2004
DOI: 10.1016/j.jcat.2004.07.013
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HDS of a model FCC gasoline over a sulfided CoMo/Al2O3 catalyst: Effect of the addition of potassium

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Cited by 116 publications
(67 citation statements)
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“…These last conditions are close to those implemented in industrial setup conditions (Brunet et al, 2005;Mey, 2004;Lauritsen, 2004;Furimsky, 2000;Rollman, 1977;Lee et al, 1984;Tauster et al, 1981). Both catalysts are modeled by the catalytic sites of MoS 3 H 3 + and WS 3 H 3 + types respectively (Joffre et al, 1984;.…”
Section: -Methyltetrahydrothiophenesupporting
confidence: 71%
“…These last conditions are close to those implemented in industrial setup conditions (Brunet et al, 2005;Mey, 2004;Lauritsen, 2004;Furimsky, 2000;Rollman, 1977;Lee et al, 1984;Tauster et al, 1981). Both catalysts are modeled by the catalytic sites of MoS 3 H 3 + and WS 3 H 3 + types respectively (Joffre et al, 1984;.…”
Section: -Methyltetrahydrothiophenesupporting
confidence: 71%
“…It is particularly challenging to remove sulfur atoms from alkylthiophene in a reductive environment without hydrogenation of olefins (in order to keep the high octane number). According to the composition of the feed to be treated, it was found that a relevant model molecule for the HDS reaction is 2-methylthiophene (called 2MT), and a relevant olefin for HydO is 2,3-dimethylbut-1-ene (called 23DMB1N) at equilibrium with 2,3-dimethylbut-2-ene [31,32].…”
Section: Kinetic Model Of Hds/hydo Selectivitymentioning
confidence: 99%
“…From a scientific point of view, it is still an open question why the CoMoS active phase exhibits an improved HDS/HydO selectivity with respect to NiMoS, being often empirically described as "more hydrogenating". The HDS/HydO selectivity has been the subject of recent experimental works on model molecules for FCC gasoline or real feed [29][30][31][32][33]. In specific conditions, it seems possible to modulate the HDS/HydO selectivity of the NiMoS [30,33] and CoMoS [34] active phases.…”
Section: Introductionmentioning
confidence: 99%
“…Tapia et al found that modification of the support with alkaline metals and rare earth metals decreases the acidity of the CoMo catalyst resulting in higher HDS selectivity [21]. Mey et al modified the properties of a commercial CoMo catalyst with potassium to minimize olefin saturation during HDS [22]. On the other hand, Miller et al…”
Section: Introductionmentioning
confidence: 99%