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Patent

Low temperature catalytic reduction of nitrogen oxides

TL;DR: In this article, the authors present commercially viable processes of the SCR type for converting nitrogen oxides to nitrogen with ammonia: (a) in the presence of an iron, cobalt, nickel, or other transition metal sulfate with Bronsted activity; (b) at a temperature of not more than 250°C; and (c) in a dry environment if room or near room temperatures are employed.
Abstract: Commercially viable processes of the SCR type for converting nitrogen oxides to nitrogen with ammonia: (a) in the presence of an iron, cobalt, nickel, or other transition metal sulfate with Bronsted activity; (b) at a temperature of not more than 250° C.; and (c) preferably in a dry environment if room or near room temperatures are employed. The process may be used to eliminate nitrogen oxides from flue gases, other exhaust gases, and the like and in other applications in which the reduction of a nitrogen oxide is wanted. Excess ammonia and/or sulfur dioxide may be maintained in the reaction mixture to promote process efficiency. The catalysts have appreciable Bronsted activity even at ambient temperatures and are capable of effecting NO x conversions with efficiencies of at least 50 percent in even demanding applications at temperatures below the 250° C. maximum. They can be unsupported or supported on a porous support. If of the latter type, the catalyst can be prepared by impregnating the support with an aqueous solution of a selected transition metal salt and then drying the impregnated support. Also, if the salt is not a sulfate, the salt is calcined and the resulting oxide reacted with a compound such as sulfur dioxide to generate the sulfate.
References
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Patent
07 Jan 1983
TL;DR: A denitration catalyst comprising at least three metal components, (A) titanium, (B) tungsten and/or magnesium, and (C) vanadium, was proposed in this paper.
Abstract: A denitration catalyst comprising at least three metal components, (A) titanium, (B) tungsten and/or magnesium, and (C) vanadium, the titanium and tungsten being contained as oxides and the magnesium and vanadium being contained in the form of an oxide or a sulfate or both, said catalyst being composed of a porous molded article of a mixture of an oxide of component A and an oxide and/or a sulfate of component B, the atomic ratio of component B to component A being from 0.01 to 1, and a vanadium compound localized in that area of said molded article which extends from its outermost surface to a depth of 500 microns or less, the content of the vanadium compound in said area being 0.1 to 15% by weight; and a method for removing nitrogen oxides from a waste gas, which comprises contacting a waste gas containing nitrogen oxides, together with ammonia and molecular oxygen, at a temperature of 150° to 650° C., with the aforesaid catalyst.

48 citations

Patent
18 Oct 1974
TL;DR: In this article, a method for treating ammonia-containing gases for removing ammonia therefrom, which comprises contacting the ammoniacontaining gases with a metal oxide catalyst having the following formula: Cr.x A.sub.y O.subz wherein Cr is chromium; A is at least one element selected from the group consisting of tin, antimony, vanadium, cobalt, silver, zinc, nickel, titanium, molybdenum, tungsten, sulfur, phosphorus, boron, germanium and zirconium; x is a numeral of
Abstract: A method for treating ammonia-containing gases for removing ammonia therefrom, which comprises contacting the ammonia-containing gases with a metal oxide catalyst having the following formula: Cr.sub.x A.sub.y O.sub.z wherein Cr is chromium; A is at least one element selected from the group consisting of tin, antimony, vanadium, cobalt, silver, zinc, nickel, titanium, molybdenum, tungsten, sulfur, phosphorus, boron, germanium and zirconium; x is a numeral of 4 to 12; y is a numeral of 0.2 to 8 and z is a numeral of 6.2 to 42, in a vapor phase at a temperature of from 200° to 500° C in the presence of molecular oxygen, and thereby the ammonia is oxidized to harmless nitrogen gas.

34 citations

Patent
12 Feb 1976
TL;DR: In this article, base metal catalysts are pretreated with selenium, sulfur or sulfur compounds and a gaseous stream comprising nitric oxide, oxygen and ammonia is passed over the pretreated catalysts.
Abstract: Base metal catalysts are pretreated with selenium, sulfur or sulfur compounds. Subsequently, a gaseous stream comprising nitric oxide, oxygen and ammonia is passed over the pretreated catalysts. The nitric oxide is reduced to nitrogen and no nitrous oxide is formed.

17 citations

Patent
13 Jun 1986
TL;DR: An SCR catalyst consisting of iron sulfate or oxysulfur iron compound carried by a mixture of ceria and alumina on a support is a SCR as mentioned in this paper.
Abstract: An SCR catalyst consisting essentially of iron sulfate or oxysulfur iron compound carried by a mixture of ceria and alumina on a support.

13 citations

Patent
24 Dec 1975
TL;DR: Solid supported catalysts for catalytic reduction of nitrogen oxide in waste gases utilizing ammonia as the reducing agent are defined in this article, where the first transition metal supported on an alumina or silica-alumina carrier is defined.
Abstract: Solid supported catalysts for catalytic reduction of nitrogen oxide in waste gases utilizing ammonia as the reducing agent, the catalyst comprising at least one metallic oxide, sulfate or phosphate of a first transition metal supported on an alumina or silica-alumina carrier; the carrier containing from 0.03 to 20% by weight sulfur, based on the weight of the carrier, calculated as a sulfate or sulfite radical.

9 citations