US2154130A - Beneficiating titaniferous ores - Google Patents
Beneficiating titaniferous ores Download PDFInfo
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- US2154130A US2154130A US157096A US15709637A US2154130A US 2154130 A US2154130 A US 2154130A US 157096 A US157096 A US 157096A US 15709637 A US15709637 A US 15709637A US 2154130 A US2154130 A US 2154130A
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- ore
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/10—Obtaining titanium, zirconium or hafnium
- C22B34/12—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
- C22B34/1236—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching
- C22B34/124—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching using acidic solutions or liquors
- C22B34/125—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching using acidic solutions or liquors containing a sulfur ion as active agent
Definitions
- Ilmenite is a mineral composed principally of titanium dioxide and ferrous oxide in the proportion of ferrous titanate, FeTiOs, together with minor amounts of other metallic or metallic oxide impurities. Whether or not the titanium dioxide and ferrous oxide are actually combined as ferrous titanate or merely intimately associated physically, as in solid solution, has not been established.
- This mineral as such, is found in many widely-scattered parts of the world, for instance, in Norway, India, and the United States. It is also found in physical association with other minerals, such as apatite, a calcium phosphate ore. Processes have been developed for separating the ilmenite from its association with these other minerals. Regardless of its source, 1.
- the yield of recoverable titanium values obtained from ground ilmenite when beneficiating this ore with sulfuric acid may vary to a certain degree directly to the extent that the particles of the ground ore are wet by the sulfuric acid. In general, when nearly all the particles are wet by the acid, the yields are high; when only a portion of the particles is wet, the yields are correspondingly lower. This is so because the particles which are not wet by the Q N sulfuric acid cling together and form agglomerates whose outside surface is the only portion attacked by the sulfuric acid.
- Our present invention comprises heating a mixture of ground titaniferous ore, concentrated sulfuric acid, and a phosphate compound in suitable proportions which, we believe will enable the sulfuric acid to wet and adhere to each individual particle of the ground ore.
- a wetting agent functions, in our opinion, to reduce the surface tension at the liquid-solid interphase between the individual particles of ore and the sulfuric acid.
- Phosphate compounds functioning as wetting agents are preferred for the practice of our invention.
- Pzos-content of a mixture of ground titaniferous ore and sulfuric acid is maintained between about 0.1 percent and about 2.0 percent, preferably between about 0.5 percent and about 1.0 percent during the heattreatment, which causes the reaction between the ore and acid to take place, improved yields of the titanium values are obtained.
- phosphoric acid may conveniently be added to the ore-sulfuric acid mixture in amounts sufficient to give the desired content of P205.
- any phosphate material such as a phosphate-bearing ore, e. g.
- apatite or a phosphate compound, e. g. trisodium phosphate, Na3PO4, which by reacting with the sulfuric acid of the reaction mixture yields phosphoric acid, may be employed in the practice of our invention.
- phosphate compounds as used in the claims attached hereto, we mean to designate those substances, such as phosphate minerals and phosphate compounds, which by interaction with sulfuric acid yield phosphoric acid.
- the phosphoric acid is added in any convenient manner, either to the ground ilmenite or concentrated sulfuric acid, or to the mixture of the two; or the three are mixed together simultaneously.
- the phosphoric acid is employed preferably as concentrated acid because, as will be understood, the concentration of the sulfuric acid will be reduced by the water added with the phosphoric acid.
- the relative proportions of ore and concentrated sulfuric acid need not be varied in any way from the common practice when practicing our invention, but the sulfuric acid may be employed in amounts sufficient to form normal salts with all base-forming elements present in the ore or, if desired, in amounts less than, or in excess of this chemically equivalent quantity. It is, however, economical to use as little sulfuric acid as possible and to obtain a more or less solid reaction cake.
- the heat-treatment is then carried out in any suitable manner, for example, according to the method set forth in U. S. Patent No. 1,889,027 of November 29, 1932, to W. F. Washburn. After the reaction is completed, the reaction mass is taken up in water in the usual way, and the resulting solution subjected to the usual treatments, such as clarification, etc., in order to obtain finally a sulfuric acid solution of the titanium originally present in the
- Table B Comparative yields-varying P205- contents [When the five reaction mixtures-Tests Nos. 1-5, Table A, were heated in the above-described manner, and the reaction products agialyzeg lfor titanium dioxide recovery, the following figures were 0 arm Percent P20 added to reac- Percent of T101- Test N 0. tion mixture content of are (based on ore recovered content) None 77. 39
- reaction masses obtained from the practice of our invention are especially useful in the preparation of titanium dioxide pigments, titanium salts, and the like.
- Method of beneficiating titaniferous ores which comprises mixing together ground titaniferous ore, concentrated sulfuric acid and a phosphate compound, the latter in such amounts that the resulting mixture will have a P205 content. based on the weight of ore in the mixture of between about 0.1 per cent and about 2.0 per cent and heating the said mixture to cause a reaction to take place between the ore and the sulfuric acid.
- Method of beneficiating titaniferous ores which comprises mixing together ground titaniferous ore, concentrated sulfuric acid and phosphoric acid, the latter in such amounts that the resulting mixture will have a P205 content, based on the weight of ore in the mixture of between about 0.1 per cent and about 2.0 per cent and heating the said mixture to cause a reaction to take place between the ore and the sulfuric acid.
- a method of ben-eficiating a titaniferous ore which includes a heat-treatment of a mixture of ground titaniferous ore and concentrated sulfuric acid
- the step which consists in adding to a mixture of ground titaniferous ore and concentrated sulfuric acid an amount of a phosphate compound such that the mixture will have a P205 content, based on the weight of ore in the said mixture, of between about 0.1 per cent and about 2.0 per cent.
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Description
Patented Apr. 11, 1939 UNlTED STATES BENEFIGIATING TITANIFEROUS ORES Franklin L. Kingsbury and William Grave, St. Louis, Mo., assignors to National Lead Company, New York, N. Y., a corporation of New Jersey No Drawing. Application August 3, 1937, Serial No. 157,096
4 Claims.
ducing of ilmenite with sulfuric acid. Ilmenite is a mineral composed principally of titanium dioxide and ferrous oxide in the proportion of ferrous titanate, FeTiOs, together with minor amounts of other metallic or metallic oxide impurities. Whether or not the titanium dioxide and ferrous oxide are actually combined as ferrous titanate or merely intimately associated physically, as in solid solution, has not been established. This mineral, as such, is found in many widely-scattered parts of the world, for instance, in Norway, India, and the United States. It is also found in physical association with other minerals, such as apatite, a calcium phosphate ore. Processes have been developed for separating the ilmenite from its association with these other minerals. Regardless of its source, 1. e., whether it was obtained as native ilmenite or by separation from associated contaminating minerals, and because it yields to attack by concentrated sulfuric acid, as distinguished from most ing mixture is then heated either by the application of external heat or by injecting live steam into the mass. When the temperature of the mass is raised sufiiciently, a reaction between the ilmenite and sulfuric acid sets in which, because of its exothermic character, requires no further added heat. It has been observed that the yields of recoverable titanium values obtainable from ilmenite secured from different sources by treating such ores with sulfuric acid varies considerably. Having addressed ourselves to this problem, we have developed means of increasing the yield values obtainable from ilmenite, regardless of its source, which means constitute the basis for our invention.
We have found that the yield of recoverable titanium values obtained from ground ilmenite when beneficiating this ore with sulfuric acid may vary to a certain degree directly to the extent that the particles of the ground ore are wet by the sulfuric acid. In general, when nearly all the particles are wet by the acid, the yields are high; when only a portion of the particles is wet, the yields are correspondingly lower. This is so because the particles which are not wet by the Q N sulfuric acid cling together and form agglomerates whose outside surface is the only portion attacked by the sulfuric acid.
Our present invention comprises heating a mixture of ground titaniferous ore, concentrated sulfuric acid, and a phosphate compound in suitable proportions which, we believe will enable the sulfuric acid to wet and adhere to each individual particle of the ground ore. Such a wetting agent functions, in our opinion, to reduce the surface tension at the liquid-solid interphase between the individual particles of ore and the sulfuric acid.
Phosphate compounds functioning as wetting agents are preferred for the practice of our invention. Thus, when the Pzos-content of a mixture of ground titaniferous ore and sulfuric acid is maintained between about 0.1 percent and about 2.0 percent, preferably between about 0.5 percent and about 1.0 percent during the heattreatment, which causes the reaction between the ore and acid to take place, improved yields of the titanium values are obtained. For example, phosphoric acid may conveniently be added to the ore-sulfuric acid mixture in amounts sufficient to give the desired content of P205. Although phosphoric acid, because of its availability is preferred, it will be understood that any phosphate material, such as a phosphate-bearing ore, e. g. apatite, or a phosphate compound, e. g. trisodium phosphate, Na3PO4, which by reacting with the sulfuric acid of the reaction mixture yields phosphoric acid, may be employed in the practice of our invention. By the expression phosphate compounds, as used in the claims attached hereto, we mean to designate those substances, such as phosphate minerals and phosphate compounds, which by interaction with sulfuric acid yield phosphoric acid. The phosphoric acid is added in any convenient manner, either to the ground ilmenite or concentrated sulfuric acid, or to the mixture of the two; or the three are mixed together simultaneously. The phosphoric acid is employed preferably as concentrated acid because, as will be understood, the concentration of the sulfuric acid will be reduced by the water added with the phosphoric acid. The relative proportions of ore and concentrated sulfuric acid need not be varied in any way from the common practice when practicing our invention, but the sulfuric acid may be employed in amounts sufficient to form normal salts with all base-forming elements present in the ore or, if desired, in amounts less than, or in excess of this chemically equivalent quantity. It is, however, economical to use as little sulfuric acid as possible and to obtain a more or less solid reaction cake. The heat-treatment is then carried out in any suitable manner, for example, according to the method set forth in U. S. Patent No. 1,889,027 of November 29, 1932, to W. F. Washburn. After the reaction is completed, the reaction mass is taken up in water in the usual way, and the resulting solution subjected to the usual treatments, such as clarification, etc., in order to obtain finally a sulfuric acid solution of the titanium originally present in the ore.
The improved results of our invention are readily perceived by examination of the following tabulated data:
Table A.Wetting of z'lmem'te are Test N 1 2 3 4 5 Percent P205 added (based on weight of ore) Percent settled after it hour These figures indicate a progressive decrease in the rate of settling, and thereby an increase in the extent the ore is wet by sulfuric acid as the Pros-content is increased.
Table B.Comparative yields-varying P205- contents [When the five reaction mixtures-Tests Nos. 1-5, Table A, were heated in the above-described manner, and the reaction products agialyzeg lfor titanium dioxide recovery, the following figures were 0 arm Percent P20 added to reac- Percent of T101- Test N 0. tion mixture content of are (based on ore recovered content) None 77. 39
The highest yields were obtained in this series of tests when adding but 0.40 percent P205, but the results are based on pilot plant tests and it is known that commercial operations always give higher yields than pilot plant tests.
Table C'.-Use of apatite (phosphate mineral) Test N0 1 2 3 4 5 Percent P added as apatite (based on weight of ore) Yield-percent T102 recovered.
None 76. 17
It will be understood that in determining the amount of phosphate to be added to the ore it may be desirable to determine first whether the titaniferous ore itself contains P206, and if so, to take this into account.
The reaction masses obtained from the practice of our invention are especially useful in the preparation of titanium dioxide pigments, titanium salts, and the like.
This description of our invention has been given for clearness of understanding and no undue limitations should be deduced therefrom, but the appended claims should be construed as broadly as possible in view of the prior art.
We claim:
1. Method of beneficiating titaniferous ores, which comprises mixing together ground titaniferous ore, concentrated sulfuric acid and a phosphate compound, the latter in such amounts that the resulting mixture will have a P205 content. based on the weight of ore in the mixture of between about 0.1 per cent and about 2.0 per cent and heating the said mixture to cause a reaction to take place between the ore and the sulfuric acid.
2. Method of beneficiating titaniferous ores, which comprises mixing together ground titaniferous ore, concentrated sulfuric acid and phosphoric acid, the latter in such amounts that the resulting mixture will have a P205 content, based on the weight of ore in the mixture of between about 0.1 per cent and about 2.0 per cent and heating the said mixture to cause a reaction to take place between the ore and the sulfuric acid.
3. Method of beneficiating titaniferous ores. which comprises mixing together ground titaniferous ore, concentrated sulfuric acid and ground apatite mineral, the latter in such amounts that the resulting mixture will have a P205 content, I
based on the Weight of ore in the mixture of between about 0.1 per cent and about 2.0 per cent and heating the said mixture to cause a reaction to take place between the ore and the sulfuric acid.
4. In a method of ben-eficiating a titaniferous ore which includes a heat-treatment of a mixture of ground titaniferous ore and concentrated sulfuric acid, the step which consists in adding to a mixture of ground titaniferous ore and concentrated sulfuric acid an amount of a phosphate compound such that the mixture will have a P205 content, based on the weight of ore in the said mixture, of between about 0.1 per cent and about 2.0 per cent.
FRANKLIN L. KINGSBURY. WILLIAM GRAVE.
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US157096A US2154130A (en) | 1937-08-03 | 1937-08-03 | Beneficiating titaniferous ores |
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US157096A US2154130A (en) | 1937-08-03 | 1937-08-03 | Beneficiating titaniferous ores |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2622006A (en) * | 1951-04-05 | 1952-12-16 | Nat Lead Co | Process for chlorinating titaniferous material |
US2622005A (en) * | 1951-04-05 | 1952-12-16 | Nat Lead Co | Method for chlorinating titaniferous material |
US2724637A (en) * | 1952-09-05 | 1955-11-22 | Nat Lead Co | Method for treating ore concentrates |
US2767053A (en) * | 1953-07-30 | 1956-10-16 | Nat Lead Co | Dissolution of titaniferous ore concentrates with amine addition |
US2822241A (en) * | 1953-08-17 | 1958-02-04 | Nat Lead Co | Digestion in sulphuric acid of titaniferous ore concentrates containing organic flotation agent |
DE1083244B (en) * | 1958-04-19 | 1960-06-15 | Giulini Ges Mit Beschraenkter | Process for the digestion of titanium ores with hydrochloric acid |
US20090226526A1 (en) * | 2005-10-28 | 2009-09-10 | Abdula Kurkayev | Nanoparticles of a heterocrystal mineral for use as a medicament and method of producing the same |
-
1937
- 1937-08-03 US US157096A patent/US2154130A/en not_active Expired - Lifetime
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2622006A (en) * | 1951-04-05 | 1952-12-16 | Nat Lead Co | Process for chlorinating titaniferous material |
US2622005A (en) * | 1951-04-05 | 1952-12-16 | Nat Lead Co | Method for chlorinating titaniferous material |
US2724637A (en) * | 1952-09-05 | 1955-11-22 | Nat Lead Co | Method for treating ore concentrates |
US2767053A (en) * | 1953-07-30 | 1956-10-16 | Nat Lead Co | Dissolution of titaniferous ore concentrates with amine addition |
US2822241A (en) * | 1953-08-17 | 1958-02-04 | Nat Lead Co | Digestion in sulphuric acid of titaniferous ore concentrates containing organic flotation agent |
DE1083244B (en) * | 1958-04-19 | 1960-06-15 | Giulini Ges Mit Beschraenkter | Process for the digestion of titanium ores with hydrochloric acid |
US20090226526A1 (en) * | 2005-10-28 | 2009-09-10 | Abdula Kurkayev | Nanoparticles of a heterocrystal mineral for use as a medicament and method of producing the same |
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