from the hydrotreater i e the hydrotreated intermediate product is introduced into a product fractionator for separation into products such as liquefied petroleum gas u201c lpg u201d naphtha diesel fuel kerosene jet fuel and or distillates in the embodiment of the process of the present invention illustrated in fig3 such further processing of the heavy fraction from the feed fractionator comprises hydrocracking wherein the heavy fraction from the feed fractionator is introduced together with waxes from the product fractionator and hydrogen into a hydrocracker exemplary waxes from the product fractionator generally have a c 46 c 64 compositional range and an end distillation point total boiling point of about 604 u00b0 c in the hydrocracker the heavy fraction and waxes are subject to hydrocracking i e catalytically cracked or split in the presence of hydrogen to lighter carbon compounds e g c 20 h 2 u2192 c 10 the effluent from the hydrocracker i e the hydrocracked intermediate product is introduced into the product fractionator for separation into product in accordance with an alternative embodiment of the process of the present invention which is illustrated in fig4 the process schematic is similar to that illustrated in fig3 except that field condensate instead of ft condensate is mixed or blended with gas plant condensate prior to introduction into the hydrotreater and ft condensate instead of field condensate is fed to the feed fractionator together with light ft liquid distillate and heavy ft liquid distillate a portion of the waxes from the product fractionator in the embodiments illustrated in fig3 and 4 may be sent to a lube base oil unit not.