Reduction of aqueous thiosulfate solutions

Claim 1

The method of converting sodium, potassium, or ammonium thiosulfate to a mixture of the corresponding carbonates and sulfides which comprises: a. contacting a reducing gas containing CO with an aqueous solution of said thiosulfate in a first reduction zone under reducing conditions selected to favor the production of the corresponding formate until a mixture of formate and unconverted thiosulfate in an effluent aqueous solution is obtained wherein only sufficient formate, stoichiometrically, has been produced to react with a predetermined amount of the unconverted thiosulfate, the amount of thiosulfate converted in said first reduction zone being between 20 and 90 weight percent of the total conversion of thiosulfate effected in this and the following step (b); and thereafter b. maintaining said effluent aqueous solution from step (a) in liquid phase in a second reduction zone under reducing conditions selected to effect reaction of the formate formed in step (a) with unreacted thiosulfate from step (a), to yield an aqueous solution containing carbonates and sulfides.

Claim 2

The method of converting sodium, potassium, or ammonium thiosulfate to a mixture of the corresponding carbonates and sulfides which comprises: a. contacting a reducing gas containing CO with an aqueous solution of said thiosulfate in a first reduction zone under reducing conditions selected to favor the production of the corresponding formate until a mixture of formate and unconverted thiosulfate in an effluent aqueous solution is obtained wherein only sufficient formate, stoichiometrically, has been produced to react with a predetermined amount of the unconverted thiosulfate, the amount of thiosulfate converted in said first reduction zone being between 20 and 90 weight percent of the total conversion of thiosulfate effected in this and the following step (b); and thereafter b. maintaining said effluent aqueous solution from step (a) in liquid phase in a second reduction zone under reducing conditions selected to effect reaction of the formate formed in step (a) with unreacted thiosulfate from step (a), to yield an aqueous solution containing carbonates and sulfides.

Claim 4

The method of converting potassium thiosulfate to a mixture of the corresponding carbonates and sulfides which comprises: a. contacting a reducing gas containing CO with an aqueous solution of said thiosulfate in a first reduction zone maintained at a temperature between 400° and 500° F. and under a pressure between 400 and 800 p.s.i.g. until a mixture of the corresponding formate and unconverted thiosulfate in an effluent aqueous solution is obtained wherein only sufficient formate, stoichiometrically, has been produced to react with a predetermined amount of the unconverted thiosulfate, the amount of thiosulfate converted in said first reduction zone being between 20 and 90 weight percent of the total conversion of thiosulfate effected in this and the following step (b); and thereafter b. maintaining said effluent aqueous solution from step (a) in liquid phase in a second reduction zone at a temperature between 450° and 550° F. and under a pressure between 400 and 800 p.s.i.g. to effect reaction of the formate formed in step (a) with unreacted thiosulfate from step (a), to yield an aqueous solution containing the corresponding carbonates and sulfides.

Claim 5

The method of converting potassium thiosulfate to a mixture of the corresponding carbonates and sulfides which comprises: a. contacting a reducing gas containing CO with an aqueous solution of said thiosulfate in a first reduction zone maintained at a temperature between 400° and 500° F. and under a pressure between 400 and 800 p.s.i.g. until a mixture of the corresponding formate and unconverted thiosulfate in an effluent aqueous solution is obtained wherein only sufficient formate, stoichiometrically, has been produced to react with a predetermined amount of the unconverted thiosulfate, the amount of thiosulfate converted in said first reduction zone being between 20 and 90 weight percent of the total conversion of thiosulfate effected in this and the following step (b); and thereafter b. maintaining said effluent aqueous solution from step (a) in liquid phase in a second reduction zone at a temperature between 450° and 550° F. and under a pressure between 400 and 800 p.s.i.g. to effect reaction of the formate formed in step (a) with unreacted thiosulfate from step (a), to yield an aqueous solution containing the corresponding carbonates and sulfides.