CATALYST FOR ELECTRODE OF FUEL CELL, METHOD FOR PREPARING THE SAME AND FUEL CELL COMPRISING THE SAME

1 . A catalyst for a fuel cell electrode, the catalyst comprising:

an active particle which comprises:

a core comprising platinum, a transition metal excluding platinum, and an oxide of a non-transition metal; and

a shell disposed on the core and comprising platinum,

wherein the active particle comprises platinum and the non-transition metal in a molar ratio of 100:1.80 to 100:4.00.

2 . The catalyst for a fuel cell electrode of claim 1 , wherein the active particle comprises platinum and the non-transition metal in a molar ratio of 100:2.00 to 100:3.80.

3 . The catalyst for a fuel cell electrode of claim 1 , wherein the active particle comprises platinum and the transition metal excluding platinum in a molar ratio of 100:15.00 to 100:40.00.

4 . The catalyst for a fuel cell electrode of claim 1 , wherein the transition metal is at least one selected from the group consisting of titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, and zinc.

5 . The catalyst for a fuel cell electrode of claim 1 , wherein the oxide of the non-transition metal is at least one selected from the group consisting of indium oxide, tin oxide, and antimony oxide.

6 . The catalyst for a fuel cell electrode of claim 1 , further comprising a carbon-based support supporting the active particle.

7 . A method of preparing the catalyst for a fuel cell electrode of claim 1 , the method comprising:

preparing a first mixture comprising a first platinum precursor, a precursor of transition metal excluding platinum, and a non-transition metal oxide precursor;

preparing a preliminary core by performing a first heat treatment on the first mixture;

preparing a second mixture comprising the preliminary core and a second platinum precursor;

preparing preliminary active particles by performing a second heat treatment on the second mixture; and

preparing active particles by performing a third heat treatment on the preliminary active particles,

wherein a molar ratio of a total sum of platinum of the first platinum precursor and the second platinum precursor to a non-transition metal of the non-transition metal oxide precursor is in a range of 100:1.80 to 100:4.00.

8 . The method of claim 7 , wherein the first platinum precursor and the second platinum precursor are each independently at least one selected from the group consisting of H 2 PtCl 4 , H 2 PtCl 6 , H 2 PtCl 6 ·6H 2 O, K 2 PtCl 4 , K 2 PtCl 6 , Pt(NH 3 ) 4 Cl 2 , and Pt(NH 3 ) 2 Cl 2 .

9 . The method of claim 7 , wherein the precursor of the transition metal excluding platinum is at least one selected from the group consisting of a nitride of the transition metal excluding platinum, a chloride of the transition metal excluding platinum, a sulfide of the transition metal excluding platinum, an acetate of the transition metal excluding platinum, an acetylacetonate of the transition metal excluding platinum, and a cyanide of the transition metal excluding platinum.

10 . The method of claim 7 , wherein the non-transition metal oxide precursor is at least one selected from the group consisting of a nitride of the non-transition metal, a chloride of the non-transition metal, a sulfide of the non-transition metal, an acetate of the non-transition metal, and an acetylacetonate of the non-transition metal.

11 . The method of claim 7 , wherein the first heat treatment is performed at 200° C. to 300° C.

12 . The method of claim 7 , wherein the second heat treatment is performed at 40° C. to 210° C.

13 . The method of claim 7 , wherein the third heat treatment is performed at 170° C. to 350° C.

14 . The method of claim 7 , wherein the preparing of the preliminary core includes performing the first heat treatment on the first mixture and a support mixture comprising a carbon-based support.

15 . A fuel cell comprising:

an oxidation electrode;

a reduction electrode; and

an electrolyte membrane disposed between the oxidation electrode and the reduction electrode,

wherein at least one selected from the group consisting of the oxidation electrode and the reduction electrode comprises the catalyst of claim 1 .