Flue gas desulfurization with oxidation of calcium sulfite in FGD discharges

Claim 2

In a method of flue gas desulfurization wherein a flue gas, containing sulfur dioxide, is contacted in a liquid scrubber unit with an aqueous slurry formed from calcium hydroxide and magnesium hydroxide, and which contains magnesium hydroxide in an amount to provide an effective magnesium ion content of between 2500 to 9000 parts per million in the liquid scrubber unit, and at least a portion of the slurry, after passage through the scrubber, containing undissolved calcium sulfite is recirculated through a thickener to produce an aqueous sludge containing calcium sulfite, the improvement wherein the calcium sulfite present in the aqueous sludge is oxidized by: separating undissolved calcium sulfite, in a sludge which contains at least about 20 weight percent solids, from the scrubbing slurry; contacting said sludge with sulfuric acid to cause dissolution of calcium sulfite in an aqueous solution; oxidizing the dissolved calcium sulfite in the aqueous solution with an oxygen-containing gas to form a calcium sulfate precipitate in an aqueous media; separating the calcium sulfate precipitate from the aqueous media; and returning aqueous media, separated from the calcium sulfate precipitate, for contact with additional sludge produced in the thickener.

Claim 3

The method of claim 1 wherein dissolution of calcium sulfite is caused by sulfuric acid in an aqueous solution having a pH of at least about 4.0.

Claim 4

A method of claim 2 wherein dissolution of calcium sulfite is caused by sulfuric acid in an aqueous solution having a pH of between about 4 to 6.5.

Claim 5

The method of claim 3 wherein dissolution of calcium sulfite is caused by sulfuric acid in an aqueous solution having a pH of between 5.2 to 5.5.

Claim 6

The method of claim 3 wherein the calcium sulfite is contacted with from about 0.1 to about 0.5 mole sulfuric acid per mole calcium sulfite.

Claim 7

The method of claim 1 wherein the sludge containing the undissolved calcium sulfite is contacted with the aqueous media separated from the calcium sulfate precipitate.

Claim 8

The method of claim 6 wherein about 20 to 100 pounds of aqueous media, separated from the calcium sulfate precipitate, is recycled for every pound of calcium sulfite provided in the sludge from the flue gas desulfurization system.

Claim 9

The method of claim 1 wherein, a further minor portion of the slurry in the liquid scrubber unit is discharged therefrom at a pH of between about 4.5 to 6.0; contacted with sulfuric acid to cause dissolution of calcium sulfite contained therein; the dissolved calcium sulfite oxidized in the aqueous solution with an oxygen-containing gas to form calcium sulfate precipitate separated from the aqueous media.

Claim 10

The method of claim 8 wherein said further minor portion comprises about one-quarter to one-third of the total discharge from the scrubbing system.

Claim 11

In a method of flue gas desulfurization wherein a flue gas, containing sulfur dioxide, is contacted in a liquid scrubber unit with an aqueous slurry formed from calcium hydroxide and magnesium hydroxide, and which contains magnesium hydroxide in an amount to provide an effective magnesium ion content of between 2500 to 9000 parts per million in the liquid scrubbing unit, and at least a portion of the slurry, after passage through the scrubber, containing undissolved calcium sulfite is recirculated through a thickener to produce an aqueous sludge containing calcium sulfite, the improvement wherein the calcium sulfite present in the aqueous sludge is oxidized by: separating undissolved calcium sulfite, in a sludge which contains at least about 20 wieght percent solids, from the scrubbing slurry; contacting said sludge with aqueous sulfuric acid, in an aqueous solution having a pH of about 5.2 to 5.5, to cause dissolution of calcium sulfite in an aqueous solution; oxidizing the dissolved calcium sulfite in the aqueous sulfuric acid solution with an oxygen-containing gas to form a calcium sulfate precipitate in an aqueous media; separating the calcium sulfate precipitate from the aqueous media; and returning aqueous media, separated from the calcium sulfate precipitate, for contact with additional sludge produced in the thickener.

Claim 12

In a method of flue gas desulfurization wherein a flue gas, containing sulfur dioxide, is contacted in a liquid scrubber unit with an aqueous slurry formed from calcium hydroxide and magnesium hydroxide, and which contains magnesium hydroxide in an amount to provide an effective magnesium ion content of between 2500 to 9000 parts per million in the liquid scrubbing unit, and at least a portion of the slurry, after passage through the scrubber, containing undissolved calcium sulfite is recirculated through a thickener to produce an aqueous sludge containing calcium sulfite, the improvement wherein the calcium sulfite present in the aqueous sludge is oxidized by: separating undissolved calcium sulfite, in a sludge which contains at least about 20 wieght percent solids, from the scrubbing slurry; contacting said sludge with aqueous sulfuric acid, in an aqueous solution having a pH of about 5.2 to 5.5, to cause dissolution of calcium sulfite in an aqueous solution; oxidizing the dissolved calcium sulfite in the aqueous sulfuric acid solution with an oxygen-containing gas to form a calcium sulfate precipitate in an aqueous media; separating the calcium sulfate precipitate from the aqueous media; and returning aqueous media, separated from the calcium sulfate precipitate, for contact with additional sludge produced in the thickener.

Claim 13

The method of claim 10 wherein the calcium sulfite is contacted with from about 0.1 to about 0.5 mole sulfuric acid per mole calcium sulfite, and about 20 to 100 pounds of aqueous media, separated from the calcium sulfate precipitate, is returned for every pound of calcium sulfite provided in the sludge from the flue gas desulfurization system.

Claim 14

The method of claim 11 wherein, a further minor portion of the slurry in the liquid scrubber unit, comprising about one-quarter to one-third of the total discharge from the scrubbing system, is discharged therefrom at a pH of between about 5.5 to 6.0; said further minor portion is contacted with an aqueous acid to cause dissolution of calcium sulfite contained therein; the dissolved calcium sulfite oxidized in the aqueous solution with an oxygen-containing gas to form calcium sulfate precipitate in an aqueous media; and the calcium sulfate precipitate separated from the aqueous media.