US890231A - Method of treating ore. - Google Patents
Method of treating ore. Download PDFInfo
- Publication number
- US890231A US890231A US40777007A US1907407770A US890231A US 890231 A US890231 A US 890231A US 40777007 A US40777007 A US 40777007A US 1907407770 A US1907407770 A US 1907407770A US 890231 A US890231 A US 890231A
- Authority
- US
- United States
- Prior art keywords
- ore
- zinc
- stack
- sulfur
- iron
- 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 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 20
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 12
- 229910052725 zinc Inorganic materials 0.000 description 12
- 239000011701 zinc Substances 0.000 description 12
- 229910052742 iron Inorganic materials 0.000 description 10
- 239000007789 gas Substances 0.000 description 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 5
- 229910052717 sulfur Inorganic materials 0.000 description 5
- 239000011593 sulfur Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000011280 coal tar Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000001066 destructive effect Effects 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 235000014380 magnesium carbonate Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- WGPCGCOKHWGKJJ-UHFFFAOYSA-N sulfanylidenezinc Chemical compound [Zn]=S WGPCGCOKHWGKJJ-UHFFFAOYSA-N 0.000 description 1
Images
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
- C22B19/00—Obtaining zinc or zinc oxide
- C22B19/04—Obtaining zinc by distilling
Definitions
- JoNEs or IRON Mo NTAIN, MICHIGAN, ASSIGNOR on ONE-HALF P TENT; OFFICE;
- the upper structure 1 consists of a carbonaceous-fuehburning-furnace 3, adapted to burn soft-coal, as the most chamber-wall, below which is indicated a conveyer 6 for-carrying off the ashes.
- This fuelfurnace is supported on a suitable foundation f off from the upper portion of the fuel-bed by upper and lower oint the gases from the lower the heat below it, are drawn through the flue into thestack 8.
- the neck 10 is best made of carbona ceous material to adapt it to resist the destructive tendency of the heat from the gases mixing in and coursing through it, the material Iiprefer to employ for the purpose being blocks of. graphite carbon, or a mixture of pulverized graphite and coke with a suitable binder, as coal-tar, compacted by hydraulic pressure to solidify the mass-and then baked to harden it.
- a chute 11' From the open lower end of the ore-stack a chute 11', having a hingedvalve 12 interposed in it; inclines downwardly to discharge into a hopper 13 surmounting the upper end of the relatively short ore-stack 14 of the structure 2, formed like the stac'k8, and communicating from between itsv ends through aflueforming neck 15, with the chamber of a fuelfurnace 16 of this last-named structure, this furnace being in all particulars, by prefer- 'ence, like and operating the same as the In the wall of the stack 14 oppo' furnace 3. site that it-h which the flue 15 connects, and
- a site should be selected on the conduit, which contains normally 'closedopenings 19- at suitable intervals apart throughout its length, may best be formed of a net-work ofwire embedded in concrete and molded in sections of cylindrical or other desired shape. stack is open'to an inclined chute 20 leading The lower end 'of'the voref down the hill tozany desired point to which "it is desired to deliver theremnant of the treated ore.
- This port 21 near its base From time to time, on o ening the valve 12, the sulfur-freed ore at t e base of the stack is permitted to fall through the chute 11 to charge the stack 14 therewith.
- the hot ore in this stack is subjected to the action of the gases from the furnace 16, passing into the stack through the flue I 15 at a temperature of from about twenty-two hundred to twenty-five hundred degrees F., which is sufficient to volatilize the zinc-constituent of the ore, the fumes of which pass through the restricted outlet 17 into the conduit 18 and become condensed in their course through the latter dropping to time through the openings 19.
- the method of .treating ore containing sulfur, zinc and iron which consists in first subjecting said ore to the action of gases from carbonaceous ,fuel at a temperature sufiicient to burn out the sulfur but insufficient to volatilize the zinc, and introducing air into the ore to enhance the burning of the sulfur, then subjecting the sulfur-freed ore to the action of similar gases at a higher temperature suflicient to volatilize the zinc but insufficient to melt the iron, condensing the zinc-fumes to recover the zinc, and saving the iron-containing remnant ofthe ore.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
useful Improvement in Methods'of Treating. Ore, of which the following is a specification.-
, Y STATES JoHN 'r. JoNEs, or IRON Mo NTAIN, MICHIGAN, ASSIGNOR on ONE-HALF P TENT; OFFICE;
CLAIR, OF DULUTH, MINNESOTA.
METHOD OF T EATING can.
Applicatio'n filed December 23, 1907. Serial No. 407,770.
To all whom it may concern: Be it known that'I, JOHN T. JoN'Es,-a citizen ofv the United States, residing at Iron Mountain, in the county of Dickinson and State of Michigan, have invented a new and The object of my invention is to provide a novel method of treating, by furnace-opera- "tion, ore containing iron, zinc-and sulfur as its principal constituents; and I have more especially devised my invention for thetreatment of a certain ore containing about 31 per-cent. iron, about 17 per cent. zinc, about per cent. sufur, and about 5. to 7 per cent. silica. The treatment consists, generore, containing hereinafter described.
ally stated, in subjecting successively the ore to heat sufficient to burn out the sulfurbut insufiicient to volatilize the zinc, and the remainder of the ore to a higher degree of heat sufiioient to volatilize the zinc, which is carried OE and condensed, the remnant of the iron and earthy materia'l, coming down in the furnace-stack, under the action of the heat, in the form of matte, which may bedisposed of in the manner The accompanying drawing'shows, by a broken view in sectional elevation, a furnaceequipment suitable for the practice of my invention? i side of a hill for the erection of two furnace- 5 suitable fuel,- on a grate 4 in the .fuinace-' chamber above an air-blast opening 5 in the I '7 to extend parallel with an ore-stack 8 rising from a foundation 9 toa heig t of one huh-- I municates, leading, thereto about midway between'the portion of the structures 1 and 2. The upper structure 1 consists of a carbonaceous-fuehburning-furnace 3, adapted to burn soft-coal, as the most chamber-wall, below which is indicated a conveyer 6 for-carrying off the ashes. This fuelfurnace is supported on a suitable foundation f off from the upper portion of the fuel-bed by upper and lower oint the gases from the lower the heat below it, are drawn through the flue into thestack 8. This stack and the furnace 'ro GEORGE A, Sr.
3 may be constructed of or lined with suitable brick, preferably of the magnesite va riety, but the neck 10 is best made of carbona ceous material to adapt it to resist the destructive tendency of the heat from the gases mixing in and coursing through it, the material Iiprefer to employ for the purpose being blocks of. graphite carbon, or a mixture of pulverized graphite and coke with a suitable binder, as coal-tar, compacted by hydraulic pressure to solidify the mass-and then baked to harden it. t I
From the open lower end of the ore-stack a chute 11', having a hingedvalve 12 interposed in it; inclines downwardly to discharge into a hopper 13 surmounting the upper end of the relatively short ore-stack 14 of the structure 2, formed like the stac'k8, and communicating from between itsv ends through aflueforming neck 15, with the chamber of a fuelfurnace 16 of this last-named structure, this furnace being in all particulars, by prefer- 'ence, like and operating the same as the In the wall of the stack 14 oppo' furnace 3. site that it-h which the flue 15 connects, and
alining w th the flue, is provided a dischargeopening 17 leading to a conduit 18, which inclines upwardly along the hill-side, at an t v Y angle of, say, about 45 degrees, and may be a For carrying out my invention to the bestadvantage, a site should be selected on the conduit, which contains normally 'closedopenings 19- at suitable intervals apart throughout its length, may best be formed of a net-work ofwire embedded in concrete and molded in sections of cylindrical or other desired shape. stack is open'to an inclined chute 20 leading The lower end 'of'the voref down the hill tozany desired point to which "it is desired to deliver theremnant of the treated ore. p
The procedure is asfollowsz' With the fire burning in the furnace 3, and supplied with combustion-promoting air through a port 22, and the stack fiiled, to the closed valve 12,
with theore to betreated, the hot gasespass- 'ing through the flue 10 into the stack and upward therein through the intersticial column of ore, burn-out the sulfur-constituent of the ore, the heat being regulated to an intensity only sufficient to drive oif'thesulfunand this sulfur-burning action being supplemented by the admission of air into the stack through a 85 thousand feet, more or less, in length. This port 21 near its base From time to time, on o ening the valve 12, the sulfur-freed ore at t e base of the stack is permitted to fall through the chute 11 to charge the stack 14 therewith. The hot ore in this stack is subjected to the action of the gases from the furnace 16, passing into the stack through the flue I 15 at a temperature of from about twenty-two hundred to twenty-five hundred degrees F., which is sufficient to volatilize the zinc-constituent of the ore, the fumes of which pass through the restricted outlet 17 into the conduit 18 and become condensed in their course through the latter dropping to time through the openings 19.
therein in the form of flakes, the accummulations of which may be withdrawn from time The 1 remainder of the ore, containing iron and earthy material reduced by the heat to matteform, falls down the chute 20 to the point of delivery, whence it may be taken for use as a flux after treating it in-known manner, if it then volatilize the zinc, and
zinc by condensation.
2. The method of treating ore containing sulfur, zinc and iron, which consists in first subjecting said ore, to the action of gases from carbonaceous fuel at a temperature recovering the suflicient to burn out the sulfur but insufficient to volatilize the zinc, then subjectingthe sulfur-freed ore to the action of similar gases at a higher temperature suflicient to volatilize the zinc, and condensing the zincfumes, for the purpose set forth.
3. The method of .treating ore containing sulfur, zinc and iron, which consists in first subjecting said ore to the action of gases from carbonaceous ,fuel at a temperature sufiicient to burn out the sulfur but insufficient to volatilize the zinc, and introducing air into the ore to enhance the burning of the sulfur, then subjecting the sulfur-freed ore to the action of similar gases at a higher temperature suflicient to volatilize the zinc but insufficient to melt the iron, condensing the zinc-fumes to recover the zinc, and saving the iron-containing remnant ofthe ore.
. JOHNT JONES. In presence of Y K. M. CORNWALL, 4 R. A. SGHAEFER.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US40777007A US890231A (en) | 1907-12-23 | 1907-12-23 | Method of treating ore. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US40777007A US890231A (en) | 1907-12-23 | 1907-12-23 | Method of treating ore. |
Publications (1)
Publication Number | Publication Date |
---|---|
US890231A true US890231A (en) | 1908-06-09 |
Family
ID=2958662
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US40777007A Expired - Lifetime US890231A (en) | 1907-12-23 | 1907-12-23 | Method of treating ore. |
Country Status (1)
Country | Link |
---|---|
US (1) | US890231A (en) |
-
1907
- 1907-12-23 US US40777007A patent/US890231A/en not_active Expired - Lifetime
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US1941592A (en) | Roasting pryites fines | |
US1973590A (en) | Recovery of zinc, lead, tin, and cadmium values | |
US890231A (en) | Method of treating ore. | |
US949474A (en) | Process of refining iron. | |
US589210A (en) | Reverberatory smelting and refining furnace | |
US1164653A (en) | Process of smelting ores. | |
US959924A (en) | Smelting process. | |
US890563A (en) | Method of treating cooper ores. | |
US592594A (en) | Xx x xglsh | |
US1301684A (en) | Process for clearing clayey ores. | |
US1884348A (en) | Method of roasting minerals containing the sulphides of zinc, iron, lead, and copper, for the recovery of the metal and the sulphur dioxide gas therefrom | |
US846216A (en) | Method of treating ores. | |
US512531A (en) | Process of treating ores | |
US88480A (en) | Improvement in the manufacture of iron and steel | |
US1985902A (en) | Concentrate burner | |
US516663A (en) | Ore-roasting furnace | |
US995542A (en) | Method of treating finely-divided substances containing iron compounds. | |
US1578694A (en) | Method of separating metal from metalliferous material | |
US735894A (en) | Treatment of zinc or other ores. | |
US798524A (en) | Ore-roasting kiln. | |
US1243798A (en) | Furnace for smelting ores. | |
US950798A (en) | Process for sintering ore. | |
US1832006A (en) | Method of and apparatus for treating quicksilver ores | |
US866280A (en) | Ore-reducing furnace. | |
US227710A (en) | adams |