NOVELTY - Producing liquid product from biomass, comprises: (a1) hydropyrolyzing biomass in hydropyrolysis reactor (10) to form carbon dioxide (CO2), carbon monoxide (CO) and light hydrocarbon gases having 1-3C, partially deoxygenated hydropyrolysis liquid and char; (a2) removing char; (a3) hydroconverting the liquid in hydroconversion reactor (11) into fully deoxygenated hydrocarbon liquid and gaseous mixture comprising CO, CO2 and 1-3C gases; (a4) steam reforming a portion of gaseous mixture to form reformed molecular hydrogen (H2); and (a5) introducing H2 to the reactor to hydropyrolyze biomass.    USE - The process is useful for producing liquid products from biomass (claimed), where the liquid products are useful in irrigation and arid areas.    ADVANTAGE - The process: is self-sustaining i.e. once it is initiated it does not require additional reactants, heat or energy from external sources; and provides the liquid product in an economical manner exhibiting excellent chemical stability with negligible to low-char and partially deoxygenated, where the liquid product is easy to transport.    DETAILED DESCRIPTION - Producing liquid products from biomass comprises: (a1) hydropyrolyzing biomass in a hydropyrolysis reactor vessel (10) containing molecular hydrogen and a deoxygenating catalyst to produce carbon dioxide (CO2), carbon monoxide (CO) and light hydrocarbon gases having 1-3C, a partially deoxygenated hydropyrolysis liquid and char; (a2) removing the char from the partially deoxygenated hydropyrolysis liquid; (a3) hydroconverting the partially deoxygenated hydropyrolysis liquid in a hydroconversion reactor vessel (11) using a hydroconversion catalyst in the presence of the CO2, CO and 1-3C gas generated in step (a1) to produce a fully deoxygenated hydrocarbon liquid and a gaseous mixture comprising CO, CO2 and 1-3C hydrocarbon gases; (a4) steam reforming a portion of the gaseous mixture using water produced in step (a1) and step (a3) to produce reformed molecular hydrogen; and (a5) introducing the reformed molecular hydrogen into the reactor vessel for hydropyrolizing the biomass. The steps (a1) and (a3) are operated at conditions that convert the biomass containing 30-70% of oxygen to water, CO and CO2.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic flow diagram of process for producing liquid product from biomass.    Hydropyrolysis reactor vessel (10)    Hydroconversion reactor vessel (11)    High pressure separators (12, 13)    Low pressure separator (14)    Steam reformer (15)