Drying method for exhaust gas catalyst
View Patent ↗A method for preparing an exhaust gas catalyst includes preparing a washcoat comprising a catalytically effective amount of at least one catalytically active metal disposed upon an oxide support; disposing the catalytically active metal-oxide support washcoat upon a catalyst substrate; drying the washcoated catalyst substrate using microwave energy to affix the precious metals to the oxide support; and conventionally calcining the dried washcoated catalyst substrate. The catalysts comprising a substrate having dispersed thereon an inorganic oxide washcoat, the washcoat having been affixed to the substrate by microwave drying, exhibit high exhaust gas purifying performance and long durability. The catalysts thus produced further provide a long in-service lifetime for reforming organic fuel species into hydrogen, carbon monoxide and light hydrocarbons used in the nitrogen oxides reduction process.
1. A process for preparing an exhaust gas catalyst comprising:
preparing a washcoat slurry comprising a catalytically effective amount of at least one catalytically active metal and an oxide support to form a catalytically active metal-oxide support;
disposing the washcoat slurry upon a catalyst substrate;
drying the washcoat slurry and catalyst substrate using microwave energy to affix the catalytically active metal to the oxide support and catalyst substrate; and
calcining the dried washcoated catalyst substrate, wherein
the at least one catalytically active metal is selected from the group consisting of gold, silver, platinum, rhodium, palladium, iridium, ruthenium, osmium, tantalum, zirconium, yttrium, cerium, nickel, copper, oxides thereof, alloys thereof and combinations thereof.
2. The process of claim 1 , wherein preparing the washcoat slurry further comprises:
disposing a catalytically effective amount of at least one catalytically active metal upon an oxide support to form a catalytically active metal-oxide support;
drying the catalytically active metal disposed upon the oxide support using microwave energy to affix the catalytically active metal to the oxide support; and
calcining the dried catalytically active metal-oxide support.
3. The process of claim 1 , further comprising:
preparing the oxide support by precipitating the oxide support from precursor solutions using energy supplied by a microwave source of energy.
4. The process of claim 1 , wherein the catalytically active metal-oxide support washcoat comprises nanometer sized catalytically active metal particles.
5. The process of claim 1 , wherein the at least one catalytically active metal comprises a mixture of rhodium and platinum.
6. The process of claim 1 , wherein the catalytically active metals include precursors selected from the group consisting of ammines, acetates, citrates, oxalates, acetonates, or mixtures thereof.
7. The process of claim 1 , wherein the step of preparing a washcoat slurry comprises disposing a catalytically effective amount of at least one catalytically active metal upon an oxide support in the absence of stabilizers and binders.
8. The process of claim 1 , wherein the step of preparing a washcoat slurry comprises disposing a catalytically effective amount of at least one catalytically active metal upon an oxide support.
9. The process of claim 1 , wherein the washcoat slurry further comprises one or more surfactants, stabilizers, binders, promoters, or combination thereof.
10. The process of claim 1 , wherein the washcoat slurry further comprises a surfactant present in a concentration of about 0.001 weight % to about 2 weight %, based on the total weight of the washcoat.
11. The process of claim 1 , wherein a microwave dried oxide support comprises precious metal particles having a length of less than about 4 nanometers across the greatest length of the particle.
12. The process of claim 1 , wherein drying the washcoated catalyst substrate comprises drying the washcoated catalyst substrate for a time sufficient to achieve a water concentration in the washcoat of about 0.001 weight % to about 2 weight %, based on the weight of the washcoat.
13. The process of claim 1 , wherein the catalyst substrate comprises a monolith, an extruded monolith, an extruded honeycomb monolith, stacked foils, a porous structure, a calcium aluminate extruded honeycomb monolith, a calcium hexaaluminate extruded honeycomb monolith, or a combination thereof.
14. The process of claim 1 , wherein the oxide support comprises an inorganic oxide, aluminum oxide, zirconium oxide, titanium oxide, aluminum-gallium oxide, delta phase aluminum oxide, gamma phase aluminum oxide, stabilized oxides, lanthanum stabilized gamma phase aluminum oxide, barium stabilized gamma phase aluminum oxide, or a combination thereof.