Catalytic changes of C1-C4 alkanes in (MoO₃)_x.(ZnO)_y.(ZrO2)_z.(B₂O₃)_k catalyst

Catalytic conversion of hydrocarbons C1-C4 in a steel flow reactor with an internal diameter of 12 mm, at normal atmospheric pressure, in the range of 550–650°, the volumetric velocity of reagent mixture 175–350 ml/min and contact time 0.5- Studied under conditions of 17.0 sec.The acidic properties of the catalysts were investigated by thermogrammed desorption of ammonia.The structure and position of the active centres of the catalyst were determined by electron microscopy, and the surface area was determined by the BET method.From aromatic hydrocarbons C1-C4, aromatic hydrocarbons are formed in the (MoO₃)_x.(ZnO)_y.(ZrO2)_z.(B₂O₃)_k catalyst with maximum yield.