Process for treating a waste gas containing sulfur oxides

Claim 2

A process for treating a gas containing sulfur oxides comprising the steps of contacting the gas with an adsorbent catalyst to remove the sulfur oxides by adsorbing the sulfur oxides on the adsorbent catalyst and then desorbing the sulfur oxides from the adsorbent catalyst, wherein the adsorbent catalyst consists essentially of at least 50 atomic percent of titanium oxide, from 2 to 50 atomic percent of at least one of iron oxide and copper oxide and up to 10 atomic percent of oxides of molybdenum, tungsten, vanadium, cobalt and nickel, said adsorbent catalyst being free of aluminum oxide, said adsorbent catalyst being prepared by molding a coprecipitate of titanium hydroxide and at least one of iron hydroxide and copper hydroxide and calcining the moldings at a temperature below 600° C. under an oxidizing atmosphere.

Claim 3

A process for treating a gas containing sulfur oxides according to claim 1, wherein the adsorbent catalyst has a specific surface area of at least 30 m 2 /g.

Claim 4

A process for treating a gas containing sulfur oxides which comprises contacting a gas containing sulfur oxides and oxygen with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g consisting essentially of at least 50 atomic percent of titanium oxide, from 2 to 50 atomic percent of at least one of iron oxide and copper oxide and up to 10 atomic percent of oxides of molybdenum, tungsten, vanadium, cobalt and nickel, said adsorbent catalyst being free of aluminum oxide, said adsorbent catalyst being prepared by molding a coprecipitate of titanium hydroxide and at least one of iron hydroxide and copper hydroxide and calcining the moldings at a temperature below 600° C. under an oxidizing atmosphere, at a temperature in the range of 250°-500° C. to adsorb sulfur oxides and then contacting the adsorbent catalyst with a reducing gas to desorb the adsorbed sulfur oxides.

Claim 5

A process for treating a gas containing sulfur oxides which comprises contacting a gas containing sulfur oxides and oxygen with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g consisting essentially of at least 50 atomic percent of titanium oxide, from 2 to 50 atomic percent of at least one of iron oxide and copper oxide and up to 10 atomic percent of oxides of molybdenum, tungsten, vanadium, cobalt and nickel, said adsorbent catalyst being free of aluminum oxide, said adsorbent catalyst being prepared by molding a coprecipitate of titanium hydroxide and at least one of iron hydroxide and copper hydroxide and calcining the moldings at a temperature below 600° C. under an oxidizing atmosphere, at a temperature in the range of 250°-500° C. to adsorb sulfur oxides and then contacting the adsorbent catalyst with a reducing gas to desorb the adsorbed sulfur oxides.

Claim 6

A process for treating a gas containing sulfur oxides, nitrogen oxides and oxygen, which comprises the steps of adding ammonia to the gas, contacting the gas with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g consisting essentially of at least 50 atomic percent of titanium oxide, from 2 to 50 atomic percent of at least one of iron oxide and copper oxide and up to 10 atomic percent of oxides of molybdenum, tungsten, vanadium, cobalt and nickel, said adsorbent catalyst being free of aluminum oxide, said adsorbent catalyst being prepared by molding a coprecipitate of titanium hydroxide and at least one of iron hydroxide and copper hydroxide and calcining the moldings at a temperature below 600° C. under an oxidizing atmosphere, at a temperature in the range of 250°-500° C. at a space velocity of 200-20,000 hr -1 to adsorb the sulfur oxides in the gas on the adsorbent catalyst and to reduce the nitrogen oxides into nitrogen and water with ammonia, contacting the adsorbent catalyst carrying the sulfur oxides adsorbed thereon with at least one reducing gas selected from the group consisting of hydrogen, carbon monoxide and methane to regenerate the adsorbent catalyst, and recovering sulfur from the sulfur-containing gas from the regeneration step.

Claim 7

A process for treating a gas containing sulfur oxides, nitrogen oxides and oxygen, which comprises the steps of adding ammonia to the gas, contacting the gas with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g consisting essentially of at least 50 atomic percent of titanium oxide, from 2 to 50 atomic percent of at least one of iron oxide and copper oxide and up to 10 atomic percent of oxides of molybdenum, tungsten, vanadium, cobalt and nickel, said adsorbent catalyst being free of aluminum oxide, said adsorbent catalyst being prepared by molding a coprecipitate of titanium hydroxide and at least one of iron hydroxide and copper hydroxide and calcining the moldings at a temperature below 600° C. under an oxidizing atmosphere, at a temperature in the range of 250°-500° C. at a space velocity of 200-20,000 hr -1 to adsorb the sulfur oxides in the gas on the adsorbent catalyst and to reduce the nitrogen oxides into nitrogen and water with ammonia, contacting the adsorbent catalyst carrying the sulfur oxides adsorbed thereon with at least one reducing gas selected from the group consisting of hydrogen, carbon monoxide and methane to regenerate the adsorbent catalyst, and recovering sulfur from the sulfur-containing gas from the regeneration step.

Claim 8

A process according to claim 4, wherein the adsorbent catalyst is a homogeneous mixture of titanium oxide and iron oxide and/or copper oxide and the adsorbent catalyst contains titanium and iron and/or copper in an atomic ratio of titanium: iron and/or copper of 98:2-50:50.

Claim 9

A process for treating a gas containing sulfur oxides, which comprises the steps of contacting a gas containing sulfur oxides and oxygen with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g that consists essentially of titanium and iron and/or copper in an atomic ratio of titanium:iron and/or copper of 98:2-50:50, said adsorbent catalyst being free of aluminum oxide, which adsorbent catalyst has been prepared by molding a coprecipitate of the titanium and iron and/or copper constituents of said adsorbent catalyst and calcining the moldings at a temperature below 600° C., the contact being effected at a temperature in the range of 250°-500° C.; contacting the adsorbent catalyst carrying the sulfur oxides adsorbed thereon with a reducing gas to desorb the sulfur oxides from the adsorbent catalyst and recovering sulfur from the sulfur-containing desorbed gas from the desorption step.

Claim 10

A process for treating a gas containing sulfur oxides, which comprises the steps of contacting a gas containing sulfur oxides and oxygen with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g that consists essentially of titanium and iron and/or copper in an atomic ratio of titanium:iron and/or copper of 98:2-50:50, said adsorbent catalyst being free of aluminum oxide, which adsorbent catalyst has been prepared by molding a coprecipitate of the titanium and iron and/or copper constituents of said adsorbent catalyst and calcining the moldings at a temperature below 600° C., the contact being effected at a temperature in the range of 250°-500° C.; contacting the adsorbent catalyst carrying the sulfur oxides adsorbed thereon with a reducing gas to desorb the sulfur oxides from the adsorbent catalyst and recovering sulfur from the sulfur-containing desorbed gas from the desorption step.

Claim 11

A process according to claim 6, wherein in the sulfur-recovery step, at least a part of sulfur dioxide contained in the desorption gas is reduced into hydrogen sulfide and the hydrogen sulfide thus formed is reacted with sulfur dioxide in the presence of a catalyst to recover elemental sulfur.

Claim 12

A process according to claim 1, wherein the adsorbent catalyst has a specific surface area of at least 50 m 2 /g.

Claim 13

A process according to claim 3, wherein the adsorbent catalyst has a specific surface area of at least 50 m 2 /g.

Claim 14

A process according to claim 1, wherein the adsorbent catalyst consists of titanium oxide and at least one of iron oxide and copper oxide.

Claim 15

A process according to claim 3, wherein the adsorbent catalyst consists of titanium oxide and at least one of iron oxide and copper oxide.

Claim 16

A process according to claim 1, wherein the adsorbent catalyst consists of titanium oxide and iron oxide.

Claim 17

A process according to claim 1, wherein the adsorbent catalyst consists of titanium oxide and copper oxide.

Claim 18

A process according to claim 1, wherein the adsorbent catalyst is contacted with the gas containing sulfur oxides at a temperature range of from 250°-500° C. and at a space velocity of 200-20,000 hr -1 .

Claim 19

A process according to claim 4, wherein 0.7-3.0 moles of ammonia are added to the gas containing sulfur oxides, nitrogen oxides and oxygen per mole of nitrogen oxides in the gas.

Claim 20

A process for treating a gas containing sulfur oxides which comprises contacting a gas containing sulfur oxides and oxygen with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g consisting essentially of at least 50 atomic percent of titanium oxide, from 2 to 50 atomic percent of at least one of iron oxide and copper oxide and up to 10 atomic percent of oxides of molybdenum, tungsten, vanadium, cobalt and nickel, said adsorbent catalyst being free of aluminum oxide, said adsorbent catalyst being prepared by molding a coprecipitate of titanium hydroxide and iron hydroxide and calcining the moldings at a temperature below 600° C. under an oxidizing atmosphere, said contacting a gas containing sulfur oxides and oxygen occurring at a temperature in the range of 250°-500° C. to adsorb sulfur oxides, and then contacting the adsorbent catalyst with a reducing gas to desorb the adsorbed sulfur oxides.

Claim 21

A process for treating a gas containing sulfur oxides which comprises contacting a gas containing sulfur oxides and oxygen with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g consisting essentially of at least 50 atomic percent of titanium oxide, from 2 to 50 atomic percent of at least one of iron oxide and copper oxide and up to 10 atomic percent of oxides of molybdenum, tungsten, vanadium, cobalt and nickel, said adsorbent catalyst being free of aluminum oxide, said adsorbent catalyst being prepared by molding a coprecipitate of titanium hydroxide and iron hydroxide and calcining the moldings at a temperature below 600° C. under an oxidizing atmosphere, said contacting a gas containing sulfur oxides and oxygen occurring at a temperature in the range of 250°-500° C. to adsorb sulfur oxides, and then contacting the adsorbent catalyst with a reducing gas to desorb the adsorbed sulfur oxides.

Claim 22

A process for treating a gas containing sulfur oxides which comprises contacting a gas containing sulfur oxides and oxygen with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g consisting essentially of at least 50 atomic percent of titanium oxide, from 2 to 50 atomic percent of at least one of iron oxide and copper oxide and up to 10 atomic percent of oxides of molybdenum, tungsten, vanadium, cobalt and nickel, said adsorbent catalyst being free of aluminum oxide, said adsorbent catalyst being prepared by molding a coprecipitate of titanium hydroxide and iron hydroxide and calcining the moldings at a temperature below 600° C. under an oxidizing atmosphere, wherein the adsorbent catalyst contains titanium and iron in an atomic ratio of titanium:iron of 98:2-50:50, said contacting gas containing sulfur oxides and oxygen occurring at a temperature in the range of 250°-500° C. to adsorb sulfur oxides, and then contacting the adsorbent catalyst with a reducing gas to desorb the adsorbed sulfur oxides.

Claim 23

A process for treating a gas containing sulfur oxides which comprises contacting a gas containing sulfur oxides and oxygen with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g consisting essentially of at least 50 atomic percent of titanium oxide, from 2 to 50 atomic percent of at least one of iron oxide and copper oxide and up to 10 atomic percent of oxides of molybdenum, tungsten, vanadium, cobalt and nickel, said adsorbent catalyst being free of aluminum oxide, said adsorbent catalyst being prepared by molding a coprecipitate of titanium hydroxide and iron hydroxide and calcining the moldings at a temperature below 600° C. under an oxidizing atmosphere, wherein the adsorbent catalyst contains titanium and iron in an atomic ratio of titanium:iron of 98:2-50:50, said contacting gas containing sulfur oxides and oxygen occurring at a temperature in the range of 250°-500° C. to adsorb sulfur oxides, and then contacting the adsorbent catalyst with a reducing gas to desorb the adsorbed sulfur oxides.

Claim 24

A process for treating a gas containing sulfur oxides which comprises contacting a gas containing sulfur oxides and oxygen with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g consisting essentially of at least 50 atomic percent of titanium oxide, from 2 to 50 atomic percent of at least one of iron oxide and copper oxide and up to 10 atomic percent of oxides of molybdenum, tungsten, vanadium, cobalt and nickel, said adsorbent catalyst being free of aluminum oxide, said adsorbent catalyst being prepared by molding a coprecipitate of titanium hydroxide and copper hydroxide and calcining the moldings at a temperature below 600° C. under an oxidizing atmosphere, with the adsorbent catalyst containing titanium and copper in an atomic ratio of titanium:copper of 98:2-50:50, said contacting gas containing sulfur oxides and oxygemn occurring at a temperature in the range of 250°-500° C. to adsorb sulfur oxides, and then contacting the adsorbent catalyst with a reducing gas to desorb the adsorbed sulfur oxides.

Claim 25

A process for treating a gas containing sulfur oxides which comprises contacting a gas containing sulfur oxides and oxygen with an adsorbent catalyst of a specific surface area of at least 30 m 2 /g consisting essentially of at least 50 atomic percent of titanium oxide, from 2 to 50 atomic percent of at least one of iron oxide and copper oxide and up to 10 atomic percent of oxides of molybdenum, tungsten, vanadium, cobalt and nickel, said adsorbent catalyst being free of aluminum oxide, said adsorbent catalyst being prepared by molding a coprecipitate of titanium hydroxide and copper hydroxide and calcining the moldings at a temperature below 600° C. under an oxidizing atmosphere, with the adsorbent catalyst containing titanium and copper in an atomic ratio of titanium:copper of 98:2-50:50, said contacting gas containing sulfur oxides and oxygemn occurring at a temperature in the range of 250°-500° C. to adsorb sulfur oxides, and then contacting the adsorbent catalyst with a reducing gas to desorb the adsorbed sulfur oxides.