US1471270A - Process for making iron and steel from smelter slags - Google Patents
Process for making iron and steel from smelter slags Download PDFInfo
- Publication number
- US1471270A US1471270A US49234121A US1471270A US 1471270 A US1471270 A US 1471270A US 49234121 A US49234121 A US 49234121A US 1471270 A US1471270 A US 1471270A
- Authority
- US
- United States
- Prior art keywords
- iron
- steel
- bath
- slag
- smelter
- 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 47
- 239000002893 slag Substances 0.000 title description 26
- 229910052742 iron Inorganic materials 0.000 title description 24
- 238000000034 method Methods 0.000 title description 12
- 230000008569 process Effects 0.000 title description 11
- 229910000831 Steel Inorganic materials 0.000 title description 8
- 239000010959 steel Substances 0.000 title description 8
- 239000003245 coal Substances 0.000 description 12
- 238000002485 combustion reaction Methods 0.000 description 9
- 239000000446 fuel Substances 0.000 description 9
- 230000009467 reduction Effects 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 6
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 5
- 235000011941 Tilia x europaea Nutrition 0.000 description 5
- 230000004907 flux Effects 0.000 description 5
- 239000004571 lime Substances 0.000 description 5
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 4
- 238000007664 blowing Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910001018 Cast iron Inorganic materials 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 229910000805 Pig iron Inorganic materials 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004160 Ammonium persulphate Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 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
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/04—Working-up slag
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Definitions
- My invention has relation to improvements in processes for making iron and steel from smelter slags, and consists in the novel features-more fully set forth in the specification and pointed out in the claims.
- the slag contains a large percentage of iron as oxide (i. e., wholly or partially combined with silica as silicate of iron) which, under the prevailing practice, is wasted.
- the smelter slag is introduced into a crucible, converter or equivalent vessel while still molten.
- an ordinary copper converter is used, eX- cept that'instead of a single row of tuyeres there are two rows, the one discharging below the surface of the bath when the converter is in blowing position, while the other will discharge above the bath.
- the molten slag After the molten slag has been introduced into the converter C, it is tilted back 7 capacity of air that is necessary to inject the to blowing position and powdered coal, or powdered coal and flux (preferably powdered lime rock) are introduced by a current of air through the lower set of tuyeres 1 and into the bath.
- powdered coal, or powdered coal and flux preferably powdered lime rock
- the amount of air that enters with the fuel, or the fuel and flux is so regulated as not to he sufficient for complete combustion of the fuel. This, obviously must be the case, because the carbon in the fuel is brought into contact with the iron oxide to effect a reduction thereof.
- the number and size of the lower row of tuyeres 1 are limited to the powdered coal, or coal and flux, into the bath, However, it is important that the amount of air be kept as low as possible so that complete combustion of the fuel does not take place.
- the coal will be replaced in the slag by the lime, and the basic constituent of the slag thus kept at a balance so as not' to reduce the fluidity thereof.
- the metallic iron will drop to the bottom of the bath and may be removed after skimming 0d the slag. As the iron is gradually replaced by the lime there is a tendency for the slag to thicken, and an increased temperature is required to maintain the necessary fluidity to carry on the operation.
- I provide a second row of tuyeres 2, above the first row and adapted to discharge air into the converter above the sur-' face of the bath.
- This air supports the combustion of the volatile combustibles, such as CO, rising from the surface of the bath, during the reduction of the iron, and furnishes additional heat, which is transmitted to the bath by radiation and conduction.
- the bath is thus kept fluid so that the reduction may proceed practically to completion.
- the slag is skimmed ofi and the iron may beremoved for cast iron or pig iron.
- the iron may be left in the converter or transferred i to an ordinary steel converter and blown to produce steel, as well understood in the art.
- the coal and flux are preferably supplied to the bath through the lower row of tuyeres 1, I do not wish to be restricted to this method as, obviously it. may be charged directly through the mouth of the converter, or otherwise. Then again if charged through the mouth of the converter the fuel and flux need not necessarily be powdered.
- the amount of fuel required may be reduced by preheating the air if desired.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Get. 16 E923. 1,4712% c. R. KUZELL PROCESS FOR MAKING IRON AND STEEL FROM SMELTER SLAGS Filed Aug. 15, 1921 Patented @ct. is, rare.
CHARLES R. KUZELL, 0F CLARKDALE, ARIZONA.
PROCESS FOR MAKING IRON AND STEEL FROM SHELTER SLAGS.
Application .filed August 15, 1921. Serial No. 492,841.
To all whom it may concern:
Be it known that 1, CHARLES R. KUZ LL, a citizen of the United States, residing at (.larkdale, in the county of Yavapai and State of Arizona, have invented certain new and useful Improvements in Processes for Making Iron and Steel from Smelter Slags, of which the following is a specification,
My invention has relation to improvements in processes for making iron and steel from smelter slags, and consists in the novel features-more fully set forth in the specification and pointed out in the claims.
.In the smelting of copper for making matte, the slag contains a large percentage of iron as oxide (i. e., wholly or partially combined with silica as silicate of iron) which, under the prevailing practice, is wasted. Now, it is the object of the present invention to recover this iron from the slag by reducing the oxide and converting the iron to cast or pig iron, although if desirable the process also contemplates the manufacture of steel from the recovered iron. The advantages of the invention will be better apparent from the following detailed description of the process, 111 connection with the drawing which represents a longitudinal section of a modified form of converter.
The smelter slag is introduced into a crucible, converter or equivalent vessel while still molten. We will assume that an ordinary copper converter is used, eX- cept that'instead of a single row of tuyeres there are two rows, the one discharging below the surface of the bath when the converter is in blowing position, while the other will discharge above the bath.
After the molten slag has been introduced into the converter C, it is tilted back 7 capacity of air that is necessary to inject the to blowing position and powdered coal, or powdered coal and flux (preferably powdered lime rock) are introduced by a current of air through the lower set of tuyeres 1 and into the bath. However, the amount of air that enters with the fuel, or the fuel and flux, is so regulated as not to he sufficient for complete combustion of the fuel. This, obviously must be the case, because the carbon in the fuel is brought into contact with the iron oxide to effect a reduction thereof. The number and size of the lower row of tuyeres 1 are limited to the powdered coal, or coal and flux, into the bath, However, it is important that the amount of air be kept as low as possible so that complete combustion of the fuel does not take place. duced by the coal it will be replaced in the slag by the lime, and the basic constituent of the slag thus kept at a balance so as not' to reduce the fluidity thereof. The metallic iron will drop to the bottom of the bath and may be removed after skimming 0d the slag. As the iron is gradually replaced by the lime there is a tendency for the slag to thicken, and an increased temperature is required to maintain the necessary fluidity to carry on the operation. For this purpose I provide a second row of tuyeres 2, above the first row and adapted to discharge air into the converter above the sur-' face of the bath. This air supports the combustion of the volatile combustibles, such as CO, rising from the surface of the bath, during the reduction of the iron, and furnishes additional heat, which is transmitted to the bath by radiation and conduction. The bath is thus kept fluid so that the reduction may proceed practically to completion.
After the reduction has proceeded to the proper degree, the slag is skimmed ofi and the iron may beremoved for cast iron or pig iron. However, if desired, the iron may be left in the converter or transferred i to an ordinary steel converter and blown to produce steel, as well understood in the art. While the coal and flux are preferably supplied to the bath through the lower row of tuyeres 1, I do not wish to be restricted to this method as, obviously it. may be charged directly through the mouth of the converter, or otherwise. Then again if charged through the mouth of the converter the fuel and flux need not necessarily be powdered.
The use of the smelter slag while still molten as it comes from the smelter furnaces results in the saving of heat in the molten slag. A further economy results from the use of coal to bring about the reduction, since coal is cheaper than coke used in standard iron blast furnace practice. Then again the type of furnace in whichthe reduction takes place will permit the making of steel in the same furnace if desired. I
In practicing the invention, the quantities As the iron oxide is reof the reagents, the manner of charging them into the bath and manipulation thereof will be determined largely by the skilled metallurgist in charge of the operation. The amount of fuel required may be reduced by preheating the air if desired.
Having described'my invention, ll claim: 1. The' process of manufacturing iron from smelter slags which consists in subjecting a charge of molten slag to the action of a blast of air charged with powdered Y carbonaceous. fuel directed into the bath of slag below the surface thereof, continuing the blowing operation with an excess of fuel in the presence of suitable fluxing material permeating the bath, and projecting above the bath a blast of a supporter of combustion.
2. The process of manufacturing iron from smelter slags which consists in introduclng into the molten slag a reducing agent in the presence of a fluxing material,
and projecting above the charge a blast of a supporter of combustion.
3. The process of manufacturing iron from smelter slags whichconsists in subjecting a charge of molten slag to a blast of .air carrying powdered-coal, introducing a suitable fluxing material into the charge, and projecting above the charge a blast of a supporter of combustion.
4. The process of manufacturing iron from smelter slags, which consists in charg- .coal reduces the iron in thecharge, and introducing a supporter of combustion above the charge.
6. The process of manufacturing iron from smelter slags which consists in placing a charge of molten slag into a treatment vessel, introducing air and powdered coal into the charge to raise the temperature of the bath, the air being insufficient to complete the combustion of the coal which effects a. reduction of the iron in the charge. introducing into 1118 charge lime to replace the iron in the charge and to form a lime slag, directing into the treatment vessel above the charge a supporter of combustion for raising the temperature of the bath.
and finally removing the iron.
In testimony whereof I hereunto afiix my signature.
CHARLES R. KUZELL.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US49234121 US1471270A (en) | 1921-08-15 | 1921-08-15 | Process for making iron and steel from smelter slags |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US49234121 US1471270A (en) | 1921-08-15 | 1921-08-15 | Process for making iron and steel from smelter slags |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1471270A true US1471270A (en) | 1923-10-16 |
Family
ID=23955883
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US49234121 Expired - Lifetime US1471270A (en) | 1921-08-15 | 1921-08-15 | Process for making iron and steel from smelter slags |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1471270A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2523092A (en) * | 1947-05-02 | 1950-09-19 | Bryk Petri Baldur | Method for extraction of iron |
| US2986458A (en) * | 1958-09-05 | 1961-05-30 | Strategic Materials Corp | Production of iron from ferrous slag materials |
-
1921
- 1921-08-15 US US49234121 patent/US1471270A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2523092A (en) * | 1947-05-02 | 1950-09-19 | Bryk Petri Baldur | Method for extraction of iron |
| US2986458A (en) * | 1958-09-05 | 1961-05-30 | Strategic Materials Corp | Production of iron from ferrous slag materials |
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