A method for producing a metal-supported zeolite for alcoholic beverages for removing at least one component selected from dimethyl sulfide, dimethyl disulfide and dimethyl trisulfide contained in alcoholic beverages, comprising: a first ion-exchange treatment step of processing a zeolite carrying a metal ion with an ammonium ion-containing aqueous solution to thereby exchange the metal ion in the zeolite for an ammonium ion, the zeolite containing a sodium Y-type zeolite in an amount of 80% by mass or more based on the total mass of the metal-supported zeolite for alcoholic beverages, and a second ion-exchange treatment step of processing the ammonium ion-supported zeolite obtained in the previous ion-exchange treatment step with a silver ion-containing acidic aqueous solution to thereby exchange the ammonium ion therein with a silver ion, wherein the Na 2 O content in the zeolite after the second ion-exchange treatment step is 0.6% by mass or more and 6.5% by mass or less; wherein the amount of silver supported in the metal-supported zeolite for alcoholic beverages is 0.15g or more relative to 1 g of zeolite and the use ratio regarding silver is 85% or more, the use ratio regarding silver being obtained according to the following expression: Use ratio % = silver-supported amount in terms of an oxide thereof in zeolite / silver charged amount in terms of an oxide thereof as theoretical value × 100 ; the silver-supported amount in terms of an oxide thereof in zeolite was quantified using an ICP emission spectrometer, 720-ES manufactured by Agilent Technologies, Inc. in the above formula; and wherein the ultraviolet-visible absorption spectra of the metal-supported zeolite for alcoholic beverages, when measured using a diffuse reflection method in a measurement range of 800 to 200 nm, gives an absorption peak between 210 ± 10 nm and between 250 and 270 nm, the height of the absorption peak UV1 observed between 250 and 270 nm and the height of the absorption peak UV2 observed between 210 nm ± 10 nm satisfy (UV1/UV2) ≤ 0.2. a first ion-exchange treatment step of processing a zeolite carrying a metal ion with an ammonium ion-containing aqueous solution to thereby exchange the metal ion in the zeolite for an ammonium ion, the zeolite containing a sodium Y-type zeolite in an amount of 80% by mass or more based on the total mass of the metal-supported zeolite for alcoholic beverages, and a second ion-exchange treatment step of processing the ammonium ion-supported zeolite obtained in the previous ion-exchange treatment step with a silver ion-containing acidic aqueous solution to thereby exchange the ammonium ion therein with a silver ion, wherein the Na 2 O content in the zeolite after the second ion-exchange treatment step is 0.6% by mass or more and 6.5% by mass or less; wherein the amount of silver supported in the metal-supported zeolite for alcoholic beverages is 0.15g or more relative to 1 g of zeolite and the use ratio regarding silver is 85% or more, the use ratio regarding silver being obtained according to the following expression: Use ratio % = silver-supported amount in terms of an oxide thereof in zeolite / silver charged amount in terms of an oxide thereof as theoretical value × 100 ; the silver-supported amount in terms of an oxide thereof in zeolite was quantified using an ICP emission spectrometer, 720-ES manufactured by Agilent Technologies, Inc. in the above formula; and wherein the ultraviolet-visible absorption spectra of the metal-supported zeolite for alcoholic beverages, when measured using a diffuse reflection method in a measurement range of 800 to 200 nm, gives an absorption peak between 210 ± 10 nm and between 250 and 270 nm, the height of the absorption peak UV1 observed between 250 and 270 nm and the height of the absorption peak UV2 observed between 210 nm ± 10 nm satisfy (UV1/UV2) ≤ 0.2. <EOS>