The H-2-distributed feeding concept using Pd/Ag-based membranes and an Ru-based catalyst in a Packed Bed Membrane Reactor (H-2-PBMR) for the synthesis of biofuels via the so-called Fischer-Tropsch Synthesis has been demonstrated. The most successful approach resulted when H-2-poor syngas (H-2/CO = 1) typically obtained from the gasification of biomass was fed directly through the reaction chamber, i.e., to the catalyst bed, whereas the H-2 needed to reach the proper stoichiometry for the FTS (H-2/CO = 2) was admitted, and properly distributed, into the catalyst bed through the Pd/Ag-based membrane by flowing H-2/He mixtures at the retentate side of the membrane. Under the optimum reaction conditions, the CO conversion measured with the H-2-distributed feeding concept is lower than that obtained in a conventional Packed Bed Reactor with H-2/CO = 2 (37.9 vs 50.7%), but significantly higher than that obtained in a conventional reactor with H-2/CO = 1 (14.1%). Remarkably, the productivity towards high-molecular hydrocarbons increases by almost 70% and the methane production decreases by one order of magnitude when using the H-2-distributed feeding concept in a Packed Bed Membrane Reactor. (C) 2015 Elsevier B.V. All rights reserved.