USRE21500E - Method of decarbonizing a carbon - Google Patents
Method of decarbonizing a carbon Download PDFInfo
- Publication number
- USRE21500E USRE21500E US21500DE USRE21500E US RE21500 E USRE21500 E US RE21500E US 21500D E US21500D E US 21500DE US RE21500 E USRE21500 E US RE21500E
- Authority
- US
- United States
- Prior art keywords
- iron
- decarbonizing
- furnace
- granules
- charge
- 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
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- 238000000034 method Methods 0.000 title description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title description 11
- 229910052799 carbon Inorganic materials 0.000 title description 11
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 92
- 229910052742 iron Inorganic materials 0.000 description 46
- 239000008187 granular material Substances 0.000 description 20
- 238000010438 heat treatment Methods 0.000 description 19
- 239000007789 gas Substances 0.000 description 16
- 239000000463 material Substances 0.000 description 9
- 238000001816 cooling Methods 0.000 description 8
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 description 8
- 230000001590 oxidative effect Effects 0.000 description 8
- 229910045601 alloy Inorganic materials 0.000 description 7
- 239000000956 alloy Substances 0.000 description 7
- 238000002844 melting Methods 0.000 description 7
- 230000008018 melting Effects 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- 238000003756 stirring Methods 0.000 description 7
- 239000002184 metal Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 5
- 229910000805 Pig iron Inorganic materials 0.000 description 5
- 235000011941 Tilia x europaea Nutrition 0.000 description 5
- 239000004571 lime Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 239000005864 Sulphur Substances 0.000 description 3
- 238000000137 annealing Methods 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 230000007935 neutral effect Effects 0.000 description 3
- 239000010453 quartz Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 2
- 229910000604 Ferrochrome Inorganic materials 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 2
- 229910001296 Malleable iron Inorganic materials 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000000110 cooling liquid Substances 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 230000003467 diminishing effect Effects 0.000 description 1
- RAQDACVRFCEPDA-UHFFFAOYSA-L ferrous carbonate Chemical compound [Fe+2].[O-]C([O-])=O RAQDACVRFCEPDA-UHFFFAOYSA-L 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000011019 hematite Substances 0.000 description 1
- 229910052595 hematite Inorganic materials 0.000 description 1
- 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 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- 229910001338 liquidmetal Inorganic materials 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- -1 purple ore 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
- 229910052683 pyrite Inorganic materials 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/02—Making metallic powder or suspensions thereof using physical processes
- B22F9/06—Making metallic powder or suspensions thereof using physical processes starting from liquid material
- B22F9/08—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
- B22F1/14—Treatment of metallic powder
- B22F1/145—Chemical treatment, e.g. passivation or decarburisation
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D3/00—Diffusion processes for extraction of non-metals; Furnaces therefor
- C21D3/02—Extraction of non-metals
- C21D3/04—Decarburising
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/02—Making metallic powder or suspensions thereof using physical processes
- B22F9/06—Making metallic powder or suspensions thereof using physical processes starting from liquid material
- B22F9/08—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
- B22F2009/0804—Dispersion in or on liquid, other than with sieves
Definitions
- My invention relates to improvements in methads for producing for instance soft iron particles to be used principally as a substitute for ordina y high grade low carbon scrap iron when mak ng steel in open hearths and electric furnaces.
- the invention has for its objects: first, to provide a cheap method suitable for decarbonizing ordinary 'or high grade white or gray pig iron; second, to provides.
- the carbon holding metal such as white or gray pig iron into more or less hollow granules, grains, a fine powder or thin flakes by means of mechanical crushing and grinding or by exposing the iron when in a liquid state to the action of water, air or steam. This may be done by pouring the iron into a pool of water or by blowing air or steam onto a jet of iron flowing from a furnace or a ladle
- the finely subdivided iron is then exp sed to the action of solid or gaseous oxydants at a temperature between 750 and 1100 C. or thereabout, preferably in the neighbourhood of 1000 C.
- the solid oxydant may consist of an iron ore, for instance hematite, purple ore, magnetite, an iron carbonate or an iron hydoxide.
- One may also use a carbonate for instance of lime, which is split up into 00: and CaO at about 1000 C.
- oxidizing gases these may consist of CO: or air or of a mixture of CO: and CO in suitable, proportions, for instance 25% CO: and CO which will greatly facilitate the oxidizing of the carbon without oxidizing the iron.
- oxidizing gases which might be free from nitrogen
- a neutral material for instance sand, crushed quartz, a powder of lime or limestone or even with an iron ore.
- a neutral material such as lime or quartz will counteract any tendency of the metal particles to sinter or stick together. If decarbonizing' by means of iron ore this should be in the shape of a fine powder in order to cause a very intimate contact between the oxydant and In Sweden November 4,
- the charge may be kept in sow motion by' rotating the furnace in which it is heated or by meansof scrapers, or other stirring means in case of a stationary furnace being employed.
- the soft iron particles obtained may also compressed into briquettes to facilitate shipping to other places.
- other metals such as Cr, Mn, W, V, M0, N1 and Co may be added in the shape of grains or powder so as to provide alloys when melted later on in an electric or other furnace.
- the heating operation maybe performed in several types of furnaces having electrical or other means for heating.
- the specific resistance of the charge may be controlled by adding more or less of a neutral material such as lime or quartz etc.
- the charge may also be heated by heat radiating from a resistance or an electric are inside of the furnace. for which purpose electrodes are inserted in proper way.
- Another way of heating consists inusingatunnelfurnaceofthetypeusedfor making malleable iron castings or for roasting iron ore briquettes charging the materials in open or covered hearths on top of cars, which are gradually heated by the furnace gases when travelling along the furnace tunnel.
- Decarbonlsing may also take place by heating the materials in annealing pots or boxes in the normal type of stationary annealing furnaces employed in the malleable iron industry.
- a coking furnace of the retort or chamber type may be employed for decarbonizing according to the invention.
- Decarbonizing may also be effected in a furnace of the pyrite roasting type in which the charge is travelling in counter current to a flow of hot gases or in a kiln for firing bricks having a plurality of chambers arranged in well known manner.
- One may, naturally, also use any 'kind of electric annealing furnaces heating the materials in pans or boxes or other receptacles of: heat r alloys.
- a method of producing low carbon iron grains consisting in heating a charge of small iron granules, obtained by rapidly cooling molten iron in acooling fluid, while stirring the charge atmosphere of which contains atthe most 25% CO: and at least 75% CO.
- a method of producing low carbon iron grains consisting in heating a charge of a mixture of small iron granules, obtained by rapidly cooling molten iron in a cooling fluid, and an easily reducible iron ore in a finely divided state,
- the atmosphere of which, containing CO:- and CO-sas. is suitably composed for oxidizing substantially only the carbon but not the iron of the granules, the heating being sumcient for decarbonizing and reducing the charge without melting it, a gas suitable for-reducing the iron ore being introduced at the end of the decarbonizing period.
- a method of producing low carbon grains 'of aniron alloy consisting of heating a charge of small granules of the alloy, obtained by rapidly cooling molten alloy in a cooling means, while stirring the charge by revolution in a combustion zone the atmosphere of which, containing C0:-
- CO-gas is suitably composed for'oxidizing substantially only the carbon but not the metals g of the granules, the heating being sufficient for decarbonizing the granules but insuficient for causing them to melt.
- a method of producing low carbon iron grains which comprises subdividing iron into small roundedgranules by rapidly cooling it while in liquid state, introducing the granules into a tubular, slightly inclining furnace, stirring the charge by rotating the furnace, heating the particles sufllciently for decarbonizing but below the melting point in an atmosphere containing a mixture of CO:- and 00-888 suitable for oxidizing only the carbon but substantially not the iron of the granules and producing the hot decarbonizing atmosphere by means of internal combustion in the furnace.
- a method ofproducing low carbon iron grains which comprises a subdivision of the iron into small rounded granules by rapidly cooling it while ln'a liquid state, introducing them into a tubular, slightly inclining furnace, stirring them by rotating the furnace and heating the .charge in an atmosphere of hot gases, produced by internal combustion of a fuel, said atmosphere containing a mixture of at most 25% C0: and 75% C0, substantially without oxidizing the iron.
- a method. of producing low carbon iron granules which comprises the heating of rounded granules of iron, obtained by rapidly cooling liquid iron, in a rotating, tubular, internally heated furnace, raising the temperature of the granules sumciently for decarbonizing but below the melting point while causing the charge to be stirred and to move in a direction opposite to that of a flow of composed of C0: and C0 and at least one of thediluting gases N2, H: and H20 and preventing a substantial oxidizingof the iron by a suitable control of the proportions between the 602- and CO-gas of the furnace atmosphere.
- a method of producing low carbon iron granules which comprises the heating and stirring of a mixture of rounded granules of iron, ob-
- Y tained by rapidly cooling molten iron, and an easily reducible iron ore in a finely divided state in a rotating, slightly inclining, tubular and internally heated furnace in an atmosphere capable of decarbonizing the granules at a temperature below the melting point and then in a reducing atmosphere for producing iron from the ore component of the charge.
- a method of producing low carbon iron grains which consists in heating granules of iron produced by rapidly cooling liquid metal together with a basic material sufliciently for decarbonizing them but below the. melting point in an atmosphere containing at least the gases C0: and CO in such proportions that substantially only carbon and sulphur are removed from theiron grains which are otherwise practically unchanged.
- a method of producing low carbon iron grains which consists in granulating the iron by rapid cooling, classifying the granules according to their sizes and then heating a graduated class of granules by itself suiilciently for decarbonizing it but below the melting point in an atmosphere of gases containing at least the gases C0: and CO in a'proportion suitable for oxidizing substantially only the carbon but not jzhe iron itself.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
s... July 2,1940
UNITED STATES HOLDING METAL,
PATENT OF Re. Zl,500 FlCE a cannon son. .nss'rsncn ma 2,170,158, dated IRON Ivar Bennerielt, Diursholm, Sweden No Drawing. Original No.
August '22, 1939, Serial No. 108,012, October 28, 1936. Application for reissue March Serial No. 325,922.
12 Claims.
, My invention relates to improvements in methads for producing for instance soft iron particles to be used principally as a substitute for ordina y high grade low carbon scrap iron when mak ng steel in open hearths and electric furnaces. The invention has for its objects: first, to provide a cheap method suitable for decarbonizing ordinary 'or high grade white or gray pig iron; second, to provides. method for eliminating at least a substantial part of the sulphur present in the pig iron; third, to provide a simple and rational method for decarbonizing pig iron at a temperature lower than the melting point; fourth, to provide a decarbonizing method that may be conveniently carried out in any one of a considerable number of heating furnaces of well known-types; fifth, to facilitate the production of high grade steel or alloys of uniform qua ity by supplying a high grade soft iron of uniform quality, available in abundant quantities; sixth, to provide a method adapted also for decarbonizing metals and alloys in general.
The several objects of my invention-are attained by first subdividing the carbon holding metal such as white or gray pig iron into more or less hollow granules, grains, a fine powder or thin flakes by means of mechanical crushing and grinding or by exposing the iron when in a liquid state to the action of water, air or steam. This may be done by pouring the iron into a pool of water or by blowing air or steam onto a jet of iron flowing from a furnace or a ladle. To obtain the iron in the shape of thin flakes it might be poured onto an iron bed or on rotating rollers Y which maybe cooled in any suitable manner.
The finely subdivided iron is then exp sed to the action of solid or gaseous oxydants at a temperature between 750 and 1100 C. or thereabout, preferably in the neighbourhood of 1000 C. The solid oxydant may consist of an iron ore, for instance hematite, purple ore, magnetite, an iron carbonate or an iron hydoxide. One may also use a carbonate for instance of lime, which is split up into 00: and CaO at about 1000 C.
If employing oxidizing gases, these may consist of CO: or air or of a mixture of CO: and CO in suitable, proportions, for instance 25% CO: and CO which will greatly facilitate the oxidizing of the carbon without oxidizing the iron. In the case of decarbonizing by means of gases, which might be free from nitrogen, one can mix the iron particles with a neutral material, for instance sand, crushed quartz, a powder of lime or limestone or even with an iron ore. The addition of a neutral material such as lime or quartz will counteract any tendency of the metal particles to sinter or stick together. If decarbonizing' by means of iron ore this should be in the shape of a fine powder in order to cause a very intimate contact between the oxydant and In Sweden November 4,
and far reaching decarbonizlng, for instance to 0.1% and less in a'couple-of hours. To facilitate still more the removal of carbon the charge may be kept in sow motion by' rotating the furnace in which it is heated or by meansof scrapers, or other stirring means in case of a stationary furnace being employed.
When required for certain reasons, for instance for decarbonizing FeCr orl 'eMn, etc., one may introduce hydrogen gas or steam into the charge and one may also cause it to be heated in vacuo, preferably in a high frequency furnace in order the small iron particles, thus facilitating a quick to facilitate the splitting up of for instance a The soft iron particles obtained may also compressed into briquettes to facilitate shipping to other places. In such briquettes other metals such as Cr, Mn, W, V, M0, N1 and Co may be added in the shape of grains or powder so as to provide alloys when melted later on in an electric or other furnace.
By adding a considerable excess of an easily reducible iron ore and using a reducing gas, for instance H2 or 00, preferably at the end of the decarbonizing period, one may obtain a corresponding increase of iron without any substantial increase of the expenses, thus reducing the cost per ton of soft iron produced. By the addition of a basic material such as lime or milk of lime or lime stone a substantial amount of the sulphur, which might be present in the charge, wfll be transformed to Gas, which may be removed in any suitable way. It isv possible that also phosphorus, which maybe present 'asaa phosphide of iron, may be removed in the same way.
If the soft ironobtained' is mixed with another solid matter, for instance coarse sand or an ex- The heating operation maybe performed in several types of furnaces having electrical or other means for heating. One might for instance employ a rotating tubular furnace of the slightly inclining type having burners for internal heating by means of oil, gas or coal powder. One may also heat the charge by means of an electric current using the charge as a resistance in well known manner. The specific resistance of the charge may be controlled by adding more or less of a neutral material such as lime or quartz etc.
The charge may also be heated by heat radiating from a resistance or an electric are inside of the furnace. for which purpose electrodes are inserted in proper way. Another way of heating consists inusingatunnelfurnaceofthetypeusedfor making malleable iron castings or for roasting iron ore briquettes charging the materials in open or covered hearths on top of cars, which are gradually heated by the furnace gases when travelling along the furnace tunnel. Decarbonlsing may also take place by heating the materials in annealing pots or boxes in the normal type of stationary annealing furnaces employed in the malleable iron industry.
Even a coking furnace of the retort or chamber type may be employed for decarbonizing according to the invention. Decarbonizing may also be effected in a furnace of the pyrite roasting type in which the charge is travelling in counter current to a flow of hot gases or in a kiln for firing bricks having a plurality of chambers arranged in well known manner. One may, naturally, also use any 'kind of electric annealing furnaces heating the materials in pans or boxes or other receptacles of: heat r alloys.
When using the method for decarbonizing other metals than pig iron it-may be advisable to use other solid oxydants than stated in the case of iron One might also find it useful to increase the temperature considerably in the case of'decarboniaing FeCr and I'eMn.
Regarding the scope of my invention and the means for successfully carrying it out in the practiseIdonotwanttolimitmyselfin anycertain way and having now fully described my invention what I do claim and desire to secure by- Letters Patent of the United States of America is: 1. A method of producing low carbon iron grains, consisting in heating a charge of small iron granules, obtained by rapidly cooling molten iron in acooling fluid, while stirring the charge atmosphere of which contains atthe most 25% CO: and at least 75% CO.
3. A method of producing low carbon iron grains, consisting in heating a charge of a mixture of small iron granules, obtained by rapidly cooling molten iron in a cooling fluid, and an easily reducible iron ore in a finely divided state,
while stirring the charge by revolution in a combustion zone the atmosphere of which, containing CO:- and CO-sas. is suitably composed for oxidizing substantially only the carbon but not the iron of the granules, the heating being sumcient for decarbonizing and reducing the charge without melting it, a gas suitable for-reducing the iron ore being introduced at the end of the decarbonizing period.
4. A method of producing low carbon grains 'of aniron alloy, consisting of heating a charge of small granules of the alloy, obtained by rapidly cooling molten alloy in a cooling means, while stirring the charge by revolution in a combustion zone the atmosphere of which, containing C0:-
and CO-gas, is suitably composed for'oxidizing substantially only the carbon but not the metals g of the granules, the heating being sufficient for decarbonizing the granules but insuficient for causing them to melt.
5. A method of producing low carbon iron grains which comprises subdividing iron into small roundedgranules by rapidly cooling it while in liquid state, introducing the granules into a tubular, slightly inclining furnace, stirring the charge by rotating the furnace, heating the particles sufllciently for decarbonizing but below the melting point in an atmosphere containing a mixture of CO:- and 00-888 suitable for oxidizing only the carbon but substantially not the iron of the granules and producing the hot decarbonizing atmosphere by means of internal combustion in the furnace.
6. In a method according to claim 5, diminishing the concentration of the CO-gas in the furnace atmosphere by introducing at least one of the diluting Ha, H2 and H10.
7. A method ofproducing low carbon iron grains which comprises a subdivision of the iron into small rounded granules by rapidly cooling it while ln'a liquid state, introducing them into a tubular, slightly inclining furnace, stirring them by rotating the furnace and heating the .charge in an atmosphere of hot gases, produced by internal combustion of a fuel, said atmosphere containing a mixture of at most 25% C0: and 75% C0, substantially without oxidizing the iron.
8. A method. of producing low carbon iron granules which comprises the heating of rounded granules of iron, obtained by rapidly cooling liquid iron, in a rotating, tubular, internally heated furnace, raising the temperature of the granules sumciently for decarbonizing but below the melting point while causing the charge to be stirred and to move in a direction opposite to that of a flow of composed of C0: and C0 and at least one of thediluting gases N2, H: and H20 and preventing a substantial oxidizingof the iron by a suitable control of the proportions between the 602- and CO-gas of the furnace atmosphere.
9. A method of producing low carbon iron granules which comprises the heating and stirring of a mixture of rounded granules of iron, ob-
Y tained by rapidly cooling molten iron, and an easily reducible iron ore in a finely divided state in a rotating, slightly inclining, tubular and internally heated furnace in an atmosphere capable of decarbonizing the granules at a temperature below the melting point and then in a reducing atmosphere for producing iron from the ore component of the charge.
10. A method of producing low carbon iron grains which consists in heating granules of iron produced by rapidly cooling liquid metal together with a basic material sufliciently for decarbonizing them but below the. melting point in an atmosphere containing at least the gases C0: and CO in such proportions that substantially only carbon and sulphur are removed from theiron grains which are otherwise practically unchanged. 1
11. A method of producing low carbon iron grains which consists in granulating the iron by rapid cooling, classifying the granules according to their sizes and then heating a graduated class of granules by itself suiilciently for decarbonizing it but below the melting point in an atmosphere of gases containing at least the gases C0: and CO in a'proportion suitable for oxidizing substantially only the carbon but not jzhe iron itself.
12. In a method according to claim 10, heating the mixture of granules of iron and'basic material in a rotating, inclining tubular furnace.
IVAR WEB-FELT.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USRE21500E true USRE21500E (en) | 1940-07-02 |
Family
ID=2087306
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US21500D Expired USRE21500E (en) | Method of decarbonizing a carbon |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | USRE21500E (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2473019A (en) * | 1948-04-13 | 1949-06-14 | Union Carbide & Carbon Corp | Production of ferrochromium |
| US2831761A (en) * | 1956-05-10 | 1958-04-22 | Walter M Weil | Method for producing low-carbon ferrochromium |
| EP0085136A3 (en) * | 1982-02-01 | 1984-03-21 | Allied Iron Company | Processed ferrous metal and process of production |
| US4497671A (en) | 1982-02-01 | 1985-02-05 | Wasserman Gary L | Processed ferrous metal and process of production |
| US6749662B2 (en) | 1999-01-29 | 2004-06-15 | Olin Corporation | Steel ballistic shot and production method |
-
0
- US US21500D patent/USRE21500E/en not_active Expired
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2473019A (en) * | 1948-04-13 | 1949-06-14 | Union Carbide & Carbon Corp | Production of ferrochromium |
| US2831761A (en) * | 1956-05-10 | 1958-04-22 | Walter M Weil | Method for producing low-carbon ferrochromium |
| EP0085136A3 (en) * | 1982-02-01 | 1984-03-21 | Allied Iron Company | Processed ferrous metal and process of production |
| US4497671A (en) | 1982-02-01 | 1985-02-05 | Wasserman Gary L | Processed ferrous metal and process of production |
| US6749662B2 (en) | 1999-01-29 | 2004-06-15 | Olin Corporation | Steel ballistic shot and production method |
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