SELECTIVE CATALYTIC REDUCTION CATALYST COMPOSITION, CATALYTIC ARTICLE COMPRISING THE SAME AND METHOD FOR PREPARING THE CATAYTIC ARTICLE
The present invention relates to a catalyst composition comprising a support, catalytically active species comprising a vanadium species, an antimony species and a tungsten species, and optionally, at least one further species selected from the group consisting of silicon species, aluminum species, zirconium species, titanium species, and cerium species; a catalytic article comprising the same, a method for preparing the catalytic article, and use of the catalyst composition or the catalytic article for selective catalytic reduction of nitrogen oxides in exhaust gases.
1 - 20 . (canceled)
21 . A catalyst composition comprising:
a support,
catalytically active species comprising a vanadium species, an antimony species, and a tungsten species, and
optionally, at least one further species is chosen from silicon species, aluminum species, zirconium species, titanium species, and cerium species.
22 . The catalyst composition according to claim 21 , wherein the vanadium species and the antimony species are in form of oxides of each, in form of a composite oxide comprising vanadium and antimony, or a combination thereof; the tungsten species is in form of an oxide thereof; and the at least one further species if present, is independently from each other, in form of SiO 2 , Al 2 O 3 , ZrO 2 , TiO 2 and CeO 2 .
23 . The catalyst composition according to claim 21 , wherein the support comprises titania, alumina, silica, zirconia, ceria, tungsten trioxide, zeolite, or any combination thereof.
24 . The catalyst composition according to claim 21 , wherein the vanadium species, calculated as V 2 O 5 , is present in the catalyst composition in an amount ranging from about 1% to about 10% by weight, relative to the total weight of the support, the catalytically active species, and the at least one further species, if present.
25 . The catalyst composition according to claim 21 , wherein the antimony species, calculated as Sb 2 O 3 , is present in the catalyst composition in an amount ranging from about 0.5% to about 20% by weight, relative to the total weight of the support, the catalytically active species, and the at least one further species, if present.
26 . The catalyst composition according to claim 21 , wherein the tungsten species, calculated as WO 3 , is present in the catalyst composition in an amount ranging from about 1% to about 20% by weight, relative to the total weight of the support, the catalytically active species, and the at least one further species, if present.
27 . The catalyst composition according to claim 21 , wherein the at least one further species if present, is independently from each in an amount from about 0.5% to about 20% by weight, calculated as respective oxides SiO 2 , Al 2 O 3 , ZrO 2 , TiO 2 and CeO 2 , relative to the total weight of the support, the catalytically active species, and the at least one further species.
28 . The catalyst composition according to claim 21 , wherein the at least one further species is a silicon species.
29 . The catalyst composition according to claim 28 , wherein the silicon species, calculated as SiO 2 , is in an amount ranging from about 0.5% to about 20% by weight, relative to the total weight of the support, the catalytically active species, and the at least one further species.
30 . The catalyst composition according to claim 21 , wherein the catalytically active species consists of a vanadium species, an antimony species, and a tungsten species, and SiO 2 .
31 . A catalytic article comprising a catalytic coating on a substrate, wherein the catalytic coating comprises a catalyst composition according to claim 21 .
32 . The catalytic article according to claim 31 , wherein the substrate is chosen from monolithic ceramic honeycomb substrate, metallic foils, and metallic corrugated sheet or metallic monolithic foam.
33 . A catalytic article in form of an extruded shape body, which comprises the catalyst composition according to claim 21 .
34 . A method for preparing the catalyst article according to claim 31 , wherein the method comprises:
1) preparing a slurry comprising particles of the support, a vanadium precursor, an antimony precursor, a tungsten precursor, and optionally one or more precursor of the at least one further species chosen from silicon species, aluminum species, zirconium species, titanium species, and cerium species; and
2) applying the slurry onto a substrate or processing the slurry into shape bodies.
35 . The method according to claim 34 , wherein the vanadium precursor is chosen from ammonium vanadate, vanadium oxalate, vanadyl oxalate, vanadium pentoxide, vanadium monoethanolamine, vanadium chloride, vanadium trichloride oxide, vanadyl sulfate, vanadium sulfate, vanadium antimonite, vanadium antimonate, and vanadium oxides.
36 . The method according to claim 34 , wherein the antimony precursor is chosen from antimony acetate, ethylene glycol antimony, antimony sulfate, antimony nitrate, antimony chloride, antimonous sulfide, antimony oxides such as Sb 2 O 3 , and antimony vanadate.
37 . The method according to claim 34 , wherein the tungsten precursor is chosen from tungsten alkoxides, tungsten halides, tungsten oxyhalides, tungstic acid, ammonium tungstate, ammonium paratungstate, and ammonium metatungstate.
38 . The method according to claim 34 , wherein the slurry prepared in step 1) comprises a silicon precursor, and the silicon precursor is chosen from silica sol, silicic acid, silicates, and alkoxysilanes.
39 . A method for selective catalytic reduction of nitrogen oxides present in a stream of exhaust gases by contacting the exhaust gases with the catalytic article according to claim 31 .