THE CORE- SHELL STRUCTURE OF CATALYST IS ONE OF THE EFFECTIVE WAYS THAT NOT ONLY REDUCED PT LOADING BUT ALSO RAISED PT UTILIZATION FOR ORR ON ELECTRODE [1-3]. IN THIS RESEARCH, BIMETALLIC ELECTROCATALYST (RU@PT) WITH CORE- SHELL STRUCTURE WERE SYNTHESIZED BY USING THE IMPREGNATION WITH HYDROTHERMAL METHOD STEP BY STEP AND WERE CHARACTERIZED BY PHYSICAL AND ELECTROCHEMICAL TECHNIQUES. PHYSICAL TECHNIQUES (XRD, TEM AND ICP) INDICATE THAT THE RU AND PT WERE SUCCESSFULLY REDUCED ON VULCAN WITH DIFFERENT MOLAR RATIO (1:1, 2:1 AND 3:1 PT:RU). THE ELECTROCHEMICAL TECHNIQUES WERE DONE IN THREE ELECTRODE SYSTEM (LSV, CV, IES AND CHRONOAMPEROMETERY) AND SINGLE CELL. THE RESULTS OF HALF-CELL STUDIES ILLUSTRATED THAT AMONG 1:1, 2:1 AND 3:1 FOR ORR, 1:1 OF PT: RUMOLAR RATIO HAD THE BEST PERFORMANCE, THERE FOR, THE MEA WAS PREPARED BY USING THIS ELECTROCATALYST IN CATHODE AND COMMERCIAL PT/C AS ANODE. ELECTRODE FABRICATION IS SIMILAR TO PREVIOUSE WORK [4]. THE XRD PATTERNS SHOW THAT THE SIZE OF ELECTROCATALYST PARTICLE WAS NANOMETER. MOREOVER, THE TEM IMAGE INDICATES THE GOOD DISPERSION OF CATALYST IN 11. BETTER PERFORMANCE OF 1:1 MOLAR RATIO CAN ATTRIBUTED TO WELL DISPERSION OF CATALYST ON VULCAN AND CONSEQUENTLY INCREASED THREE PHASE ZONE. THE ELECTROCHEMICAL RESULTS EMPHASIS THIS IDEA (FIG. 3 AND 4). AS IT CAN SEE IN TABLE 1, EXCHANGE CURRENT DENSITY, ELECTROACTIVE SURFACE AREA AND CHARGE TRANSFER RESISTANCE OF 11(1:1 OF PT: RU) ARE THE BEST. THE ELECTRODE AREA OF MEA IS 5 CM2, AND THE CATALYST LOADING IS 0.3 MG.CM-2. THE N-112 WAS USED AS MEMBRANE AND ACTIVATION PROCESS WAS 0.6V AT 10H. THE POLARIZATION CURVE AND POWER DENSITY OF SINGLE CELL WERE OBTAINED (FIG. 5). MAXIMUM POWER DENSITY OF THIS CELL IS 547 MW.CM-2. THIS RESULT IS COMPARABLE TO OTHER REPORTED [1-3]. BY APPLIED DIFFERENT GAS PRESSURE AND ANODE HUMIDIFICATION CAN ACHIEVED THE BETTER RESULTS.