Conversion of alkali metal sulfate to the carbonate
AssigneeThe United States of America as represented by the United States Department of Energy
InventorAtul C. Sheth
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AssigneeThe United States of America as represented by the United States Department of Energy
InventorAtul C. Sheth
Estimating the term…
A process for converting potassium sulfate to potassium carbonate in which a mixture of potassium sulfate and calcium oxide are reacted at a temperature in the range of between about 700.degree. C. and about 800.degree. C. with a gaseous mixture having a minor amount of hydrogen and/or carbon monoxide in a diluent with the calcium oxide being present in an amount not greater than about 20 percent by weight of the potassium sulfate to produce an aqueous mixture of potassium sulfide, potassium bisulfide, potassium hydroxide and calcium sulfide and a gaseous mixture of steam and hydrogen sulfide. The potassium and calcium salts are quenched to produce an aqueous slurry of soluble potassium salts and insoluble calcium salts and a gaseous mixture of steam and hydrogen sulfide. The insoluble calcium salts are then separated from the aqueous solution of soluble potassium salts. The calcium salts are dried to produce calcium sulfide, calcium bisulfide and steam, and then, the calcium sulfide and calcium bisulfide are converted to the oxide and recycled. The soluble potassium salts are carbonated to produce potassium carbonate which is concentrated and the precipitated crystals separated. The sulfur-containing compounds are further treated.
A process for converting alkali metal sulfate to the corresponding carbonate comprising reacting the alkali metal sulfate with a gaseous mixture containing up to about 20 volume percent of a reductant selected from the group consisting of hydrogen, carbon monoxide and combinations thereof in an inert diluent with an oxide of a metal selected from the class consisting of calcium, zinc, iron and mixtures thereof present in the range of between about 5 percent by weight and about 20 percent by weight of the alkali metal sulfate at a temperature in the range of between about 700.degree. C. and about 800.degree. C. to convert not less than about eighty percent of the alkali metal sulfate alkali metal sulfide, bisulfide or hydroxide in a time span not to exceed about one hour producing said alkali metal sulfide, bisulfide or hydroxide, and the sulfide of the selected metal oxide;
A process for converting potassium sulfate to potassium carbonate comprising passing a mixture of potassium sulfate and calcium oxide to a reducing station and there reacting said mixture for a time not to exceed about one hour to convert not less than about 80% of the sulfate potassium sulfide, potassium bisulfide, or potassium hydroxide at a temperature of about 750.degree. C. with a gaseous mixture having a minor amount of up to about 20 volume percent reductants selected from the group consisting of hydrogen, carbon monoxide and mixtures thereof in an inert diluent wherein the calcium oxide is present in an amount not greater than about 20 percent by weight of the potassium sulfate to produce a liquid mixture of said potassium sulfide, potassium bisulfide or potassium hydroxide and calcium sulfide and a gaseous mixture of steam and hydrogen sulfide;
Dependencies are inferred from the claim text.