US4301123A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Methods of processing uraniferous ores
Assignee: Orano Demantelement SAS
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Filing: 1979-05-02
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Granted: 1981-11-17
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Expires: 1999-05-02
Abstract
Abstract Refractory uranium is crushed and impregnated with a concentrated aqueous solution of sulphuric acid to provide a mixture which retains a solid phase consistency. The impregnated mixture is disintegrated in an aqueous solution to form a thick paste or pulp. The pulp is digested for a duration not exceeding 10 hours and the uranium recovered by solid/liquid separation. The sulphuric acid content of the concentrated solution is selected for the residual acidity at the end of pulp digestion to be of from 10 g/l to 40 g/l.
Inventors
- 👤 Michel Gruet
- 👤 Paul Lafforgue
- 👤 Pierre Michel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 05:19
CPC Classifications
C; C22; C22B; C22B60/00; C22B60/02; C22B60/0204; C22B60/0217; C22B60/0221; C22B60/0226; C22B60/0234
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
121 words
Method of processing uranium ore, particularly refractory ores, comprising the steps of: crushing the ore, impregnating the ore with a concentrated aqueous solution of sulphuric acid for a period not exceeding 30 minutes, the volume of solution per unit weight of crushed ore being selected to obtain a mixture which retains a solid phase consistency and does not reach a sticky condition, disintegrating the impregnated mixture with an aqueous solution into a thick paste or pulp, digesting the pulp for a duration not exceeding 10 hours, and carrying out solid/liquid separation, wherein the sulphuric acid content of the concentrated solution is selected for the residual acidity at the end of pulp digestion to be of from 10 g/l to 40 g/l.
Claim 2
Dependent Claim
121 words
Method of processing uranium ore, particularly refractory ores, comprising the steps of: crushing the ore, impregnating the ore with a concentrated aqueous solution of sulphuric acid for a period not exceeding 30 minutes, the volume of solution per unit weight of crushed ore being selected to obtain a mixture which retains a solid phase consistency and does not reach a sticky condition, disintegrating the impregnated mixture with an aqueous solution into a thick paste or pulp, digesting the pulp for a duration not exceeding 10 hours, and carrying out solid/liquid separation, wherein the sulphuric acid content of the concentrated solution is selected for the residual acidity at the end of pulp digestion to be of from 10 g/l to 40 g/l.
Claim 3
Dependent Claim
32 words
Method according to claim 1, wherein during the impregnation step, a volume of from 0.06 to 0.20 m 3 of concentrated solution per metric ton of ore is added to the ore.
Claim 4
Dependent Claim
22 words
Method according to claim 1 or 2, wherein the time duration of the impregnation step is of from 10 to 15 minutes.
Claim 5
Dependent Claim
25 words
Method according to claim 1 or 2, wherein water and sulphuric acid in the impregnation solution are in a ratio of about 1:1 per weight.
Claim 6
Dependent Claim
39 words
Method according to claim 1, for the treatment of ores containing reducing substances, wherein an oxidizing agent selected from the group consisting of nitric acid, nitrates and mixtures of nitric acid and nitrates is added to the impregnation solution.
Claim 7
Dependent Claim
44 words
Method according to claim 5, wherein the nitrous vapours resulting from the action of the oxidizing agent are recovered, regenerated into nitric acid or nitrate and recycled to the impregnation step, the losses being compensated by the addition of fresh nitric acid or nitrate.
Claim 8
Dependent Claim
32 words
Method according to claim 1, 2, or 5, wherein the disintegration and digestion in thick pulp form lasts from 1 to 10 hours, at a temperature of from 60° to 85° C.
Claim 9
Dependent Claim
33 words
Method according to claim 1, 2, 5, or 6, wherein the disintegration and pulp digestion are carried out with a liquid content comprising between 0.45 and 0.7 m 3 /ton of solid material.
Claim 10
Dependent Claim
41 words
Method according to claim 1 or 2, characterized in that an oxidizing agent is added only during disintegration and digestion in paste form, the oxidizing agent being selected from the group consisting of chlorates, manganese dioxide, hydrogen peroxide, and mixtures thereof.
References Cited (Backward Citations)
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US2849280A
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US3808306A
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US4131639A
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US4098866A
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-11-16 | 1985-05-18 | 1985-11-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-11-16 | 1989-05-18 | 1989-11-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-11-16 | 1993-05-18 | 1993-11-17 | $7700.00 | Window Closed / Lapsed |