초록 ▼

Compositions comprising a component containing (i) an acidic oxide support, (ii) an alkali metal and/or alkaline earth metal or mixtures thereof, (iii) a transition metal oxide having oxygen storage capability, and (iv) a transition metal selected from Groups Ib and/or IIb of the Periodic Table prov

Compositions comprising a component containing (i) an acidic oxide support, (ii) an alkali metal and/or alkaline earth metal or mixtures thereof, (iii) a transition metal oxide having oxygen storage capability, and (iv) a transition metal selected from Groups Ib and/or IIb of the Periodic Table provide NO.sub.x control performance in FCC processes. The acidic oxide support preferably contains silica alumina. Ceria is the preferred oxygen storage oxide. Cu and Ag are preferred Group I/IIb transition metals. The compositions are especially useful in the cracking of hydrocarbon feedstocks having above average nitrogen content.

대표청구항 ▼

[ What is claimed is:] [1.] A NO.sub.x removal composition suitable for reducing NO.sub.x emissions during catalyst regeneration in a fluid catalytic cracking process, said composition comprising particles having a particle size of about 20-200 .mu.m and consisting essentially of (i) an acidic oxide

[ What is claimed is:] [1.] A NO.sub.x removal composition suitable for reducing NO.sub.x emissions during catalyst regeneration in a fluid catalytic cracking process, said composition comprising particles having a particle size of about 20-200 .mu.m and consisting essentially of (i) an acidic oxide support containing at least 50 wt. % alumina, (ii) about 1-10 parts by weight, measured as alkali metal oxide, of at least one alkali metal, (iii) at least 1 part by weight of CeO.sub.2 and (iv) about 0.01-5.0 parts by weight, measured as metal oxide, of a transition metal selected from Group Ib of the Periodic Table, all of said parts by weight being per 100 parts by weight of said acidic oxide support material. [9.] A fluid cracking catalyst comprising (a) a cracking component suitable for catalyzing the cracking of hydrocarbons, and (b) a NO.sub.x reduction component consisting essentially of (i) an acidic oxide support containing at least 50 wt % alumina, (ii) about 1-10 parts by weight, measured as alkali metal oxide, of at least one alkali metal; (iii) at least 1 part by weight of a CeO.sub.2, and (iv) 0.01-5.0 parts by weight total, measured as metal oxide, of a transition metal selected from Group Ib of the Periodic Table, all of said parts by weight being per 100 parts by weight of said acidic oxide support material, said NO.sub.x reduction components comprising particles having a particle size of 20-200 .mu.m and being present in the cracking catalyst in a sufficient NO.sub.x reducing amount. The cracking catalyst of claim 9 wherein said cracking catalyst comprises an admixture of component (a) and component (b). The cracking catalyst of claim 9 wherein said catalyst comprises integral particles which contain both components (a) and (b). The cracking catalyst of claim 9 wherein the NO.sub.x reduction component (b) comprises about 0.1 to 15 wt % of the cracking catalyst. [13.] A method of reducing NO.sub.x emission during fluid cracking of a hydrocarbon feedstock into lower molecular weight components, said method comprising contacting a hydrocarbon feedstock with a cracking catalyst at elevated temperature whereby lower molecular weight hydrocarbon components are formed, said cracking catalyst comprising (a) a cracking component suitable for catalyzing the cracking of hydrocarbons, and (b) a NO.sub.x reduction component consisting essentially of (i) an acidic oxide support containing at least 50 wt. % alumina, (ii) about 1-10 parts by weight, measured as alkali metal oxide, of at least one alkali metal; (iii) at least 1 part by weight of a CeO.sub.2, and (iv) 0.01-5.0 parts by weight total, measured as metal oxide, of a transition metal selected from Group Ib of the Periodic Table, all of said parts by weight being per 100 parts by weight of said acidic oxide support material, said NO.sub.x reduction components comprising particles having a particle size of 20-200 .mu.m and being present in the cracking catalyst in a sufficient NO.sub.x reducing amount. The method of claim 13 wherein said cracking catalyst is fluidized during contacting said hydrocarbon feedstock. The method of claim 14 further comprising recovering used cracking catalyst from said contacting step and treating said used catalyst under conditions to regenerate said catalyst. The method of claim 13 wherein said hydrocarbon feedstock contains at least 0.1 wt % nitrogen.