Extractant solvent restoration in the process for recovery of uranium from phosphoric acid

Claim 2

A process of purifying organic extractant solvent in a uranium recovery process, comprising the steps of: (A) passing phosphoric acid solution containing uranium values and contaminants into an extractor means and contacting it with a water-immiscible, organic extractant solvent composition, having a uranium extraction coefficient of at least about 2.0, to extract uranium values and contaminants from the acid solution, and then (B) passing the organic solvent, containing uranium values and contaminants, into a stripper means, to strip uranium values from the organic solvent, and to provide a stripped organic solvent stream still containing contaminants and having a lowered uranium extraction coefficient value, and then (C) passing from about 5 vol. % to about 35 vol. % of the stripped organic solvent stream from the stripper means into a water scrubber means and contacting it with water, containing no more than about 3 vol. % phosphoric acid as an impurity, to scrub contaminants from the organic solvent and raise its uranium extraction coefficient value, to provide a scrubbed water-immiscible, organic extractant solvent composition stream and a water stream containing contaminants, and then (D) passing the scrubbed organic solvent back to the extractor means, and (E) passing the contaminated water stream into at least one purification means, to provide a purified water stream which is fed back into the scrubber means.

Claim 3

The method of claim 1, where the volume ratio of water:organic solvent in step (C) is between about 1:0.2 to 1:2.5.

Claim 4

The method of claim 1, where the purification means in step (E) contains activated carbon having an internal surface area of over about 600 sq. meters/gram.

Claim 5

The method of claim 3, where the solvent and water countercurrent contact each other in step (C).

Claim 6

The method of claim 1, where the uranium extraction coefficient of the organic solvent after step (C) is over 2.0.

Claim 7

The method of claim 1, where the extractant solvent composition comprises dialkyl phosphoric acid, trialkyl phosphine oxide and hydrocarbon diluent.

Claim 8

The method of claim 1, where the extractant solvent composition comprises di(2-ethylhexyl) phosphoric acid, trioctyl phosphine oxide and hydrocarbon diluent.

Claim 9

A process of purifying stripped organic extractant solvent in a uranium recovery process, comprising the steps of: (A) passing phosphoric acid solution containing uranium values and contaminants into an extractor means and contacting it with a water-immiscible, organic extractant solvent composition, having a uranium extraction coefficient of at least about 2.0, to extract uranium values and contaminants from the acid solution, and then (B) passing the organic solvent, containing uranium values and contaminants, directly into a stripper means, to strip uranium values from the organic solvent, and to provide a stripped organic solvent stream still containing contaminants and having a lowered uranium extraction coefficient value, and then (C) passing from about 5 vol.% to about 35 vol.% of the stripped organic solvent stream from the stripper means into a water scrubber means and countercurrent contacting it with water containing no more than about 3 vol.% phosphoric acid as an impurity, in a volume ratio of water:organic solvent of between about 1:0.2 to 1:2.5, to scrub contaminants from the organic solvent and raise its uranium extraction coefficient value, to provide a scrubbed water-immiscible, organic extractant solvent composition stream and a water stream containing contaminants, and then (D) passing the scrubbed organic solvent back to the extractor means, and (E) passing the contaminated water stream into at least one purification means, to provide a purified water stream which is fed back into the scrubber means.

Claim 10

A process of purifying stripped organic extractant solvent in a uranium recovery process, comprising the steps of: (A) passing phosphoric acid solution containing uranium values and contaminants into an extractor means and contacting it with a water-immiscible, organic extractant solvent composition, having a uranium extraction coefficient of at least about 2.0, to extract uranium values and contaminants from the acid solution, and then (B) passing the organic solvent, containing uranium values and contaminants, directly into a stripper means, to strip uranium values from the organic solvent, and to provide a stripped organic solvent stream still containing contaminants and having a lowered uranium extraction coefficient value, and then (C) passing from about 5 vol.% to about 35 vol.% of the stripped organic solvent stream from the stripper means into a water scrubber means and countercurrent contacting it with water containing no more than about 3 vol.% phosphoric acid as an impurity, in a volume ratio of water:organic solvent of between about 1:0.2 to 1:2.5, to scrub contaminants from the organic solvent and raise its uranium extraction coefficient value, to provide a scrubbed water-immiscible, organic extractant solvent composition stream and a water stream containing contaminants, and then (D) passing the scrubbed organic solvent back to the extractor means, and (E) passing the contaminated water stream into at least one purification means, to provide a purified water stream which is fed back into the scrubber means.

Claim 11

The method of claim 8, where the extractant solvent composition comprises di(2-ethylhexyl) phosphoric acid, trioctyl phosphine oxide and hydrocarbon diluent, and the filter means in step (E) contains activated carbon having an internal surface area of over about 600 sq. meters/gram.