Claims
- 1. A method of preparing a high-grade alloy from a low-grade ore, said low-grade ore comprising oxides of iron and a certain metal and said high-grade alloy comprising iron and a percentage of said metal which is greater than that present in said low-grade ore, said method comprising the steps of:
- providing an electric furnace having a hearth, said hearth being divided by divider means into first and second basins, said furnace further comprising electrodes in said first and second basins;
- feeding a first charge consisting of a major portion of said low-grade ore and a minor portion of a reductant into said first basin;
- applying an electric current to the charge in said first basin to reduce the iron oxide in said low-grade ore to form molten iron in said first basin and to form an enriched layer of molten charge and slag thereabove, said enriched layer having a higher percentage of said certain metal than said low-grade ore;
- allowing said layer to flow to said second basin;
- feeding a second charge of said low-grade ore and a greater portion of reductant into said second basin;
- applying an electric current to the materials within said second basin to form said high-grade alloy; and
- controlling the temperature and the amount of reductant in said first and second basins to cause substantially only iron to be reduced in said first basin and to form said high-grade alloy in said second basin.
- 2. The method set forth in claim 1 comprising the further steps of continuously feeding said charges to said first and second basins and tapping iron from said first basin and said high-grade alloy from said second basin.
- 3. The method set forth in claim 1 wherein said low-grade ore is a low-grade manganese ore and wherein said high-grade alloy is ferromanganese.
- 4. The method set forth in claim 3 wherein the ratio of manganese to iron in said low-grade ore is about 4-5:1 and the ratio of manganese to iron in said ferromanganese is 7-8:1.
- 5. The method set forth in claim 1 wherein said first furnace charge contains about 90 to 99% ore and about 1 to about 10% carbon as said reductant and said second furnace charge consists of about 70 to 85% ore and about 15 to about 30% carbon as said reductant.
- 6. The method set forth in claim 3 wherein said first furnace charge consists primarily of low-grade manganese ore having a manganese-to-iron ratio of about 4-5:1 and a small quantity of carbon and said second furnace charge consists of a major portion of said low-grade manganese ore and a minor portion of carbon, the proportion of carbon in said second furnace charge being about 10 to 20 times greater than the percentage of carbon in said first furnace charge.
- 7. The method set forth in claim 6 wherein the first charge is about 90 to 99% ore and about 10-1% carbon and said second furnace charge is about 70-85% ore and about 30-15% carbon.
- 8. The method set forth in claim 1 wherein said divider is formed of a carbon containing material and wherein a titanium containing material is added to said furnace charge for forming titanium carbide on the surface of said divider.
- 9. The method set forth in claim 1 wherein said low-grade ore is a chromium ore and said high-grade alloy is ferrochromium.
- 10. The method set forth in claim 9 wherein the ratio of chromium to iron in said low-grade ore is about 4-5:1 and the ratio of chromium to iron in said ferrochromium tapped from said second basin is about 7-8:1.
- 11. A method for producing high-grade ferromanganese from a low-grade manganese ore comprising the steps of:
- providing an electric arc furnace including a hearth having a divider therein to form two basins; said furnace having electrodes within said basins to apply an electric current and to heat materials contained therein;
- feeding a first charge consisting of a major portion of said low-grade manganese ore and a minor portion of carbon into said first basin;
- applying a current to said electrodes to melt said charge and to reduce the iron contained therein to form molten iron, the amount of carbon used in said first charge and the temperature within said first basin being sufficient to remove a substantial amount of the iron from said first charge without removing a substantial amount of the manganese therefrom;
- said feeding and applying steps being continued so that a pool of molten iron is formed in said first basin and a layer of molten ore and slag ore is formed thereabove, said molten pool filling said basin to a level adjacent to but below the height of said divider whereby said molten iron is not allowed to flow to said second basin but said molten ore and slag may freely flow thereto;
- feeding a second charge of said low-grade manganese ore and a greater proportion of carbon into said second basin whereby the materials contained therein include such second charge together with the manganese enriched molten layer and slag produced in said first basin;
- applying an electric current to the electrodes within said second basin to form a molten pool of ferromanganese therein, the amount of carbon and the temperature applied in said second zone being sufficient to produce said ferromanganese.
- 12. The method set forth in claim 11 wherein said charging and applying steps are performed continuously and wherein molten iron is tapped from said first basin and molten ferromanganese is tapped from said second basin.
- 13. The method set forth in claim 11 wherein the ratio of manganese to iron in said low-grade ore is about 4-5:1 and the ratio of manganese to iron in said ferromanganese is about 7-8:1.
- 14. A method for producing high-grade ferrochromium from a low-grade chromium ore comprising the steps of:
- providing an electric arc furnace including a hearth having a divider therein to form two basins; said furnace having electrodes within said basins to apply an electric current and to heat materials contained therein;
- feeding a first charge consisting of a major portion of said low-grade chromium ore and a minor portion of carbon into said first basin;
- applying a current to said electrodes to melt said charge and to reduce the iron contained therein to form molten iron, the amount of carbon used in said first charge and the temperature within said first basin being sufficient to remove a substantial amount of the iron from said first charge without removing a substantial amount of the chromium therefrom;
- said feeding and applying steps being continued so that a pool of molten iron is formed in said first basin and a layer of molten ore and slag ore is formed thereabove, said molten pool filling said basin to a level adjacent to but below the height of said divider whereby said molten iron is not allowed to flow to said second basin but said molten ore and slag may freely flow thereto;
- feeding a second charge of said low-grade chromium ore and a greater proportion of carbon into said second basin whereby the materials contained therein include such second charge together with the chromium enriched molten layer and slag produced in said first basin;
- applying an electric current to the electrodes within said second basin to form a molten pool of ferrochromium therein, the amount of carbon and the temperature applied in said second zone being sufficient to produce said ferrochromium.
- 15. The method set forth in claim 14 wherein said charging and applying steps are performed continuously and wherein molten iron is tapped from said first basin and molten ferrochromium is tapped from said second basin.
- 16. The method set forth in claim 14 wherein the ratio of chromium to iron in said low-grade chromium ore is about 4-5:1 and the ratio of chromium to iron in said ferrochromium is about 7-8:1.
- 17. A method for producing silicomanganese comprising the steps of:
- providing an electric furnace having a hearth, said hearth including dividing means to provide first and second basins within said hearth, electrodes being provided in said first and second basins for applying an electric current to heat the materials contained therein;
- feeding a first charge of high-grade manganese ore into said first basin together with an amount of carbon sufficient to reduce a substantial amount of the iron contained in said ore and a portion of the manganese contained therein;
- applying a charge to the electrodes in said first basin to generate a temperature therein sufficient to melt said ore and to reduce ferromanganese therefrom, producing a manganese rich layer of molten charge and slag thereabove, said ferromanganese forming a pool substantially filling said first basin;
- allowing said molten charge and slag to flow from said first basin to said second basin;
- feeding a second charge of lower-grade manganese containing ore into said second basin together with silica and carbon, the ratio of manganese-to-iron of said second charge ore being less than said ratio in said first charge;
- applying an electric current to the electrodes in said second basin to melt said charge and to form a molten pool of silicomanganese in said second basin.
- 18. The method set forth in claim 17 wherein the manganese-to-iron ratio of said high-grade manganese ore is about 7:1 and the ratio of manganese-to-iron in said lower-grade manganese ore is about 5:1.
- 19. The method set forth in claim 17 wherein the temperature within said second basin is higher than the temperature in said first basin.
CROSS-REFERENCE TO RELATED APPLICATIONS
This application is a continuation-in-part application of U.S. patent application Ser. No. 281,973 filed Jul. 10, 1981 now abandoned which in turn was a division of U.S. patent application Ser. No. 170,651, filed Jul. 21, 1980 and now U.S. Pat. No. 4,307,872 issued Dec. 29, 1981.
US Referenced Citations (4)
Divisions (1)
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Number |
Date |
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Parent |
170651 |
Jul 1980 |
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Continuation in Parts (1)
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Number |
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281973 |
Jul 1981 |
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