US4446115A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of recovering tantalum from silicon-containing tantalum scrap
Assignee: Toshiba Corp
•
Filing: 1982-03-02
•
Granted: 1984-05-01
•
Expires: 2002-03-02
Abstract
Abstract Disclosed is method of recovering tantalum from silicon-containing tantalum scrap, which comprises dissolving said scrap in an inorganic acid, bringing the resulting solution into contact with an anionic exchange resin, followed by washing said anionic exchange resin with (a) a solution of 3 to 10 mol/l. of hydrofluoric acid or (b) a solution of strongly acidic medium containing 0.01 to 0.5 mol/l. of hydrofluoric acid and 1 to 6 mol/l. of a strong acid, and then washing the same with an aqueous solution of a mixture composed of hydrofluoric acid, aqueous ammonia and an ammonium salt.
Inventors
- 👤 Hiroshi Endo
- 👤 Naoyuki Hirate
- 👤 Masao Tezuka
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 10:49
CPC Classifications
C; C01; C01G; C01G35/00; C01G35/003; C22; C22B; C22B3/00; C22B3/20; C22B3/42; C22B34/00; C22B34/20; C22B34/24; Y; Y02; Y02P; Y02P10/00; Y02P10/20
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
148 words
A method of recovering tantalum from tantalum-containing scrap containing at least silicon and niobium as impurities to produce a recovered tantalum product containing less than about 200 ppm of silicon, consisting essentially of the steps of: dissolving in an inorganic acid a tantalum scrap containing at least silicon and niobium to form a solution; contacting said solution with an anionic exchange resin; first washing said contacted exchange resin with (a) a solution of about 3 to 10 mol/l of hydrofluoric acid or (b) a solution of a strongly acidic medium comprising from about 0.01 to 0.5 mol/l of hydrofluoric acid and from about 1 to 6 mol/l of a strong acid to remove the impurities; further washing said exchange resin with an aqueous solution of a mixture comprising hydrofluoric acid, aqueous ammonia and an ammonium salt to produce a tantalum eluate; and recovering tantalum from the tantalum eluate.
Claim 2
Independent Claim
148 words
A method of recovering tantalum from tantalum-containing scrap containing at least silicon and niobium as impurities to produce a recovered tantalum product containing less than about 200 ppm of silicon, consisting essentially of the steps of: dissolving in an inorganic acid a tantalum scrap containing at least silicon and niobium to form a solution; contacting said solution with an anionic exchange resin; first washing said contacted exchange resin with (a) a solution of about 3 to 10 mol/l of hydrofluoric acid or (b) a solution of a strongly acidic medium comprising from about 0.01 to 0.5 mol/l of hydrofluoric acid and from about 1 to 6 mol/l of a strong acid to remove the impurities; further washing said exchange resin with an aqueous solution of a mixture comprising hydrofluoric acid, aqueous ammonia and an ammonium salt to produce a tantalum eluate; and recovering tantalum from the tantalum eluate.
Claim 3
Dependent Claim
23 words
A method according to claim 1, wherein said anionic exchange resin is of strongly basic quarternary ammonium type or strongly basic piridinium type.
Claim 4
Dependent Claim
32 words
A method according to claim 1, wherein said strongly acidic medium includes at least one strong acid selected from the group consisting of hydrochloric acid, nitric acid, sulfuric acid and perchloric acid.
Claim 5
Dependent Claim
23 words
A method according to claim 1, wherein the concentration of said hydrofluoric acid in the solution (a) ranges from 6 to 9 mol/l.
Claim 6
Dependent Claim
44 words
A method according to claim 1, wherein the concentration of hydrofluoric acid contained in the solution (b) of strongly acidic medium containing hydrofluoric acid ranges from 0.1 to 0.3 mol/l. and the concentration of strong acid contained therein ranges from 2 to 4 mol/l.
Claim 7
Dependent Claim
26 words
A method according to claim 1, wherein said ammonium salt is selected from the group consisting of ammonium chloride, ammonium nitrate, ammonium sulfate and ammonium perchlorate.
Claim 8
Dependent Claim
28 words
A method according to claim 1, wherein the pH of said solution of the mixture comprising hydrofluoric acid, aqueous ammonia and ammonium salt ranges from 3 to 6.
Claim 9
Dependent Claim
57 words
A method according to claim 1, wherein the pH of said solution of the mixture comprising hydrofluoric acid, aqueous ammonia and ammonium salt ranges from 5 to 6, 3 to 4, 2 to 4, or 3 to 5 in the case where said ammonium salt therein is ammonium chloride, ammonium nitrate, ammonium sulfate or ammonium perchlorate, respectively.
Claim 10
Dependent Claim
29 words
A method of recovering tantalum from silicon-containing tantalum as defined in claim 1, wherein said recovery step comprises recovering tantalum pentaoxide by precipitation and subsequent dehydration of the precipitate.
Claim 11
Dependent Claim
32 words
A method according to claim 9, wherein said recovering step comprises: adjusting the pH of said tantalum eluate to precipitate tantalum hydroxide; and dehydrating said tantalum hydroxide to obtain said tantalum pentoxide.
Claim 12
Dependent Claim
19 words
A method according to claim 10, wherein said pH is adjusted to a value of at least about 6.
Claim 13
Dependent Claim
14 words
A method according to claim 11, wherein adjusting the pH comprises adding aqueous ammonia.
Claim 14
Dependent Claim
40 words
A method according to claim 1, wherein there is produced a recovered tantalum product containing less than about 10 ppm of silicon and wherein the concentration of said hydrofluoric acid in the solution (a) ranges from 6 to 9 mol/l.
Claim 15
Dependent Claim
61 words
A method according to claim 1, wherein there is produced a recovered tantalum product containing less than about 10 ppm of silicon and wherein the concentration of hydrofluoric acid contained in the solution (b) of strongly acidic medium containing hydrofluoric acid ranges from 0.1 to 0.3 mol/l and the concentration of strong acid contained therein ranges from 2 to 4 mol/l.
References Cited (Backward Citations)
US2937072A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-05-01 | 1987-10-31 | 1988-05-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-05-01 | 1991-10-31 | 1992-05-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-05-01 | 1995-10-31 | 1996-05-01 | $7700.00 | Window Closed / Lapsed |