Abstract
New types of hydrodesulfurization (HDS) catalyst Re-Ni-Mo/ γ-Al2O3 was prepared
and tested separately with two prepared conventional HDS catalysts (Ni-Mo/ γ-Al2O3
and Co-Mo//γ-Al2O3) by using a pilot plant hydrotreatment unit. Activities of three
prepared hydrodesulfurization catalysts were examined in hydrodesulfurization
(HDS) of atmospheric gas oil at different temperatures 275 to 350 °C and LHSV 1 to
4 h-1
, the reactions conducted under constant pressure 40 bar and H2/HC ratio 500
ml/ml .Moreover, the hydrogenation of aromatic (HAD) in gas oil has been studied.
HDS was much improved by adding promoter Re to the Ni-Mo/Al2O3 catalyst. The
results showed that Re-Ni-Mo/ γ-Al2O3 have more activity in desulfurization than NiMo//γ-Al2O3 and Co-Mo/ γ-Al2O3 catalysts. The efficiency of hydrodesulfurization
was markedly reduced over the Co -Mo/ γ-Al2O3.Also the result showed that NiMo//γ-Al2O3 have a minimum aromatic content 15.44 %
and tested separately with two prepared conventional HDS catalysts (Ni-Mo/ γ-Al2O3
and Co-Mo//γ-Al2O3) by using a pilot plant hydrotreatment unit. Activities of three
prepared hydrodesulfurization catalysts were examined in hydrodesulfurization
(HDS) of atmospheric gas oil at different temperatures 275 to 350 °C and LHSV 1 to
4 h-1
, the reactions conducted under constant pressure 40 bar and H2/HC ratio 500
ml/ml .Moreover, the hydrogenation of aromatic (HAD) in gas oil has been studied.
HDS was much improved by adding promoter Re to the Ni-Mo/Al2O3 catalyst. The
results showed that Re-Ni-Mo/ γ-Al2O3 have more activity in desulfurization than NiMo//γ-Al2O3 and Co-Mo/ γ-Al2O3 catalysts. The efficiency of hydrodesulfurization
was markedly reduced over the Co -Mo/ γ-Al2O3.Also the result showed that NiMo//γ-Al2O3 have a minimum aromatic content 15.44 %
Keywords
HDS catalyst
Hydrodesulfurization
Hydrogenation of aromatic
physical adsorption