US3244510A - Method of making electrical steel having superior magnetic properties - Google Patents
Method of making electrical steel having superior magnetic properties Download PDFInfo
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- US3244510A US3244510A US280907A US28090763A US3244510A US 3244510 A US3244510 A US 3244510A US 280907 A US280907 A US 280907A US 28090763 A US28090763 A US 28090763A US 3244510 A US3244510 A US 3244510A
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
- C21C7/076—Use of slags or fluxes as treating agents
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/02—Ferrous alloys, e.g. steel alloys containing silicon
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- 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
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- FIG. 1 is a graph illustrating such effect. As is shown in the graph, the lower the carbon content and the lower the sulphur and oxygen contents, the lower will be the watt loss.
- This invention is not limited to the use with a single fixed type of furnace. However, more satisfactory results have been found to be obtainable with the tilting open-hearth furnace than with the L-D oxygen converter or the stationary open-hearth furnace.
- deoxidizers such as aluminum, silicon, etc., singly or mixed, to the molten metal in the ladle in order to remove oxygen therefrom.
- the agents thus added react with the oxygen in the bath, or mass of molten metal, to form deoxidation products. The greater part of the deoxidation products is removed from the bath but not completely.
- the variety and quantity of the deoxidizers can be so regulated that the products which are formed as a result of the reaction of the deoxidizers with the oxygen in the bath be made highly fluid and their melting point be lowered, the formation of the residual products in the bath, especially that of the deoxidation products having a high melting point, which are evenly dispersed in the entire bath and affect adversely the magnetic properties of the steels, can be prevented.
- FIG. 1 is a graph illustrating the influence of carbon, oxygen, sulphur, and phosphorus on the hysteresis loss of the electrical steels
- FIG. 2 is a diagram illustrating partial section of the apparatus used in connection with this invention.
- the apparatus illustrated in FIG. 2 comprises a tilting open-hearth furnace 11 having a spout 12 from which a stream of slag free molten metal 13 issues, striking a slag layer 14 at the surface 15 of a body of molten metal 16 in a tap ladle 17 into which the molten metal 13 is poured.
- a hopper 19 containing agents to be added which are a mixture of solid particles or granules of aluminum, calcium, silicon, soda ash, fluorspar, cryolite, synthetic electric furnace slag, etc., and has a mechanism to regulate the pouring quantity and the pouring position.
- a chute 18 of the hopper is arranged so as to cause the stream of the addition agents, to be adjusted and to pour in the desired quantity, to continuously strike the bath of the ladle 17 at the same point as does the entering stream of molten metal.
- the addition agents in the ladle 17 contribute to deoxidation and desulphurization of the charge, while on the other hand the flux, which has a low melting point, melts instantly, and, because of its lower gravity, covers the bath surface forming a slag layer 14.
- the size of the granules is preferably limited to 10-50 mm. in diameter for deoxidizers and 10 mm. or under for other slag forming and purifying agents: the smaller the size the more advantageous will they be for the actual operations of this invention.
- the chute 18 is arranged so as to cause a stream of the mixture 21 to strike the slag surface 14 and the metal surface 15 at the same point as does the stream of entering molten metal so that complete and continuous mixing is accomplished at the point of entry of the streams into the molten metal bath 16.
- Silicon or silicon compound which may be added at this stage is selected and regulated quantitatively accord: ing to the requirements of the type of steel to be produced.
- the quantity of aluminum and calcium is regulated according to the volume of silicon added, and it is fixed in consideration of the amount needed to realize complete deoxidization of the charge and low melting temperature of the deoxidized products.
- the desulphurization is accomplished with a flux consisting of the sodium carbonate and calcium fluoride or cryolite, or the like.
- W/50 1.55-1.61 w./kg.-watts per kilogram at 10,000 gausses and 50 cycles.
- the solid particles of silicon together with other fluxing or purifying materials are added to the metal while it is still in the stream.
- the invention is not limited, however, to the producing of electrical silicon steel and other alloys may be produced from the molten metal by directing into the stream of molten metal a stream of solid particles including an alloying material such as particles of molybdenum or tungsten or chromium or nickel or vanadium or titanium or copper or compounds or alloys thereof in addition to or instead of silicon or silicon compound or alloy according to what resultant alloy it is desired to produce.
- the method of producing low loss high permeability silicon steel which comprises the steps of charging an iron alloy into a furnace, reducing the carbon content in the furnace, tapping the furnace and causing a stream of molten metal to issue into a ladle to form a mass of molten steel in the ladle, and directing a stream of flux particles against the molten iron stream at its point of entry into the ladle at the molten metal level, said flux particles comprising silicon and a desulphurization agent which react with the steel to form a slag highly fluid at molten iron temperature.
- the method of producing electrical steel which comprises the steps of introducing a stream of molten silicon steel into a ladle to form a bath of molten metal and simultaneously directing against the molten steel stream, at its point of entry into the bath at the molten metal level, a stream of desulphurization agent comprising a substance selected from' the group consisting of cryolite and a mixture of sodium carbonate and calcium fluoride in the form of granules 10 millimeters in diameter or under.
- the method of producing electrical steel which comprises the steps of melting a silicon steel having a nitrogen content below 0.003% in a furnace, tapping the furnace to form a stream of molten metal directed into a ladle to form a molten steel bath and continuously directing against the stream of metal at its point of entry into the bath a flux stream composed of solid particles of silicon and a substance selected from the group consisting of cryolite and a mixture of sodium carbonate and calcium fluoride.
- the method of producing silicon steel which comprises the steps of melting the steel, pouring the steel in the form of a stream of molten metal into a ladle to form a bath of molten metal and continuously directing against the stream of molten metal, at its point of entry into the bath, a flux stream composed of desulphurizing and deoxidizing agents and silicon.
- the method of producing silicon steel with a sulphur content as low as 0.006% and total content of oxidized inclusions not over 0.02% which comprises the steps of melting a steel having a composition including approximately 0.028% carbon, 0.04% manganese, a trace of silicon, 0.010% phosphorous and 0.011% sulphur and a nitrogen content of 0.003% or less, pouring the steel into a ladle as a stream of molten metal to form a bath of molten steel and directing a stream of flux particles against the molten metal stream at its point of entry into the bath, said flux particles comprising 2 to 10 kilograms each of soda ash and fiu'orspar per ton of molten metal.
- the method of producing electrical steel with a loss between 1.55 and 1.61 watts per kilogram at 10,000 gausses and cycles which comprises the steps of melting a steel having the composition of approximately 0.028% carbon, 0.04% manganese, a trace of silicon, 0.010% phosphorous, 0.011% sulphur, pouring the molten steel into a ladle in a stream to form a bath of molten steel and projecting against the stream of molten steel at its point of entry into the bath a stream of solid particles of silicon, desulphurizer and deoxidizer.
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Description
Aprll 1956 v N. P. GOSS ETAL METHOD OF MAKING ELECTRICAL STEEL HAVING SUPERIOR MAGNETIC PROPERTIES Filed May 16, 1963 VZOO O O W 5 mm 6 V0, N N A W O 2 U. vb w l M m u 2 n m NC a 5a m 09 0 6 m O I n 4 I O o o o 4 51-1020 WATANABE Ko KUMA/ 55/20 TEUDA ATTOENEYE.
United States Patent 3,244,510 METHGD 0F MAKIN G ELECTRICAL STEEL HAV- IN G SUPERIOR MAGNETIC PROPERTHES Norman P. Goss, South Euclid, Ohio, and Show Watauabe, Ko Kumai, Seizo Tsuda, and Hideo Matsuoka, all of Hirohata-ku, Himeji, Japan, assignors to Fuii Iron & Steel Co., Ltd., Tokyo, Japan Filed May 16, 1963, Ser. No. 280,907 6 Claims. (Cl. 75-55) This invention relates to the production of electrical steels which have superior magnetic properties. An object of the invention is to improve ladle practice in the production of electrical steels and to produce electrical steels having superior magnetic properties, with ease and without incurring a large amount of expenditure.
For magnetic materials to be used for electrical equipment and machinery, it is highly desirable to use materials of low watt loss and. high permeability. Such materials are usually produced by rolling and heat-treating steels whose silicon content is or under, e.g., between 0.25% and 3.0%. It is well known that the degree of purity of the steel has a marked effect upon their watt loss and permeability. FIG. 1 is a graph illustrating such effect. As is shown in the graph, the lower the carbon content and the lower the sulphur and oxygen contents, the lower will be the watt loss.
While it is comparatively easy to remove carbon from the steels to obtain lower watt loss and better permeability either by open-coiled annealing or by continuous annealing in an atmosphere of relatively high dew point, sulphur can be removed only by subjecting the steels to a high temperature annealing for a long time. Such treatment is both operationally difficult as well as expensive, especially for electrical steels of field-grade and motorgrade which are sold at relatively low prices.
As illustrated in FIG. 1, in order to obtain desirable magnetic properties, it is necessary to reduce carbon to 0.02% or under and sulphur to 0.01% or under. This can be achieved in the furnace by ordinary steelmaking process by selecting materials to be charged and by lengthening the refining period.
However, it is not easy to regulate the process so that sulphur in each heat be 0.010% or under constantly.
it is accordingly an object of our invention to provide a simple and economical operation of removing sulphur and reducing non-metallic inclusions in the electrical steels such as silicon steels during their melting, tapping, and reladling.
This invention is not limited to the use with a single fixed type of furnace. However, more satisfactory results have been found to be obtainable with the tilting open-hearth furnace than with the L-D oxygen converter or the stationary open-hearth furnace.
It is a matter of common practice to add deoxidizers such as aluminum, silicon, etc., singly or mixed, to the molten metal in the ladle in order to remove oxygen therefrom. The agents thus added react with the oxygen in the bath, or mass of molten metal, to form deoxidation products. The greater part of the deoxidation products is removed from the bath but not completely. If, however, the variety and quantity of the deoxidizers can be so regulated that the products which are formed as a result of the reaction of the deoxidizers with the oxygen in the bath be made highly fluid and their melting point be lowered, the formation of the residual products in the bath, especially that of the deoxidation products having a high melting point, which are evenly dispersed in the entire bath and affect adversely the magnetic properties of the steels, can be prevented.
It is also a well known practice to use soda ash, fluorspar, etc., for desulphurization. However, there has "ice been no case in which deoxidation and desulphurization are effected simultaneously. We have succeeded in effecting the two processes simultaneously with alloying and removing inclusions to limits never before attained, thereby removing almost completely the undesirable elements formed in the bath, so that electrical steels having superior magnetic characteristics may be produced easily and economically.
The following shows actual operations of the process:
FIG. 1 is a graph illustrating the influence of carbon, oxygen, sulphur, and phosphorus on the hysteresis loss of the electrical steels, and FIG. 2 is a diagram illustrating partial section of the apparatus used in connection with this invention.
The apparatus illustrated in FIG. 2 comprises a tilting open-hearth furnace 11 having a spout 12 from which a stream of slag free molten metal 13 issues, striking a slag layer 14 at the surface 15 of a body of molten metal 16 in a tap ladle 17 into which the molten metal 13 is poured. There is a hopper 19 containing agents to be added which are a mixture of solid particles or granules of aluminum, calcium, silicon, soda ash, fluorspar, cryolite, synthetic electric furnace slag, etc., and has a mechanism to regulate the pouring quantity and the pouring position. A chute 18 of the hopper is arranged so as to cause the stream of the addition agents, to be adjusted and to pour in the desired quantity, to continuously strike the bath of the ladle 17 at the same point as does the entering stream of molten metal. The addition agents in the ladle 17 contribute to deoxidation and desulphurization of the charge, while on the other hand the flux, which has a low melting point, melts instantly, and, because of its lower gravity, covers the bath surface forming a slag layer 14.
In order to precipitate reaction of the addition agents, the size of the granules is preferably limited to 10-50 mm. in diameter for deoxidizers and 10 mm. or under for other slag forming and purifying agents: the smaller the size the more advantageous will they be for the actual operations of this invention. The molten metal poured afterwards now runs through this slag layer 14 into the bath, thus filtering out solid. oxide inclusions.
The chute 18 is arranged so as to cause a stream of the mixture 21 to strike the slag surface 14 and the metal surface 15 at the same point as does the stream of entering molten metal so that complete and continuous mixing is accomplished at the point of entry of the streams into the molten metal bath 16.
Silicon or silicon compound which may be added at this stage is selected and regulated quantitatively accord: ing to the requirements of the type of steel to be produced.
The quantity of aluminum and calcium is regulated according to the volume of silicon added, and it is fixed in consideration of the amount needed to realize complete deoxidization of the charge and low melting temperature of the deoxidized products.
The desulphurization is accomplished with a flux consisting of the sodium carbonate and calcium fluoride or cryolite, or the like.
Following are the results of actual operations.
The process of this invention on the molten metal containing C, 0.028%; Si, trace; S, 0.011%; Mn, 0.04%; and P, 0.010%; was carried out with the addition of de oxidizer, and 210 kgs. each of soda ash and fluorspar per ton of the molten metal. The result showed that the sulphur content has been reduced from 0.011% at the time of tapping to 0.006%. The total content of oxidized inclusions have also been reduced to 0.02% or under, which is approximately 50% lower than the reduction achieved by other conventional processes. Best results are obtained from a melt having a nitrogen content of 0.003% or less.
Silicon steel thus produced with content of 1.3% silicon, has been rolled. to a sheet of 0.5 mm. thickness and the following superior magnetic characteristics have been obtained:
Watt loss (W/50): 1.55-1.61 w./kg.-watts per kilogram at 10,000 gausses and 50 cycles.
Flux density (H25): 16.2-16.6 kg.kilogausses at a field strength of 25 Gilberts per centimeter.
In producing silicon steel the solid particles of silicon together with other fluxing or purifying materials are added to the metal while it is still in the stream. The invention is not limited, however, to the producing of electrical silicon steel and other alloys may be produced from the molten metal by directing into the stream of molten metal a stream of solid particles including an alloying material such as particles of molybdenum or tungsten or chromium or nickel or vanadium or titanium or copper or compounds or alloys thereof in addition to or instead of silicon or silicon compound or alloy according to what resultant alloy it is desired to produce.
While the invention has been described as embodied in concrete form and as operating in a specific manner in accordance with the provisions of the patent statutes, it should be understood that the invention is not limited thereto, since various modifications will suggest themselves to those skilled in the art without departing from the spirit of the invention.
What is claimed. is:
1. The method of producing low loss high permeability silicon steel which comprises the steps of charging an iron alloy into a furnace, reducing the carbon content in the furnace, tapping the furnace and causing a stream of molten metal to issue into a ladle to form a mass of molten steel in the ladle, and directing a stream of flux particles against the molten iron stream at its point of entry into the ladle at the molten metal level, said flux particles comprising silicon and a desulphurization agent which react with the steel to form a slag highly fluid at molten iron temperature.
2. The method of producing electrical steel which comprises the steps of introducing a stream of molten silicon steel into a ladle to form a bath of molten metal and simultaneously directing against the molten steel stream, at its point of entry into the bath at the molten metal level, a stream of desulphurization agent comprising a substance selected from' the group consisting of cryolite and a mixture of sodium carbonate and calcium fluoride in the form of granules 10 millimeters in diameter or under.
3. The method of producing electrical steel which comprises the steps of melting a silicon steel having a nitrogen content below 0.003% in a furnace, tapping the furnace to form a stream of molten metal directed into a ladle to form a molten steel bath and continuously directing against the stream of metal at its point of entry into the bath a flux stream composed of solid particles of silicon and a substance selected from the group consisting of cryolite and a mixture of sodium carbonate and calcium fluoride.
4. The method of producing silicon steel, which comprises the steps of melting the steel, pouring the steel in the form of a stream of molten metal into a ladle to form a bath of molten metal and continuously directing against the stream of molten metal, at its point of entry into the bath, a flux stream composed of desulphurizing and deoxidizing agents and silicon.
5. The method of producing silicon steel with a sulphur content as low as 0.006% and total content of oxidized inclusions not over 0.02% which comprises the steps of melting a steel having a composition including approximately 0.028% carbon, 0.04% manganese, a trace of silicon, 0.010% phosphorous and 0.011% sulphur and a nitrogen content of 0.003% or less, pouring the steel into a ladle as a stream of molten metal to form a bath of molten steel and directing a stream of flux particles against the molten metal stream at its point of entry into the bath, said flux particles comprising 2 to 10 kilograms each of soda ash and fiu'orspar per ton of molten metal.
6. The method of producing electrical steel with a loss between 1.55 and 1.61 watts per kilogram at 10,000 gausses and cycles which comprises the steps of melting a steel having the composition of approximately 0.028% carbon, 0.04% manganese, a trace of silicon, 0.010% phosphorous, 0.011% sulphur, pouring the molten steel into a ladle in a stream to form a bath of molten steel and projecting against the stream of molten steel at its point of entry into the bath a stream of solid particles of silicon, desulphurizer and deoxidizer.
References Cited by the Examiner UNITED STATES PATENTS 1,318,164 10/1919 McConnell -46 1,770,395 7/1930 Frevert 75-55 1,925,247 9/1933 Hennig 7546 2,146,926 2/1939 Andrews 7555 2,305,052 12/1942 Yoc om 7546 2,540,173 2/1951 Olivo 75--78 2,799,575 7/1957 Tisdale et al 7555 2,866,703 12/1958 6058 7555 2,990,272 6/1961 Shaw et a1. 7555 3,099,552 7/1963 Landig et al 7557 DAVID L. RECK, Primary Examiner.
B. HENKIN, Assistant Examiner.
Claims (1)
1. THE METHOD OF PRODUCING LOW LOSS HIGH PERMEABILITY SILICON STEEL WHICH COMPRISES THE STEPS OF CHARGING AN IRON ALLOY INTO A FURNACE, REDUCING THE CARBON CONTENT IN THE FURNACE, TAPPING THE FURNACE AND CAUSING A STREAM OF MOLTEN METAL TO ISSUE INTO A LADLE TO FORM A MASS OF MOLTEN STEEL IN THE LADLE, AND DIRECTING A STREAM OF FLUX PARTICLES AGAINST THE MOLTEN IRON STREAM AT ITS POINT OF ENTRY INTO THE LADLE AT THE MOLTEN METAL LEVEL, SAID FLUX PARTICLES COMPRISING SILICON AND A DESULPHURIZATION AGENT WHICH REACT WITH THE STEEL TO FORM A SLAG HIGHLY FLUID AT MOLTEN IRON TEMPERATURE.
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US280907A US3244510A (en) | 1963-05-16 | 1963-05-16 | Method of making electrical steel having superior magnetic properties |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3768996A (en) * | 1970-07-10 | 1973-10-30 | Arbed | Granular additive for electrorefining of steel |
Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1318164A (en) * | 1919-10-07 | John mcconnell | ||
US1770395A (en) * | 1928-02-21 | 1930-07-15 | Harry L Frevert | Process of desulphurizing ferrous metal |
US1925247A (en) * | 1929-08-16 | 1933-09-05 | Charles T Hennig | Purifying ferrous metals |
US2146926A (en) * | 1938-02-11 | 1939-02-14 | Brassert & Co | Method for the removal of sulphur from molten ferrous metal |
US2305052A (en) * | 1939-12-09 | 1942-12-15 | Gordon M Yocom | Manufacture of acid bessemer steel |
US2540173A (en) * | 1948-01-30 | 1951-02-06 | Olivo Mario | Cupola briquette |
US2799575A (en) * | 1953-07-16 | 1957-07-16 | Molybdenum Corp | Method of producing iron and steel and composition therefor |
US2866703A (en) * | 1956-05-28 | 1958-12-30 | Diamond Alkali Co | Treated molten metal |
US2990272A (en) * | 1960-03-29 | 1961-06-27 | Allegheny Ludlum Steel | Desulphurizing molten iron |
US3099552A (en) * | 1958-10-21 | 1963-07-30 | Gen Electric | Method of making low sulfur steel |
-
1963
- 1963-05-16 US US280907A patent/US3244510A/en not_active Expired - Lifetime
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1318164A (en) * | 1919-10-07 | John mcconnell | ||
US1770395A (en) * | 1928-02-21 | 1930-07-15 | Harry L Frevert | Process of desulphurizing ferrous metal |
US1925247A (en) * | 1929-08-16 | 1933-09-05 | Charles T Hennig | Purifying ferrous metals |
US2146926A (en) * | 1938-02-11 | 1939-02-14 | Brassert & Co | Method for the removal of sulphur from molten ferrous metal |
US2305052A (en) * | 1939-12-09 | 1942-12-15 | Gordon M Yocom | Manufacture of acid bessemer steel |
US2540173A (en) * | 1948-01-30 | 1951-02-06 | Olivo Mario | Cupola briquette |
US2799575A (en) * | 1953-07-16 | 1957-07-16 | Molybdenum Corp | Method of producing iron and steel and composition therefor |
US2866703A (en) * | 1956-05-28 | 1958-12-30 | Diamond Alkali Co | Treated molten metal |
US3099552A (en) * | 1958-10-21 | 1963-07-30 | Gen Electric | Method of making low sulfur steel |
US2990272A (en) * | 1960-03-29 | 1961-06-27 | Allegheny Ludlum Steel | Desulphurizing molten iron |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3768996A (en) * | 1970-07-10 | 1973-10-30 | Arbed | Granular additive for electrorefining of steel |
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