초록 ▼

A pollution control catalyst for a catalytic converter comprising the exhaust system of an internal combustion engine, said catalyst including a refractory oxide support, and an activated phase therefor comprised of 0.3 to 7% by weight cerium based upon the weight of said support, 0.1 to 3.5% by wei

A pollution control catalyst for a catalytic converter comprising the exhaust system of an internal combustion engine, said catalyst including a refractory oxide support, and an activated phase therefor comprised of 0.3 to 7% by weight cerium based upon the weight of said support, 0.1 to 3.5% by weight iron, also based upon the weight of said support, at least one platinum or palladium metal, and at least one iridium or rhodium metal.

대표청구항 ▼

1. A catalyst composition for the conversion of carbon monoxide, hydrocarbons, and nitrogen oxides comprising a refractory oxide support, and an activated phase deposited on said support consisting essentially of 0.3 to 7% by weight cerium based upon the weight of said support, 0.1 to 3.5% by weight

1. A catalyst composition for the conversion of carbon monoxide, hydrocarbons, and nitrogen oxides comprising a refractory oxide support, and an activated phase deposited on said support consisting essentially of 0.3 to 7% by weight cerium based upon the weight of said support, 0.1 to 3.5% by weight iron, also based upon the weight of said support, at least one platinum or palladium metal, and at least one iridium or rhodium metal, the ratio of the at least one platinum or palladium metal to the at least one iridium or rhodium metal being between about 5:1 and about 250:1. 2. The catalyst composition as defined by claim 1, said support comprising a refractory oxide selected from the group consisting of silica, alumina, aluminosilicate, and the mixed oxides alumina/silica, alumina/zirconium oxide, alumina/cerium oxide, alumina/titanium oxide, and admixtures thereof. 3. The catalyst composition as defined by claim 2, said refractory oxide being alumina having a specific surface area ranging from 25 to 250 m 2 /g, a total pore volume ranging from 0.5 to 2 cm 3 /g, and a macropore volume, of those pores having a diameter greater than 1,000 A, ranging from 0.05 to 0.6 cm 3 /g. 4. The catalyst composition as defined by claim 3, said specific surface area ranging from 70 to 150 m 2 /g, said total pore volume ranging from 0.8 and 1.7 cm 3 /g, and said macropore volume ranging from 0.2 to 0.5 cm 3 /g. 5. The catalyst composition as defined by claims 1 or 3, comprising from about 0.04 to 0.5% by weight of said at least one platinum or palladium metal based upon the weight of the support. 6. The catalyst composition as defined by claim 5, comprising from about 0.002 to 0.1% by weight of said at least one iridium or rhodium metal based upon the weight of the support. 7. The catalyst composition as defined by claim 6, comprising from about 0.05 to 0.15% by weight of said at least one platinum or palladium metal, and from about 0.005 to 0.02% by weight of said at least one iridium or rhodium metal. 8. The catalyst composition as defined by claim 7, comprising from about 0.5 to 2% by weight of said iron. 9. The catalyst composition as defined by claim 6, said activated phase consisting essentially of cerium, iron, rhodium and at least one platinum or palladium metal. 10. The catalyst composition as defined by claim 6, said activated phase further comprising at least one metal selected from the group consisting of copper, nickel, manganese, tin, germanium, uranium and rhenium. 11. The catalyst composition as defined by claim 10, said further at least one metal being present in an amount by weight, based upon the weight of the support, of from 0.5 to 5%. 12. The catalyst composition as defined by claim 3, said alumina support having been prepared by autoclaving agglomerates of active alumina in a neutral or acid medium, and thence drying and calcining the product resulting therefrom. 13. The catalyst composition as defined by claim 3, said alumina support having been prepared by: (i) mixing an ultrafine boehmite or pseudoboehmite sol, the boehmite sol being free from amorphous alumina and the concentration by weight of the sol, expressed as Al 2 O 3, being between 10 and 25%, and at a pH below 7.5, with between 30 and 95% by weight total solids of spheroidal alumina particles essentially in the form of at least one of the phases selected from the group consisting of the gamma, delta and theta phases, said particles having a micropore volume of between 0.4 and 1 cm 3 /g and a specific surface area of between about 100 and 350 m 2 /g, and the diameters of the particles being between about 1 and 50 microns; (ii) spheroidally shaping and gelling into beads droplets of said resulting mixture; and (iii) drying and calcining said gelled beads at a temperature of between about 550° and 1,100° C. 14. The catalyst composition as defined by claim 13, the pH of mixing ranging from 4 to 7, said spheroidal alumina particles having a micropore volume ranging from 0.7 to 1 cm 3 /g and the diameters of said particles being such that at least 50% have a diameter φ and a mean value φ M such that φ=φ M ±20%φ M . 15. The catalyst composition as defined by claim 3, said alumina support having been treated with a pore-forming agent selected from the group consisting of cellulose, naphthalene, natural gum and synthetic polymer. 16. The catalyst composition as defined by claim 3, said alumina support having been heat-stabilized by means of a member selected from the group consisting of an alkaline earth metal, silica, a trivalent rare earth, and admixtures thereof. 17. The catalyst composition as defined by claims 1 or 3, comprised of 0.3 to 4.4% by weight cerium based upon the weight of said support. 18. A catalyst composition for the conversion of carbon monoxide, hydrocarbons, and nitrogen oxides comprising a refractory oxide support, and an activated phase deposited on said support consisting essentially of 0.3 to 7% by weight cerium based upon the weight of said support, 0.1 to 3.5% by weight iron, also based upon the weight of said support, at least one platinum or palladium metal, and at least one iridium metal. 19. The catalyst composition as defined by claim 1, wherein the ratio of the at least one platinum or palladium metal to the at least one iridium or rhodium metal is between about 7.5:1 and about 30:1. 20. The catalyst composition as defined by claim 1, wherein the ratio of the at least one platinum or palladium metal to the at least one iridium or rhodium metal is about 10:1.