The results of research on reception of the sale  diesel are resulted   fuel on a basis hydrogenating processes of  fraction 200–350⁰C TSP.  In the beginning from distillate delete heteronuclear connections with the help the catalyst  of mack GCD-205 at 340–360⁰C  3.0–4.0 MPa and the volume  speed of giving raw materials  1.0 h^-1. Hydrogenation process is carried out using a nickel-chromium catalyst at  280⁰C, hydrogen pressure of 5 MPa, feed  raw materials 0.5–1.0 h^-1. This above stated process allows to receive liquid  hydrocarbons from TSP and subjecting them hydrogenation process to receive  safe diesel fuel cleaned of from sulphur and aromatic hydrocarbons