4.7 Article

Hydrotreating and hydrodemetalation of raw jatropha oil using mesoporous Ni-Mo/?-Al2O3 catalyst

Journal

FUEL
Volume 326, Issue -, Pages -

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2022.125108

Keywords

Hydrodemetalation; Hydrotreating; Raw jatropha oil; Ni-Mo/gamma-Al2O3; Renewable green diesel; Deactivation

Funding

  1. Department of Science and Technology (DST), India
  2. UGC MANF

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The study demonstrates the effectiveness of a heterogeneous mesoporous Ni-Mo/gamma-Al2O3 catalyst in removing metals from non-edible raw jatropha oil (RJO) during hydrodemetalation (HDM). Lower temperatures favor HDM, while higher temperatures promote RJO conversion. The catalyst shows promising potential for improving catalyst aging and green diesel production.
During the hydroprocessing reactions, one of the major reason for the deactivation of the catalyst and pore blockage of the active sites of the catalyst is the metals present in feed. It is extremely important to remove the metals to improve catalyst aging, therefore a heterogeneous mesoporous Ni-Mo/gamma-Al2O3 catalyst was used for hydrodemetalation (HDM) of untreated non-edible raw jatropha oil (RJO). The results show that the highest HDM of 83.4% was achieved at 250 ? temperature, 5 h(-1) LHSV, and 666 (V/V) H-2/feed ratio. The highest RJO conversion (97.2%) was obtained at 420 ? temperature with simultaneously 68.4% HDM. Lower temperature (250 ?) was more favourable for HDM due to minimum C-C cracking reactions than high temperature (420 ?), which favours more C-C/C-O bond cleavage. The catalyst shows prolonged activity up to 162 h, as compared to reported catalysts. TGA study of the spent catalyst indicates a 7.8 wt% coke deposition, complemented by TEM results. 13C solid-state NMR revealed saturated hydrocarbon-type compounds deposited over the catalyst supported by FTIR analysis. The physicochemical properties of bimetallic Ni-Mo catalyst show suitable surface area and pore diameter for the diffusion of triglycerides over the surface and pores of the catalyst. The catalyst showed the potential for HDM of RJO at a lower temperature of 250 ? and green diesel (C15-C18) production at a higher temperature of 420 ?.

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