NOVELTY - Producing a renewable fuel from biomass, comprises: (a) converting biomass in a biomass conversion unit (24) and separating the converted biomass into a fluid phase and a solid phase; (b) separating the fluid phase into a non-condensable gas phase, a renewable bio-oil and process water; (c) fractionating the renewable bio-oil into a water stream, a full range bio-naphtha stream and a topped bio-oil stream; and (d) molecularly recombining the oxygenates of 5C or lower within the process water, the bio-naphtha stream and the water stream to produce a recovered organic stream (ROS).    USE - The process is useful for producing a renewable fuel comprising renewable jet fuel, renewable gasoline, renewable diesel and/or renewable fuel oil from biomass (all claimed), which is useful as a feedstock to produce useful biofuels. The biomass comprises: a lignocellulosic material comprising forestry waste such as wood chips, saw dust, pulping waste, and tree branches; an agricultural waste such as corn stover, wheat straw, and bagasse; and/or energy crops such as Eucalyptus, switch grass and coppice.    ADVANTAGE - The improved process is capable of producing the renewable fuel with high efficiency and yield.    DETAILED DESCRIPTION - Producing a renewable fuel from biomass, comprises: (a) converting biomass in a biomass conversion unit (24) in the presence of a biomass conversion catalyst and separating the converted biomass into a fluid phase and a solid phase; (b) separating the fluid phase into a non-condensable gas phase, a renewable bio-oil and process water; (c) fractionating the renewable bio-oil into a water stream, a full range bio-naphtha stream and a topped bio-oil stream, where the topped bio-oil stream comprises 6C or higher oxygenates; (d) molecularly recombining the oxygenates of 5C or lower within the process water, the full range bio-naphtha stream and the water stream to produce a recovered organic stream (ROS) comprising 6C or greater oxygenates and a clear aqueous stream; (e) forming a slurry catalyst mix from the ROS and a soluble hydroprocessing active phase; (f) feeding at least a portion of biomass conversion catalyst and the catalyst mix into a slurry-phase hydroprocessor reactor; (g) forming a solid-phase slurry dispersed catalyst comprising atomically dispersoids of the active phase onto a support comprising the biomass conversion catalyst in the slurry-phase hydroprocessor reactor; (h) feeding the topped bio-oil stream into the slurry-phase hydroprocessor reactor and subjecting the topped bio-oil stream to hydrogenation in the presence of the solid-phase slurry dispersed catalyst; and (i) obtaining renewable fuels originating from hydrogenated topped bio-oil stream. An INDEPENDENT CLAIM is included for enhancing the recovery of renewable fuels from biomass, comprising (a1) subjecting a treated biomass feedstream to cracking in a fluidized catalytic cracking unit in the presence of a biomass conversion catalyst, (b1) separating a renewable oil phase from the fluid stream, (c1) fractionating the renewable oil phase into a full range bio-naphtha stream and a topped bio-oil stream comprising C6 or greater oxygenates, (d1) feeding the topped bio-oil stream into a slurry-phase hydroprocessor reactor, (e1) adding a metal or a metal containing compound comprising the active phase of a solid-phase slurry dispersed catalyst to the slurry-phase hydroprocessor reactor and depositing the active phase onto a solid support, (f1) subjecting the topped bio-oil stream to hydrogenation, and (g1) obtaining the renewable fuels from a stream originating from the hydrogenated topped bio-oil stream.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of an integrated biomass conversion system for producing a renewable fuel.    Biomass conversion unit (24)    Solid/vapors disengaging system (32)    Regenerator (42)    First fractionator (54)    Recombinator. (58)