Catalytic process for removing sulfur dioxide from gas streams

Claim 2

A process for removing sulfur dioxide from a gas stream containing sulfur dioxide comprising passing a gas stream containing sulfur dioxide and a sufficient amount of carbon monoxide or hydrogen to reduce at least a portion of said sulfur dioxide to elemental sulfur through a reaction chamber charged with a material of the formula Ln 2 O 3 . Co 2 O 3 , where Ln is either Y or Gd, to catalytically produce at a sufficiently elevated temperature a product stream containing elemental sulfur and carbon dioxide or water, and thereafter removing said elemental sulfur from said product stream.

Claim 3

The process of claim 1 wherein the temperature in said reaction chamber is in the range of from about 450°C to about 700°C.

Claim 4

The process of claim 1 wherein said material is Y 2 O 3 . Co 2 O 3 .

Claim 5

The process of claim 1 wherein said material is Gd 2 O 3 . Co 2 O 3 .

Claim 6

The process of claim 1 wherein said process is characterized by a sulfur dioxide removal efficiency greater than about 90%.

Claim 7

The process of claim 1 wherein said process is characterized by a sulfur dioxide removal efficiency greater than about 90% even in the presence of oxygen in said reaction chamber.

Claim 8

The process of claim 1 wherein the production of said product stream proceeds even in the presence of oxygen in said reaction chamber.

Claim 9

The process of claim 1 wherein not greater than minimal amounts of hydrogen sulfide and carbonyl sulfide are produced during the catalytic production of said elemental sulfur.

Claim 10

The process of claim 1 wherein said carbon monoxide or hydrogen in said gas stream is in an amount not greater than the stoichiometric amount thereof required for reduction of all oxidants in said gas stream.

Claim 11

The process of claim 1 wherein said carbon monoxide or hydrogen in said gas stream is within ± 15% of the stoichiometric amount required for complete reduction of all oxidants in said gas stream.

Claim 12

The process of claim 1 wherein a portion of said carbon monoxide or hydrogen in said gas stream is generated in situ.

Claim 13

The process of claim 1 wherein a portion of said carbon monoxide or hydrogen in said gas stream is added thereto from an external source.

Claim 14

A process for removing sulfur dioxide from a gas stream containing sulfur dioxide comprising adding carbon monoxide or hydrogen to a gas stream containing sulfur dioxide and oxygen to thereby provide a gaseous reaction stream, the total amount of carbon monoxide or hydrogen in said gaseous reaction stream being approximately the stoichiometric amount required for reduction of all oxidants in said gaseous reaction stream, heating said gaseous reaction stream to a temperature in the range from about 450°C to about 700°C, passing said heated gaseous reaction stream through at least one reaction chamber charged with a material represented by the formula Ln 2 O 3 . Co 2 O 3 , where Ln is either Y or Gd, to catalytically produce a product stream comprising elemental sulfur, carbon dioxide or water, and not greater than minimal quantities of hydrogen sulfide and carbonyl sulfide, and thereafter remving said elemental sulfur from said product stream.

Claim 15

A process for removing sulfur dioxide from a gas stream containing sulfur dioxide comprising adding carbon monoxide or hydrogen to a gas stream containing sulfur dioxide and oxygen to thereby provide a gaseous reaction stream, the total amount of carbon monoxide or hydrogen in said gaseous reaction stream being approximately the stoichiometric amount required for reduction of all oxidants in said gaseous reaction stream, heating said gaseous reaction stream to a temperature in the range from about 450°C to about 700°C, passing said heated gaseous reaction stream through at least one reaction chamber charged with a material represented by the formula Ln 2 O 3 . Co 2 O 3 , where Ln is either Y or Gd, to catalytically produce a product stream comprising elemental sulfur, carbon dioxide or water, and not greater than minimal quantities of hydrogen sulfide and carbonyl sulfide, and thereafter remving said elemental sulfur from said product stream.

Claim 16

The process of claim 13 wherein said material is Y 2 O 3 . Co 2 O 3 .

Claim 17

The process of claim 13 wherein said material is Gd 2 O 3 . Co 2 O 3 .

Claim 18

The process of claim 13 wherein said gaseous reaction stream contains a minor concentration of oxygen, and the production of said elemental sulfur proceeds even in the presence of said oxygen in said gaseous reaction stream.

Claim 19

The process of claim 13 wherein said carbon monoxide or hydrogen in said gaseous reaction stream is within ± 15% of the stoichiometric amount required for complete reduction of all oxidants in said gaseous reaction stream.

Claim 20

The process of claim 1 wherein said material is supported on a magnesia carrier.

Claim 21

The process of claim 13 wherein said material is supported on a magnesia carrier.

Claim 22

The process of claim 1 wherein said material is supported on a zirconia carrier.

Claim 23

The process of claim 13 wherein said material is supported on a zirconia carrier.