2020
DOI: 10.1016/j.fuel.2020.117363
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Hydrotreating atmospheric gasoil and co-processing with rapeseed oil using supported Ni-Mo and Co-Mo carbide catalysts

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Cited by 17 publications
(13 citation statements)
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“…For most hydrocarbon classes, we can even provide far more details, for example, hydrocarbon class distribution by carbon number. As clamined by several studies, the n -paraffin content of the diesel fraction changed the most during the hydroprocessing of raw vegetable oil or its blends with petroleum streams. To investigate this claim in more detail, Figure shows the distribution of normal paraffins by carbon number (nC15–nC18) for all diesel samples, presented in two panels, due to the very different concentration range. In general, n -heptadecane and n -octadecane, shown in Figure b, are produced at 10 times higher concentration than n -pentadecane and n -hexadecane (Figure a), especially in diesel samples obtained from canola oil/HVGO blends.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…For most hydrocarbon classes, we can even provide far more details, for example, hydrocarbon class distribution by carbon number. As clamined by several studies, the n -paraffin content of the diesel fraction changed the most during the hydroprocessing of raw vegetable oil or its blends with petroleum streams. To investigate this claim in more detail, Figure shows the distribution of normal paraffins by carbon number (nC15–nC18) for all diesel samples, presented in two panels, due to the very different concentration range. In general, n -heptadecane and n -octadecane, shown in Figure b, are produced at 10 times higher concentration than n -pentadecane and n -hexadecane (Figure a), especially in diesel samples obtained from canola oil/HVGO blends.…”
Section: Resultsmentioning
confidence: 99%
“…The co-hydroprocessing of different vegetable oils with petroleum feedstocks has been studied by a number of research groups. Most of the published studies have focused on the hydroprocessing performance (such as conversions of hydrodesulfurization (HDS), hydrodenitrogenation (HDN), hydrodeoxygenation (HDO), catalyst deactivation and stability, etc.) rather than on a detailed analysis and characterization of the derived products from co-processing petroleum and biomass feedstocks.…”
Section: Introductionmentioning
confidence: 99%
“…No solids were found for the commercial catalysts compared to the solids produced by the two phonolite-derived catalysts. This solid production could be due to the reaction of glycerol [ 24 ]. Here, glycerol can be transformed into propane and propylene, and into carbonaceous solids when phonolite catalysts are present, in which case the gaseous products include lower amounts of C3 gases (propylene, propane) ( Table 5 ).…”
Section: Resultsmentioning
confidence: 99%
“…This addition increases the catalyst activity significantly due to the ensemble and ligand effects. The effect of promotor addition has already been described for hydrotreating model molecules [169,170] and industrial feedstocks [162], resulting in a significant increase in HDS activity of the MoCx of up to 80%. This activity is comparable with conventional hydrotreating catalysts, but the HDN is still low.…”
Section: Sulphur-free Catalystsmentioning
confidence: 99%