Production of potassium sulfate and hydrogen chloride
AssigneePennzoil Company
InventorJohn B. Sardisco
Life of this patent
Estimating the term…
Abstract
Potassium sulfate (K.sub.2 SO.sub.4) is prepared by reaction of potassium chloride and sulfuric acid in an aqueous medium by initially removing evolved HCl in the gaseous form at temperatures of about 65.degree.-120.degree. C., then removing the remaining HCl as an HCl/water azeotrope at temperatures of about 90.degree. to 110.degree. C., restoring to the reaction mixture the amount of water removed with the azeotrope, and permitting the potassium sulfate to crystallize from the solution.
Claims6
A method for the production of potassium sulfate and potassium hydrogen sulfate which comprises initially reacting potassium chloride and sulfuric acid in an aqueous medium at a temperature of about 65.degree. to 120.degree. C. under conditions to form hydrogen chloride and removing a portion of the hydrogen chloride from the reaction zone by gaseous evolution, thereafter subjecting the resulting aqueous solution to azeotropic distillation at temperatures in the range of from 90.degree. to 110.degree. C., and removing an HCl/water azeotrope until the remainder of the hydrogen chloride has been removed, and form a resulting aqueous slurry, thereafter adding to the resulting aqueous slurry an amount of water which is substantially equivalent to the amount of water removed with the azeotrope to again form an aqueous solution, cooling the aqueous solution to a temperature of about 30.degree.-75.degree. C., to allow a solid precipitate to crystallize from solution, and recovering the solid which comprises a mixture of potassium sulfate and potassium hydrogen sulfate.
A continuous procedure for the production of potassium sulfate which comprises reacting potassium chloride and sulfuric acid in an aqueous medium in an initial reaction step at a temperature of about 65.degree. to 120.degree. C. under conditions to form hydrogen chloride and removing a portion of the hydrogen chloride from the reaction zone by gaseous evolution, thereafter subjecting the resulting aqueous solution to azeotropic distillation at temperatures in the range of 90.degree.-110.degree. C while removing an HCl/water azeotrope and continuing removal of the azeotrope until the remainder of the hydrogen chloride has been removed;
- and form an aqueous slurry, thereafter adding to the aqueous slurry an amount of water which is substantially equivalent to the amount of water removed with the azeotrope to again form an aqueous solution, cooling the resulting solution to a temperature in the range of about 30.degree.-75.degree. C. to allow a solid precipitate to crystallize from solution, separating the solid precipitate from the solution, recycling the separated solution to the initial reaction step, washing the separated solid precipitate with a member selected from the group consisting of water and an aqueous solution containing potassium sulfate, to form a solid and a wash filtrate, recycling the wash filtrate to be initial reaction step and recovering the solid comprising potassium sulfate.
Dependencies are inferred from the claim text.