with heavier quality and petroleum residues is unavoidable. Hydroprocessing is a preferable process for heavy oil upgrading. The process is operated with the presence of a catalyst, and catalysis plays an important role in the process. An overview regarding the catalyst design such as the catalyst active metal, active phase, support properties, and catalyst structure for heavy oil hydroprocessing is provided. There also include some recent advancements related to catalytic hydroprocessing of heavy oils and residue processes. Further catalyst performance improvement will likely come from catalyst optimization and better catalyst deactivation resistance resulting from metal poisoning and coke formation.
“…[2][3][4][5][6][7][8][9][10][11][12][13][14][15]. The problems of fixed-bed processes in the case of heavy oil fractions include a high rate of catalysts deactivation due to the presence of local overheating zones caused by highly exothermic reactions and the formation of condensation products and coke deposits, which block both the pores of the support and the catalytically active sites [16,17]. A modern approach to the hydroprocessing of heavy crude oil consists in the use of slurry reactors with meso-or nanosized dispersed-phase catalysts [17][18][19][20][21][22][23][24][25][26][27][28][29].…”
Section: Introductionmentioning
confidence: 99%
“…The problems of fixed-bed processes in the case of heavy oil fractions include a high rate of catalysts deactivation due to the presence of local overheating zones caused by highly exothermic reactions and the formation of condensation products and coke deposits, which block both the pores of the support and the catalytically active sites [16,17]. A modern approach to the hydroprocessing of heavy crude oil consists in the use of slurry reactors with meso-or nanosized dispersed-phase catalysts [17][18][19][20][21][22][23][24][25][26][27][28][29]. This approach ensures a uniform heat distribution in the reaction zone, a high degree of conversion of raw materials, a decrease in the rate of deactivation due to coking, and the possibility of easy catalyst removal from the reactor [30][31][32].…”
Section: Introductionmentioning
confidence: 99%
“…Dispersed catalysts, both preliminarily synthesized with the use of supports (ex situ) and in situ formed from water-soluble or oil-soluble metal compounds in the reaction medium, are successfully used in slurry hydroprocesses [17,[33][34][35][36][37][38][39][40][41][42].…”
The nickel–tungsten sulfide catalysts for the hydroconversion of hydrocarbons were prepared from oil-soluble nickel and tungsten precursor compounds in situ with the use of silica, alumina, titania, zeolite Y, and amorphous aluminosilicate as additives in a vacuum gas oil medium. It was found that the catalytic activity in hydrocracking depends on the concentration of acid sites in the resulting catalyst. With the use of oxide additives, the dispersion and the promoter ratio of the in situ formed sulfide particles increased in the order SiO2–Al2O3–TiO2. It was noted that the promoter ratio of sulfide particles obtained with the use of aluminosilicate additives depended on their porous structure peculiarities. The use of titanium dioxide as a catalytic system component made it possible to reach high activity in hydrocracking, hydrodearomatization, and hydrodesulfurization, which was comparable to that of a system based on zeolite Y, a highly acidic component.
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