2014
DOI: 10.1016/j.jcat.2014.07.002
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Synthesis of NiMo hydrodesulfurization catalyst supported on a composite of nano-sized ZSM-5 zeolite enwrapped with mesoporous KIT-6 material and its high isomerization selectivity

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Cited by 114 publications
(102 citation statements)
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“…To meet this requirement, hydrodesulfurization (HDS) has a high potential for the removal of sulfur atoms from diesel fuels . The greatest challenge in ultra‐deep (with S content below 10 ppm) HDS is the removal of highly refractory organosulfur compounds such as 4,6‐dimethyldibenzothiophene (4,6‐DMDBT) from diesel fuels, because the steric hindrance of the methyl groups at the 4 and 6 positions strongly restricts desulfurization . The catalysts commonly employed in the petrochemical industry to remove sulfur atoms from transportation fuels are cobalt‐ or nickel‐promoted MoS 2 or WS 2 supported on γ‐alumina .…”
Section: Introductionmentioning
confidence: 99%
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“…To meet this requirement, hydrodesulfurization (HDS) has a high potential for the removal of sulfur atoms from diesel fuels . The greatest challenge in ultra‐deep (with S content below 10 ppm) HDS is the removal of highly refractory organosulfur compounds such as 4,6‐dimethyldibenzothiophene (4,6‐DMDBT) from diesel fuels, because the steric hindrance of the methyl groups at the 4 and 6 positions strongly restricts desulfurization . The catalysts commonly employed in the petrochemical industry to remove sulfur atoms from transportation fuels are cobalt‐ or nickel‐promoted MoS 2 or WS 2 supported on γ‐alumina .…”
Section: Introductionmentioning
confidence: 99%
“…Highly refractory sulfur‐containing compounds such as 4,6‐DMDBT undergo HDS by direct desulfurization (DDS) and hydrogenation desulfurization (HYD) over conventional catalysts: DDS produces 3,3′‐dimethylbiphenyl (3,3′‐DMBP) as the desulfurized product, and HYD produces tetrahydro‐ and hexahydro‐ 4,6‐DMDBT as intermediates, which can be further desulfurized to yield 3,3′‐dimethylcyclohexylbenzenes (3,3′‐DMCHB) and 3,3′‐dimethylbicyclohexyls (3,3′‐DMBCH). Due to the hindrance caused by the two methyl groups at the 4 and 6 positions, which strongly prevent the adsorption of the sulfur atom at the active sites of the catalysts through sigma‐adsorption, sulfur removal from 4,6‐DMDBT mainly proceeds through the HYD pathway . Thus, catalysts must possess both high hydrogenation activity to achieve the hydrogenation of aromatic rings and high hydrogenolysis activity to achieve the removal of sulfur atoms .…”
Section: Introductionmentioning
confidence: 99%
“…For example, metal sulfide clusters (MoS x ) dispersed inside the micropores of zeolite Y and ZSM-5 have high activity in toluene hydrogenation and hydrodesulfurization of dibenzothiophene [33,34]. Nevertheless, conventional zeolites cannot accomplish deep hydrogenation of the polyaromatic hydrocarbons due to their pore size limitation [35][36][37]. Recently, mesoporous zeolites with excellent catalytic activity for the conversion of bulky molecules have been successfully synthesized [38][39][40][41][42][43][44][45][46].…”
Section: Introductionmentioning
confidence: 99%
“…Thus, the development of novel catalysts which not only show improved desulfurization but also preservation of the octane number is of crucial importance for hydro-upgrading technology. This has been realized by using MZC materials such as L/MCM-41 [35], Beta/SBA-15 [37], ZSM-5/KIT6 [94], and Beta/KIT6 [95] as advanced supports for the preparation of HDS catalysts. Especially, Du et al [36] recently developed excellent HDS catalysts by using micro/mesoporous composite Beta/FDU-12 (BF) as a support additive mixed with γ-Al 2 O 3 (BFA).…”
Section: Hydroconversionmentioning
confidence: 99%