Abstract
Thermal solid–solid interactions in cobalt treated MoO
3/Al
2O
3 system were investigated using X-ray powder diffraction. The solids were prepared by wet impregnation method using Al(OH)
3, ammonium molybdate and cobalt nitrate solutions, drying at 100
°C then calcination at 300, 500, 750 and 1000
°C. The amount of MoO
3, was fixed at 16.67
mol% and those of cobalt oxide were varied between 2.04 and 14.29
mol% Co
3O
4. Surface and catalytic properties of various solid samples precalcined at 300 and 500
°C were studied using nitrogen adsorption at −196
°C, conversion of isopropanol at 200–500
°C and decomposition of H
2O
2 at 30–50
°C.
The results obtained revealed that pure mixed solids precalcined at 300
°C consisted of AlOOH and MoO
3 phases. Cobalt oxide-doped samples calcined at the same temperature consisted also of AlOOH, MoO
3 and CoMoO
4 compounds. The rise in calcination temperature to 500
°C resulted in complete conversion of AlOOH into very poorly crystalline γ-Al
2O
3. The further increase in precalcination temperature to 750
°C led to the formation of Al
2(MoO
4)
3, κ-Al
2O
3 besides CoMoO
4 and un-reacted portion of Co
3O
4 in the samples rich in cobalt oxide. Pure MoO
3/Al
2O
3 preheated at 1000
°C composed of MoO
3–αAl
2O
3 solid solution (acquired grey colour). The doped samples consisted of the same solid solution together with CoMoO
4 and CoAl
2O
4 compounds.
The increase in calcination temperature of pure and variously doped solids from 300 to 500
°C increased their specific surface areas and total pore volume which suffered a drastic decrease upon heating at 750
°C. Doping the investigated system with small amounts of cobalt oxide (2.04 and 4
mol%) followed by heating at 300 and 500
°C increased its catalytic activity in H
2O
2 decomposition. This increase, measured at 300
°C, attained 25.4- and 12.9-fold for the solids precalcined at 300 and 500
°C, respectively. The increase in the amount of dopant added above this limit decreased the catalytic activity which remained bigger than those of un-treated catalysts. On the other hand, the doping process decreased the catalytic activity of treated solids in isopropanol conversion especially the catalysts precalcined at 300
°C. This treatment modified the selectivities of treated solids towards dehydration and dehydrogenation of reacted alcohol.
The activation energies of H
2O
2 decomposition were determined for pure and variously doped solids. The results obtained were discussed in light of induced changes in chemical composition and surface properties of the investigated system due to doping with cobalt oxide.