US3841861A

US3841861A - Addition agent for deoxidizing and recarburizing degassed steel and method employing the same

Info

Publication number: US3841861A
Application number: US00302832A
Authority: US
Inventors: R Miltenberger
Original assignee: National Steel Corp
Current assignee: National Steel Corp
Priority date: 1969-04-15
Filing date: 1972-11-01
Publication date: 1974-10-15
Anticipated expiration: 1991-10-15

Abstract

An addition agent is provided for deoxidizing and recarburizing vacuum degassed steel which consists essentially of carbon, aluminum and/or silicon, manganese and iron, and a binder therefor when in the form of briquettes. The invention also provides a novel method of deoxidizing and recarburizing vacuum degassed steel which utilizes the addition agent of the invention. In one variant of the invention, a melt of steel prepared by a basic oxygen process is vacuum degassed and then deoxidized and recarburized with the addition agent of the invention to produce molten killed steel having an ultra low oxygen content which may be continuously cast to produce steel shapes with properties similar to rimmed steel.

Description

United States Patent Miltenberger Oct. 15, 1974 [5 ADDITION AGENT FOR DEOXIDIZING AND 3,230,074 1/1966 Roy 75/49 RECARBURIZING DEGASSED STEEL AND w p tt Ol'llS t METHOD EMPLOYING THE SAME 3,512,957 5 1970 Brotzmann 75/49 [75] Inventor: Robert S. Miltenberger, Weirton,

W. Va.

[73] Assignee: National Steel Corporation,

Pittsburgh, Pa.

[22] Filed: Nov. 1, 1972 [21] Appl. No.: 302,832

Related US. Application Data [62] Division of Ser. No. 816,418, April 15, 1969, Pat,

[52] US. Cl 75/53, 75/58, 164/82 [51] Int. Cl. C21c 7/06, B22d 11/00 [58] Field of Search 75/48, 53,49, 58, 129, 75/51; 164/56, 82

[56] References Cited UNITED STATES PATENTS 2,068,793 1/1937 Frauenknecht 75/48 2,726,952 12/1965 Morgan 75/49 3,218,157 11/1965 Dobrowsky 75/51 Primary ExaminerL. Dewayne Rutledge Assistant Examiner-Peter D. Rosenberg Attorney, Agent, or Firm-Shanley and O'Neil [57] ABSTRACT An addition agent is provided for deoxidizing and recarburizing vacuum degassed steel which consists essentially of carbon, aluminum and/or silicon, manganese and iron, and a binder therefor when in the form of briquettes. The invention also provides a novel method of deoxidizing and recarburizing vacuum degassed steel which utilizes the addition agent of the invention. In one variant of the invention, a melt of steel prepared by a basic oxygen process is vacuum degassed and then deoxidized and recarburized with the addition agent of the invention to produce molten killed steel having an ultra low oxygen content which may be continuously cast to produce steel shapes with properties similar to rimmed steel.

11 Claims, N0 Drawings ADDITION AGENT FOR DEOXIDIZING AND RECARBURIZING DEGASSED STEEL AND METHOD EMPLOYING THESAME This is a division, of application Ser. No. 816,418, filed Apr. 15, 1969, now US. Pat. No. 3,702,243.

BACKGROUND OF THE INVENTION One recent important innovation in steel making is the casting of molten steel continuously into semifinished shapes such as blooms, slabs and billets. The successful continuous casting of shapes equivalent in section to conventional semifmished shapes eliminates the ingot and primary mill stages of conventional prior art rolled steel production, and thus affords important economic advantages.

Although the continuous casting of steel appears to be simple in principle, there are many difficulties inherent in the process. This is due in part to the high melting point, high specific heat, and low thermal conductivity of steel, and the necessity for close control of variables such as the temperature of the molten steel in the tundish, which supplies molten steel to the water cooled mold. Additionally, it is necessary that the molten steel be killed sufficiently so that it will not effervesce in the mold to an extent such that blowholes form in the surface of the shapes as they are cast. Any tendency of the molten steel to effervesce excessively and form blowholes in the thin skin that is initially formed around the molten steel interior of the shapes is very undesirable. This is true from the standpoint of weakening the skin and increasing the chance of escape of molten steel therefrom, as well as from the standpoint of surface imperfections. The initial thickness of the skin on the shape as it is withdrawn from the mold is dependent to some extent on the temperature of the molten metal in the tundish. Also, the initial temperature of the molten steel fed to the mold is of importance as the solidification rate must be predictable so as to form a skin of sufficient thickness and strength to support the casting. It is therefore apparent that an entirely successful continuous casting operation depends to a large extent upon providing deoxidized steel which is at a uniform proper casting temperature which does not vary greatly from melt to melt.

The melt of steel to be continuously cast may be prepared by any suitable prior art steel making practice. However, the basic oxygen process results in substantially lower costs and thus is often preferred.

In accordance with one prior art basic oxygen process, the converter is charged with scrap, molten ferrous metal from a blast furnace, and other conventional charge materials necessary to produce a low carbon steel upon blowing with oxygen. In instances where the melt is to be cast into conventional ingots, the final temperature need not be higher than about 2,900F. and it is possible. to stop the blowafter the manganese, silicon, phosphorus and sulfur have been reduced to desirable levels. Under these conditions, the carbon remains at a level sufficiently high to impart strength to the steel even after vacuum degassing. However, in instances where the melt is to be cast continuously into semifinished shapes, the melt temperature should be about 50-75F. higher, i.e., about 2,950-2,975F. and thus if the heats are overcharged with scrap it is necessary to continue the blow for a longer period of time to assure that the higher melt temperature is attained.

This usually lowers the carbon content to about 0.04-0.06 percent. The oxygen content is about 500-700 parts per million, and it is necessary to deoxidize the steel before continuous casting. Deoxidation may be effected by making aluminum and/or silicon additions, but in such instances the steel contains undesirably high aluminum, silicon, aluminum oxide and/or silicate contents for certain uses such as container stock. As a result, it is necessary to deoxidize the steel by vacuum degassing. The molten steel is degassed by subjecting it to a sharply reduced pressure, and preferably to a vacuum approaching l2 millimeters of mercury or less. Several suitable prior art processes are known, such as the Dortmund-Hoerder (D-H) process and the Ruhrstahl-Heraeus (R-H) process. In these processes, the molten steelis subjected to a vacuum in an evacuated vessel for a sufficient period of time to evolve the gases and for the gases to be removed by a vacuum connection. The reaction of carbon with oxygen to produce carbon monoxide which is evolved is highly endothermic, and thus the initial temperature of the melt is reduced substantially in instances where it is desired to reduce the oxygen content to below parts per million. The carbon content is also reduced markedly, and usually to 0.03 percent or less. Thus insufficient carbon remains in the steel to provide strength for certain end uses such as container stocks.

In view of the foregoing, the preparation of blackplate strip or sheet for container stock presents a series of problems which have not been adequately solved by the prior art in instances where it is desired to combine a basic oxygen steelmaking process with vacuum degassing and continuous casting.

SUMMARY OF THE INVENTION The present invention provides a novel exothermic addition agent which is especially useful for deoxidizing and recarburizing vacuum degassed steel. The addition agent consists essentially of carbon, aluminum and/or silicon, and iron. A binder may be present when the ingredients arein particulate form initially and it is desired to form briquettes therefrom.

The invention also provides a novel method of deoxidizing and recarburizing vacuum degassed steel which utilizes the above described addition agent of the invention. Inasmuch as the aluminum and/or silicon contents of the addition agent react exothermically with oxygen contained in the molten steel, this offsets the endothermic reaction between carbon and oxygen and aids in maintaining the desired temperature of the melt for continuous casting.

In one preferred variant of the invention, steel prepared by a basic oxygen process may be vacuum degassed, and then further deoxidized and recarburized with the addition agent of the invention to produce a molten killed steel having an ultra low oxygen content.- The molten steel remains at a sufficiently high temperature for continuous casting, and it is possible to produce semifinished steel shapes therefrom having prop erties similar to rimmed or capped steel. The carbon content is sufficiently high to impart strength and allow the finished steel to be used where rimmed or capped steel has been used heretofore.

DETAILED DESCRIPTION OF THE INVENTION INCLUDING PREFERRED VARIANTS THEREOF The addition agent of the invention consists essentially of (1) carbon, (2) aluminum and/or silicon, (3) manganese and (4) iron. Each ingredient has an important function and contributes to the unique properties of the overall composition. For instances, the carbon recarburizes the vacuum degassed steel, increases strength, and provides additional carbon for reaction with oxygen in the melt to produce carbon monoxide and carbon dioxide which are evolved. The aluminum and/or silicon react exothermically with oxygen contained in the molten steel and reduce the reaction rate between the carbon and oxygen. The carbon alone reacts violently with the oxygen content of the melt, and this causes metal splashing and spitting into the vacuum duct of the degassing apparatus which is undesirable. The ductwork of the degassing apparatus is refractory lined in the vicinity of the vacuum chamber, and steel deposited on the refractory linings will later be oxidized by the preheater or gas burner. The iron oxide thus produced will attack the refractory linings and cause excessive wear and eventually premature failure. The aluminum and/or silicon also deoxidize the molten steel, and the exothermic reaction thereof with oxygen offsets at least to some extent the heat loss due to the endothermic reaction of the carbon with oxygen. The iron and manganese are economic specific gravity increasing agents or sinkers," and the manganese also insures an increase in the manganese content of the steel which is desirable.

The ratio by weight of carbon to the exothermic sub stance, i.e., aluminum, silicon, and mixtures or alloys thereof, should be between about 1:4 and 3:2 and is preferably about 1:1. The manganese, iron and mixtures or alloys thereof may be present in a combined amount by weight of at least 25 percent and perferably at least 50 percent of the total weight of carbon and the exothermic substance. However, for best results the weight of manganese and/or iron should not exceed the combined weight of carbon and the exothermic substance.

One specific additive composition which is especially useful contains 3040 parts by weight of carbon, 30-40 parts by weight of aluminum, and -40 parts by weight of combined manganese and/or iron. Still another specific composition which is especially useful contains 30-40 parts by weight of carbon, 30-40 parts by weight of silicon, and 2040 parts by weight of combined manganese and/or iron.

The sources of carbon need not differ from those used in the prior art for recarburizing molten steel. For example, the carbon source may be graphite, carbon black, petroleum coke, coke prepared from coal, or other suitable carbonaceous materials. The particle size of the carbon is not critical and may vary from the microscopic particles in carbon black to grannules of graphite or coke of a size suitable for briquetting.

In instances where the exothermic substance is aluminum, it may be in the form of, for example, aluminum shot, aluminum turnings, aluminum powder or grannules, chopped aluminum wire, shredded aluminum sheet, or suitable aluminum alloys and aluminum containing compositions which do not contain deleterious ingredients. When silicon is the exothermic substance, it may be in the form of, for example, elemental silicon, ferrosilicon, silicomanganese, and other suitable alloys or silicon-containing substances which do not include deleterious ingredients. The siliconcontaining material may be in a particulate form such as powder, pellets, grannules or fines of a size suitable for briquetting.

The manganese and/or iron may be present as metallic manganese, metallic iron, ferromanganese, or other suitable manganese and/or iron-containing substances which do not include deleterious ingredients. The manganese and/or iron-containing material may be, for example, in the form of shot, pellets, grannules or lines of a size suitable for briquetting. The manganese and/or iron are preferably present in an amount to increase the specific gravity of the mixture sufficiently to assure that the additive will be immersed in or sink into the ferrous metal melt to be treated.

When a binder is present and the ingredients are in particulate form, the addition agent may be formed into desired shapes or compacts. In most instances, the binder should be present in an amount of about l-l0 parts by weight for each parts by weight of the remaining ingredients, and preferably in an amount of about 1-5 parts by weight. The specific nature of the binder is not of importance so long as it is effective and does not contain substances which would be deleterious, but preferably the binder is a substance which will decompose at the temperature of the melt and leave little or no residue. The binder may be in accordance with prior art practice, and it may include one or more substances such as molasses or other sugar containing substances, starch and starch derivatives, bituminous materials such as coal tar, petroleum asphalt, pitches, and their component fractions including resins and asphaltenes, proteinaceous derivatives or adhesives such as casein and glue, synthetic thermoplastic and thermosetting resins such as phenol-formaldehyde resins, and inorganic materials such as alkali metal silicates and other water soluble silicates. It is understood that still other suitable prior art binders for metallurgical additives may be employed when desired.

The binder may be mixed with the remaining ingredients in particulate form, and briquettes or shapes may be prepared by applying pressure thereto, balls or generally spherical shapes may be prepared by molding or compacting the mixture, the mixture may be extruded in the form of elongated or rod-like shapes which are cut into desired lengths, or other suitable methods may be used. Regardless of the method of manufacture or the configuration of the shapes, they are referred to herein as being briquettes for purposes of simplifying the dicussion. The briquettes may be of any suitable size, but are preferably not more than about 3 inches in one dimension. The briquettes may be, for example, about 0.25-3 inches, but better results are usually obtained with briquettes having a size of about 0.5-2 inches. Briquettes having a generally spherical configuration and a diameter of about l-3 inches usually give the best results.

In instances where a binder is not employed and the ingredients are in particulate form, the mixture may be partially fused or sintered to cause the particles to adhere together upon cooling. In instances where the agglomerated product thus produced contains particles which are too large, they may be reduced in size by crushing to the size range noted above for the briquettes. It is also possible to pack the ingredients into ferrous metal containers without a binder being present, and then apply pressure to the filled containers to thereby compact the same and increase the specific gravity. The compacted filled containers may be added to ferrous metal melts in the same manner as the briquettes referred to herein.

When practicing the method of the invention, the addition agent is added to a melt of steel which is subjected to a reduced pressure to produce degassed steel in an amount to further deoxidize and recarburize the steel to a desired extent. For instance, one or more portions of the addition agent may be added to the steel while it is being vacuum degassed and/or after it has been vacuum degassed to a desired oxygen content. Preferably, at least some degassing is performed after the addition agent has been added to aid in removing any additional carbon monoxide that is evolved.

The amount of the addition agent to be used may vary over wide ranges, but preferably it is added in an amount' to provide no more than 0.05 percent by weight, and preferably less than 0.02 percent by weight, of residual aluminum and/or silicon in the treated steel. ln instances where the steel melt to be treated is prepared by a basic oxygen process, then the addition agent may be added at a rate to provide the carbon and exothermic substance in a combined amount of about 0.5-4 pounds per ton of steel, and preferably in an amount of about 2.0-2.5 pounds per ton of steel. The best results are often obtained with about 2.25 pounds of the carbon and exothermic substance per ton of steel.

The combination of vacuum degassing and the deoxidizing effect of the exothermic substance is sufficient to assure that the deoxidized and recarburized steel will not effervesce in the mold sufficiently to produce a rimming action of surface blowholes when the steel is continuously cast. The low carbon steels produced by a basic oxygen process and which are preferred in practicing the presentinvention contain not more than 0.15 percent and often less than 0.10 percent carbon, and in most instances about 0.06-0.08 percent carbon. The manganese content is less than 1.0 percent and usually about 0.25-0.75 percent the silicon content is less than 0.05 percent and usually below 0.02 percent, the phosphorus content is less than 0.05 percent and usually below 0.02 percent, the sulfur content is less than 0.05 percent and usually below 0.03 percent, and the remainder is iron and incidental impurities. Trace amounts of tramp elements such as copper, tin, lead, zinc and the like may be present, but their concentrations are very low. The oxygen content of the steel is below 1,000 parts per million (ppm), and is usually about 500-700 ppm.

When a steel of the above type is subjected to vacuum degassing by the D-H or R-l-I process the carbon content is lowered to about 0.02-0.04 percent and the oxygen content to approximately 200 ppm. After adding the addition agent of the invention, the carbon content may be raised to its initial value of about 0.06-0.08 percent, and the oxygen content is lowered to below 100 ppm. Thus in one preferred variant, the addition agent is added in an amount to recarburize low carbon vacuum degassed steel produced bya basic oxygen process to provide a final carbon content which is approximately the same as that which existed prior to degassing. The oxygen content of the degassed and recarburized steel thus produced is less than 100 ppm.

The temperature of the recarburized killed steel is not reduced markedly and it may be continuously cast without difficulty in accordance with prior art practices 7 to produce semifinished steel shapes such as blooms,

slabs and billets. Thesemifinished shapes may be finished into final products in accordance with prior art practices. For instance, slabs may be rolled to produce blackplate sheet or strips for container stock as the carbon content in the recarburized steel is sufficiently high for this purpose. The steel produced by the continuous casting process has the general properties of rimmed or capped steel and the aluminum and/or silicon contents are sufficiently low so that the rigid container stock specifications may be met with respect to these substances.

Basic oxygen steelmaking processes and apparatus, vacuum degassing processes and apparatus, and continuous casting processes and apparatus for use in preparing melts to be vacuum degassed and continuously cast in accordance with the invention are disclosed in numerous patents and literature references, and in the text The Making, Shaping and Treating ofSreel, 8th Edition, edited by Harold E. McGannon, (1964), the disclosures of which are incorporated herein by reference. Pages 453-456, 552-556, and 664-666 of The Making, Shaping and Treating of Steel are especially pertinent.

The invention is further illustrated by the following specific examples.

EXAMPLE I A melt of steel is prepared by a basic oxygen process following prior art steelmaking practices, and is transferred from the converter to a ladle for degassing. The ladle contains 300 tons of the molten steel. Prior to degassing, the steel has a temperature of 2,950F. and contains 0.06 percent carbon, 0.35 percent manganese, less than 0.01 percent silicon, less than 0.01 percent phosphorus, less than 0.025 percent sulfur, 600-700 parts per million of oxygen, and the remainder iron and trace amounts of incidental impurities.

The steel is degassed employing conventional R-l-l degassing apparatus and techniques until the oxygen content is reduced to 200 parts per million. At this time, the steel contains only 0.02 percent carbon.

One-inch briquettes prepared from a particulate mixture containing 30 parts by weight of graphite, 30 parts by weight of aluminum, 35 parts by weight of ferromanganese, and 5 parts by weight of molasses as a binder are added in an amount of 1,300 pounds. The degassing is allowed to proceed after the addition until a constant vacuum is reached thereby indicating that the steel is degassed.

After degassing, deoxidizing and recarburizing the melt by the above procedure, the carbon content is 0.06 percent and the oxygen content is less then parts per million. The temperature of the melt is 2,910F. and the molten steel is continuously cast following prior art practices to produce slabs. The slabs are then hot and cold rolled to produce blackplate which meets all specifications for container stock, including tinplate specifications, as the silicon content is less than 0.02 percent.

EXAMPLE II The general procedure of Example I is repeated except as noted below.

The additive is in the form of 2-inch spheres or balls containing 25 parts by weight of carbon, 25 parts by weight of silicon (as ferrosilicon), 45 parts by weight of manganese and iron (as ferromanganese and ferrosilicon), and parts by weight of molasses as a binder. The additive is added in an amount of 1,600 pounds, rather than 1,300 pounds as in Example l,.but otherwise the degassing, deoxidizing and recarburizing procedure is the same.

The blackplate product meets all specifications for galvanized sheet stock and the results in general are substantially the same as in Example 1, except for a slightly higher silicon content. The steel could also be hot rolled and/or cold rolled to produce other products in sheet or strip form, or structural shapes, plate, etc.

EXAMPLE III A melt of steel is prepared and transferred to a ladle following the general procedure of Example I. This specific melt contains 0.06% carbon and 400-500 parts per million of oxygen, but otherwise the composition is the same as in Example I. The melt is degassed using the same R-H apparatus that was used in Example I, but the procedure is changed as noted below. The steel is degassed for minutes, during which time the vacuum stabilizes, and then 1,200 pounds of the briquettes of Example I are added at the rate of 200 pounds per minute to the 300 tons of steel in the ladle. The vacuum cycle is continued during the addition and for approximately 5 minutes after the addition is completed.

The degassed, 'deoxidized and recarburized molten steel contains approximately 0.06 percent carbon, and substantially less than 100 parts per million of oxygen. The molten steel may be continuously cast to produce slabs and the slabs rolled to produce excellent blackplate for container stock as in Example 1.

I claim:

1. A method of continuously casting steel comprising the steps of preparing a melt of steel by a basic oxygen process, subjecting the melt of steel to a reduced pressure to produce molten partially deoxidized degassed steel having carbon and oxygen contents which are substantially lower than were present in the melt initially, and further deoxidizing and recarburizing the melt of steel by adding thereto an addition agent consisting essentially of a plurality of briquettes, each of the said plurality of briquettes consisting essentially of 1) carbon, (2) at least one substance which reacts exothermically with oxygen contained in the molten steel selected from the group consisting of aluminum and silicon, (3) manganese and (4) iron, the said plurality of briquettes having a size of about 0.25-3 inches and having a ratio by weight of carbon to the said exothermic substance between about 1:4 and 32, the manganese and iron being present in the said plurality of briquettes in a combined amount of at least 25 percent of the'total weight of carbon and the said exothermic substance and in an amount to increase the specific gravity suffrciently whereby the briquettes sink into the said melt of steel, the melt of deoxidized and recarburized degassed steel having a carbon content substantially higher than would be present in the absence of the addition agent and the final oxygen content being suffrciently low whereby it may be continuously cast, and thereafter continuously casting the melt of steel.

2. The method of' claim 1 wherein the steel as produced by the basic oxygen process contains not more than 0.15 percent'carbon, less than 1.0 percent manganese, less than 0.1 percent silicon, less than 0.05 percent phosphorus, less than 0.05 percent sulfur, less than 1.000 parts per million of oxygen and the remainder iron and incidental impurities, the addition agent is added in an amount to recarburize the steel to approximately the carbon content that existed prior to degassing, and the oxygen content of the deoxidized and recarburized degassed steel is less than parts per million.

3. The method of claim 2 wherein the addition agent is added in an amount to provide the said carbon and exothermic substance in a combined amount of about 0.5-4 pounds per ton of steel. 4. The method of claim 2 wherein the initial carbon content of the steel is about 0.06-0.08 percent and the addition agent is added in an amount to provide the said carbon and exothermic substance in a combined amount of about 2.0-2.5 pounds per ton of steel.

5. The method of claim 3 wherein the said addition agent contains carbon in an amount of about 30-40 parts by weight, the exothermic substance is aluminum and the aluminum is present in an amount of about 30-40 parts by weight, and the manganese and iron are present in a combined amount of about 20-40 parts by weight.

6. The method of claim 5 wherein the said carbon, aluminum, manganese and iron in the addition agent are in particulate form initially, a binder therefor is also present in an amount to bind the particles together in the said briquettes, the binder being present in an amount of about 1-10 parts by weight for each 100 parts by weight of the remaining ingredients of the briquettes.

7..The method of claim 6 wherein the briquettes are in the form of spheres having a size of about 1-3 inches, the addition agent is added in an amount to recarburize the steelto approximately the carbon content that existed prior to degassing, and the degassing of the melt of steel is continued after at least a portion of the addition agent is added, the oxygen content of the deoxidizedand recarburized degassed steel being less than 100 parts per million.

8. The method of claim 3 wherein the said addition agent contains carbon in an amount of about 30-40 parts by weight, the exothermic substance is silicon and the silicon is present in an amount of about 30-40 parts by weight, and the manganese and iron are present in a combined amount of about 20-40 parts by weight.

9. The method of claim 8 wherein the said carbon, silicon, manganese and iron are in particulate form initially, a binder therefore is also present in an amount to bind the particles together in the said briquettes, the binder being present in an amount of about 1-10 parts by weight for each I00 parts by weight of the remaining ingredients of the briquettes.

10. The method of claim 9 wherein the briquettes are in the form of spheres having a diameter of about l-3 inches, the addition agent is added in an amount to recarburize the steel to approximately the carbon content that existed prior to degassing, and the degassing of the melt of steel is continued after at least a portion of the addition agent is added, the oxygen content of the deoxidized and recarburized degassed steel being less than 100 parts per million.

l 1. The method of claim 2 wherein the initial carbon content of the steel is about 0.060.08 percent and the oxygen content is about 500-700 parts per million, the steel is subjected to vacuum degassing to provide an oxprovide the said carbon and exothermic substance in a combined amount of about 0.5-4 pounds per ton of steel, the residual exothermic substance content of the deoxidized and recarburized degassed steel being less ygen content not greater than about 200 parts per mil- 5 than 0.05 percent.

lion, and the addition agent is added in an amount to

Claims

1. A METHOD OF CONTINOUSLY CASTING STEEL COMPRISING THE STEPS OF PREPARING A METAL OF STEEL BY A BASIC OXYGEN PROCESS, SUBJECTING THE METAL OF STEEL TO A REDUCED PRESSURE TO PRODUCE MOLTEN PARTIALLY DEOXIDIZED DEGASED STEEL HAVING CARBON AND OXYGEN CONTENTS WHICH ARE SUGSTANTIALLY LOWER THAN WERE PRESENT IN THE MELT INITIALLY, AND FURTHER DEOXIDIZING AND RECARBURIZING THE MELT OF STEEL BY ADDING THERETO AN ADDITION AGENT CONSISTING ESSENTIALLY OF A PLURALITY OF BRIQUETTES, EACH OF THE SAID PLURALITY OF BRIQUETTES CONSISTING ESSENTIALLY (1) CARBON, (2) AT LEAST ONE SUBSTANCE WHICH REACTS EXOTHERMICALLY WITH CONSISTING OF ALUMINUM AND SILICON, (3) MANGANESE AND (4) IRON, THE SAID PLURALITY OF BRIQUETTES HAVING A SIZE OF ABOUT 0.25-3 INCHES AND HAVING A RATIO BY WEIGHT OF CARBON TO THE IRON, THE SAID PLURALITY OF BRIQUETTES HAVING A SIZE OF ABOUT SAID EXOTHERMIC SUBSTANCE BETWEEN ABOUT 1:4 AND 3:2, THE MANGANESE AND IRON BEING PRESENT IN THE SAID PLURALITY OF BRIQUETTES IN A COMBINED AMOUNT OF AT LEAST 25 PERCENT OF THE TOTAL WEIGHT OF CARBON AND THE SAID EXOTHERMIC SUBSTANCE AND IN AN AMOUNT OT INCREASE THE SPECIFIC GRAVITY SUFFICIENTLY WHEREBY THE BRIQUETTES SINK INTO THE SAID MELT OF STEEL, THE MELT OF DEOXIDIZED AND RECARBURIZED DEGASSED STEEL HAVING A CARBON CONTENT SUBSTANTIALLY HIGHER THAN WOULD BE PRESENT IN THE ABSENCE OF THE ADDITION AGENT AND THE FINAL OXYGEN CONTENT BEING SUFFICIENTLY LOW WHEREBY IT MAY BE CONTINOUSLY CAST, AND THEREAFTER CONTINOUSLY CASTING THE MELT OF STEEL.

2. The method of claim 1 wherein the steel as produced by the basic oxygen process contains not more than 0.15 percent carbon, less than 1.0 percent manganese, less than 0.1 percent silicon, less than 0.05 percent phosphorus, less than 0.05 percent sulfur, less than 1.000 parts per million of oxygen and the remainder iron and incidental impurities, the addition agent is added in an amount to recarburize the steel to approximately the carbon content that existed prior to degassing, and the oxygen content of the deoxidized and recarburized degassed steel is less than 100 parts per million.

3. The method of claim 2 wherein the addition agent is added in an amount to provide the said carbon and exothermic substance in a combined amount of about 0.5-4 pounds per ton of steel.

4. The method of claim 2 wherein the initial carbon content of the steel is about 0.06-0.08 percent and the addition agent is added in an amount to provide the said carbon and exothermic substance in a combined amount of about 2.0-2.5 pounds per ton of steel.

7. The method of claim 6 wherein the briquettes are in the form of spheres having a size of about 1-3 inches, the addition agent is added in an amount to recarburize the steel to approximately the carbon content that existed prior to degassing, and the degassing of the melt of steel is continued after at least a portion of the addition agent is added, the oxygen content of the deoxidized and recarburized degasseD steel being less than 100 parts per million.

9. The method of claim 8 wherein the said carbon, silicon, manganese and iron are in particulate form initially, a binder therefore is also present in an amount to bind the particles together in the said briquettes, the binder being present in an amount of about 1-10 parts by weight for each 100 parts by weight of the remaining ingredients of the briquettes.

10. The method of claim 9 wherein the briquettes are in the form of spheres having a diameter of about 1-3 inches, the addition agent is added in an amount to recarburize the steel to approximately the carbon content that existed prior to degassing, and the degassing of the melt of steel is continued after at least a portion of the addition agent is added, the oxygen content of the deoxidized and recarburized degassed steel being less than 100 parts per million.

11. The method of claim 2 wherein the initial carbon content of the steel is about 0.06-0.08 percent and the oxygen content is about 500-700 parts per million, the steel is subjected to vacuum degassing to provide an oxygen content not greater than about 200 parts per million, and the addition agent is added in an amount to provide the said carbon and exothermic substance in a combined amount of about 0.5-4 pounds per ton of steel, the residual exothermic substance content of the deoxidized and recarburized degassed steel being less than 0.05 percent.