Hydrodesulfurization (HDS) of sour crude oil is an effective way to address the corrosion problems in refineries

and is an economic way to process sour crude oil in an existing refinery built for sweet oil. In the current study

the HDS of Siberian crude oil was carried out in a slurry reactor. The Co-Mo

Ni-Mo

and Ni-W catalysts supported on

γ

-Al

2

O

3

were compared at the temperature of 340℃ and the pressure of 4.5 MPa. The HDS activity follows the order of Co-Mo Ni-Mo Ni-W at a high concentration of H

2

S

and the difference between Co-Mo and Ni-Mo becomes insignificant at a low concentration of H

2

S. The influence of reaction temperature 320-360℃ and reaction pressure 3-5.5 MPa was investigated

and both play a positive role in the HDS reaction. A kinetic model over Ni-Mo/Al

2

O

3

in the slurry reactor was established. The activation energy is estimated as 60.34 kJ·mol

-1

; the orders of sulfur components and hydrogen partial pressure are 1.43 and 1.30

respectively. The kinetic parameters are compared with those in a trickle-bed reactor

implying that the mass transfer is greatly enhanced in

the slurry reactor. The back mixing effect is present in the slurry reactor and can be reduced by a multi-stage design

which would lead to higher reactor efficiency in industrial application.