USRE13861E - William b - Google Patents
William b Download PDFInfo
- Publication number
- USRE13861E USRE13861E US RE13861 E USRE13861 E US RE13861E
- Authority
- US
- United States
- Prior art keywords
- metal
- carbon
- steel
- furnace
- iron
- Prior art date
Links
- 229910052751 metal Inorganic materials 0.000 description 74
- 239000002184 metal Substances 0.000 description 74
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 54
- 229910052799 carbon Inorganic materials 0.000 description 52
- 238000007670 refining Methods 0.000 description 44
- 229910000831 Steel Inorganic materials 0.000 description 36
- 239000010959 steel Substances 0.000 description 36
- 229910000805 Pig iron Inorganic materials 0.000 description 32
- 229910000499 pig iron Inorganic materials 0.000 description 32
- 238000000034 method Methods 0.000 description 24
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 20
- 238000004519 manufacturing process Methods 0.000 description 14
- 229910052742 iron Inorganic materials 0.000 description 10
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 10
- 229910052698 phosphorus Inorganic materials 0.000 description 10
- 239000011574 phosphorus Substances 0.000 description 10
- 241000282898 Sus scrofa Species 0.000 description 8
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical compound [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 8
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 8
- 229910052717 sulfur Inorganic materials 0.000 description 8
- 239000011593 sulfur Substances 0.000 description 8
- 229910052710 silicon Inorganic materials 0.000 description 6
- 239000010703 silicon Substances 0.000 description 6
- 238000007664 blowing Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 239000012467 final product Substances 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 102100013109 EPB41L5 Human genes 0.000 description 2
- 101710026739 EPB41L5 Proteins 0.000 description 2
- 241001272996 Polyphylla fullo Species 0.000 description 2
- 210000003625 Skull Anatomy 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 2
- 239000003830 anthracite Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 230000002939 deleterious Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 230000002349 favourable Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- PWHULOQIROXLJO-UHFFFAOYSA-N manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 2
- 229910052748 manganese Inorganic materials 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052752 metalloid Inorganic materials 0.000 description 2
- 150000002738 metalloids Chemical class 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
Definitions
- I introduce molten pig metal into a Bessemer converter and blow it therein until the silicon and incidentally a large proportion of any manganese which may be in it has been eliminated and the carbon reduced to a definite percentage, preferably to about .05 per cent., which percentage can be .gaged with accuracy because it is about the percentage containedin the metal at the time when the flame drops, a phenomenon which is well known and readily recognized by the skilled blower.
- I then add to the desiliconized and substantially decarburized metal a proportion of carbon sufiicient to raise its carbon content to a definite percentage, preferably to about .3 per cent., though this percentage ma be varied.
- the carbonaddition is prefera 1 made by adding to the Bessemer meta in the ladle pig iron either in the form of,cold pig or molten pig, and as the percentage of carbon of the Bessemer metal is substantially constant, the amount of pig metal to be added in the ladle can be readily determined with substantial precision.
- the carbon may be introduced by adding anthracite coal or powdered coke to the metal instead of adding carbon in the form of pig iron. If pig iron is added, it is preferably ,in the molten condition. The metal is thus enriched in carbon to about the same peroentage as steel.
- the recarburized metal may be charged into an electrically heated furnace where it is treated preferably with basic additions for removal of sulfur and phosphorus, and for increase of its heat to bring 1t mto the re-' fined and heated condition 1ng into the ingot. molds.
- pig iron is preferable to other recarburizing and deoxidizing means because some of the metalloids ordinarily contained therein, such as silicon for example, are more efficient than carbon at low temperatures. It is desirable to keep the temperature low, as this facilitates the extraction of phosphorus in the refining furnace. T he' recarburizing operation permits of supplying the metal at the desired low temperature because if the metal were not recarburized it wouldskull in the ladle except at high temperatures.
- the invention may be applied not only in connectionwith electric furnaces, but with. basis open-hearth furnaces and also with acid open hearth practically any of the usual refining operations whichare customarily varied inaccordance with the raw material and the desired product. It is well known that in all these refining furnaces, which use scrap, pig iron and ore, better steel can be made by using a higher percentage of scrap; the scrap being steel already with oxids and other deleterious elements removed and being subjected to a further refinement inreusing it in a new" charge.
- the blown metal rec'arburized as above described is as good as scrap steel because-the oxids and other impurities have been eliminated therefrom with the sole exception that it still contains too high a percentage of phosphorus and sulfur to be good steel.
- the metal which is. carried to the furnace by my process is nearly or as good as scrap steel. The result is a final product of uniform high quality. The process is much faster than the previous processes for I making the same quality of-steel.
- the refining furnace the metal supplied furnaces; in fact, with.
- the recarburizing may be done in the ladle between the converter and the refining furnace or it may be done in the converter after the blow has been stopped.
- l/Vhere pig iron is used it may be taken molten from a mixer, cupola or other source of supply. Enough carbon should be added, in the recarburizing operation, to make the metal boil when it is poured on or in the refining furnace, so as to mix the metal and shorten the time of heat, thus securing the desired operation with a minimum of iron ore or oxid of iron so as to keep the finalproduct as free from oxids as'possible.
- open hearth furnace usually has four or five times the containing capacity of the Bessemer converter.
- the slag-forming materials in the open hearth furnace which contain oxids are in excess for the first additions of bessemerized metal.
- the transfer ladle may be held to receive several successive heats from the Bessemer converter or it may receive heats from several Bessemer. converters blown simultaneousl y.
- What I claim is 1. In the manufacture of steel, the steps consisting 'of removing the carbon of pig iron to a substantially definite percentage, then recarburizing to a sufficient extent to lessen skulling during transfer, and then transferring the metal to and treating it in an electric furnace.
- metal to and treating it in an electric furv carbon have been oxidized out and the metal contains iron oxid, merized metal and thereby eliminating the major portion of the iron oxid and producing a metal which is substantially steel containing an excess of phosphorus, sulfur or the like, and then transferring the metal to and refining it in the usual way in a refining furnace to produce steel of the desired composition and quality.
Description
y UNITED STATES PATENT OFFICE.
WILLIAM R. WALKER, or NEW Yonx, N. Y.
MANUFACTURE OF STEEL.
Specification of Reissued Letters Patent. Reissued J 5 1915 No Drawing. Original No. 1014,425, dated January 9, 1912, Serial No. 502,865.
Reissue No. 13,538, dated February 25, 1913, Serial No. 739,414. This application for reissue filed October 9, 1914. Serial No.
To all whom it may concern:
Be it known that I, VVILLLAM R. WALKER, a citizen of the United States, residing in the city, county, and State of New .York, have invented an Improvement in the Manufacture of Steel, of which the following is a specification.
n the practice of my invention, I introduce molten pig metal into a Bessemer converter and blow it therein until the silicon and incidentally a large proportion of any manganese which may be in it has been eliminated and the carbon reduced to a definite percentage, preferably to about .05 per cent., which percentage can be .gaged with accuracy because it is about the percentage containedin the metal at the time when the flame drops, a phenomenon which is well known and readily recognized by the skilled blower. I then add to the desiliconized and substantially decarburized metal a proportion of carbon sufiicient to raise its carbon content to a definite percentage, preferably to about .3 per cent., though this percentage ma be varied. The carbonaddition is prefera 1 made by adding to the Bessemer meta in the ladle pig iron either in the form of,cold pig or molten pig, and as the percentage of carbon of the Bessemer metal is substantially constant, the amount of pig metal to be added in the ladle can be readily determined with substantial precision. The carbon may be introduced by adding anthracite coal or powdered coke to the metal instead of adding carbon in the form of pig iron. If pig iron is added, it is preferably ,in the molten condition. The metal is thus enriched in carbon to about the same peroentage as steel. It is also deoxldized by means of the added carbon and, where pig iron is used for recarburizing, by means of themanganeseand silicon in the pigiron, being in fact substantially steel containing an excess of phosphorus, sulfur or the like such as are commonly removed in refining furnaces of the electric type or of the open' hearth or other suitable type. For example, the recarburized metal may be charged into an electrically heated furnace where it is treated preferably with basic additions for removal of sulfur and phosphorus, and for increase of its heat to bring 1t mto the re-' fined and heated condition 1ng into the ingot. molds.
The importance of adding carbon to the blown metal before introducing itinto the refining furnace is that in this way the loss by skulling 1s lessened, and by bringing the metal to a definite carbon content the heats proper for eastand finished steel, are eliminated by whati everdeoxidizing agents may be present.
As theidecarbu'rized metal is low in carbon when taken from the converter and is often transferred a considerable distance to the refining furnace, a considerable amount of this metal will solidify in the ladle and form skulls therein. This skulling action will reduce the amount of metal poured into the refining furnacefrom the ladle, and as the skulling action willvary, the amount poured in will vary. By adding carbon to the metal before its-being carried to the refining furnace, I raise its carbon content and thus lower its melting point, and hence prevent or greatly lessen. the amount of skulling during the transfer to the refining furnace. This, therefore, makes the charges more uniform in amount as poured into the refining furnace.
The obtainin of a uniform carbon content is rendere easy'by adding carbon to the blown meta]. rather than by attempting to stop the blow at the desired point, for to determine'the point of stopping before the flame drops is very difiicult, while to add the necessary percentage of carbon to the bath depleted of carbon is easy.
I am aware that it is old to eliminate practically all of the'carbon in steel before recarburizing and do not desire to claim this, but I dodesire to claim the recarbu-Q time during which the metal is to be held in the ladle before pouring into the refining furnace, being greater as the'time is longer.
As above stated, pig iron is preferable to other recarburizing and deoxidizing means because some of the metalloids ordinarily contained therein, such as silicon for example, are more efficient than carbon at low temperatures. It is desirable to keep the temperature low, as this facilitates the extraction of phosphorus in the refining furnace. T he' recarburizing operation permits of supplying the metal at the desired low temperature because if the metal were not recarburized it wouldskull in the ladle except at high temperatures.
The invention may be applied not only in connectionwith electric furnaces, but with. basis open-hearth furnaces and also with acid open hearth practically any of the usual refining operations whichare customarily varied inaccordance with the raw material and the desired product. It is well known that in all these refining furnaces, which use scrap, pig iron and ore, better steel can be made by using a higher percentage of scrap; the scrap being steel already with oxids and other deleterious elements removed and being subjected to a further refinement inreusing it in a new" charge. The blown metal rec'arburized as above described is as good as scrap steel because-the oxids and other impurities have been eliminated therefrom with the sole exception that it still contains too high a percentage of phosphorus and sulfur to be good steel. As these elements are easily removed in the refining furnace the metal which is. carried to the furnace by my process is nearly or as good as scrap steel. The result is a final product of uniform high quality. The process is much faster than the previous processes for I making the same quality of-steel.
It has heretofore been proposed, with a number of variations, to use first the Bessemer converter and then the open-hearth or other refining furnace. These processes being generally referred to as the duplex proc-v ess, and it is well known that this process is extremely rapid, occupying only a small fraction of the time required for straight open-hearth or similar processes. But the product of these duplex processes is not generally believed to be as good as true openhearthsteel, The bessemerized metal used in the duplex processescontains so much oxid of iron and the removal of this oxidis so slow and difiicult in the open-hearth, that the productis not of the first grade. By my method of recarburizing between the converter. and
the refining furnace the metal supplied furnaces; in fact, with.
low temperature which is most favorable for thisoperation and consequently the operation is very rapid.
The recarburizing may be done in the ladle between the converter and the refining furnace or it may be done in the converter after the blow has been stopped. l/Vhere pig iron is used it may be taken molten from a mixer, cupola or other source of supply. Enough carbon should be added, in the recarburizing operation, to make the metal boil when it is poured on or in the refining furnace, so as to mix the metal and shorten the time of heat, thus securing the desired operation with a minimum of iron ore or oxid of iron so as to keep the finalproduct as free from oxids as'possible.
In the duplex process they open hearth furnace usually has four or five times the containing capacity of the Bessemer converter. The slag-forming materials in the open hearth furnace which contain oxids are in excess for the first additions of bessemerized metal. To improve this condition and to givetime for the carbon and other deoxidizers to better do their work of deoxidation, I prefer to have the vessel which transfers the Bessemer metal to the'openhearth furnace as nearly of the same capacity as the open-hearth furnace as possible. The transfer ladle may be held to receive several successive heats from the Bessemer converter or it may receive heats from several Bessemer. converters blown simultaneousl y.
In the ordinary duplex process there is a certain loss of iron in the blowing operation. In my improved process, since not all the pig iron is blown, there is a saving of metal amounting to a substantial item. For this reason the process may be used on higher priced iron than was possible with former processes involving blowing operations.
What I claim is 1. In the manufacture of steel, the steps consisting 'of removing the carbon of pig iron to a substantially definite percentage, then recarburizing to a sufficient extent to lessen skulling during transfer, and then transferring the metal to and treating it in an electric furnace.
2. In the manufacture of steel, the steps consisting in bessemerizing pig iron, reducing its carbon to a substantially definite percentage, then adding carbon to a sufficient extent to lessen skulling during transfer, and then transferring the metal to and treating it in an electric furnace.
3. Inthe manufacture of steel, the steps consisting of bessemerizing pig iron to a point where the flame drops, then removing themetal from the converter, adding carbon extent to lessen skulland transferring the thereto to a suflicient ing during transfer,
metal to and treating it in an electric furv carbon have been oxidized out and the metal contains iron oxid, merized metal and thereby eliminating the major portion of the iron oxid and producing a metal which is substantially steel containing an excess of phosphorus, sulfur or the like, and then transferring the metal to and refining it in the usual way in a refining furnace to produce steel of the desired composition and quality.
6. In the manufacture of steel the steps recarbur izing the besse which consist in first bessemerizing pig iron, recarburizing the bessemerized metal so as to lower its melting point and prevent skulling in the ladle, thereby also eliminating iron oxid and then transferring the metal to and refining it in the usual way in a refining furnace.
7. In the manufacture of steel, the steps consistirfg of first bessemerizing pig iron, then introducing pig iron into the bessemerized metal to recarburize the same and to eliminate iron oxid therefrom by means of the deoxidizing agents present in the pig iron and afterward refining the bessemerized metal in the usual way in a refining furnace.
In Witness whereof, I have hereunto signed my name in the presence of two subscribing Witnesses.
"WILLIAM R. WALKER.
Witnesses GEO. G. HussEL, LULU STUBENYALL.
Family
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