NOVELTY - Process-I for producing a blended fuel from renewable feedstocks comprises generating at least one paraffin rich component from a first renewable feedstock comprising glycerides, generating a cyclic rich component from a second renewable feedstock comprising pyrolysis oil and blending the paraffin rich and the cyclic rich components to form the blended fuel.    USE - The process is useful for producing a blended fuel from renewable feedstocks, where the blended fuel is a diesel boiling point range blended fuel, an aviation boiling point range blended fuel and a gasoline boiling point range blended fuel (all claimed) e.g. a kerosene type fuel including JP-8.    ADVANTAGE - The process enables: blending of paraffin rich component (generated from glycerides and free fatty acids in feedstocks e.g. plant and animal oils) and cyclic rich component (generated from biomass derived pyrolysis oil) such that the resulting target fuel comprises two components that were produced from renewable feedstocks; production of the paraffin rich and the cyclic rich components from the same renewable source; and integration of the different steps which produce the paraffin rich and the cyclic rich components with economical manner.    DETAILED DESCRIPTION - Process-I for producing a blended fuel from renewable feedstocks comprises: (a) generating at least one paraffin rich component from a first renewable feedstock comprising at least glycerides, comprising (i) treating the glycerides and free fatty acids in the renewable feedstock in a first reaction zone by hydrogenating and deoxygenating the glycerides using a catalyst at reaction conditions in the presence of hydrogen to provide a first reaction zone product stream comprising hydrogen, water, carbon dioxide and a hydrocarbon fraction comprising paraffins in the diesel boiling point range, (ii) introducing the hydrocarbon fraction comprising paraffins to a second reaction zone to contact an isomerization and selective hydrocracking catalyst at isomerization and selective cracking conditions to selectively hydrocrack at least a portion of the paraffins and to isomerize the paraffins and generate a branched paraffin-enriched stream and (iii) cooling the branched paraffin-enriched stream and the gaseous stream and separating a gaseous component comprising at least hydrogen and carbon dioxide from the paraffin rich component and a water component; (b) generating a cyclic rich component from a second renewable feedstock comprising pyrolysis oil, comprising (iv) partially deoxygenating the pyrolysis oil in a first pyrolysis oil deoxygenation zone by contacting the pyrolysis oil with a first deoxygenation and hydrogenation catalyst in the presence of hydrogen at deoxygenation conditions to produce a partially deoxygenated pyrolysis oil stream comprising water, gasses, light ends and hydrocarbons, (v) passing the partially deoxygenated pyrolysis oil stream to a separation zone to separate a water, gasses and light ends stream from a hydrocarbon stream and (vi) passing the hydrocarbon stream to a second pyrolysis oil deoxygenation zone and deoxygenating the hydrocarbon stream by contacting with a second deoxygenation catalyst under deoxygenation conditions, to generate a cyclic rich component comprising cyclic hydrocarbon compounds useful as a fuel or a fuel blending component in the boiling point ranges of gasoline, aviation and/or diesel; and (c) blending the paraffin rich component and the cyclic rich component to form at least one blended fuel which is a gasoline boiling point range blended fuel, a diesel boiling point range blended fuel and/or an aviation boiling point range blended fuel. INDEPENDENT CLAIMS are included for:    (1) a process-II for producing a blended fuel from renewable feedstocks comprising: the step (a); (b1) generating a cyclic rich component from a second renewable feedstock comprising pyrolysis oil, comprising: deoxygenating the pyrolysis oil in a deoxygenation zone by contacting, in the presence of hydrogen at deoxygenation conditions, the pyrolysis oil with a first deoxygenation and hydrogenation catalyst in a first portion of the deoxygenation zone with a second deoxygenation catalyst in a second portion of the deoxygenation zone to produce a deoxygenated pyrolysis oil stream comprising water, gasses, light ends and cyclic hydrocarbons; and passing the deoxygenated pyrolysis oil stream to a separation zone to separate a water, gasses and light ends stream from a cyclic rich component comprising cyclic hydrocarbon compounds useful as a fuel or a fuel blending component in the boiling point ranges of gasoline, aviation and/or diesel; and the step (c);    (2) a diesel boiling point range blended fuel, an aviation boiling point range blended fuel, and a gasoline boiling point range blended fuel produced by the process-I;    (3) a blended fuel meeting the specification of MTL-DTL-83133 where at least one component of the blended fuel is the aviation boiling point range blended fuel produced by the process-I;    (4) a blended fuel comprising the gasoline boiling point range blended fuel, aviation boiling point range blended fuel, diesel boiling point range blended fuel and a component produced from processing a petroleum feedstock; and    (5) a process-III for producing a blended fuel from renewable feedstocks comprising: the step (a); (b2) generating a cyclic rich component from a second renewable feedstock comprising pyrolysis oil, comprising: deoxygenating the pyrolysis oil in a deoxygenation zone by contacting, in the presence of hydrogen at deoxygenation conditions, the pyrolysis oil with a mixture of a first deoxygenation catalyst and a second deoxygenation catalyst to produce a deoxygenated pyrolysis oil stream comprising water, gasses, light ends and cyclic hydrocarbons where the first deoxygenation catalyst is a hydrotreating catalyst and the second deoxygenation catalyst is a hydrocracking catalyst; and passing the deoxygenated pyrolysis oil stream to a separation zone to separate a water, gasses and light ends stream from a cyclic rich component comprising cyclic hydrocarbon compounds useful as a fuel or a fuel blending component in the boiling point ranges of gasoline, aviation, and/or diesel; and the step (c).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the process for generating paraffin rich component.    Hot high pressure hydrogen stripper (8)    Rectification zone (23)    Hydrogen separator (26)    Air cooler (32)    Product separator (34)