Author/Authors :
Takht Ravanchi ، M نويسنده Catalyst Research Group, Petrochemical Research and Technology Co., National Petrochemical Co., Tehran, Iran , , Fadaeerayeni، S نويسنده Catalyst Research Group, Petrochemical Research and Technology Co., National Petrochemical Co., Tehran, Iran , , Rahimi Fard، M نويسنده Catalyst Research Group, Petrochemical Research and Technology Co., National Petrochemical Co., Tehran, Iran ,
Abstract :
In the present research, egg-shell Pd-Ag/?-Al2O3 catalysts prepared by impregnation
method using self-improved spherical alumina support with BET 13.34m2/g and pore
volume 0.36cm3/g were used for the hydrogenation of acetylene in the presence of a
large excess of ethylene (tail-end cuts) and their activity-selectivity patterns were
compared with the commercial one. All of the synthesized catalysts were tested under
60°C, 10bar, space velocity 6500h-1 and H2/C2H2 ratio 1.5 (mol/mol) which is the same
as an industrial plant.
The effect of impregnation operating parameters, such as pH of the impregnation
solution and impregnation type, on palladium penetration depth and palladium uptake
was investigated.pH 1.5 is best for impregnation solution.Catalytic performance tests
showed that for Pd-Ag/?-Al2O3 catalysts,sequential impregnation was a suitable
method for the active metal. By controlling the synthesis condition, the best Pd-Ag/?-
Al2O3 sample was an egg-shell one in which Pd was loaded evenly in a layer with
thickness 20-30µm. This sample gave ethylene selectivity of 100% and acetylene
conversion of 58% which is higher than the commercial one.