Mechanochemical activation of industrial catalysts: 1. Catalytic properties of STK, NTK-10-1, and nickel-chromia catalysts and their mechanical mixtures in redox reactions involving nitrogen oxide, carbon monoxide, and hydrocarbons
Vf. Tret'Yakov et al., Mechanochemical activation of industrial catalysts: 1. Catalytic properties of STK, NTK-10-1, and nickel-chromia catalysts and their mechanical mixtures in redox reactions involving nitrogen oxide, carbon monoxide, and hydrocarbons, PETR CHEM, 40(5), 2000, pp. 326-331
The effect of mechanochemical activation on the activity of mechanical mixt
ures of the industrial catalysts STK and NTK-10-1 and a nickel-chromia cata
lyst as binary compositions in the reactions of selective reduction of nitr
ogen oxides with propane in the presence of oxygen and severe oxidation of
hydrocarbons (using toluene as an example), as well as the activity of the
mechanochemical catalyst SNM-1, which is similar to the industrial catalyst
in composition, in the reaction of deep oxidation of CO were examined. It
was shown that the activity of catalytic compositions prepared by joint gri
nding of components in a planetary activator in the reaction of selective r
eduction of nitrogen oxides with propane substantially depended on the cond
itions of mechanochemical treatment (grinding body load and grinding time).
At the optimum load on the materials of the system (load 1 : 5, grinding t
ime 10 min), the activity of the catalytic compositions obtained from the c
atalysts NTK-10-1 and Ni-Cr oxide by the mechanochemical procedure was note
d to increase as manifested by shifting the NO conversion temperature maxim
um to lower temperatures by 100 degrees C. It was found that the catalytic
activity of mechanical mixtures and mechanochemical systems (regardless of
their preparation conditions) in the reaction of deep oxidation of toluene
is higher than that of the individual catalysts composing the formulations.
The catalyst prepared from corresponding oxides by the mechanochemical pro
cedure to have the same composition as the industrial catalyst SNM-1 obtain
ed by the traditional coprecipitation method exhibits approximately the sam
e activity as the latter in CO oxidation reaction. In the view of high envi
ronmental safety of the technology of catalyst preparation by the mechanoch
emical method, opportunities for the synthesis of catalysts of various comp
ositions with properties superior to those of analogous industrial catalyst
s prepared by the conventional procedures and for rapid launching of produc
tion of catalysts of any prescribed composition, this method was shown to h
old much promise.