Catalyst for purifying diesel engine exhaust gas and method for production thereof
View Patent ↗A catalyst which purges a diesel engine exhaust gas of HC, CO, and SOF and reduces the emission of particulates as well and a method for the production thereof are provided. The catalyst for purifying a diesel engine exhaust gas has deposited on a refractory three-dimensional structure a catalyst component comprising silica-alumina supporting at least one noble metal selected from the group consisting of platinum, palladium, and rhodium and zeolite. This catalyst is produced by adding a noble metal component into a slurry of silica-alumina thereby inducing chemical adsorption, then adding zeolite to the resultant mixture thereby obtaining a mixed slurry of a noble metal-supporting silica-alumina and zeolite, dipping a refractory three-dimensional structure in the slurry thereby inducing deposition of the catalyst component, and subsequently calcining the resultant composite.
1. A catalyst for purifying a diesel engine exhaust gas, formed by depositing on a refractory three-dimensional structure a catalyst component comprising silica-alumina having an average particle diameter of 10-45 μm, at least one noble metal selected from the group consisting of platinum, palladium, and rhodium, and beta zeolite, wherein the at least one noble metal is supported on the silica-alumina, but not on the beta zeolite.
2. A catalyst according to claim 1 , wherein the mass ratio of silica/alumina in said silica-alumina is in the range of 0.02-1.
3. A catalyst according to claim 1 , wherein the mass ratio of silica/alumina in said beta zeolite is in the range of 10-150.
4. A catalyst according to claim 1 , wherein said silica-alumina has a BET specific surface area in the range of 100-400 m 2 /g and the mass ratio of SiO 2 to Al 2 O 3 is in the ratio of 0.02-1.
5. A catalyst according to claim 1 , wherein said silica-alumina is in a powdery form.
6. A catalyst according to claim 1 , wherein the mass ratio of silica-alumina to zeolite is in the range of 0.5-5.
7. A catalyst according to claim 1 , wherein the amount of said at least one noble metal is in the range of 0.01-5 g per liter of the volume of the catalyst.
8. A catalyst according to claim 1 , wherein said catalyst component further contains at least one element selected from the group consisting of titanium, zirconium, and rare earth elements.
9. A method for the production of a catalyst for purifying a diesel engine exhaust gas, characterized by
adding a noble metal component into a slurry of silica-alumina having an average particle diameter of 10-45 μm, thereby inducing chemical adsorption,
adding beta zeolite to the resultant mixture thereby obtaining a mixed slurry,
dipping a refractory three-dimensional structure in said mixed slurry thereby inducing deposition of a catalyst component, and
calcining the composite consequently obtained.
10. A method according to claim 9 , wherein the mass ration of silica/alumina in said silica-alumina is in the range of 0.02-1.
11. A method according to claim 9 , wherein the mass ratio of silica/alumina in said beta zeolite is in the range of 10-150.
12. A method according to claim 9 , wherein said silica/alumina has a BET specific surface area in the range of 100-400 m 2 /g and the mass ratio of SiO 2 to Al 2 O 3 is in the ratio of 0.02-1.
13. A method according to claim 9 , wherein said silica-alumina is in a powdery form.
14. A method according to claim 9 , wherein the mass ratio of silica-alumina to zeolite is in the range of 0.5-5.
15. A method according to claim 9 , wherein the amount of said noble metal is in the range of 0.01-5 g per liter of the volume of the catalyst.
16. A method according to claim 9 , wherein said catalyst component further contains at least one element selected from the group consisting of titanium zirconium, and rare earth elements.
17. A method according to claim 9 , wherein the addition of the noble metal component into the slurry of silica-alumina is carried out at the temperature of 15-500° C.
18. The catalyst according to claim 1 , wherein the mass ratio of the silica-alumina and the beta zeolite is in the range of 0.8-3.
19. The method according to claim 9 , wherein the mass ratio of the silica-alumina and the beta zeolite is in the range of 0.8-3.
20. The catalyst according to claim 1 , wherein the mass ratio of silica and alumina in the silica-alumina is in the range of 0.05-0.5.
21. The catalyst according to claim 1 , wherein the mass ratio of silica and alumina in the beta zeolite is in the range of 18-50.