Selective catalytic oxidation of ammonia to water and nitrogen
View Patent ↗A catalyst includes a platinum coating deposited on a silica support. The support has an average surface area between about 100 m 2 /g and about 120 m 2 /g. The platinum coating is between about 5 wt % and about 15 wt % of the catalyst. The combination of the selected surface area, silica support, and selected amount of platinum coating provides a catalytic activation temperature below 200° C. and avoids the formation of NO x .
1. A method of removing ammonia from a gaseous mixture, comprising the step of removing ammonia from a gaseous mixture by oxidizing ammonia at a temperature below about 200° C. to produce gaseous nitrogen and water using a silica support having a catalyst coating; and
wherein the step of removing ammonia from a gaseous mixture by oxidizing ammonia at a temperature below about 200° C. to produce gaseous nitrogen and water includes providing said silica support to oxidize the ammonia, said silica support having an average surface area between about 100 m 2 /g and about 120 m 2 /g and a catalyst coating including platinum, said catalyst coating being supported by said support, and said catalyst coating comprising between about 5 wt % and about 15 wt % of a combined mass of said support and said catalyst coating.
2. The method of claim 1 , wherein said silica support is granule shaped.
3. The method of claim 1 , wherein said silica support is disk shaped.
4. The method of claim 1 , wherein said silica support is a silica aerogel.
5. The method of claim 2 , wherein said silica support includes a silica washcoat, and wherein said silica washcoat increases a surface area of the silica support.
6. The method of claim 5 , wherein said catalyst coating is supported on said silica washcoat.
7. The method of claim 1 , wherein said catalyst coating comprises approximately 10 wt % of a combined mass of said support and said catalyst coating.