The results of the development of technology for interstage separation of reformate in the reforming process with a fixed-bed catalyst are discussed. It has been shown that the proposed isolation of the 150A degrees C-FBP fraction from the feedstock can significantly increase the yield of aromatic hydrocarbons, to improve the selectivity of the process, to increase the reformate yield (by 6-8 wt % on a feed basis), and to lower the charge of an expensive platinum catalyst in a reactor to 20%.