A method for producing a polypropylene-based resin foamed molded article, comprising extruding a foamable molten resin, obtained by kneading a base resin and a physical blowing agent, through a die to form a foamed parison, and blow molding the foamed parison, said base resin comprising a branched polypropylene-based resin, a linear polypropylene-based resin and a recovered raw material that is recovered in the course of production of the polypropylene-based resin foamed molded article and that includes a resin that contains the branched polypropylene-based resin and the linear polypropylene-based resin which are kneaded together at least once with an extruder, wherein the branched polypropylene-based resin has a melt tension (230°C) of greater than 100 mN and a melt flow rate (230°C, load of 2.16 kg) of 0.1 to 15 g/10 min, the linear polypropylene-based resin has a melt tension (230°C) of less than 30 mN (not inclusive of 0) and a melt flow rate (230°C, load of 2.16 kg) of 5 to 25 g/10 min, the recovered raw material has a melt tension (230°C) of 5 to 50 mN and a melt flow rate (230°C, load of of 2.16 kg) of 2 to 50 g/10 min, wherein a difference (T m A - T m B) between a melting point T m A of the branched polypropylene-based resin and a melting point T m B of the linear polypropylene-based resin is -5°C to 5°C, a difference (T c A - T c B) between a crystallization temperature T c A of the branched polypropylene-based resin and a crystallization temperature T c B of the linear polypropylene-based resin is 0 to 10°C, a mixing amount of the branched polypropylene-based resin in the base resin is 5% by weight or more and 15% by weight or less based on 100% by weight of the base resin and a mixing amount of the recovered raw material in the base resin is more than 65% by weight and 90% by weight or less based on 100% by weight of the base resin, and a weight ratio (A:B) of the mixing amount of the branched polypropylene-based resin to a mixing amount of the linear polypropylene-based resin in the base resin is 80:20 to 40:60, and wherein the linear polypropylene-based resin is homopolypropylene. said base resin comprising a branched polypropylene-based resin, a linear polypropylene-based resin and a recovered raw material that is recovered in the course of production of the polypropylene-based resin foamed molded article and that includes a resin that contains the branched polypropylene-based resin and the linear polypropylene-based resin which are kneaded together at least once with an extruder, wherein the branched polypropylene-based resin has a melt tension (230°C) of greater than 100 mN and a melt flow rate (230°C, load of 2.16 kg) of 0.1 to 15 g/10 min, the linear polypropylene-based resin has a melt tension (230°C) of less than 30 mN (not inclusive of 0) and a melt flow rate (230°C, load of 2.16 kg) of 5 to 25 g/10 min, the recovered raw material has a melt tension (230°C) of 5 to 50 mN and a melt flow rate (230°C, load of of 2.16 kg) of 2 to 50 g/10 min, wherein a difference (T m A - T m B) between a melting point T m A of the branched polypropylene-based resin and a melting point T m B of the linear polypropylene-based resin is -5°C to 5°C, a difference (T c A - T c B) between a crystallization temperature T c A of the branched polypropylene-based resin and a crystallization temperature T c B of the linear polypropylene-based resin is 0 to 10°C, a mixing amount of the branched polypropylene-based resin in the base resin is 5% by weight or more and 15% by weight or less based on 100% by weight of the base resin and a mixing amount of the recovered raw material in the base resin is more than 65% by weight and 90% by weight or less based on 100% by weight of the base resin, and a weight ratio (A:B) of the mixing amount of the branched polypropylene-based resin to a mixing amount of the linear polypropylene-based resin in the base resin is 80:20 to 40:60, and wherein the linear polypropylene-based resin is homopolypropylene.