2005
DOI: 10.1016/j.cattod.2005.07.136
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Highly active sulfided CoMo catalyst on nano-structured TiO2

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Cited by 34 publications
(26 citation statements)
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“…These results are in line with those found previously over sulfided CoMo catalysts used for HDS reactions. For example, Escobar et al [30] prepared CoMo HDS catalyst supported on high surface area (>300 m 2 g -1 ) nano-structured TiO 2 and tested in dibenzothiophene HDS. They found that the activity of CoMo/titania catalyst was two-fold to that of an alumina-supported commercial CoMo catalyst.…”
Section: Resultsmentioning
confidence: 99%
“…These results are in line with those found previously over sulfided CoMo catalysts used for HDS reactions. For example, Escobar et al [30] prepared CoMo HDS catalyst supported on high surface area (>300 m 2 g -1 ) nano-structured TiO 2 and tested in dibenzothiophene HDS. They found that the activity of CoMo/titania catalyst was two-fold to that of an alumina-supported commercial CoMo catalyst.…”
Section: Resultsmentioning
confidence: 99%
“…In fact, transformation of titania into nanotubes yields materials with specific surface area as large as 400 m 2 /g [17], opening the possibility of using this material as catalyst support in several processes. Recently, we have reported that nanostructured CoMoS/titania (i.e., cobalt-molybdenum on titania nanotubes) are twice as active in dibenzothiophene hydrodesulphurization as compared with the corresponding alumina-supported catalyst [18].…”
Section: Introductionmentioning
confidence: 99%
“…The promotional effect of 8.5 was reached after deposition of Co onto presulfided Mo catalysts supported on ZrO 2 -TiO 2 with molar ratio ZrO 2 /TiO 2 60/40 and BET surface area 165 m 2 g -1 , which resulted in 10% activity improvement in comparison with Al 2 O 3 supported catalyst [44]. Two fold higher HDS activities of CoMo catalysts were reported over nano-structured TiO 2 possessing BET surface area about 330 m 2 g -1 [46] and TiO 2 nanotubes of BET surface area 236 m 2 g -1 [47] than over Al 2 O 3 -supported counterparts but without referring on promotional effects. A relatively high promotional effect of 10 was obtained in the case of Ni supported over wide-pore ZrO 2 -TiO 2 Mo catalyst (molar ratio ZrO 2 /TiO 2 30/70 and BET surface area about 300 m 2 g -1 ) employing chelating agent assisted impregnation technique [45].…”
Section: Hydrodesulfurization Activitymentioning
confidence: 86%
“…Open symbols-Mo catalysts, filled symbols-CoMo catalysts with Co deposited by SIM or CIM, halffilled symbols-CoMo catalysts with Co deposited by MIM over presulfided Mo catalysts promotional effects of 2.4 and 2.9 in the case of Co over zirconia-and titania-supported catalysts, respectively, in [42] or 3.3 over both supports in [16] were reported while they were about 5 or 11 over alumina-supported counterparts resulting in high integral HDS activity. On contrary, it is believed that further improvement of the ZrO 2 and TiO 2 based catalysts lie in tailored preparation of their mixed form with desirable textural properties [43][44][45] or nanostructured forms [46,47]. The CoMo catalyst supported on solvo-thermally treated ZrO 2 -TiO 2 with molar ratio ZrO 2 /TiO 2 30/70 and BET surface area 313 m 2 g -1 exhibited promotional effect about 3.2 but exceeded the HDS activity of a reference Al 2 O 3 -supported counterpart about twofold [43].…”
Section: Hydrodesulfurization Activitymentioning
confidence: 97%