US4098868A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of titanium trichloride from ilmenite
Assignee: Honeywell UOP LLC
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Filing: 1977-04-27
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Granted: 1978-07-04
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Expires: 1997-04-27
Abstract
Abstract Titanium metal values may be recovered from a titanium bearing source by roasting said source in a reducing atmosphere, leaching the source with aqueous hydrogen chloride at an elevated temperature, cooling and saturating the leached solution with gaseous hydrogen chloride to precipitate hydrated ferrous chloride, separating the precipitated ferrous chloride from the soluble titanium chloride, raising the temperature of the solution to precipitate the titanium, separating and recovering the crystallized titanium compound.
Inventors
- 👤 William K. Tolley
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 09:22
CPC Classifications
C; C01; C01G; C01G23/00; C01G23/02
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
116 words
A process for obtaining titanium metal values from ilmenite ore which comprises the steps of: (a) subjecting said ore to a reductive roast at a temperature of from about 600° to about 900° C.; (b) leaching the resultant roasted ore with aqueous hydrogen chloride at an elevated temperature to form a solution of titanium trichloride and ferrous chloride; (c) cooling and saturating the leach solution with gaseous hydrogen chloride to precipitate ferrous chloride; (d) separating the precipitated ferrous chloride from titanium trichloride solution; (e) raising the temperature of the last-named solution to about 20° to about 30° C. to precipitate hydrated titanium trichloride; and (f) separating and recovering the crystallized titanium trichloride from the leach liquor.
Claim 2
Dependent Claim
116 words
A process for obtaining titanium metal values from ilmenite ore which comprises the steps of: (a) subjecting said ore to a reductive roast at a temperature of from about 600° to about 900° C.; (b) leaching the resultant roasted ore with aqueous hydrogen chloride at an elevated temperature to form a solution of titanium trichloride and ferrous chloride; (c) cooling and saturating the leach solution with gaseous hydrogen chloride to precipitate ferrous chloride; (d) separating the precipitated ferrous chloride from titanium trichloride solution; (e) raising the temperature of the last-named solution to about 20° to about 30° C. to precipitate hydrated titanium trichloride; and (f) separating and recovering the crystallized titanium trichloride from the leach liquor.
Claim 3
Dependent Claim
29 words
The process as set forth in claim 1 in which said roasted ore is leached at a temperature in the range of from about 80° to about 110° C.
Claim 4
Dependent Claim
32 words
The process as set forth in claim 1 in which said leach solution is saturated with hydrogen chloride at a temperature in the range of from about 0° to about 20° C.
Claim 5
Dependent Claim
19 words
The process as set forth in claim 1 in which said leach liquor is recycled to the leaching step.
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) | 1981-07-03 | 1982-01-02 | 1982-07-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-07-03 | 1986-01-02 | 1986-07-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-07-03 | 1990-01-02 | 1990-07-04 | $7700.00 | Window Closed / Lapsed |