US829907A - Process of reduction of iron, &c., from their ores. - Google Patents
Process of reduction of iron, &c., from their ores. Download PDFInfo
- Publication number
- US829907A US829907A US16770003A US1903167700A US829907A US 829907 A US829907 A US 829907A US 16770003 A US16770003 A US 16770003A US 1903167700 A US1903167700 A US 1903167700A US 829907 A US829907 A US 829907A
- Authority
- US
- United States
- Prior art keywords
- iron
- ores
- sulfid
- oxid
- metal
- 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
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title description 42
- 229910052742 iron Inorganic materials 0.000 title description 20
- 238000000034 method Methods 0.000 title description 12
- 229910052751 metal Inorganic materials 0.000 description 22
- 239000002184 metal Substances 0.000 description 22
- 150000002739 metals Chemical class 0.000 description 9
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 229910052717 sulfur Inorganic materials 0.000 description 6
- 239000011593 sulfur Substances 0.000 description 6
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000011019 hematite Substances 0.000 description 4
- 229910052595 hematite Inorganic materials 0.000 description 4
- 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 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- -1 lead and copper Chemical class 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- MBMLMWLHJBBADN-UHFFFAOYSA-N Ferrous sulfide Chemical compound [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 230000003993 interaction Effects 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
- 239000006028 limestone Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052683 pyrite Inorganic materials 0.000 description 1
- 239000011028 pyrite Substances 0.000 description 1
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 1
- 229910052952 pyrrhotite Inorganic materials 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
-
- 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
- C22B5/00—General methods of reducing to metals
- C22B5/02—Dry methods smelting of sulfides or formation of mattes
- C22B5/10—Dry methods smelting of sulfides or formation of mattes by solid carbonaceous reducing agents
Definitions
- This invention relates to improvementsin the reduction of iron and other metals from their ores and the object of this invention is to effect such reduction by the interaction of the ores Without the intervention of a reducingblast such as is involved in the usual blastfurnace operations.
- My invention consists in treating the oxid and sulfid of iron or similar refractory oxid and sulfid ores in an electric furnace, the proportion of the oxid and sulfid mecanic such that a portion of the sulfur will be expelled and the remainder taken up by the oxygen of the ore, and nearly the whole of the iron or metal will be freed in the metallic state.
- the process is applicable to other'metals of the iron groupsuch as nickel, cobalt, and manganese.
- I may use any suit able oxid ores, such as hematite or magnetite, and I may usethe carbonate in lace of the oxid, it being understood that in the heat of. the electric furnace the carbonicacid gas would pass off, leaving an oxid.
- I may use pyrites or other sulfid ore or waste products containing iron sulfid. Some ores contain both oxid and sulfid, and such are readily utilizable in this process, enough being added of the deficient ingredient to make up the proper relative roportion.
- Waste products containing part y roasted sulfid or sulfid together with sulfate are'also utilizable, due allowance .being made for the proportions of oxygen present.
- the silica or other gangue associated with-the ores is converted to a sla and the coalescence of the reduced metal facilitated by the addition of a suitable fluxing materialsuch, for instance, as limestone.
- Hematite and pyrites both in pulverized or crushed state, are mixed in the proportions, say, of two of hematite to one. of pyrite, by Weight, and are placed with a suitable amount of fluxing material in an electric furnace, and a current of sufficient intensity and volume passed through the mass to meltvit and to furnish the heat necessary for the reaction.
- the temperature required to bring aboutthe reaction is considerably higher than is attained in the ordinary iron blast-furnace.
- the precise temperature can not be definitely stated, hood of 3,000 to 4,000 centigrade and possibly higher. I After-the mass has reached a molten condition the current is increased, thereby raising the temperature.
- chrome-iron can be obtained by melting an oxid of chromium with a sulfid of iron or generally a mixture of ores of difieir-nt metals of the iron or chromium groups or complex ores of such groups, such as pyrrhotite, may be used to give any desired alloy.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
. CHARLES S. BRADLEY, YORK, N. Y.
PROCESS OF REDUCTION OF IRON, 800., FROM THEIR ORES- Specification of Letters Patent.
Patented Aug. 28, 1906.
Application filed July 31, 1903. Serial No. 167,700.
To all whom/it may concern:
Be it known that I, CHARLES S. BRADLEY, a citizen of the United States, residing at New York, in the county and State of New York, have invented certain new and useful Improvements in the Reduction of Iron and other Metals from Their Ores, of which the following is a specification.
This invention relates to improvementsin the reduction of iron and other metals from their ores and the object of this invention is to effect such reduction by the interaction of the ores Without the intervention of a reducingblast such as is involved in the usual blastfurnace operations.
It is known that some metals, such as lead and copper, can be reduced by fusing together suitable proportions of their oxids and sulfids, the sulfur and oxygen of the ores combining to form sulfur dioxid, which passes off, while the metal from both kinds of ore remains in substantially pure condition. So
far as I know such a process has not been attempted in connection with iron or if attempted has not been commercially success- The reaction required in the case of oxid of iron and sulfid of iron is endothermic, and the requisite rate of supply of heat is so great that it cannot be effected in a combustionfurnace either by contact of a blast or by conduction. Moreover, the oxid and sulfid of iron are so refractory that it would be impracticable to heat them by a blast sufficiently to induce this reaction with any cer tainty of results.
My invention consists in treating the oxid and sulfid of iron or similar refractory oxid and sulfid ores in an electric furnace, the proportion of the oxid and sulfid beim such that a portion of the sulfur will be expelled and the remainder taken up by the oxygen of the ore, and nearly the whole of the iron or metal will be freed in the metallic state. The process is applicable to other'metals of the iron groupsuch as nickel, cobalt, and manganese.
In carrying out my invention I may use any suit able oxid ores, such as hematite or magnetite, and I may usethe carbonate in lace of the oxid, it being understood that in the heat of. the electric furnace the carbonicacid gas would pass off, leaving an oxid. For the sulfid ingredient I may use pyrites or other sulfid ore or waste products containing iron sulfid. Some ores contain both oxid and sulfid, and such are readily utilizable in this process, enough being added of the deficient ingredient to make up the proper relative roportion. Waste products containing part y roasted sulfid or sulfid together with sulfate are'also utilizable, due allowance .being made for the proportions of oxygen present. The silica or other gangue associated with-the ores is converted to a sla and the coalescence of the reduced metal facilitated by the addition of a suitable fluxing materialsuch, for instance, as limestone.
- The following isan example of the process: Hematite and pyrites, both in pulverized or crushed state, are mixed in the proportions, say, of two of hematite to one. of pyrite, by Weight, and are placed with a suitable amount of fluxing material in an electric furnace, and a current of sufficient intensity and volume passed through the mass to meltvit and to furnish the heat necessary for the reaction. The temperature required to bring aboutthe reaction is considerably higher than is attained in the ordinary iron blast-furnace. The precise temperature can not be definitely stated, hood of 3,000 to 4,000 centigrade and possibly higher. I After-the mass has reached a molten condition the current is increased, thereby raising the temperature. When the temperature of the, reaction is attained, the charge boils violently with copious evolution of fumes of S0,. boilingperiodis from three thousand to six thousand four hundred amperes at a pressure of from forty to seventy volts. The sulfuf dioxid passes off and may be collected and utilized for the manufacture of sulfuric acid, or otherwise, and -the iron from both-ores collects at the bottom of the furnace and may be tapped out into suitable molds. It will be understood that carbon, manganese, or other agent may be added to the melted iron to produce any desired quality of metal. The current-terminals if of carbon will naturally be attacked 'to some extent, but will not carburize the metal appreciably. I prefer to use an alternating current in the fur-, nace, so that there is no resulting electrolyticaction. Instead of mixing the materials before heating one material may be heated first and the other added while the heat is though it is'probably in the neighbor- The current during this continued. By this means anadjustment of resistance may be obtained, it being understood that the ores are of Widely-varying resistance.
The reaction in case hematite and pyrites are used is as follows:
In case of other materials than iron the process would be carried out in similar manner; but it Will be understood that it is not applicable to metals which are volatile at the temperatures which would exist in the electric furnace even out of proximity to the electrodes. This excludes not only metals such as copper and lead, which are, moreover, readily reducible by ordinary heating means. It is of course applicable to the production of alloys of such. metals. Thus a chrome-iron can be obtained by melting an oxid of chromium with a sulfid of iron or generally a mixture of ores of difieir-nt metals of the iron or chromium groups or complex ores of such groups, such as pyrrhotite, may be used to give any desired alloy.
Having thus described my invention, the following is What I claim as new therein and desire to secure by Letters Pa nt:
The process of refining ores of a metal of the iron group, which consists in heating to a temperature above that obtained in combustion-furnaces, the sulfid and oxid of the same metal together in an electric furnace, in such proportions that a portion'of the sulfur will be expelled and the remainder will be taken up by the oxygen of the ore.
2. The process of reducing the oxid and of the same metal by an electric current passed through the same, until they react to liberate sulfur, and form sulfur dioxid and free metal.
The process of reducing the oxid and sulfid of iron, which consists in heating to a temperature above that of combustion-furnaces said oxid and sulfid and a fluxing material in an electric furnace, until they melt A and react to liberate sulfur, and form sulfur dioxid and free iron.
4. The process of reducing ores of metals of the iron group, which consists in heating of said group with a sulfur-bearing ore of said group together with a fluxing material to a temperature above that of combustion-fur:
naces, thereby freeing the metal of bothkinds of ore.
5. The herein-described process which con sists in heating in the electric furnace an oxid of the metal of the iron group and a sulfid of the same metal, and separately collecting the resulting sulfur dioxid and free metal.
CHARLES S. BRADLEY.- Witnesses:
H RRY E. KNIGHT; J. GREEN.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US16770003A US829907A (en) | 1903-07-31 | 1903-07-31 | Process of reduction of iron, &c., from their ores. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US16770003A US829907A (en) | 1903-07-31 | 1903-07-31 | Process of reduction of iron, &c., from their ores. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US829907A true US829907A (en) | 1906-08-28 |
Family
ID=2898383
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US16770003A Expired - Lifetime US829907A (en) | 1903-07-31 | 1903-07-31 | Process of reduction of iron, &c., from their ores. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US829907A (en) |
-
1903
- 1903-07-31 US US16770003A patent/US829907A/en not_active Expired - Lifetime
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