Solid supported catalysts for catalytic reduction of nitrogen oxides in waste gases

Claim 2

In a method for the preparation of a catalyst for the reduction of nitrogen oxides in waste gases utilizing ammonium as the reducing agent; said catalyst comprising an alumina or silica-alumina type carrier supporting a compound or mixture of compounds selected from the group consisting of oxides, sulfates and phosphates of a first transition metal of the Periodic Table; which method comprises supporting at least one salt of a first transition metal of the periodic table on said carrier, drying at 100° C to 150° C and threafter calcining at 300° C to 600° C to form said compound or mixture of compounds; the improvement which comprises preparing the carrier by adding powdered alumina or powdered silica-alumina to an aqueous solution containing a reagent selected from the group consisting of aluminum sulfate, sulfuric acid, ammonium sulfate, and ammonium sulfite and thereafter kneading, molding and drying the mixture at 100° C to 150° C followed by calcination at 300° C to 600° C; thereby to produce a carrier containing from 0.03 to 20% by weight sulfur, based on the weight of the carrier when calculated as a sulfate or sulfite radical, and having a specific surface area of at least 50 m 2 /g and a pore volume of from 0.5 to 1.5 cc/g.

Claim 3

In a method for the preparation of a catalyst for the reduction of nitrogen oxides in waste gases utilizing ammonia as the reducing agent; said catalyst comprising an alumina or silica-alumina type carrier supporting a compound or mixture of compounds selected from the group consisting of oxides, sulfates and phosphates of a first transition metal of the Periodic Table; which method comprises supporting at least one salt of a first transition metal of the periodic table on said carrier, drying at 100° C to 150° C and thereafter calcining at 300° C to 600° C to form said compound or mixture of compounds; the improvement which comprises preparing said carrier by adding to an aqueous solution of sodium aluminate an aqueous solution of a compound selected from the group consisting of aluminum sulfate, sulfuric acid, ammonium sulfate, ammonium sulfite and mixtures thereof; thereby to form a hydrogel of alumina, and thereafter sequentially performing the steps of: 1. dehydrating and drying the hydrogel to form fine particles, 2. suspending the particles in water, filtering and washing, and 3. drying the washed particles at 100° C to 150° C and calcining at 300° C to 600° C; thereby to produce a carrier containing from 0.03 to 20% by weight sulfur, based on the weight of the carrier when calculated as a sulfate or sulfite radical, and having a specific surface area of at least 50 m 2 /g and a pore volume of from 0.5 to 1.5 cc/g.

Claim 4

In a method for the preparation of a catalyst for the reduction of nitrogen oxides in waste gases utilizing ammonia as the reducing agent; said catalyst comprising an alumina or silica-alumina type carrier supporting a compound or mixture of compounds selected from the group consisting of oxides, sulfates and phosphates of a first transition metal of the Periodic Table; which method comprises supporting at least one salt of a first transition metal of the periodic table on said carrier, drying at 100° C to 150° C and thereafter calcining at 300° C to 600° C to form said compound or mixture of compounds; the improvement which comprises preparing said carrier by adding to an aqueous solution of sodium aluminate an aqueous solution of a compound selected from the group consisting of aluminum sulfate, sulfuric acid, ammonium sulfate, ammonium sulfite and mixtures thereof; thereby to form a hydrogel of alumina, and thereafter sequentially performing the steps of: 1. dehydrating and drying the hydrogel to form fine particles, 2. suspending the particles in water, filtering and washing, and 3. drying the washed particles at 100° C to 150° C and calcining at 300° C to 600° C; thereby to produce a carrier containing from 0.03 to 20% by weight sulfur, based on the weight of the carrier when calculated as a sulfate or sulfite radical, and having a specific surface area of at least 50 m 2 /g and a pore volume of from 0.5 to 1.5 cc/g.

Claim 5

In a method for the preparation of a catalyst for the reduction of nitrogen oxides in waste gases utilizing ammonia as the reducing agent; said catalyst comprising an alumina or silica-alumina type carrier supporting a compound or mixture of compounds selected from the group consisting of oxides, sulfates and phosphates of a first transition metal of the Periodic Tables; which method comprises supporting at least one salt of a first transition metal of the periodic table on said carrier, drying at 100° C to 150° C and thereafter calcining at 300° C to 600° C to form said compound or mixture of compounds; the improvement which comprises preparing the carrier by impregnating it by soaking in an aqueous solution of a compound selected from the group consisting of aluminum sulfate, sulfuric acid, ammonium sulfate, ammonium sulfite and mixtures thereof, and thereafter drying the impregnated carrier and calcining it at from 300° C to 600° C; thereby to produce a carrier containing from 0.03 to 20% by weight sulfur, based on the weight of the carrier when calculated as a sulfate or sulfite radical, and having a specific surface area of at least 50 m 2 /g and a pore volume of from 0.5 to 1.5 cc/g.

Claim 6

In a method for the preparation of a catalyst for the reduction of nitrogen oxides in waste gases utilizing ammonia as the reducing agent; said catalyst comprising an alumina or silica-alumina type carrier supporting a compound or mixture of compounds selected from the group consisting of oxides, sulfates and phosphates of a first transition metal of the Periodic Tables; which method comprises supporting at least one salt of a first transition metal of the periodic table on said carrier, drying at 100° C to 150° C and thereafter calcining at 300° C to 600° C to form said compound or mixture of compounds; the improvement which comprises preparing the carrier by impregnating it by soaking in an aqueous solution of a compound selected from the group consisting of aluminum sulfate, sulfuric acid, ammonium sulfate, ammonium sulfite and mixtures thereof, and thereafter drying the impregnated carrier and calcining it at from 300° C to 600° C; thereby to produce a carrier containing from 0.03 to 20% by weight sulfur, based on the weight of the carrier when calculated as a sulfate or sulfite radical, and having a specific surface area of at least 50 m 2 /g and a pore volume of from 0.5 to 1.5 cc/g.

Claim 7

A method as in claim 1 wherein the carrier is prepared by the steps of: 1. adding sulfuric acid to an aqueous solution of sodium silicate to form a hydrogel of silica, 2. adding a reagent selected from the group consisting of an aqueous solution of aluminum sulfate and an aqueous solution of sodium aluminate together with an aqueous solution selected from the group consisting of sulfuric acid, ammonium sulfate, ammonium sulfite and mixtures thereof, 3. adding aqueous ammonia to form a hydrogel of silica-alumina, 4. dehydrating, drying to produce fine particles, suspending the particles in water, filtering and washing, 5. drying at 100° C to 150° C and calcining at from 300° to 600° C.

Claim 8

A method as in claim 1, wherein said salt of a first transition metal of the Periodic Table is selected from the group consisting of nitrates, carbonates, chlorides, sulfates, and phosphates.

Claim 9

A method as in claim 1, wherein said salt of a first transition metal of the Periodic Table is selected from the group consisting of formates, acetates and oxalates.

Claim 10

A method as in claim 1, wherein said salt of a first transition metal of the Periodic Table is selected from the group consisting of ammonium acetate complex salts and ammonium oxalate complex salts.

Claim 11

A product prepared by the method of claim 1.

Claim 12

A product prepared by the method of claim 2.

Claim 13

A product prepared by the method of claim 3.

Claim 14

A product prepared by the method of claim 4.

Claim 15

A product prepared by the method of claim 5.

Claim 16

A product prepared by the method of claim 6.

Claim 17

A product prepared by the method of claim 7.