NOVELTY - Production of hydrocarbon products obtained from a feedstock including a nonpretreated organic-oil, comprises hydro reforming the feedstock in the presence of hydrogen and a hydro reforming catalyst including a transition metal and support to obtain a liquid waste including at least an aqueous phase and at least an organic phase, hydro-treating and/or hydrocracking at least a part of the organic phase of the liquid waste to obtain a hydrocarbon effluent.    USE - The method is useful for production of hydrocarbon products obtained from a feedstock including at least a nonpretreated organic-oil (claimed), where the hydrocarbon products such as chemical products are useful for producing liquid fuels such as biofuel for air transport, marine and land applications.    ADVANTAGE - The method is capable of effectively producing hydrocarbon products obtained from the feedstock with reduced hydrogen consumption and without the formation of solids and deactivation of catalyst thus maximizing the deoxygenized oil yield.    DETAILED DESCRIPTION - Production of hydrocarbon products obtained from a feedstock including at least a nonpretreated organic-oil, comprises hydro reforming the feedstock in the presence of hydrogen and a hydro reforming catalyst including at least a transition metal consisting of groups 3 to 12 elements and at least a support consisting of activated carbons, silicon carbides, silcas, transition aluminas, silcas alumina, zirconium oxide, cerium oxide, titanium oxide and transition metal aluminates to obtain a liquid waste including at least an aqueous phase and at least an organic phase, and hydro-treating and/or hydrocracking at least a part of the organic phase of the liquid waste to obtain a hydrocarbon effluent, where a part of the organic phase of the liquid waste is recycled in the hydro reforming step, a mixture with the feedstock includes an organic-oil with a recycle ratio equal to the ratio of the mass throughput of the organic phase on the mass throughput of the non-pretreated organic-oil of 0.05-2 and the hydrocarbon effluent is not recycled in the hydro reforming step.