Highly dispersed metal catalyst and related methods

1. A process of forming a catalytic metal onto a catalyst support, the process comprising the steps of:

preparing an aqueous solution comprising a promoter precursor having a promoter cation of Sn or Co and a catalytic metal precursor comprising H 2 PtCl 6 comprising a catalytic metal of Pt with each of the promoter of Sn or Co and the catalytic metal of Pt being in amounts substantially equivalent by moles to form a catalyst and promoter solution in which the promoter precursor and the catalytic metal precursor are dissolved such that the promoter precursor provides an active ion of either Sn 2+ or Co 2+ having an opposite charge of a charge of an active ion of the catalytic metal precursor comprising PtCl 6 2− ,

selecting a porous catalyst support with surfaces having adequate surface area;

adjusting the pH of the resulting catalyst and promoter solution;

immersing the catalyst support in the catalyst and promoter solution in which both the catalyst precursor and promoter precursor are dissolved, such that the porous catalyst support is impregnated with the catalytic metal and the catalyst support is in contact with the catalyst and promoter solution for impregnation;

removing the catalyst support from the catalyst and promoter solution;

drying the impregnated catalyst support under ambient conditions that prevents capillary effect transfer of the impregnating from an interior of the catalyst support to an exterior of the catalyst support with the catalytic metal being further dried at or above 100° C.;

performing a catalyst calcination step under elevated temperatures; and

achieving a single atomic dispersion of the Pt of at least 90% with a 1.1 or greater wt % Pt loading.

2. The process according to claim 1 wherein the catalytic metal is further dried at or above 100° C.

3. The process according to claim 1 wherein the calcination step is done in the presence of at least one of air, hydrogen, inert gas, or combination thereof.

4. The process according to claim 3 wherein the calcination step is performed at a temperature between 450° and 700° C.

5. The process according to claim 1 wherein the catalytic metal occupies less than 0.5% of the catalyst surface area.

6. The process according to claim 1 wherein the catalyst support is porous, and its surface area is between about 385 m 2 /g and about 1,475 m 2 /g.

7. The process according to claim 1 wherein at least a portion of the catalytic metal forms an atomic structure on the catalyst support such that every atom of the catalytic metal is capable of interaction during catalytic activity to provide the single atomic dispersion of the catalytic metal and a value for the single atomic dispersion is determined using a hydrogen-oxygen titration dispersion calculation based on the ratio of the number of moles of adsorptive chemisorbed to the number of moles of the catalytic metal.

8. The process according to claim 1 wherein the platinum is present at between 1.1 to 1.5% weight loading and a dispersion value greater than 100% using a hydrogen-oxygen titration dispersion calculation based on the ratio of the number of moles of adsorptive chemisorbed to the number of moles of platinum in the catalytic metal.

9. The process according to claim 1 , wherein the catalytic metal is cycled between about 500° C. and ambient without losing dispersion value determined using a hydrogen-oxygen titration dispersion calculation based on the ratio of the number of moles of adsorptive chemisorbed to the number of moles of the catalytic metal.

10. The process according to claim 1 wherein the catalyst support is selected from the group consisting of activated carbon, alumina, silica, silica-alumina, or molecular sieves.