A light cobalt catalyzed Fischer-Tropsch (F-F) wax was subjected to hydrocracking in the range of temperature 319-351 degrees C and hydrogen pressure between 3.5 and 6.0 MPa. The catalyst used was platinum on amorphous silica-alumina. Hydrocracking reaction led to an increase of middle distillate yield tip to 85% with a contemporary increase of iso-paraffins concentration which resulted in a remarkable improvement of cold flow properties of the products The freezing point Of C(10)-C(14) fraction passed from - 23 to -45 degrees C while the pour point Of C(15)-C(22) fraction decreased from 13 to - 23 degrees C. The latter fraction displayed high cetane numbers ranging between 75 and 80. Changes in carbon distribution and molecular structure of products during hydrocracking have been rationalized in the light of the accepted hydrocracking mechanism where n-paraffins undergo to consecutive isomerization reactions leading to isomers with progressively higher branching degree and concomitant cracking reaction. Experimental evidences Support the view that apparent reactivity of n-paraffins is chain length dependent. increasing with the molecular weight. Detailed characterization by NMR and GC showed that branching groups abundance in the middle distillate products was the following. methyl >> ethyl > propyl Emission tests carried out with FT diesel and commercial ultra low sulfur diesel showed that FT diesel has excellent combustion properties and leads to a reduction of emissions. (C) 2009 Elsevier B.V. All rights reserved.