US3281235A - Method for concentrating ores - Google Patents
Method for concentrating ores Download PDFInfo
- Publication number
- US3281235A US3281235A US395048A US39504864A US3281235A US 3281235 A US3281235 A US 3281235A US 395048 A US395048 A US 395048A US 39504864 A US39504864 A US 39504864A US 3281235 A US3281235 A US 3281235A
- Authority
- US
- United States
- Prior art keywords
- ores
- ore
- minette
- iron
- gangue
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title description 27
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- 229910052595 hematite Inorganic materials 0.000 description 7
- 239000011019 hematite Substances 0.000 description 7
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 description 7
- 229910052742 iron Inorganic materials 0.000 description 6
- 239000012141 concentrate Substances 0.000 description 5
- 239000013078 crystal Substances 0.000 description 5
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 5
- 238000001816 cooling Methods 0.000 description 3
- 235000013980 iron oxide Nutrition 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 2
- 239000006148 magnetic separator Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000003801 milling Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000010587 phase diagram Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/02—Roasting processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B1/00—Conditioning for facilitating separation by altering physical properties of the matter to be treated
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B1/00—Conditioning for facilitating separation by altering physical properties of the matter to be treated
- B03B1/02—Preparatory heating
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/02—Well-drilling compositions
-
- 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
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
Definitions
- the present invention relates to a method of concentrating ores, especially minette ores (oolitic iron ores) from which the gangue or matrix is substantially eliminated after a crushing operation While separating the hematite content therefrom.
- the ores are first subjected to a selected crushing operation by means of which the ore is divided into the more concentrated oolite fraction and the gangue.
- a selected crushing operation by means of which the ore is divided into the more concentrated oolite fraction and the gangue.
- autogenous milling methods are employed.
- the method of magnetized roasting has heretofore been employed.
- the pre-concentrate is heated to a temperature of approximately 1,000 C. and is reduced by hydrogen, carbon or methane so as to form magnetite.
- the goods are subjected for a longer period of time to this temperature.
- an object of the present invention to provide a method of separating ores, especially minette ores, by means of which it is possible to produce in a very simple manner highly concentrated ores with a very low gangue content.
- the method according to the present invention is characterized primarily in that the ores are, prior to being crushed, heated to a temperature at which on one had a melting phase is formed and at which, on the other hand, the hematite does not yet become decomposed, and in that subsequently, this condition is so-to-speak frozen by means of a fast cooling process.
- idiomorpheous hematites are formed in which practically the entire iron contents of the ore are 3,281,235 Patented Oct. 25, 1966 ICC concentrated. These hematites are embedded in the melt which approximately represents the entire gangue. In this way, the ultra-fine structure of the ore is destroyed. During the disintegrating process, therefore, a concentrate is obtained which is almost entirely free of gangue.
- the gangue melts in a temperature range in which the hematite does not become decomposed or disintegrated.
- a particularly favorable melt of the gangue is obtained with minette ore mixtures.
- the heating of the ores necessary according to the present invention may, for instance, be effected according to the so-called fluidized bed method.
- various other known methods and devices are applicable. It is not deemed necessary to go into the details of these known methods.
- the separation to be effected after the freezing of the melt and the subsequent crushing or milling may also be efiected in any convenient manner, for instance by means of a high power field magnetic separator.
- Example A minette ore concentrate was heated to slightly more than 1200 C. (The limit in the phase diagram for the CaO/Fe O system at 1230 C. is lowered by approximately 30 C. due to the presence of SiO and A1 0 The thus obtained condition of the minette ore concentrate was frozen by a fast cooling process in which the temperature dropped from 120 0 C. to 1000 in a time period of about 3 minutes.
- the iron content of the oolite is practically completely crystallized in perfect hematite crystals in an almost iron-free calcic silicious and almuinous glass phase. Due to the fast cooling process, the melting phase contains hair-like gaps and the original form of the ool-ites can still be recognized.
- the length of the edges of the hematite crystals amounts to approximately 25 to 30 microns. If subsequently the obtained product is milled so as to have a mean size of approximately 40 microns, the hematite phase can easily be separated from the remainder.
- a method of concentrating iron ore including iron oxide which comprises; heating the ore to about 1200 C. for a length of time to cause crystallization of the iron oxide into hematite crystals, quickly reducing the temperature of the heated ore to preserve the crystals, crushing the cooled ore, and separating out the said crystals.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Geology (AREA)
- Geochemistry & Mineralogy (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Environmental & Geological Engineering (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
United States Patent M 3,281,235 METHOD FOR CON CENTRATHNG ORES Hannes Anna, Oelde, Westphalia, Germany, assignor to Polysius G.m.b.H., Neubeckum, Germany No Drawing. Filed Sept. 8, 1964, Ser. No. 395,048 Claims priority, applicatio; Germany, Sept. 16, 1963,
,593 1 Claim. (Ci. 75-1) The present invention relates to a method of concentrating ores, especially minette ores (oolitic iron ores) from which the gangue or matrix is substantially eliminated after a crushing operation While separating the hematite content therefrom.
With heretofore known methods for pre-concentrating base or low-grade ores, especially minette ores, the ores are first subjected to a selected crushing operation by means of which the ore is divided into the more concentrated oolite fraction and the gangue. For this purpose, generally autogenous milling methods are employed.
For purposes of further concentrating this pro-concentrate, aside from so-called flotation methods and other separating methods employing a wet process, the method of magnetized roasting has heretofore been employed. According to this last-mentioned method, the pre-concentrate is heated to a temperature of approximately 1,000 C. and is reduced by hydrogen, carbon or methane so as to form magnetite. In order to obtaind as complete a reduction as possible, the goods are subjected for a longer period of time to this temperature. Subsequently, the goods .are milled in a wet process and are separated in a low power field magnetic separator.
With this known method the drawback is encountered that in spite of relatively high heat consumption with numerous ores, especially minette ores, only a rather small concentration can be obtained. With minette ores, this is due to the fine granularity and the ultra-fine distribution of the water containing iron oxides, which two factors bring about that with the improvement in the magnetic properties, basically only the high-grade iron particles are separated from the low-grade particles contained in the goods.
Furthermore, various methods of directly reducing minette ores to metallic iron are known. It is, however, doubtful whether these methods are very economical.
It is, therefore, an object of the present invention to provide a method of separating ores, especially minette ores, by means of which it is possible to produce in a very simple manner highly concentrated ores with a very low gangue content.
It is a further object of the present invention to provide -a method as set forth in the preceding paragraph by means of which the ores can very easily be separated from the gangue.
The method according to the present invention is characterized primarily in that the ores are, prior to being crushed, heated to a temperature at which on one had a melting phase is formed and at which, on the other hand, the hematite does not yet become decomposed, and in that subsequently, this condition is so-to-speak frozen by means of a fast cooling process.
According to the method of the present invention, very well crystallized idiomorpheous hematites are formed in which practically the entire iron contents of the ore are 3,281,235 Patented Oct. 25, 1966 ICC concentrated. These hematites are embedded in the melt which approximately represents the entire gangue. In this way, the ultra-fine structure of the ore is destroyed. During the disintegrating process, therefore, a concentrate is obtained which is almost entirely free of gangue.
As will be evident from the above, it is essential for the method according to the present invention, that the gangue melts in a temperature range in which the hematite does not become decomposed or disintegrated. A particularly favorable melt of the gangue is obtained with minette ore mixtures.
The heating of the ores necessary according to the present invention may, for instance, be effected according to the so-called fluidized bed method. However, also various other known methods and devices are applicable. It is not deemed necessary to go into the details of these known methods. The separation to be effected after the freezing of the melt and the subsequent crushing or milling may also be efiected in any convenient manner, for instance by means of a high power field magnetic separator.
In order further to clarify the essence of the present invention, the following example may be given:
Example A minette ore concentrate was heated to slightly more than 1200 C. (The limit in the phase diagram for the CaO/Fe O system at 1230 C. is lowered by approximately 30 C. due to the presence of SiO and A1 0 The thus obtained condition of the minette ore concentrate was frozen by a fast cooling process in which the temperature dropped from 120 0 C. to 1000 in a time period of about 3 minutes.
As microphotos show, the iron content of the oolite is practically completely crystallized in perfect hematite crystals in an almost iron-free calcic silicious and almuinous glass phase. Due to the fast cooling process, the melting phase contains hair-like gaps and the original form of the ool-ites can still be recognized. The length of the edges of the hematite crystals amounts to approximately 25 to 30 microns. If subsequently the obtained product is milled so as to have a mean size of approximately 40 microns, the hematite phase can easily be separated from the remainder.
It is, of course, to be understood that the present invention is, by no means, limited to the particular method described above, but comprises any modifications within the scope of the appended claims.
What is claimed is:
A method of concentrating iron ore including iron oxide which comprises; heating the ore to about 1200 C. for a length of time to cause crystallization of the iron oxide into hematite crystals, quickly reducing the temperature of the heated ore to preserve the crystals, crushing the cooled ore, and separating out the said crystals.
References Cited by the Examiner UNITED STATES PATENTS 1,655,608 1/1928 Hyde -5 1,847,596 3/1932 Cavers et al. 75-5 2,648,600 1/1950 Reeve 751 BENJAMIN HENKIN, Primary Examiner.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEP32593A DE1187202B (en) | 1963-09-16 | 1963-09-16 | Process for enriching ores |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3281235A true US3281235A (en) | 1966-10-25 |
Family
ID=7372825
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US395048A Expired - Lifetime US3281235A (en) | 1963-09-16 | 1964-09-08 | Method for concentrating ores |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US3281235A (en) |
| BE (1) | BE652311A (en) |
| DE (1) | DE1187202B (en) |
| GB (1) | GB1049208A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3867128A (en) * | 1972-12-18 | 1975-02-18 | Jr James Thomas Hancock | Process for producing high specific gravity material from low grade iron ore |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1655608A (en) * | 1926-12-22 | 1928-01-10 | Dwight & Lloyd Sintering Compa | Process for treating aluminum-bearing ores |
| US1847596A (en) * | 1928-11-26 | 1932-03-01 | Thomas W Cavers | Art of sintering ore fines, flue dust, sulphide, or other concentrates |
| US2648600A (en) * | 1948-11-19 | 1953-08-11 | United Steel Companies Ltd | Concentration of iron ore |
-
1963
- 1963-09-16 DE DEP32593A patent/DE1187202B/en active Pending
-
1964
- 1964-08-26 BE BE652311D patent/BE652311A/xx unknown
- 1964-08-31 GB GB35531/64A patent/GB1049208A/en not_active Expired
- 1964-09-08 US US395048A patent/US3281235A/en not_active Expired - Lifetime
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1655608A (en) * | 1926-12-22 | 1928-01-10 | Dwight & Lloyd Sintering Compa | Process for treating aluminum-bearing ores |
| US1847596A (en) * | 1928-11-26 | 1932-03-01 | Thomas W Cavers | Art of sintering ore fines, flue dust, sulphide, or other concentrates |
| US2648600A (en) * | 1948-11-19 | 1953-08-11 | United Steel Companies Ltd | Concentration of iron ore |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3867128A (en) * | 1972-12-18 | 1975-02-18 | Jr James Thomas Hancock | Process for producing high specific gravity material from low grade iron ore |
Also Published As
| Publication number | Publication date |
|---|---|
| DE1187202B (en) | 1965-02-18 |
| BE652311A (en) | 1964-12-16 |
| GB1049208A (en) | 1966-11-23 |
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