Oxidizing desulphuration of petrol fraction by hydrogen peroxide at presence of Mo-containing catalyst
The process of oxidative desulphurization of the catalytic cracking gasoline has been studied in the flow-type system over a heterogeneous Мo-containing catalyst with the purpose of lowering the time of contact between feedstock and reagents. It has been established that the conduction of the process in the flow-type system under optimal conditions (Т = 200°С and Vvol. = 0,5 h-1) ensures desulphurization of the total sulphur up to 81%.