US4190633A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Crud handling circuit
Assignee: Freeport Mcmoran Resource Partners Ltd
•
Filing: 1977-04-08
•
Granted: 1980-02-26
•
Expires: 1997-04-08
Abstract
Abstract A method for handling the problem of crud formation in the solvent extraction of wet-process phosphoric acid is described. Crud is the name ordinarily given to the thick interfacial layer of semi-floatable material which tends to form and accumulate, and which interferes with many of the extraction processes and, in particular, with the solvent extraction of wet-process phosphoric acid. The method described provides for the operation of the solvent extraction stages in a manner that allows the formation and temporary accumulation of crud in those stages whereupon the solvent and the crud are then removed from the extraction stages and treated in a series of operations which include a clarification step, an acid removal step, a water wash step and a caustic treatment step, which steps effectively separate the solvent from the crud, and remove the crud components from the system and regenerate otherwise unusable solvent. The invention is particularly applicable to the solvent extraction of wet-process phosphoric acid for the recovery of uranium by the reductive stripping technique.
Inventors
- 👤 Jay C. Smith
- 👤 Ronald J. Manuel
- 👤 James E. McAllister
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 06:47
CPC Classifications
C; C22; C22B; C22B60/00; C22B60/02; C22B60/0204; C22B60/0217; C22B60/0252; C22B60/026; B; B01; B01D; B01D11/00; B01D11/04; C01; C01B; C01B25/00; C01B25/16; C01B25/18; C01B25/234; C01B25/237; C01B25/238; C01B25/46; C01B25/461
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
192 words
A process for treating semi-floatable, crud-forming material formed during the extraction of dissolved constituents from aqueous wet process phosphoric acid phase using an organic solvent extractant phase, comprising the steps of: (a) operating the solvent extraction stages of the process to allow the formation of the semi-floatable crud material; (b) removing at least a portion of the semi-floatable crud material, together with a portion of the solvent, from said stages; and, (c) separating the removed solvent from the semi-floatable crud material by the steps of: (i) clarifying the removed solvent and semi-floatable crud material to remove organic material therefrom; (ii) subjecting the underflow from the clarification step to a settling process to remove acid therefrom; (iii) washing the solvent and semi-floatable crud material in amounts sufficient to further remove acid therefrom; and; (iv) mixing the solvent and semi-floatable crud material with an aqueous caustic solution containing between 0.2-2.0% NaOH (by weight) and between 0-3% Na 2 CO 3 (by weight) wherein the mixture of crud and caustic has a pH of between 4.5 and 11.0, in an amount sufficient to remove the solvent from the semi-floatable crud material and regenerate said solvent.
Claim 2
Dependent Claim
192 words
A process for treating semi-floatable, crud-forming material formed during the extraction of dissolved constituents from aqueous wet process phosphoric acid phase using an organic solvent extractant phase, comprising the steps of: (a) operating the solvent extraction stages of the process to allow the formation of the semi-floatable crud material; (b) removing at least a portion of the semi-floatable crud material, together with a portion of the solvent, from said stages; and, (c) separating the removed solvent from the semi-floatable crud material by the steps of: (i) clarifying the removed solvent and semi-floatable crud material to remove organic material therefrom; (ii) subjecting the underflow from the clarification step to a settling process to remove acid therefrom; (iii) washing the solvent and semi-floatable crud material in amounts sufficient to further remove acid therefrom; and; (iv) mixing the solvent and semi-floatable crud material with an aqueous caustic solution containing between 0.2-2.0% NaOH (by weight) and between 0-3% Na 2 CO 3 (by weight) wherein the mixture of crud and caustic has a pH of between 4.5 and 11.0, in an amount sufficient to remove the solvent from the semi-floatable crud material and regenerate said solvent.
Claim 3
Dependent Claim
28 words
The method of claim 1 comprising the further step of recycling the removed and regenerated solvent back into the solvent extraction stage of the wet-process phosphoric acid process.
Claim 4
Dependent Claim
14 words
The method of claim 1 wherein the washing operation is conducted in two stages.
Claim 5
Dependent Claim
22 words
The method of claim 1 wherein the aqueous caustic solution contains 0.5% NaOH and 1.0% Na 2 CO 3 ) (by weight).
Claim 6
Dependent Claim
24 words
The method of claim 1 wherein the volumetric flow ratio of the aqueous to the solvent/crud in step (iv) is between 2/1 and 4/1.
Claim 7
Dependent Claim
21 words
The method of claim 1 wherein the volumetric flow ratio of the aqueous to the solvent/crud in step (iv) approximately 2.5/1.
Claim 8
Dependent Claim
24 words
The method of claim 1 comprising the further step of recycling the acid removed in said settling process back into said solvent extraction stages.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-02-25 | 1983-08-27 | 1984-02-26 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-02-25 | 1987-08-27 | 1988-02-26 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-02-25 | 1991-08-27 | 1992-02-26 | $7700.00 | Window Closed / Lapsed |