초록 ▼

A selective catalytic reduction body for the removal of nitrogen oxides (NO.sub.x), comprising about 5 to 80% by weight of vanadium, about 0 to 60% by weight of molybdenum, about 0 to 20% by weight of nickel and about 0 to 20% by weight of cobalt, which catalytic body is economically favorable in pr

A selective catalytic reduction body for the removal of nitrogen oxides (NO.sub.x), comprising about 5 to 80% by weight of vanadium, about 0 to 60% by weight of molybdenum, about 0 to 20% by weight of nickel and about 0 to 20% by weight of cobalt, which catalytic body is economically favorable in production cost and superior in removing the nitrogen oxides from exhaust gas, can keep is activity high for a long time by virtue of excellent thermal resistance and poison resistance to sulfur oxides and other chemicals, exhausts un-reacted ammonia and heavy metal fly ash at the lowest amount, and allows the catalyst volume necessary to obtain the same removal degree and the pressure loss attributed to the volume to be minimized.

대표청구항 ▼

[ What is claimed is:] [2.] A selective catalytic reduction honeycomb for the removal of nitrogen oxides, which comprises about 5 to 40% by weight of vanadium, about 0.1 to 10% by weight of molybdenum, about 0.1 to 5% by weight of iron, about 0.1 to 5% by weight of nickel, about 20 to 50% by weight

[ What is claimed is:] [2.] A selective catalytic reduction honeycomb for the removal of nitrogen oxides, which comprises about 5 to 40% by weight of vanadium, about 0.1 to 10% by weight of molybdenum, about 0.1 to 5% by weight of iron, about 0.1 to 5% by weight of nickel, about 20 to 50% by weight of alumina, and about 0.1 to 2% by weight of cobalt, prepared from a spent catalyst composition from heavy oil upgrading facilities of an oil refinery after a hydro-desulfurization process. [3.] A method for removing nitrogen oxides out of exhaust gas containing oxygen and nitrogen oxides, wherein said exhaust gas is flowed through the selective catalytic reduction honeycomb of claim 2 at a temperature of 200 to 400.degree. C. in the presence of ammonia, to selectively reduce the nitrogen oxides into nitrogen and water.