Sulfur dioxide removal process

Claim 2

In a process for the removal of sulfur dioxide from gas in which sulfur dioxide is absorbed from the gas into an aqueous absorption solution of sodium sulfite to form the corresponding bisulfite, the resulting bisulfite-containing absorption solution is desorbed to form sulfur dioxide, a sulfite-containing absorption solution is regenerated for recycling, and in which sodium sulfate is in the absorption-desorption medium, the improvement for reducing the amount of sodium sulfate in the system comprising chemically-reducing an aqueous solution or slurry containing a major amount of sodium sulfate on a dry basis, separated as a purge from said absorption-desorption system by contacting said aqueous solution or slurry with a reducing atmosphere under reducing conditions at an elevated temperature, quenching the resulting mixture and obtaining an aqueous liquid product which contains a major amount of the total sodium content as carbonate and bicarbonate and a minor amount as bisulfide on a dry basis, carbonating said aqueous liquid product to increase substantially the amount of sodium bicarbonate therein, decreasing the amount of sodium bisulfide in said carbonated liquid product by a major amount, and passing resulting liquid product to said sulfur dioxide absorption-desorption system.

Claim 3

A process of claim 1 in which said chemical reduction is conducted at a temperature of about 800° to 1050° C.

Claim 4

A process of claim 6 in which said quenching comprises passing products of said combustion into a quench liquid comprising material previously prepared by said chemical reduction.

Claim 5

The process of claim 1 in which the weight ratio of sodium sulfate to the total amount of other sodium compounds in said aqueous medium which is chemically-reduced is at least about 2.5:1.

Claim 6

A process of claim 1 in which aqueous liquid containing a minor amount of sodium thiosulfate is withdrawn from the desorption zone of said sulfur dioxide absorption-desorption system and also charged to said chemical reduction.

Claim 7

The process of claim 1 in which said decrease in the amount of sodium bisulfide is accomplished during evaporation of water from said carbonated aqueous liquid product.

Claim 8

The process of claim 6 in which the amount of water evaporated is sufficient to increase the total salt content of the material undergoing treatment by at least about 25 weight percent.

Claim 9

In a process for the removal of sulfur dioxide from gas in which sulfur dioxide is absorbed from the gas into an aqueous absorption solution of sodium sulfite to form the corresponding bisulfite, the resulting bisulfite-containing absorption solution is desorbed to form sulfur dioxide, a sulfite-containing absorption solution is regenerated for recycling, and in which sodium sulfate is in the absorption-desorption medium, the improvement for reducing the amount of sodium sulfate in the system comprising separating a material containing a major amount of sodium sulfate on a dry basis from spent absorption medium having a major amount of sodium bisulfite on a dry basis, chemically-reducing an aqueous solution or slurry containing said sodium sulfate separated from said spent absorption-desorption medium, by burning a fluid fuel with less than the stoichiometric amount of oxygen for complete combustion of said fuel, to obtain a reducing atmosphere and contacting said aqueous solution or slurry with said reducing atmosphere under reducing conditions at an elevated temperature, quenching the resulting mixture and obtaining an aqueous liquid product which contains a major amount of the total sodium content as carbonate and bicarbonate and a minor amount of sodium bisulfide on a dry basis, carbonating said quenched aqueous liquid product to increase substantially the amount of sodium bicarbonate therein, decreasing the amount of sodium bisulfide in said carbonated liquid product by a major amount, and passing resulting liquid product to said sulfur dioxide absorption-desorption system.

Claim 10

In a process for the removal of sulfur dioxide from gas in which sulfur dioxide is absorbed from the gas into an aqueous absorption solution of sodium sulfite to form the corresponding bisulfite, the resulting bisulfite-containing absorption solution is desorbed to form sulfur dioxide, a sulfite-containing absorption solution is regenerated for recycling, and in which sodium sulfate is in the absorption-desorption medium, the improvement for reducing the amount of sodium sulfate in the system comprising separating a material containing a major amount of sodium sulfate on a dry basis from spent absorption medium having a major amount of sodium bisulfite on a dry basis, chemically-reducing an aqueous solution or slurry containing said sodium sulfate separated from said spent absorption-desorption medium, by burning a fluid fuel with less than the stoichiometric amount of oxygen for complete combustion of said fuel, to obtain a reducing atmosphere and contacting said aqueous solution or slurry with said reducing atmosphere under reducing conditions at an elevated temperature, quenching the resulting mixture and obtaining an aqueous liquid product which contains a major amount of the total sodium content as carbonate and bicarbonate and a minor amount of sodium bisulfide on a dry basis, carbonating said quenched aqueous liquid product to increase substantially the amount of sodium bicarbonate therein, decreasing the amount of sodium bisulfide in said carbonated liquid product by a major amount, and passing resulting liquid product to said sulfur dioxide absorption-desorption system.

Claim 11

The process of claim 8 in which said decrease in the amount of sodium bisulfide is accomplished during evaporation of water from said carbonated aqueous liquid product.

Claim 12

The process of claim 9 in which the weight ratio of sodium sulfate to the total amount of other sodium compounds in said aqueous medium which is chemically-reduced is at least about 2.5:1.

Claim 13

The process of claim 10 in which aqueous material subjected to carbonation consists essentially of about 10 to 35 weight percent of total sodium salts.

Claim 14

A process of claim 8 in which said chemical reduction is conducted at a temperature of about 800° to 1050° C.

Claim 15

A process of claim 12 in which said quenching comprises passing products of said combustion into a quench liquid of material previously prepared by said chemical reduction.

Claim 16

A process of claim 9 in which gas produced during said evaporation of water is oxidized to form sulfur dioxide from hydrogen sulfide therein, and resulting sulfur dioxide containing gas is passed to the absorption zone of said sulfur dioxide absorption-desorption system.

Claim 17

A process of claim 14 in which gas from said carbonation is also charged to said oxidation in which sulfur dioxide is formed.

Claim 18

A process of claim 15 in which gas from said quenching is also charged to said oxidation in which sulfur dioxide is formed.

Claim 19

A process of claim 9 in which said aqueous liquid containing a minor amount of sodium thiosulfate is withdrawn from the desorption zone of said sulfur dioxide absorption-desorption system and also charged to said chemical reduction.

Claim 20

The process of claim 12 in which said quenched aqueous liquid product contains a greater weight amount of sodium carbonate than sodium bicarbonate, and said quenched aqueous liquid product is carbonated to increase the weight ratio of sodium bicarbonate to sodium carbonate to at least about 1.5:1.

Claim 21

A process of claim 18 in which aqueous liquid containing a minor amount of sodium thiosulfate is withdrawn from the desorption zone of said sulfur dioxide absorption-desorption system and also charged to said chemical reduction.

Claim 22

The process of claim 18 in which said decrease in sodium bisulfide content of said carbonated liquid occurs while evaporating water therefrom.

Claim 23

The process of claim 20 in which the amount of water evaporated is sufficient to increase the total salt content of the material undergoing treatment by at least about 25 weight percent.

Claim 24

In a process for the removal of sulfur dioxide from gas in which sulfur dioxide is absorbed from the gas into an aqueous absorption solution of sodium sulfite to form the corresponding bisulfite, the resulting bisulfite-containing absorption solution is desorbed to form sulfur dioxide, a sulfite-containing absorption solution is regenerated for recycling, and in which sodium sulfate is in the absorption-desorption medium, the improvement for reducing the amount of sodium sulfate in the system comprising separating a material containing a major amount of sodium sulfate on a dry basis from spent absorption medium having a major amount of sodium bisulfite on a dry basis, chemically-reducing an aqueous solution or slurry containing said sodium sulfate separated from said spent absorption-desorption medium by burning a fluid fuel with less than the stoichiometric amount of oxygen for complete combustion of said fuel, at a temperature of about 800° to 1050° C. to obtain a reducing atmosphere and contacting said aqueous solution or slurry with said reducing atmosphere under reducing conditions at an elevated temperature, quenching the resulting mixture by contact with previously prepared product of said chemical reduction at a temperature of about 60° to 115° C., and carbonating said quenched aqueous liquid product at a temperature of about 30° to 100° C. to form a product in which the weight ratio of sodium bicarbonate to sodium carbonate is at least about 1.5:1, evaporating water from the carbonated product at a temperature of about 60° to 110° C. to increase the salt content of the carbonated product by at least about 25%, and passing resulting liquid product to said sulfur dioxide absorption-desorption system.

Claim 25

In a process for the removal of sulfur dioxide from gas in which sulfur dioxide is absorbed from the gas into an aqueous absorption solution of sodium sulfite to form the corresponding bisulfite, the resulting bisulfite-containing absorption solution is desorbed to form sulfur dioxide, a sulfite-containing absorption solution is regenerated for recycling, and in which sodium sulfate is in the absorption-desorption medium, the improvement for reducing the amount of sodium sulfate in the system comprising separating a material containing a major amount of sodium sulfate on a dry basis from spent absorption medium having a major amount of sodium bisulfite on a dry basis, chemically-reducing an aqueous solution or slurry containing said sodium sulfate separated from said spent absorption-desorption medium by burning a fluid fuel with less than the stoichiometric amount of oxygen for complete combustion of said fuel, at a temperature of about 800° to 1050° C. to obtain a reducing atmosphere and contacting said aqueous solution or slurry with said reducing atmosphere under reducing conditions at an elevated temperature, quenching the resulting mixture by contact with previously prepared product of said chemical reduction at a temperature of about 60° to 115° C., and carbonating said quenched aqueous liquid product at a temperature of about 30° to 100° C. to form a product in which the weight ratio of sodium bicarbonate to sodium carbonate is at least about 1.5:1, evaporating water from the carbonated product at a temperature of about 60° to 110° C. to increase the salt content of the carbonated product by at least about 25%, and passing resulting liquid product to said sulfur dioxide absorption-desorption system.