US1349322A - Process of treating oxid ores of manganese - Google Patents
Process of treating oxid ores of manganese Download PDFInfo
- Publication number
- US1349322A US1349322A US255388A US25538818A US1349322A US 1349322 A US1349322 A US 1349322A US 255388 A US255388 A US 255388A US 25538818 A US25538818 A US 25538818A US 1349322 A US1349322 A US 1349322A
- Authority
- US
- United States
- Prior art keywords
- manganese
- ores
- oxid
- ore
- treating
- 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
Classifications
-
- 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
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/005—Pretreatment specially adapted for magnetic separation
- B03C1/015—Pretreatment specially adapted for magnetic separation by chemical treatment imparting magnetic properties to the material to be separated, e.g. roasting, reduction, oxidation
Definitions
- the present invention is a novel process whereby oxid ores of manganese (including wateror other partial concentrates derived from such ores) are readily and economically concentrated to a marketable grade.
- the process involves subjecting the ores or partial concentrates to a reduction treatment, whereby certain chemical and physical changes are brought about, followed by magnetic treatment of the modified ore to produce the manganese concentrate.
- the reduction of the ore to the manganous oxid stage may be practised when some or all of the ore is present as the.
- the higher oxids of manganese present in the ore or partial concentrate are first reduced, either wholly or to a substantial extent, to the lowest or manganous oxid, MnO.
- the degree of subdivision of the ore necessary for proper reduction varies greatly: for example, some very porous ores require crushing only'to pass a 2 or 3 inch ring, while certain denser ores may require crush ing to 10 mesh or finer.
- Reduction is accomplished by heating the ore in presence of reducing gases, such for example as hydrogen, producer as, or the like, to a temperature of 300 or higher. The higher the temperature the more rapidly the reduction takes place.
- a multiple-hearth circular roasting furnace of the MacDougal type; a straight line furnace of the Edwards type; or rotary kilns either externally or internally fired; are all suitable for the purpose.
- the ore is next cooled in such manner as to avoid material reoxidation. This may be accomplishedby quenching the hot ore in water out of contact with air, or by cooling in a reducing atmosphere.
- the reduced and cooled ore is then crushed to whatever degree of subdivision may be necessary to liberate the particles of reduced manganese mineral from the gangue. This will vary with the particular ore, but in general any considerable portion of fines should be avoided.
- the properly subdivided reduced ore is then passed through a magnetic separator, which may be either of the wet or dry type.
- a magnetic separator which may be either of the wet or dry type.
- the middlings are re-crushed in order to free the mineral particles, and again passed through the magnetic separator.
- a useful variation of the process, applicable to'ores containing iron or other minerals more magnetic than the lower oxids of manganese, is to remove such minerals either before or after reduction as may be most readily accomplished, using for this purpose a magnetic field of lower intensity than thatrequired for the lower oxids of manganese.
- This operation is then followed by the passage of the ore after reduction (in case the reducing treatment was not applied before the first operation), through a magnetic separator having a sufficiently high magnetic intensity to effect the separation of the lower oxids of manganese from the sililca and other nonmagnetic gangue materia s.
- the process may also be combined with water-concentration, or other methods of concentration; and also with other processes for the recovery of any precious metal contained in the ore.
- One example of suchapplication is the case of a very low-grade ore from which a substantial portion of a manganese mineral containing silver may be separated by water-concentration.
- partial concentrate thus produced contains the major portion of the manganese and silver, and may be subjected to the reduction treatment, the silver being thereafter extracted by cyaniding or other method applicable to free-milling ores.
- the manganese content is brought to marketable grade, either before or after the recovery of the silver, by magnetic separation.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
UNITED STATES PATENT OFFICE.
GALEN HOWELL CLEVENGER, OF COLORADO SPRINGS, COLORADO, AND MARTINUS HENDRIGUS GABON,
or WELTEVREDEN,
JAVA, DUTCH EAST INDIES,
ASSIGNORS TO RESEARCH CORPORATION, OF NEW YORK, N. Y., A CORPORA- TION OF NEW YORK.
PROCESS OF TREATING OXID ORES OF MANGANESE.
No Drawing.
To all whom it may concern:
Be it known that we, (1) GALEN HOWELL CLEVENGER, a citizen of the United States, and (2) MARTINUS HENnRioUs GARoN, a subject of the Queen of Holland, reslding at (1) Colorado Springs, county of El Paso State of Colorado, and (2) Weltevreden, Java, Dutch East Indies, have invented certain new and useful Improvements in Processes of Treating ()xid Ores of Manganese, of which the following is a specification.
Considerable difficulty has been heretofore experienced in the preparation of marketable concentrates from low grade oxid ores of manganese. Water-concentration as ordinarily practised for the concentration of other ores is at best applicable only to certain types of manganese ores, and in general does not afford a very high recovery. Flotation as now practised is not applicable to ores of this type.
The present invention is a novel process whereby oxid ores of manganese (including wateror other partial concentrates derived from such ores) are readily and economically concentrated to a marketable grade. The process involves subjecting the ores or partial concentrates to a reduction treatment, whereby certain chemical and physical changes are brought about, followed by magnetic treatment of the modified ore to produce the manganese concentrate.
It is well known that simple application of heat to manganese dioXid-results in the expulsion of a portion of the oxygen, yielding manganic oxid Mn O This is generally more magnetic than the dioxid. We have discovered that when manganic oxid is further reduced, the resulting lower oxids, including the so-called manganous-manganic oxid Mn O and more especially manganous oxid MnO are still more strongly magnetic, and can be more readily and completely separated from the gangue. Moreover the heat treatment under reducing conditions tends to consolidate the original fine amorphous material and to impart to it a more or less crystalline character. The physical changes undergone by the ore are of such nature that it breaks more freely from the gangue when crushed, and is decidedly more susceptible to treatment by magnetic separation.
It is not necessary in all cases to carry Specification of Letters Patent.
Patented Aug. 10, 1920.
Application filed September 23, 1918. Serial No. 255,388.
the reduction of the ore to the manganous oxid stage, as the invention may be practised when some or all of the ore is present as the.
' with the invention is as follows it being understood that the invention is not restricted to the details of the manipulative treatment:
The higher oxids of manganese present in the ore or partial concentrate are first reduced, either wholly or to a substantial extent, to the lowest or manganous oxid, MnO. The degree of subdivision of the ore necessary for proper reduction varies greatly: for example, some very porous ores require crushing only'to pass a 2 or 3 inch ring, while certain denser ores may require crush ing to 10 mesh or finer. Reduction is accomplished by heating the ore in presence of reducing gases, such for example as hydrogen, producer as, or the like, to a temperature of 300 or higher. The higher the temperature the more rapidly the reduction takes place. A multiple-hearth circular roasting furnace of the MacDougal type; a straight line furnace of the Edwards type; or rotary kilns either externally or internally fired; are all suitable for the purpose.
The ore is next cooled in such manner as to avoid material reoxidation. This may be accomplishedby quenching the hot ore in water out of contact with air, or by cooling in a reducing atmosphere. The reduced and cooled ore is then crushed to whatever degree of subdivision may be necessary to liberate the particles of reduced manganese mineral from the gangue. This will vary with the particular ore, but in general any considerable portion of fines should be avoided.
The properly subdivided reduced ore is then passed through a magnetic separator, which may be either of the wet or dry type. We have found the Wetherill separator particularly well suited to this work, which in general requires a rather high magnetic intensity. There generally result three prodnets, to wit: the concentrate which is sufficiently high-grade for marketing; the tailings which can be rejected; and themiddlings which require further treatment. The middlings are re-crushed in order to free the mineral particles, and again passed through the magnetic separator.
A useful variation of the process, applicable to'ores containing iron or other minerals more magnetic than the lower oxids of manganese, is to remove such minerals either before or after reduction as may be most readily accomplished, using for this purpose a magnetic field of lower intensity than thatrequired for the lower oxids of manganese. This operation is then followed by the passage of the ore after reduction (in case the reducing treatment was not applied before the first operation), through a magnetic separator having a sufficiently high magnetic intensity to effect the separation of the lower oxids of manganese from the sililca and other nonmagnetic gangue materia s.
The process may also be combined with water-concentration, or other methods of concentration; and also with other processes for the recovery of any precious metal contained in the ore. One example of suchapplication is the case of a very low-grade ore from which a substantial portion of a manganese mineral containing silver may be separated by water-concentration. The
partial concentrate thus produced contains the major portion of the manganese and silver, and may be subjected to the reduction treatment, the silver being thereafter extracted by cyaniding or other method applicable to free-milling ores. The manganese content is brought to marketable grade, either before or after the recovery of the silver, by magnetic separation.
1. Process of treating oxid ores of mananese com risin effectin reduction there-- of to a-state lower than the manganic oxid state, and then concentrating the manganese content by magnetic separation.
2. Process of treating oxid ores of manganese, comprising effecting reduction thereof to a state lower than the manganic oxid state, cooling the reduced ore under conditions to avoid reoxidation, and then concentrating the manganese content by magnetic separation.
3. Process of treating oxicl ores of manganese, comprising etfecting reduction thereof substantially to the state of maganous oxid, and then concentrating the manganese content by magnetic separation.
4. Process of treating oxid ores of manganese, comprising efi'ecting reduction thereof substantiallyto the state of manganous oxid, cooling the reduced ore .under conditions to avoid reoxidation, and the'n concentrating the manganese content by magnetic separation.
5, Process of treating oxid ores of manganese containing silver, comprising concentrating the manganese and silver contents thereof; subjecting the resulting partial concentrate to a reducing treatment; and
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US255388A US1349322A (en) | 1918-09-23 | 1918-09-23 | Process of treating oxid ores of manganese |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US255388A US1349322A (en) | 1918-09-23 | 1918-09-23 | Process of treating oxid ores of manganese |
Publications (1)
Publication Number | Publication Date |
---|---|
US1349322A true US1349322A (en) | 1920-08-10 |
Family
ID=22968100
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US255388A Expired - Lifetime US1349322A (en) | 1918-09-23 | 1918-09-23 | Process of treating oxid ores of manganese |
Country Status (1)
Country | Link |
---|---|
US (1) | US1349322A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2830890A (en) * | 1955-07-22 | 1958-04-15 | Strategic Udy Metallurg & Chem | Process for the production of ferromanganese from low-grade manganese-bearing materials |
US3149961A (en) * | 1961-09-27 | 1964-09-22 | R N Corp | Processing of manganiferous ores |
US3864118A (en) * | 1973-02-07 | 1975-02-04 | Bethlehem Steel Corp | Method for producing manganese oxide pellets |
US4020143A (en) * | 1974-08-26 | 1977-04-26 | Kennecott Copper Corporation | Use of raw manganese nodules for oxidation leaching of reductively roasted manganese nodules |
US4044094A (en) * | 1974-08-26 | 1977-08-23 | Kennecott Copper Corporation | Two-stage fluid bed reduction of manganese nodules |
-
1918
- 1918-09-23 US US255388A patent/US1349322A/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2830890A (en) * | 1955-07-22 | 1958-04-15 | Strategic Udy Metallurg & Chem | Process for the production of ferromanganese from low-grade manganese-bearing materials |
US3149961A (en) * | 1961-09-27 | 1964-09-22 | R N Corp | Processing of manganiferous ores |
US3864118A (en) * | 1973-02-07 | 1975-02-04 | Bethlehem Steel Corp | Method for producing manganese oxide pellets |
US4020143A (en) * | 1974-08-26 | 1977-04-26 | Kennecott Copper Corporation | Use of raw manganese nodules for oxidation leaching of reductively roasted manganese nodules |
US4044094A (en) * | 1974-08-26 | 1977-08-23 | Kennecott Copper Corporation | Two-stage fluid bed reduction of manganese nodules |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3160496A (en) | Process for treating ironpyrites | |
US1349322A (en) | Process of treating oxid ores of manganese | |
US2556215A (en) | Method of producing high-grade iron oxide from ores rich in nickeliferous pyrrhotite | |
US4368176A (en) | Desulfurizing roast of pyrite bearing polymetallic raw material | |
US3589892A (en) | Process for liberating copper from sulfide ores | |
US3149961A (en) | Processing of manganiferous ores | |
CN106756093B (en) | A kind of refractory zinc oxide material thermochemical surface modification-flotation recovery method of lead and zinc | |
US4135913A (en) | Thermal concentration of non-ferrous metal values in sulfide minerals | |
CN115066390B (en) | Process for producing copper metal from copper concentrate without generating waste | |
US3313601A (en) | Recovery of metal values from oxygenated ores | |
US2765988A (en) | Reduction of iron ores | |
US1348068A (en) | Process for the treatment of manganese ores | |
US1901102A (en) | Ore conditioning process | |
US1822995A (en) | Metallurgical process | |
US1506663A (en) | Treatment of oxidized ores | |
US1518626A (en) | Treatment of copper-lead matte | |
US2756136A (en) | Method of chloridizing sintering of zinciferous materials with elimination of lead and similar contaminants | |
US3856505A (en) | Process for obtaining nickel concentrates from nickel oxide ores | |
US3068090A (en) | Alkali metal salts and base additions in non-titaniferous ore reductions | |
US3479177A (en) | Process for removing arsenic from arsenic-containing iron minerals | |
US1546854A (en) | Ore treatment | |
US1727492A (en) | Process of recovering cadmium | |
US1401733A (en) | Desulfurization of zinc sulfid ores | |
US722809A (en) | Method of treating ores. | |
US1874370A (en) | Method of treating ores |