Dewatering of flue gas desulfurization sulfite solids

Claim 2

In an improved process for the removal of SO 2 from an input gas stream containing SO 2 wherein the input gas stream is contacted, in a gas-liquid scrubbing zone, with an aqueous scrubbing slurry containing an alkaline reagent wherein said alkaline reagent contained in said scrubbing slurry is selected from the group consisting of lime, limestone, or mixtures thereof at scrubbing conditions selected to form a resulting treated gas stream containing substantially less SO 2 than said input gas stream and a resulting SO 2 enriched scrubbing slurry containing as a substantial portion of the solids therein calcium sulfite hemihydrate; subsequently effecting at least a partial dewatering of said SO 2 enriched scrubbing slurry; and removing the resulting at least partially dewatered sludge to waste disposal; the improvement in combination therewith for substantially increasing the yield of solids in said dewatered sludge to thereby render same eminently suitable for use in solid landfill waste disposal operations, which improved process comprises adding to and maintaining in said aqueous scrubbing slurry from about 250 ppm to about 2500 ppm of thiosulfate ion, said improved process characterized by the fact that the addition and maintenance of said amounts of thiosulfate ion in said aqueous scrubbing slurry is sufficient to effect therein a crystal habit of the calcium sulfite hemihydrate comprising a substantial portion of the solids therein in a tabular prismatic mode and substantially eliminates therein the occurrence of porous lamellar aggregates of randomly oriented micaceous crystallites of said calcium sulfite hemihydrate, thereby altering the agglomerative characteristics of said crystallites in the spent slurry removed from said gas-liquid scrubbing zone to a mode which substantially increases the settling rate thereof and results in the ultimate dewatering of said sludge up to the range of about 80 to 90 percent solids by weight.

Claim 3

An improved process as defined in claim 1 wherein the source of said thiosulfate ion is selected from the group consisting of thiosulfate salts of sodium, potassium, ammonium, calcium, magnesium, and mixtures thereof.

Claim 4

An improved process as defined in claim 2 wherein the source of said thiosulfate ion is the sodium salt of thiosulfuric acid.

Claim 5

An improved process as defined in claim 1 wherein said source of thiosulfate ion is derived by the reduction of polythionic acid salt to thiosulfate ion in said scrubbing slurry, said polythionic acid salt selected from the group consisting of alkali and alkaline earth salts of trionic and tetronic acids.

Claim 6

An improved process as defined in claim 2 wherein the thiosulfate ion concentration ranges from about 300 ppm to about 1000 ppm.

Claim 7

An improved process as defined in claim 2 wherein the thiosulfate ion concentration is maintained at about 600 ppm.

Claim 8

In an improved process for the removal of SO 2 from an input gas stream containing SO 2 wherein the input gas stream is contacted, in a gas-liquid scrubbing zone, with an aqueous scrubbing solution containing a dissolved alkaline reagent at scrubbing conditions selected to form a resulting treated gas stream containing substantially less SO 2 than said input gas stream and a resulting SO 2 enriched scrubbing solution having an increased sulfur loading; introducing at least a portion of the resulting SO 2 enriched scrubbing solution into scrubbing reagent recovery means, together with a stream of slurry containing substantially undissolved alkaline reagent, wherein said alkaline reagent contained in said surry is selected from the group consisting of lime, limestone, or mixtures thereof said slurry containing said substantially undissolved alkaline reagent having a pH greater than the pH of said solution containing said dissolved reagent; maintaining both of said alkaline reagents in intimate contact in said scrubbing reagent recovery means at conditions sufficient to convert at least a portion of said dissolved alkaline reagent therein to a decreased sulfur loading substantially equivalent to that of said aqueous scrubbing solution prior to its SO 2 enrichment and returning same to said gas-liquid scrubbing zone and converting at least a portion of said undissolved alkaline reagent introduced into said scrubbing reagent recovery means to crystallites of calcium sulfite hemihydrate to thereby effect the production of an SO 2 enriched slurry; subsequently effecting at least a partial dewatering of said SO 2 enriched slurry; and removing the resulting at least partially dewatered sludge to waste disposal; the improvement in combination therewith for substantially increasing the yield of solids in said dewatered sludge to thereby render same eminently suitable for use in solid landfill waste disposal operations, which improved process comprises adding to said scrubbing reagent recovery means from about 250 ppm to about 2500 ppm of thiosulfate ion, said improved process characterized by the fact that the addition of said amounts of thiosulfate ion in said scrubbing reagent recovery means is sufficient to effect therein a crystal habit of the calcium sulfite hemihydrate comprising a substantial portion of the solids therein in a tabular prismatic mode and substantially eliminates therein the occurrence of porous lamellar aggregates of randomly oriented micaceous crystallites of said calcium sulfite hemihydrate thereby altering the agglomerative characteristics of said crystallites in the slurry removed from said scrubbing reagent recovery means to a mode which substantially increases the settling rate thereof and results in the ultimate dewatering of said sludge up to the range of about 80 to about 90 percent solids by weight.

Claim 9

In an improved process for the removal of SO 2 from an input gas stream containing SO 2 wherein the input gas stream is contacted, in a gas-liquid scrubbing zone, with an aqueous scrubbing solution containing a dissolved alkaline reagent at scrubbing conditions selected to form a resulting treated gas stream containing substantially less SO 2 than said input gas stream and a resulting SO 2 enriched scrubbing solution having an increased sulfur loading; introducing at least a portion of the resulting SO 2 enriched scrubbing solution into scrubbing reagent recovery means, together with a stream of slurry containing substantially undissolved alkaline reagent, wherein said alkaline reagent contained in said surry is selected from the group consisting of lime, limestone, or mixtures thereof said slurry containing said substantially undissolved alkaline reagent having a pH greater than the pH of said solution containing said dissolved reagent; maintaining both of said alkaline reagents in intimate contact in said scrubbing reagent recovery means at conditions sufficient to convert at least a portion of said dissolved alkaline reagent therein to a decreased sulfur loading substantially equivalent to that of said aqueous scrubbing solution prior to its SO 2 enrichment and returning same to said gas-liquid scrubbing zone and converting at least a portion of said undissolved alkaline reagent introduced into said scrubbing reagent recovery means to crystallites of calcium sulfite hemihydrate to thereby effect the production of an SO 2 enriched slurry; subsequently effecting at least a partial dewatering of said SO 2 enriched slurry; and removing the resulting at least partially dewatered sludge to waste disposal; the improvement in combination therewith for substantially increasing the yield of solids in said dewatered sludge to thereby render same eminently suitable for use in solid landfill waste disposal operations, which improved process comprises adding to said scrubbing reagent recovery means from about 250 ppm to about 2500 ppm of thiosulfate ion, said improved process characterized by the fact that the addition of said amounts of thiosulfate ion in said scrubbing reagent recovery means is sufficient to effect therein a crystal habit of the calcium sulfite hemihydrate comprising a substantial portion of the solids therein in a tabular prismatic mode and substantially eliminates therein the occurrence of porous lamellar aggregates of randomly oriented micaceous crystallites of said calcium sulfite hemihydrate thereby altering the agglomerative characteristics of said crystallites in the slurry removed from said scrubbing reagent recovery means to a mode which substantially increases the settling rate thereof and results in the ultimate dewatering of said sludge up to the range of about 80 to about 90 percent solids by weight.

Claim 10

An improved process as defined in claim 7 wherein the source of said thiosulfate ion is selected from the group consisting of thiosulfate salts of sodium, potassium, ammonium, calcium, magnesium, and mixtures thereof.

Claim 11

An improved process as defined in claim 8 wherein the source of said thiosulfate ion is the sodium salt of thiosulfuric acid.

Claim 12

An improved process as defined in claim 7 wherein said source of thiosulfate ion is derived by the reduction of polythionic acid salt to thiosulfate ion in said slurry, said polythionic acid salt selected from the group consisting of alkali and alkaline earth salts of trionic and tetronic salts.

Claim 13

An improved process as defined in claim 8 wherein the thiosulfate ion concentration ranges from about 300 ppm to about 1000 ppm.

Claim 14

An improved process as defined in claim 8 wherein the thiosulfate ion concentration is maintained at about 600 ppm.