2001
DOI: 10.1006/jcat.2000.3103
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Influences of the Hydrogen Sulfide Partial Pressure and of a Nitrogen Compound on the Hydrodeoxygenation Activity of a CoMo/Carbon Catalyst

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Cited by 127 publications
(78 citation statements)
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“…[215][216][217][218][219] The model feedstock was a mixture of 4-methylacetophenone, ethyldecanoate, and guaiacol as shown in Figure 20. The ketone group is easily and selectively hydrogenated into a methylene group above 200°C.…”
Section: Hydrodeoxygenationmentioning
confidence: 99%
“…[215][216][217][218][219] The model feedstock was a mixture of 4-methylacetophenone, ethyldecanoate, and guaiacol as shown in Figure 20. The ketone group is easily and selectively hydrogenated into a methylene group above 200°C.…”
Section: Hydrodeoxygenationmentioning
confidence: 99%
“…Besides, the basic support promotes formation of short edge-bonded MoS 2 slabs (with Lewis acid on each edge plane) and thus increases the edge plane area suitable for the promotion by Ni or Co [99]. [48,168].…”
Section: Aluminamentioning
confidence: 99%
“…Environmental regulations have been modified to allow that lower levels of sulfured compounds to be ejected to the atmosphere. Industrially, the removal of organosulfur and organonitrogen compounds in fuel oils is being carried out by means of a simultaneous hydrodesulfurization (HDS) and hydrodenitrogenation (HDN) process at around 350 °C using catalysts based on CoMo or NiMo, which involves the C-S and C-N bond cleavage to produce H 2 S and NH 3 , respectively (Zaczepinski, 1996, Kabe et al, 1999Ferrari et al, 2001;Caeiro, et al, 2007). Deep desulfurization of diesel fuels is particularly challenging due to the difficulty of reduce aromatic sulfur compounds, particularly 4,6-dialkyldibenzothiophenes, using conventional hydrodesulfurization processes (HDS).…”
Section: Desulfurization Of Light Oil Using Ionic Liquidsmentioning
confidence: 99%