Stabilization of wet-process phosphoric acid

Claim 1

A method for the preparation of merchant grade phosphoric acid stabilized against sludge formation which comprises concentrating a wet process phosphoric acid solution having a P 2 O 5 content of about 28% to 32% by weight and containing in said solution Fe, Al, Si, F, and Na and K impurities to a P 2 O 5 content of about 35% to 42% by weight; adding to the concentrated acid solution in a reaction tank, about 0.1 to 1.0% by weight of inorganic oxidizing agent to change the redox potential of the solution to increase the solubility of said Fe and Al impurities and to maintain same in said acid solution, adding to said concentrated acid solution in said reaction tank about 0.1 to 1.0% of activated silica; aging the thus treated solution for a time sufficient for said silica to react with said F impurities in said concentrated acid solution and cause formation of a solid phase precipitate and a liquid phase of stabilized phosphoric acid containing substantial amounts of said Fe and Al impurities; separating the liquid and solid phases by a first centrifugation; concentrating the separated liquid phase from the first centrifugation to a P 2 O 5 content of at least 50% by weight; separating the solids formed in the concentrated liquid phase by a second centrifugation to obtain a clarified product solution having less than 1% solids; and recycling the solids from the second centrifugation to said reaction tank.

Claim 2

A method for the preparation of merchant grade phosphoric acid stabilized against sludge formation which comprises concentrating a wet process phosphoric acid solution having a P 2 O 5 content of about 28% to 32% by weight and containing in said solution Fe, Al, Si, F, and Na and K impurities to a P 2 O 5 content of about 35% to 42% by weight; adding to the concentrated acid solution in a reaction tank, about 0.1 to 1.0% by weight of inorganic oxidizing agent to change the redox potential of the solution to increase the solubility of said Fe and Al impurities and to maintain same in said acid solution, adding to said concentrated acid solution in said reaction tank about 0.1 to 1.0% of activated silica; aging the thus treated solution for a time sufficient for said silica to react with said F impurities in said concentrated acid solution and cause formation of a solid phase precipitate and a liquid phase of stabilized phosphoric acid containing substantial amounts of said Fe and Al impurities; separating the liquid and solid phases by a first centrifugation; concentrating the separated liquid phase from the first centrifugation to a P 2 O 5 content of at least 50% by weight; separating the solids formed in the concentrated liquid phase by a second centrifugation to obtain a clarified product solution having less than 1% solids; and recycling the solids from the second centrifugation to said reaction tank.