Patent US3977863A successfully refreshed from Google Patents.
US3977863A
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Process for selectively chlorinating the titanium content of titaniferous materials
Assignee: EIDP Inc
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Filing: 1975-02-26
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Granted: 1976-08-31
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Expires: 1995-02-26
Abstract
Abstract A reduction/chlorination process is provided for the treatment of titaniferous materials such as ilmenite ores. The chlorination is selective in that the titanium constituent of the titaniferous material is chlorinated, but there is no appreciable net yield of iron chloride from the iron constituent. Where other metals such as vanadium are present they may be chlorinated with the titanium. The reduction utilizes as the reductant an amount of carbonaceous material which, based on oxygen in the titaniferous material, is at least stoichiometric to produce carbon monoxide. The selective chlorination utilizes as the chlorinating agent either ferrous chloride (FeCl 2 ) alone or certain combinations of ferrous chloride and one or more other chlorine-containing members, notably molecular chlorine (Cl 2 ) and hydrogen chloride (HCl). The use of ferric chloride (FeCl 3 ) as a part or all of the chlorinating agent is the equivalent of using a FeCl 2 /0.5 Cl 2 mixture. Preferably, sufficient chlorine atoms are provided by the chlorinating agent to react with essentially all of the titanium in the titaniferous material. An elevated temperature in the range of 950° to 1400°C. is maintained during the chlorination, but depending upon the composition of the chlorinating agent, there may be a minimum temperature in the range which is needed to maintain selectivity.
Inventors
- 👤 Hans Hellmut Glaeser
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 14:33
CPC Classifications
C; C22; C22B; C22B34/00; C22B34/10; C22B34/12; C22B34/1218; C22B34/1222; Y; Y02; Y02P; Y02P10/00; Y02P10/20
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
162 words
Process for chlorinating the titanium constituent of a titaniferous material without an appreciable net yield of iron chloride from the iron constituent of said titaniferous material determined on the basis of said titaniferous material prior to contact with a chlorinating agent, whereby said iron constituent is recoverable in the metallic state, by intimately contacting said material with a chlorinating agent at an elevated temperature of 950° to 1400°C. and in the presence of a carbonaceous reductant, said chlorinating agent comprising FeCl 2 and HCl, the amount of said chlorinating agent being sufficient to furnish at least 4 chlorine atoms per atom of titanium in the titaniferous material and the ratio in the chlorinating agent of the atoms of chlorine provided by the HCl to FeCl 2 being no more than about 4, the atomic ratio of carbon in said carbonaceous reductant to oxygen in said material being at least about 1, whereby said ratio is at least stoichiometric to produce carbon monoxide.
Claim 2
Dependent Claim
162 words
Process for chlorinating the titanium constituent of a titaniferous material without an appreciable net yield of iron chloride from the iron constituent of said titaniferous material determined on the basis of said titaniferous material prior to contact with a chlorinating agent, whereby said iron constituent is recoverable in the metallic state, by intimately contacting said material with a chlorinating agent at an elevated temperature of 950° to 1400°C. and in the presence of a carbonaceous reductant, said chlorinating agent comprising FeCl 2 and HCl, the amount of said chlorinating agent being sufficient to furnish at least 4 chlorine atoms per atom of titanium in the titaniferous material and the ratio in the chlorinating agent of the atoms of chlorine provided by the HCl to FeCl 2 being no more than about 4, the atomic ratio of carbon in said carbonaceous reductant to oxygen in said material being at least about 1, whereby said ratio is at least stoichiometric to produce carbon monoxide.
Claim 3
Dependent Claim
23 words
Process according to claim 1 wherein the titaniferous material contains in excess of about 10% by weight each of titanium and of iron.
Claim 4
Dependent Claim
21 words
Process according to claim 1 wherein the titaniferous material is an oxidic ore containing about 20 to 50% by weight titanium.
Claim 5
Dependent Claim
37 words
Process according to claim 1 wherein the carbon in said carbonaceous reductant is present in an amount of at least 10% exccess over the stoichiometric amount required to react with all of the oxygen in said material.
Claim 6
Dependent Claim
11 words
Process according to claim 1 wherein the carbonaceous material is carbon.
Claim 7
Dependent Claim
17 words
Process according to claim 5 wherein said carbon has a particle size from 0.1 to 10 mm.
Claim 8
Dependent Claim
15 words
Process according to claim 5 wherein said carbon is selected from charcoal, coal or coke.
Claim 9
Dependent Claim
10 words
Process according to claim 7 wherein said carbon is charcoal.
Claim 10
Dependent Claim
10 words
Process according to claim 7 wherein said carbon is coal.
Claim 11
Dependent Claim
10 words
Process according to claim 7 wherein said carbon is coke.
Claim 12
Dependent Claim
27 words
Process according to claim 1 wherein the reaction is carried out to chlorinate at least about 75% by weight of the titanium content of the titaniferous material.
Claim 13
Dependent Claim
29 words
Process according to claim 1 wherein the reaction is carried out to convert at least about 90% by weight of the iron in the titaniferous material to metallic iron.
Claim 14
Dependent Claim
195 words
Process for chlorinating the titanium constituent of a titaniferous material without an appreciable net yield of iron chloride from the iron constituent of said titaniferous material determined on the basis of said titaniferous material prior to contact with a chlorinating agent, whereby said iron constituent is recoverable in the metallic state, by the steps of 1. mixing said titaniferous material with a carbonaceous reductant, the atomic ratio of carbon in said carbonaceous reductant to oxygen in said titaniferous material being at least about 1, whereby said ratio is at least stoichiometric to produce carbon monoxide, 2. heating the mixture of step (1) to a temperature of at least 500°C. to at least partially prereduce said titaniferous material, and 3. intimately contacting the heated mixture of step (2) with a chlorinating agent at an elevated temperature of 950° to 1400°C., said chlorinating agent comprising FeCl 2 and HCl, the amount of said chlorinating agent being sufficient to furnish at least 4 chlorine atoms per atom of titanium in said titaniferous material and the ratio in the chlorinating agent of the atoms of chlorine provided by the HCl to FeCl 2 being no more than about 4.
Claim 15
Dependent Claim
195 words
Process for chlorinating the titanium constituent of a titaniferous material without an appreciable net yield of iron chloride from the iron constituent of said titaniferous material determined on the basis of said titaniferous material prior to contact with a chlorinating agent, whereby said iron constituent is recoverable in the metallic state, by the steps of 1. mixing said titaniferous material with a carbonaceous reductant, the atomic ratio of carbon in said carbonaceous reductant to oxygen in said titaniferous material being at least about 1, whereby said ratio is at least stoichiometric to produce carbon monoxide, 2. heating the mixture of step (1) to a temperature of at least 500°C. to at least partially prereduce said titaniferous material, and 3. intimately contacting the heated mixture of step (2) with a chlorinating agent at an elevated temperature of 950° to 1400°C., said chlorinating agent comprising FeCl 2 and HCl, the amount of said chlorinating agent being sufficient to furnish at least 4 chlorine atoms per atom of titanium in said titaniferous material and the ratio in the chlorinating agent of the atoms of chlorine provided by the HCl to FeCl 2 being no more than about 4.
Claim 16
Dependent Claim
17 words
Process according to claim 13 wherein in step (2) said mixture is heated to at least 950°C.
Claim 17
Dependent Claim
15 words
Process according to claim 13 wherein in step (2) said mixture is heated to 1100°C.
Claim 18
Dependent Claim
17 words
Process according to claim 15 wherein in step (2) said mixture is heated for about 2 hours.
References Cited (Backward Citations)
DE1045382B
Cited
US3859077A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-08-31 | 1980-03-01 | 1980-08-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-08-31 | 1984-03-01 | 1984-08-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-08-31 | 1988-03-01 | 1988-08-31 | $7700.00 | Window Closed / Lapsed |