2004
DOI: 10.1016/j.apcata.2004.07.016
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Migration of surface species on supports: a proof of their role on the synergism between CoSx or NiSx and MoS2 in HDS

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Cited by 57 publications
(48 citation statements)
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“…The Co/SiO 2 and Mo/SiO 2 beds were separated by 5 mm of SiO 2 . After that, other supports (g-Al 2 O 3 ) 4 , other distances (up to 10 mm) 5 , other donors (Mn, Fe, Ni, Cu and Zn) 6 , other separators 5,7 , and other acceptors (W and Re) 6,8 have been studied in order to find the variables that improve this synergism via Hso. Moreover, other feed gas oil, dibenzothiophene (DBT) 9 , and 4,6 dimethyldibenzothiophene (4,6 DMDBT) 10 have been used.…”
Section: In 2003mentioning
confidence: 99%
“…The Co/SiO 2 and Mo/SiO 2 beds were separated by 5 mm of SiO 2 . After that, other supports (g-Al 2 O 3 ) 4 , other distances (up to 10 mm) 5 , other donors (Mn, Fe, Ni, Cu and Zn) 6 , other separators 5,7 , and other acceptors (W and Re) 6,8 have been studied in order to find the variables that improve this synergism via Hso. Moreover, other feed gas oil, dibenzothiophene (DBT) 9 , and 4,6 dimethyldibenzothiophene (4,6 DMDBT) 10 have been used.…”
Section: In 2003mentioning
confidence: 99%
“…Though traditional HDS catalysts are highly efficient in removing thiols, sulfides, and disulfides, they are inefficient in ultra-deep desulfurization of refractory sulfur-containing compounds, such as 4,6-dimethydibenzothiophene (4,6-DMDBT). Therefore, development of novel HDS catalysts with super high activity is needed [5][6][7][8][9][10][11][12][13][14].…”
Section: Introductionmentioning
confidence: 99%
“…As in previous studies [18][19][20][21][22][23] beds were diluted with SiO 2 (BASF D11-10) at a v/v ratio of 1:1, and the remainder of the reactor was filled with SiC.…”
Section: Reaction Conditionsmentioning
confidence: 99%
“…All the catalysts were prepared as reported previouly [18][19][20][21][22][23] The support for all catalysts was γ-Al 2 O 3 , BASF D10-10 (N 2 BET 212 m 2 g -1 ) with a particle size of 0.84 and 1.19 mm. The nominal metal content of the precursors was 0.5, 1.5 and 3.0 atoms nm -2 for the monometallic catalysts while for bimetallic catalysts, 1.6 atoms nm -2 Ni, 2.9 atoms nm -2 Mo and 0.5 atoms nm -2 Re were used.…”
Section: Preparation Of Catalystsmentioning
confidence: 99%
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