EFFECT OF LOADING ON HYDRODESULFURIZATION ACTIVITY OF MO AL2O3 AND MO/C SULFIDE CATALYSTS PREPARED BY SLURRY IMPREGNATION WITH MOLYBDIC ACID/

Citation
E. Hillerova et M. Zdrazil, EFFECT OF LOADING ON HYDRODESULFURIZATION ACTIVITY OF MO AL2O3 AND MO/C SULFIDE CATALYSTS PREPARED BY SLURRY IMPREGNATION WITH MOLYBDIC ACID/, Applied catalysis. A, General, 138(1), 1996, pp. 13-26
Citations number
41
Categorie Soggetti
Chemistry Physical","Environmental Sciences
ISSN journal
0926860X
Volume
138
Issue
1
Year of publication
1996
Pages
13 - 26
Database
ISI
SICI code
0926-860X(1996)138:1<13:EOLOHA>2.0.ZU;2-1
Abstract
The MoO3/alumina and Mo/active carbon catalysts of various loadings we re prepared by the new slurry impregnation method (SIM). The slurry of MoO3 in water was added to the support. The pH of the slurry was 2.5 and this was favourable for the adsorption of molybdate anions on alum ina and active carbon with the point of zero charge 7.0 and 7.5, respe ctively. The low solubility of MoO3 was sufficient to transport molybd enum species from solid MoO3 to the adsorbed phase. The equilibrium wa s achieved after 5 weeks at 30-50 degrees C. The calcination was not n ecessary and was left out. This was especially advantageous for active carbon support which is susceptible to oxidative damage. The maximum loading achieved was 18 and 31 wt.-% MoO3 for Al2O3 (195 m(2) g(-1)) a nd active carbon (1100 m(2) g(-1)), respectively. The activity was tes ted in the hydrodesulfurization of thiophene at 1.6 MPa and 250-400 de grees C. The activity of the SIM samples was similar to the activity o f the catalysts prepared by the conventional impregnation method (CIM) with ammonium heptamolybdate. The dependence of the activity on loadi ng for the SIM samples was the same as reported in the literature for CIM catalysts. On alumina the activity per unit of molybdena was const ant in the whole range of the loading 0-18 wt.-% MoO3. On active carbo n it gradually decreased in the whole range of the loading from 0 to 3 1 wt.-% MoO3. It is concluded that the nature of the SIM catalysts is the same as of the CIM catalysts but the SIM possesses several advanta ges.