Process to prepare paraffins and waxes, the process at least comprising the following steps: (a) providing a Fischer-Tropsch product stream comprising paraffins having from 10 to 300 carbon atoms; (b) subjecting the Fischer-Tropsch product stream of step (a) to a hydrogenation step, thereby obtaining a hydrogenated Fischer-Tropsch product stream comprising 10 to 300 carbon atoms; (c) separating the hydrogenated Fischer-Tropsch product stream of step (b), thereby obtaining at least a fraction comprising 10 to 17 carbon atoms and a fraction comprising 18 to 300 carbon atoms; (d) separating the hydrogenated fraction comprising 18 to 300 carbon atoms of step (c), thereby obtaining one or more first light waxes having a congealing point according to ASTM D938 in the range of 30 to 75°C and a second heavy wax having a congealing point according to ASTM D938 in the range of 75 to 120°C; e) hydrofinishing one or more wax fractions having a congealing point in the range of 30 to 75°C of step (d) thereby obtaining one or more hydrofinished wax fractions having a congealing point according to ASTM D938 in the range of 30 to 75°C; wherein the second heavy wax of step (d) is separated, thereby obtaining at least one distillate wax fraction having a congealing point according to ASTM D938 in the range of between 75 to 85°C and at least one residual wax fraction having a congealing point according to ASTM D938 in the range of from 95 to 120°C; and wherein the heavy distillate wax fraction having a congealing point in the range of between 75 to 85°C is hydrofinished to obtain a hydrofinished heavy distillate wax fraction having a congealing point according to ASTM D938 in the range of between 75 and 85°C. (a) providing a Fischer-Tropsch product stream comprising paraffins having from 10 to 300 carbon atoms; (b) subjecting the Fischer-Tropsch product stream of step (a) to a hydrogenation step, thereby obtaining a hydrogenated Fischer-Tropsch product stream comprising 10 to 300 carbon atoms; (c) separating the hydrogenated Fischer-Tropsch product stream of step (b), thereby obtaining at least a fraction comprising 10 to 17 carbon atoms and a fraction comprising 18 to 300 carbon atoms; (d) separating the hydrogenated fraction comprising 18 to 300 carbon atoms of step (c), thereby obtaining one or more first light waxes having a congealing point according to ASTM D938 in the range of 30 to 75°C and a second heavy wax having a congealing point according to ASTM D938 in the range of 75 to 120°C; e) hydrofinishing one or more wax fractions having a congealing point in the range of 30 to 75°C of step (d) thereby obtaining one or more hydrofinished wax fractions having a congealing point according to ASTM D938 in the range of 30 to 75°C; wherein the second heavy wax of step (d) is separated, thereby obtaining at least one distillate wax fraction having a congealing point according to ASTM D938 in the range of between 75 to 85°C and at least one residual wax fraction having a congealing point according to ASTM D938 in the range of from 95 to 120°C; and wherein the heavy distillate wax fraction having a congealing point in the range of between 75 to 85°C is hydrofinished to obtain a hydrofinished heavy distillate wax fraction having a congealing point according to ASTM D938 in the range of between 75 and 85°C. wherein the second heavy wax of step (d) is separated, thereby obtaining at least one distillate wax fraction having a congealing point according to ASTM D938 in the range of between 75 to 85°C and at least one residual wax fraction having a congealing point according to ASTM D938 in the range of from 95 to 120°C; and wherein the heavy distillate wax fraction having a congealing point in the range of between 75 to 85°C is hydrofinished to obtain a hydrofinished heavy distillate wax fraction having a congealing point according to ASTM D938 in the range of between 75 and 85°C.