TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Process: The process further comprises: separating the paraffin rich component into a gasoline boiling point range paraffin rich component, a diesel boiling point range paraffin rich component, and an aviation boiling point range paraffin rich component and separating the cyclic rich component into a gasoline boiling point range cyclic rich component, a diesel boiling point range cyclic rich component and an aviation boiling point range cyclic rich component; separating the blended fuel produced in step (c) in a fractionation zone to separate the gasoline boiling point range blended fuel, the diesel boiling point range blended fuel and the aviation boiling point range blended fuel; selectively separating, in a hot high pressure hydrogen stripper, a gaseous stream comprising hydrogen, water and carbon dioxide from the first reaction zone product stream to generate the hydrocarbon fraction comprising paraffins; recycling to a rectification zone in the hot high pressure hydrogen stripper a portion of the paraffin rich component; recycling a portion of the hydrocarbon fraction comprising paraffins to the first reaction zone at a volume ratio of recycle to renewable feedstock of 2:1-8:1; recycling a portion of the cyclic rich component to the partial deoxygenation zone and/or the full deoxygenation zone where the volume ratio of recycle to feed to the deoxygenation zone is 2:1-8:1; recycling at least a portion of the branched paraffin-enriched stream to the second reaction zone; pre-treating the first renewable feedstock and/or the second renewable feedstock in one or more pretreatment zones at pretreatment conditions to remove at least a portion of contaminants in the feedstocks; and mixing one or more additives to at least one of the diesel boiling point range blended fuel, the aviation boiling point range blended fuel and the gasoline boiling point range blended fuel. In the process-I: a portion of the hydrogen is separated from the branched paraffin enriched stream and recycled to the hot high pressure hydrogen stripper; the first and second reaction zones are operated at 40-400 degrees C and a pressure of 689-13790 kPa; the partial deoxygenation zone is operated at a pressure of 3.4-20.6 MPa and at 200-400 degrees C; the full deoxygenation zone is operated at a pressure 689 kPa-13.8 MPa and at a temperature of about 300-500 degrees C; the hot high pressure hydrogen stripper is operated at a temperature of about 40-300 degrees C and a pressure of about 689-13790 kPa; the hot high pressure hydrogen stripper is operated at a pressure that is within 1034 kPa that of the first reaction zone and the second reaction zone is operated at a pressure at least 345 kPa greater than that of the first reaction zone; and at least one of the renewable feedstocks is in a mixture or co-feed with a petroleum hydrocarbon feedstock and the petroleum hydrocarbon feedstock is co-processed with the renewable feedstock. Preferred Components: The branched paraffin enriched stream further comprises hydrogen and paraffins in the diesel, gasoline and aviation boiling point ranges. The first and second renewable feedstocks are derived from a single renewable source.