US910082A - Blast-furnace smelting. - Google Patents
Blast-furnace smelting. Download PDFInfo
- Publication number
- US910082A US910082A US43811408A US1908438114A US910082A US 910082 A US910082 A US 910082A US 43811408 A US43811408 A US 43811408A US 1908438114 A US1908438114 A US 1908438114A US 910082 A US910082 A US 910082A
- Authority
- US
- United States
- Prior art keywords
- furnace
- smelting
- blast
- ores
- heat
- 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
- 238000003723 Smelting Methods 0.000 title description 23
- 239000000446 fuel Substances 0.000 description 14
- 238000002485 combustion reaction Methods 0.000 description 12
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 239000000571 coke Substances 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 230000004907 flux Effects 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000003921 oil Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 239000003610 charcoal Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
- 239000003208 petroleum Substances 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 229910021385 hard carbon Inorganic materials 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 241000722270 Regulus Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical compound [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid 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
- 230000008569 process Effects 0.000 description 1
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 1
- 229910052683 pyrite Inorganic materials 0.000 description 1
- 239000011028 pyrite Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/0073—Selection or treatment of the reducing gases
Definitions
- My invention herein described relates to the treatment of oxidized ores.
- the invention is an improvement in the smelting method as heretofore practiced and consists in supplying heat generated outside the furnace, to the shaft thereof, preferably from crude petroleum or gas, the heat thus supplied being utilized in lieu of the solid carbonaceous fuel, as coke, charcoal or their equivalents theretofore used.
- the method includes supplying air to the furnace, independently of the heat generated outside and forced into the furnace.
- I utilize a blast furnace shaft of the same general design as those in common use for pyrite smelting or copper matting, and, with some modifications, for lead smelting, and ha ting auxiliary thereto a fire-box or combustion chamber of suitable proportions for burning the necessary quantity of crude oil or petroleum, to supply an adequate equivalent of heat to the shaft of the furnace into which the ores and fluxes for smelting are charged, to consummate the smelting continuously to completion as such ores and fluxes are charged in, the heat from the crude oil or petroleum being used instead of coke, or other solid carbon, as fuel only, in oxidizing smelting and not for producing any other reactions involved.
- the oil or gas fuel in this system is burned in a fire box or combustion chamber, segregated entirely as to combustion from the ores and fluxes being smelted in the blast furnace, so that the chemical reactions incident to the combustion of carbonaceous fuel for the production of heat necessary for smelting shall not take place in contact with the ores being 50 smelted, in order to avoid the complications involved in burning carbonaceous fuel in contact with the ores and fluxes or with the air blast in a smelting operation whose necessary reactions are Wholly oxidizing, as in smelting sulfid ores to a regulus or matte product Specification of Letters Patent.
- Air is blown into such a furnace for the purpose of furnishing the oxygen necessary to oxidize the waste materials, as the sulfur and the iron of the sulfid ores, the latter to iron oxid to combine with the silica in the ore to form a fluid slag to How freely away to the dump, the sulfur up the chimney to the atmosphere.
- Oxygen has a stronger affinity for carbonaceous fuel, as coke or charcoal or oil, than it has for iron or sulfur, and hence when such carbonaceous fuel'as coke or charcoal or oil is charged into the furnace with the ores, or as oil is burned in the air blast of the furnace, no reaction can take place of oxygen with iron and sulfur until the carbonaceous fuel has been fully satisfied with oxygen or unless there is a surplus of oxygen going into the furnace over and above that demanded by the carbonaceous fuel.
- the heat, necessary to be supplied to the smelting furnace is produced by burning oil or gas to its ultimate products of combustion in a combustion chamber outside of the blast furnace where the ore is smelted, and the heat so produced is conveyed by convection through suit-able ducts together with the inert gases of combustion, into the smelting furnace, and so the necessary heat for smelting the ores is supplied to the furnace without the counteractive effect involved where carbonaceous fuel is burned in the atmosphere of the furnace or in contact with the ores being smelted.
- A is a blast furnace of usual construction, having twyers B.
- a fire box or combustion chamber is shown at O,
- H is a pipe leading from a blower of usual heat, with the products of combustion generated in the fire box are forced directly into the blast furnace against the pressure, if any, maintained in the blast furnace stack A by the air blast from the blower supplying the twyers.
- FIG. E is a general form of bustle pipe with an air'duct F delivering the air blast from a blower necessary to the process of smelting the ores in the stack.
- One form of such air duct F (Fig, 2) is made as a slot or rectangular opening parallel with the plane of the furnace'hearth, and preferably of such proportions as to admit the full blast of air fromthe blower G without constriction, as is involved in theruse of the twyers B shown in Fig. 1 and commonly employed at the entrance to the furnace.
- Some air may be necessary in the'reducing furnace for such ofiice, among other things, as producing car'- bon monoxid from coke or charcoal charged on'with the ores for reducing oxids to metals.
- liquid or gaseous fuel as a reducing agent, to which the air may be accurately supplied in such proportions as to produce carbon lnonoxid and thus secure perfect and complete reduction of oxide to their metals.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
J. W. NBSMITH. BLAST FURNACE SMELTING. APPLICATION FILED mm: 12, 1909.
Patented Jan. 19,
n: NORRIS vEYERs co., msmunmu. n. a
UNETED STATES PATENT OFFKQE.
JOHN W. NESMITH, OF DENVER, COLORADO, ASSIGNOR TO COLORADO IRON WORKS COMPANY, OF DENVER, COLORADO.
BLAST-FURNACE SMELTING.
T all whom 2'2, may concern Be it known that I, J OHN W'. NnsMrrn, citizen of the United States, residing at Denver, Colorado, have invented certain new 5 and useful Improvements in Blast-Furnace Smelting, of which the following is a specification.
My invention herein described relates to the treatment of oxidized ores.
The invention is an improvement in the smelting method as heretofore practiced and consists in supplying heat generated outside the furnace, to the shaft thereof, preferably from crude petroleum or gas, the heat thus supplied being utilized in lieu of the solid carbonaceous fuel, as coke, charcoal or their equivalents theretofore used. The method includes supplying air to the furnace, independently of the heat generated outside and forced into the furnace.
An apparatus for carrying the invention into effect is illustrated in the accompanying drawing, in which the figure is a sectional view.
I utilize a blast furnace shaft of the same general design as those in common use for pyrite smelting or copper matting, and, with some modifications, for lead smelting, and ha ting auxiliary thereto a fire-box or combustion chamber of suitable proportions for burning the necessary quantity of crude oil or petroleum, to supply an adequate equivalent of heat to the shaft of the furnace into which the ores and fluxes for smelting are charged, to consummate the smelting continuously to completion as such ores and fluxes are charged in, the heat from the crude oil or petroleum being used instead of coke, or other solid carbon, as fuel only, in oxidizing smelting and not for producing any other reactions involved.
The oil or gas fuel in this system is burned in a fire box or combustion chamber, segregated entirely as to combustion from the ores and fluxes being smelted in the blast furnace, so that the chemical reactions incident to the combustion of carbonaceous fuel for the production of heat necessary for smelting shall not take place in contact with the ores being 50 smelted, in order to avoid the complications involved in burning carbonaceous fuel in contact with the ores and fluxes or with the air blast in a smelting operation whose necessary reactions are Wholly oxidizing, as in smelting sulfid ores to a regulus or matte product Specification of Letters Patent.
Application filed June 12, 1908.
Air is blown into such a furnace for the purpose of furnishing the oxygen necessary to oxidize the waste materials, as the sulfur and the iron of the sulfid ores, the latter to iron oxid to combine with the silica in the ore to form a fluid slag to How freely away to the dump, the sulfur up the chimney to the atmosphere.
Oxygen has a stronger affinity for carbonaceous fuel, as coke or charcoal or oil, than it has for iron or sulfur, and hence when such carbonaceous fuel'as coke or charcoal or oil is charged into the furnace with the ores, or as oil is burned in the air blast of the furnace, no reaction can take place of oxygen with iron and sulfur until the carbonaceous fuel has been fully satisfied with oxygen or unless there is a surplus of oxygen going into the furnace over and above that demanded by the carbonaceous fuel. In other words, the combustion of carbonaceous fuel in the atmosphere of the blast furnace smelting to a matte product, is essentially counteractive of the oxidizing reactions involved in such smelting methods, and hence the use of carbonaceous fuel burning in contact with ores being smelted, under the action of the air blast is entirely avoided in this method.
In my improved method the heat, necessary to be supplied to the smelting furnace, is produced by burning oil or gas to its ultimate products of combustion in a combustion chamber outside of the blast furnace where the ore is smelted, and the heat so produced is conveyed by convection through suit-able ducts together with the inert gases of combustion, into the smelting furnace, and so the necessary heat for smelting the ores is supplied to the furnace without the counteractive effect involved where carbonaceous fuel is burned in the atmosphere of the furnace or in contact with the ores being smelted.
In some cases, so much coke or other hard carbon is used in the furnace stack with the ores as is necessary to the reducing reaction from oxid to metal or other necessary reactions of such nature involved in such reducing smelting, but no hard carbon is used in the furnace stack for producing heat, or for other purposes than that named above.
In the drawings, A is a blast furnace of usual construction, having twyers B. A fire box or combustion chamber is shown at O,
in which petroleum or other fluid or gaseous hydrocarbon is burned for the production of heat.
H is a pipe leading from a blower of usual heat, with the products of combustion generated in the fire box are forced directly into the blast furnace against the pressure, if any, maintained in the blast furnace stack A by the air blast from the blower supplying the twyers.
E is a general form of bustle pipe with an air'duct F delivering the air blast from a blower necessary to the process of smelting the ores in the stack. One form of such air duct F (Fig, 2) is made as a slot or rectangular opening parallel with the plane of the furnace'hearth, and preferably of such proportions as to admit the full blast of air fromthe blower G without constriction, as is involved in theruse of the twyers B shown in Fig. 1 and commonly employed at the entrance to the furnace. Some air may be necessary in the'reducing furnace for such ofiice, among other things, as producing car'- bon monoxid from coke or charcoal charged on'with the ores for reducing oxids to metals.
The twyers B or the air blast duct F, as the case may be, and the heat duct D in the form shown, enter the furnace A preferably in so near proximity to each other that the heat and heated gases from the combustion chamber C meet and-commingle with the air blast, if any, within the blast furnace, thus warming or heating the air blast immediately 011 its entrance and avoiding the paralyzing effect of cold air in the smelting Zone, while at the same time the heat over and above that utilized for heating the air in the blast furnace A necessary for the smelting operation, is provided through the heat duct D from the combustion chamber C.
In this method of smelting to lead base bullion or other metals, it is also convenient to use liquid or gaseous fuel as a reducing agent, to which the air may be accurately supplied in such proportions as to produce carbon lnonoxid and thus secure perfect and complete reduction of oxide to their metals.
I claim The herein describedmethod of treating oxidized ores, which consist in feeding a mixture of ores and fluxes and such carbonaceous material as is necessary for the reactions involved in the reduction of such ore to metals into a blast furnace, burning a suit able fuel exterior to the blast furnace and passing the hot combusted products into the WVINTHROP R. CADY, H. B. LOWDEN.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US43811408A US910082A (en) | 1908-06-12 | 1908-06-12 | Blast-furnace smelting. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US43811408A US910082A (en) | 1908-06-12 | 1908-06-12 | Blast-furnace smelting. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US910082A true US910082A (en) | 1909-01-19 |
Family
ID=2978520
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US43811408A Expired - Lifetime US910082A (en) | 1908-06-12 | 1908-06-12 | Blast-furnace smelting. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US910082A (en) |
-
1908
- 1908-06-12 US US43811408A patent/US910082A/en not_active Expired - Lifetime
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