US3885956A - Method and composition for the treatment of ferrous melts and process for making the treating composition - Google Patents
Method and composition for the treatment of ferrous melts and process for making the treating composition Download PDFInfo
- Publication number
- US3885956A US3885956A US471908A US47190874A US3885956A US 3885956 A US3885956 A US 3885956A US 471908 A US471908 A US 471908A US 47190874 A US47190874 A US 47190874A US 3885956 A US3885956 A US 3885956A
- Authority
- US
- United States
- Prior art keywords
- particles
- calcium carbide
- magnesium
- melt
- method defined
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- 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
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/02—Dephosphorising or desulfurising
-
- 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
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/02—Dephosphorising or desulfurising
- C21C1/025—Agents used for dephosphorising or desulfurising
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
- Y10T428/2991—Coated
Definitions
- ABSTRACT A composition for the desulfurization of a ferrous melt [211 App, 471908 comprises particles of calcium carbide coated with metallic magnesium to protect them against moisture- [52] U.S. Cl 75/53; 75/58; 117/100 B laden air. Th coated particles can be blown by a [51] Int. Cl.
- the present invention relates to a process for or method of desulfurizing a ferrous melt, to a composition for this purpose and to a method of making the composition. More particularly, the invention relates to desulfurization of a ferrous melt using a calciumcarbide based composition.
- Still another object of the invention is to provide a process for the treatment of ferrous melt whereby desulfurization can be carried out more economically and efficiently and without the danger incumbent upon earlier use of calcium carbide.
- Still another object of the invention is to provide a method of making the improved desulfurizing agent.
- the metal may be present in an amount up to about 50% by weight of the granulate which may consist of particles with a particle size of 0.3 to 5 mm.
- the granulate which may consist of particles with a particle size of 0.3 to 5 mm.
- the metal sheath For the desulfurization of pig iron, between 5 and 25 percent of the weight of each particle should be constituted by the metal sheath.
- the metal sheath forms a hermetic seal for the carbide-containing core, the storage, displacement, handling and use of the granulate is greatly simplified.
- the system is also safer, there is not danger of explosion or flashing and a spontaneous decomposition with all of the negative results thereofneed not be feared.
- the particles of the present invention are more effective in terms of the amount of carbide per unit weight of the melt treated than the uncoated carbide itself, in spite of the fact that one would ordinarily believe that the coating would reduce the activity of the carbide.
- the magnesium coating serves as a deoxidation medium for the melt, the oxygen potential or concentration is reduced and hence desulfurization effectiveness, which increases with decreasing oxygen potential, tends to rise.
- the deoxidation reaction is highly exothermic and a portion of the heat generated in the coating is available to melt or soften the calcium carbide far more rapidly than would be the case if the heat were merely picked up by contact with the melt, especially since the latter is generally at a lower temperature than the normal softening point of calcium carbide. Because of the accelerated melting or flowing of the calcium carbide core, there is greater contact between the calcium carbide and the iron melt and hence an increased efficiency,
- the coated desulfurizing agent according to the invention is fed to the melt in an amount of 0.05 to 0.5 percent by weight thereof, depending of course upon the ultimate sulfur content which is tolerable in the product.
- the particles may be injected by means of a lance deep into the bath so that a particularly intimate and long contact between the particles of the metal of the bath is ensured so that there is no noticeable magnesium loss through the surface of the bath.
- the gas for displacement of the particles can be nitrogen, argon or carbon dioxide and, of course, serves to mix the bath and further ensure the intimate contact mentioned above.
- the desulfur izing agent of the present invention is made by treating a mixture of calcium oxide and magnesium oxide in a carbide-producing electrothermal furnace of the closed type in the presence of carbon, the melt being granulated and treated with vapors of magnesium generated in the furnace.
- the coated calcium carbide can be drawn from the system in a steady state material flow balance, i.e. the
- the magnesium may be coated onto CaC granules otherwise produced.
- the calcium carbide particles, which are to be coated by magnesium, may contain other compounds which are soluble or chemically nonreactive with the carbide. These substances include lime, bauxite, feldspar and coke breeze.
- the cores to be coated may have a parti cle size of 0.2 to 5 mm.
- the raw materials for the electro-smelting furnace consist ofburned dolomite or mixtures of dolomite and magnesite in any desired proportion or as additives to burned lime.
- the magnesium vapor produced by the reaction system electrical furnace is condensed upon the calcium carbide products for a period sufficient to obtain the desired coating thickness.
- the carbide can be coated with metal vapors from other sources and we may generate magnesium vapors by other means for this purpose.
- Other coating metals can include barium and alumi num and their alloys.
- coating of the cores may be carried out using a melt of the metal. Because of the fact that mixtures of dolomite and magnesite may be used as raw materials the process has been found to be highly economical and we may operate with high concentrations of magnesium oxide because the reduction of the magnesium oxide is highly effective.
- FIG. 1 is a flow diagram of a system illustrating the invention.
- FIG. 2 is a section through a particle of the type used in the present process.
- SPECIFIC DESCRIPTION In the drawing, we show a system for the desulfuriz ing of a metal melt I in a ladle 11 consisting of a steel shell I2 lined at 13 with refractory material and in which a lance I4 is immersed.
- the lance 14 receives the desulfurizing particles or granules from a hopper I via a duct 16, the particles being entrained in an argon stream displaced to the lance as represented by the pump I7.
- the particles 18 within the hopper may consist of cores [9 of calcium carbide and sheaths 20 of magnesium.
- FIG. I also shows the production of the coated particlesv Carbon I (line 21), magnesium oxide (line 22), and calcium oxide (line 23), either individually or in the form of dolomite/magnesite mixture to which carbon has been added, are combined so that the mixture of the reactants is passed at 24 into a calcium carbide producing electro-smelting furnace 25 from which the calcium carbide is discharged at 26, is cooled at 27 and is granulated at 28 by conventional means. The granules are then placed upon a coating surface 29 of a vapordepositoon chamber 30 which may be evacuated at 3].
- Magnesium vapor conducted via line 32 from the electro-smelting furnace, is supplied to the vapor deposition chamber 30 and coats the cooled particles, carbon oxides being evacuated at III.
- the coated particles are led at 33 to the hopper I8.
- tons of a pig iron melt containing 0.5 percent sulfur is desulfurized using particles as shown in FIG. 2.
- the particles consist of cores of calcium carbide having a particle size of about 2 mm and carry a magnesium coating such that the magnesium content of each particle represents 10 percent by weight thereof.
- the product is supplied to the charge in the furnace be blowing with argon through a lance. 400 kg of the particles are added and the ultimate sulfur content is found to be less than 0.01 percent by weight.
- a method of desulfurizing a ferrous melt comprising the steps of introducing into said melt particles of a size between 0.3 and 5mm and having a core of calcium carbide coated with a metal sheath of magnesium constituting 5 to 25 percent by weight of the particles.
- a desulfurizing agent consisting of a mass of calcium carbide particles individually coated with a metal sheath of magnesium constituting 5 to 25 percent by weight of said particles, said particles having a particle size between 0.3 and 5 mm.
- a method of making a desulfurizing agent for a ferrous melt comprising the steps of smelting a calcium oxide/magnesium oxide mixture and carbon in an elec tro-smelting ealeiummarbide-producing furnace to form magnesium vapor and calcium carbide; granulating calcium carbide as produced in said furnace; and coating the granules of calcium carbide thus produced with magnesium condensed from said vapor.
- magnesium oxide is formed at least in part by burned dolomite.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
- Treatment Of Steel In Its Molten State (AREA)
Abstract
A composition for the desulfurization of a ferrous melt comprises particles of calcium carbide coated with metallic magnesium to protect them against moisture-laden air. The coated particles can be blown by a lance into the melt.
Description
United States Patent Obst et a1. May 27, 1975 1 METHOD AND COMPOSITION FOR THE [56] References Cited TREATMENT OF FERROUS MELTS AND IT STATES PATENTS PROCESS FOR MAKING THE TREATING 1.84 323 3 1932 Davies 1 75/53 COMPOSITION 2,692,196 10/1954 Hulme .1 75/58 v 2,863,755 12/1958 Kurzinski 75/58 [75] Inventors. Karl Heinz Obst, Jurgen 3,467,167 9/1969 Mahin H 75/58 Stradtmann, both of Wuelfrath, 3
,575,695 4/1971 Mlyashlta n 75/58 Germany; Paul Metz, Luxembourg; 3 622 302 H971 Ha yas 1 75/58 Francls W" Esch, Allemboth 3,656,989 4 1972 Layland 75/58 of Luxembourg 3,681,050 8/1972 Ueki 75 53 {73] Assignees: Rheinische Kalksteinwerke GmbH, I
w lf th G Acieries Primary Exammer-P. D. Rosenberg Reunies de Burbah Eih Dude|ange Attorney, Agent, or FirmKarl F. Ross; Herbert S.A., ARBED, Luxembourg, Dubno Luxembourg 221 Filed: May 21, 1974 [57] ABSTRACT A composition for the desulfurization of a ferrous melt [211 App, 471908 comprises particles of calcium carbide coated with metallic magnesium to protect them against moisture- [52] U.S. Cl 75/53; 75/58; 117/100 B laden air. Th coated particles can be blown by a [51] Int. Cl. C2lc 7/00 lanc n he m [58] Field of Search 75/53, 58; 117/100 B N, YAPOK 10 Claims, 2 Drawing Figures (PB/DE mom/ems 27 ELECTROFURNKE Ca C coouna mum/1.4110" Mirna 4' m4 TIIV6 CNTED HIT/(LES METHOD AND COMPOSITION FOR THE TREATMENT OF FERROUS MELTS AND PROCESS FOR MAKING THE TREATING COMPOSITION FIELD OF THE INVENTION The present invention relates to a process for or method of desulfurizing a ferrous melt, to a composition for this purpose and to a method of making the composition. More particularly, the invention relates to desulfurization of a ferrous melt using a calciumcarbide based composition.
BACKGROUND OF THE INVENTION It has been proposed heretofore to desulfurize ferrous-metal melts, such as baths of crude or pig iron, steel and ferroalloys by introducing calcium carbide into the bath and carrying out a solid-liquid interphasal reaction therein.
The desulfurizing property of calcium carbide with respect to sulfur-containing iron melts is well known. However, because the softening point of calcium carbide lies above l,800C and the treatment of the melt generally takes place at temperatures between 1,250C and 1,600C, the reaction is seldom quantitative and unsatisfactorily large proportions of the relatively expensive calcium carbide pass unused into the desulfurization slag.
It has been proposed heretofore to incorporate inorganic compounds such as lime or feldspar with the carbide to lower the softening or melting point thereof by a fluxing-type action. It is also known to process a mixture of magnesium particles or magnesium alloy particles and calcium carbide into bodies which are used for desulfurization.
However, all of the prior art systems for effecting desulfurization with calcium carbide have the common disadvantage that the calcium carbide must be protected against contact with moist atmospheric air since it is highly reactive therewith to form acetylene, Furthermore, not only is there a problem with the storage and handling of the calcium carbide because of safety, health and economic reasons, but the earlier systems have been found to be generally unsatisfactory for most desulfurization processes.
OBJECTS OF THE INVENTION It is the principal object of the present invention to provide a composition, substance or material for the desulfurization of a ferrous melt whereby the aforementioned disadvantages will be obviated and which can be readily handled and stored for long periods without appreciable danger, even in the presence of moist atmospheric air.
Still another object of the invention is to provide a process for the treatment of ferrous melt whereby desulfurization can be carried out more economically and efficiently and without the danger incumbent upon earlier use of calcium carbide.
Still another object of the invention, is to provide a method of making the improved desulfurizing agent.
It is, further, an object of the invention, to provide an improved method of treating a steel melt and an improved treatment system which is more effective and efficient for desulfurization than calcium carbide alone or earlier materials based thereon.
It is also an object of the invention to provide a simple and economical method of making such a desulfurization substance.
SUMMARY OF THE INVENTION These objects and others which will become apparent hereinafter are attained, in accordance with the present invention, by encasing a granulate of calcium carbide in a sheath or coating of a metal resistant to atmospheric deteroriation and present in an amount of at least 2% by weight of the particles, the metal preferable being magnesium.
The metal may be present in an amount up to about 50% by weight of the granulate which may consist of particles with a particle size of 0.3 to 5 mm. For the desulfurization of pig iron, between 5 and 25 percent of the weight of each particle should be constituted by the metal sheath.
Since the metal sheath forms a hermetic seal for the carbide-containing core, the storage, displacement, handling and use of the granulate is greatly simplified. Of course, the system is also safer, there is not danger of explosion or flashing and a spontaneous decomposition with all of the negative results thereofneed not be feared.
Surprisingly, the particles of the present invention are more effective in terms of the amount of carbide per unit weight of the melt treated than the uncoated carbide itself, in spite of the fact that one would ordinarily believe that the coating would reduce the activity of the carbide. Firstly, because the magnesium coating serves as a deoxidation medium for the melt, the oxygen potential or concentration is reduced and hence desulfurization effectiveness, which increases with decreasing oxygen potential, tends to rise. Secondly, the deoxidation reaction is highly exothermic and a portion of the heat generated in the coating is available to melt or soften the calcium carbide far more rapidly than would be the case if the heat were merely picked up by contact with the melt, especially since the latter is generally at a lower temperature than the normal softening point of calcium carbide. Because of the accelerated melting or flowing of the calcium carbide core, there is greater contact between the calcium carbide and the iron melt and hence an increased efficiency,
The coated desulfurizing agent according to the invention is fed to the melt in an amount of 0.05 to 0.5 percent by weight thereof, depending of course upon the ultimate sulfur content which is tolerable in the product. The particles may be injected by means of a lance deep into the bath so that a particularly intimate and long contact between the particles of the metal of the bath is ensured so that there is no noticeable magnesium loss through the surface of the bath.
The gas for displacement of the particles can be nitrogen, argon or carbon dioxide and, of course, serves to mix the bath and further ensure the intimate contact mentioned above.
According to a feature of the invention, the desulfur izing agent of the present invention is made by treating a mixture of calcium oxide and magnesium oxide in a carbide-producing electrothermal furnace of the closed type in the presence of carbon, the melt being granulated and treated with vapors of magnesium generated in the furnace.
The coated calcium carbide can be drawn from the system in a steady state material flow balance, i.e. the
calcium carbide withdrawn together with the magnesium vapor and carbon oxides being precisely equal to the calcium oxide, magnesium oxide and carbon input. Of course, the calcium carbide can be partly or fully withdrawn from a conventional calcium carbide synthesis or a portion of the calcium carbide produced in accordance with the invention may be diverted to other markets for use of calcium carbide. The magnesium may be coated onto CaC granules otherwise produced. The calcium carbide particles, which are to be coated by magnesium, may contain other compounds which are soluble or chemically nonreactive with the carbide. These substances include lime, bauxite, feldspar and coke breeze. The cores to be coated may have a parti cle size of 0.2 to 5 mm.
Most advantageously. the raw materials for the electro-smelting furnace consist ofburned dolomite or mixtures of dolomite and magnesite in any desired proportion or as additives to burned lime. The magnesium vapor produced by the reaction system electrical furnace is condensed upon the calcium carbide products for a period sufficient to obtain the desired coating thickness. Of course, the carbide can be coated with metal vapors from other sources and we may generate magnesium vapors by other means for this purpose. Other coating metals can include barium and alumi num and their alloys. Of course, instead of vapor deposition, coating of the cores may be carried out using a melt of the metal. Because of the fact that mixtures of dolomite and magnesite may be used as raw materials the process has been found to be highly economical and we may operate with high concentrations of magnesium oxide because the reduction of the magnesium oxide is highly effective.
BRIEF DESCRIPTION OF THE DRAWING The above and other objects, features and advantages of the present invention will become more readily apparent from the following description in which:
FIG. 1 is a flow diagram of a system illustrating the invention; and
FIG. 2 is a section through a particle of the type used in the present process.
SPECIFIC DESCRIPTION In the drawing, we show a system for the desulfuriz ing of a metal melt I in a ladle 11 consisting of a steel shell I2 lined at 13 with refractory material and in which a lance I4 is immersed. The lance 14 receives the desulfurizing particles or granules from a hopper I via a duct 16, the particles being entrained in an argon stream displaced to the lance as represented by the pump I7.
As will be apparent from FIG. 2, the particles 18 within the hopper may consist of cores [9 of calcium carbide and sheaths 20 of magnesium.
FIG. I also shows the production of the coated particlesv Carbon I (line 21), magnesium oxide (line 22), and calcium oxide (line 23), either individually or in the form of dolomite/magnesite mixture to which carbon has been added, are combined so that the mixture of the reactants is passed at 24 into a calcium carbide producing electro-smelting furnace 25 from which the calcium carbide is discharged at 26, is cooled at 27 and is granulated at 28 by conventional means. The granules are then placed upon a coating surface 29 of a vapordepositoon chamber 30 which may be evacuated at 3]. Magnesium vapor, conducted via line 32 from the electro-smelting furnace, is supplied to the vapor deposition chamber 30 and coats the cooled particles, carbon oxides being evacuated at III. The coated particles are led at 33 to the hopper I8.
EXAMPLE In a ladle as illustrated in FIG. I, tons of a pig iron melt containing 0.5 percent sulfur is desulfurized using particles as shown in FIG. 2. The particles consist of cores of calcium carbide having a particle size of about 2 mm and carry a magnesium coating such that the magnesium content of each particle represents 10 percent by weight thereof. The product is supplied to the charge in the furnace be blowing with argon through a lance. 400 kg of the particles are added and the ultimate sulfur content is found to be less than 0.01 percent by weight.
We claim:
I. A method of desulfurizing a ferrous melt comprising the steps of introducing into said melt particles of a size between 0.3 and 5mm and having a core of calcium carbide coated with a metal sheath of magnesium constituting 5 to 25 percent by weight of the particles.
2. The method defined in claim I wherein said particles are charged into said melt in an amount ranging between 005 and 0.5 percent by weight thereof.
3. The method defined in claim 2 wherein said particles are entrained into said melt close to the bottom thereof in a gas stream.
4. A desulfurizing agent consisting of a mass of calcium carbide particles individually coated with a metal sheath of magnesium constituting 5 to 25 percent by weight of said particles, said particles having a particle size between 0.3 and 5 mm.
5. The desulfurizing agent defined in claim 4 wherein said calcium carbide contains a soluble or chemically nonreactive inorganic substance incorporated therewith in the cores of said particles.
6. A method of making a desulfurizing agent for a ferrous melt comprising the steps of smelting a calcium oxide/magnesium oxide mixture and carbon in an elec tro-smelting ealeiummarbide-producing furnace to form magnesium vapor and calcium carbide; granulating calcium carbide as produced in said furnace; and coating the granules of calcium carbide thus produced with magnesium condensed from said vapor.
7. The method defined in claim 6 wherein said magnesium oxide is formed at least in part by burned dolomite.
8. The method defined in claim 6 wherein said mix ture is in part by dolomiteor magnesite-enriehed burned lime.
9. The method defined in claim 6 wherein an excess of magnesium vapor is produced by said furnace beyond that which is required to coat granules of calcium carbide produced from said furnace, the excess magne sium vapor being used to coat calcium carbide granules derived from another source.
[0. The method defined in claim 6, further comprising the step of entraining the particles coated with magnesium into a ferrous melt by a gas stream through a lance reaching to the bottom of the melt.
Claims (10)
1. A METHOD OF DESULFURIZING A FERROUS MELT COMPRISING THE STEPS OF INTRODUCING INTO SAID MELT PARTICLES OF A SIZE BETWEEN 0.3 AND 5MM AND HAVING A CORE OF CALCIUM CARBIDE COATED WITH A METAL SHEATH OF MAGNESIUM CONSTITUTING 5 TO 25 PERCENT BY WEIGHT OF THE PARTICLES.
2. The method defined in claim 1 wherein said particles are charged into said melt in an amount ranging between 0.05 and 0.5 percent by weight thereof.
3. The method defined in claim 2 wherein said particles are entrained into said melt close to the bottom thereof in a gas stream.
4. A desulfurizing agent consisting of a mass of calcium carbide particles individually coated with a metal sheath of magnesium constituting 5 to 25 percent by weight of said particles, said particles having a particle size between 0.3 and 5 mm.
5. The desulfurizing agent defined in claim 4 wherein said calcium carbide contains a soluble or chemically nonreactive inorganic substance incorporated therewith in the cores of said particles.
6. A method of making a desulfurizing agent for a ferrous melt comprising the steps of smelting a calcium oxide/magnesium oxide mixture and carbon in an electro-smelting calcium-carbide-producing furnace to form magnesium vapor and calcium carbide; granulating calcium carbide as produced in said furnace; and coating the granules of calcium carbide thus produced with magnesium condensed from said vapor.
7. The method defined in claim 6 wherein said magnesium oxide is formed at least in part by burned dolomite.
8. The method defined in claim 6 wherein said mixture is in part by dolomite- or magnesite-enriched burned lime.
9. The method defined in claim 6 wherein an excess of magnesium vapor is produced by said furnace beyond that which is required to coat granules of calcium carbide produced from said furnace, the excess magnesium vapor being used to coat calcium carbide granules derived from another source.
10. The method defined in claim 6, further comprising the step of entraining the particles coated with magnesium into a ferrous melt by a gas stream through a lance reaching to the bottom of the melt.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US471908A US3885956A (en) | 1974-05-21 | 1974-05-21 | Method and composition for the treatment of ferrous melts and process for making the treating composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US471908A US3885956A (en) | 1974-05-21 | 1974-05-21 | Method and composition for the treatment of ferrous melts and process for making the treating composition |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3885956A true US3885956A (en) | 1975-05-27 |
Family
ID=23873457
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US471908A Expired - Lifetime US3885956A (en) | 1974-05-21 | 1974-05-21 | Method and composition for the treatment of ferrous melts and process for making the treating composition |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3885956A (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3998625A (en) * | 1975-11-12 | 1976-12-21 | Jones & Laughlin Steel Corporation | Desulfurization method |
| US4014686A (en) * | 1976-02-23 | 1977-03-29 | United States Steel Corporation | Deoxidation of open type steels for improved formability |
| US4033762A (en) * | 1976-06-03 | 1977-07-05 | Kozo Sato | Method for preventing oxidation of melted metal |
| US4076522A (en) * | 1975-11-14 | 1978-02-28 | Aikoh Co., Ltd. | Method for the desulfurization of molten iron |
| EP0170407A1 (en) * | 1984-06-27 | 1986-02-05 | The BOC Group, Inc. | Agents for the removal of impurities from a molten metal and a process for producing same |
| EP0257718A1 (en) * | 1986-08-25 | 1988-03-02 | The Dow Chemical Company | Injectable reagents for molten metals |
| US4765830A (en) * | 1986-08-25 | 1988-08-23 | The Dow Chemical Company | Injectable reagents for molten metals |
| US4786322A (en) * | 1986-01-27 | 1988-11-22 | The Dow Chemical Company | Magnesium and calcium composite |
| US4988387A (en) * | 1989-03-13 | 1991-01-29 | Hoechst Aktiengesellschaft | Agent and process for desulfurizing molten metals |
| US5480127A (en) * | 1994-02-11 | 1996-01-02 | Leybold Durferrit Gmbh | Apparatus for the melting and treatment of metal |
| US5720830A (en) * | 1992-11-19 | 1998-02-24 | Sheffield Forgemasters Limited | Engineering ferrous metals and method of making thereof |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1848323A (en) * | 1928-05-04 | 1932-03-08 | Davies Edith Vail | Composition of matter for use in metallurgical operations |
| US2692196A (en) * | 1951-12-07 | 1954-10-19 | Air Reduction | Method and apparatus for treating molten metal |
| US2863755A (en) * | 1957-04-22 | 1958-12-09 | Union Carbide Corp | Oil-treated calcium carbide for desulfurization of iron |
| US3467167A (en) * | 1966-09-19 | 1969-09-16 | Kaiser Ind Corp | Process for continuously casting oxidizable metals |
| US3575695A (en) * | 1967-10-18 | 1971-04-20 | Nippon Kokan Kk | Deoxidation method of molten steel |
| US3622302A (en) * | 1968-02-15 | 1971-11-23 | Kobe Steel Ltd | Method for removing arsenic from metals or alloys |
| US3656989A (en) * | 1969-03-19 | 1972-04-18 | Foseco Int | Production of metal-impregnated porous coke materials |
| US3681050A (en) * | 1970-03-27 | 1972-08-01 | Aikoh Co | Agent for desulfurizing molten pig iron |
-
1974
- 1974-05-21 US US471908A patent/US3885956A/en not_active Expired - Lifetime
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1848323A (en) * | 1928-05-04 | 1932-03-08 | Davies Edith Vail | Composition of matter for use in metallurgical operations |
| US2692196A (en) * | 1951-12-07 | 1954-10-19 | Air Reduction | Method and apparatus for treating molten metal |
| US2863755A (en) * | 1957-04-22 | 1958-12-09 | Union Carbide Corp | Oil-treated calcium carbide for desulfurization of iron |
| US3467167A (en) * | 1966-09-19 | 1969-09-16 | Kaiser Ind Corp | Process for continuously casting oxidizable metals |
| US3575695A (en) * | 1967-10-18 | 1971-04-20 | Nippon Kokan Kk | Deoxidation method of molten steel |
| US3622302A (en) * | 1968-02-15 | 1971-11-23 | Kobe Steel Ltd | Method for removing arsenic from metals or alloys |
| US3656989A (en) * | 1969-03-19 | 1972-04-18 | Foseco Int | Production of metal-impregnated porous coke materials |
| US3681050A (en) * | 1970-03-27 | 1972-08-01 | Aikoh Co | Agent for desulfurizing molten pig iron |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3998625A (en) * | 1975-11-12 | 1976-12-21 | Jones & Laughlin Steel Corporation | Desulfurization method |
| US4076522A (en) * | 1975-11-14 | 1978-02-28 | Aikoh Co., Ltd. | Method for the desulfurization of molten iron |
| US4014686A (en) * | 1976-02-23 | 1977-03-29 | United States Steel Corporation | Deoxidation of open type steels for improved formability |
| US4033762A (en) * | 1976-06-03 | 1977-07-05 | Kozo Sato | Method for preventing oxidation of melted metal |
| EP0170407A1 (en) * | 1984-06-27 | 1986-02-05 | The BOC Group, Inc. | Agents for the removal of impurities from a molten metal and a process for producing same |
| US4786322A (en) * | 1986-01-27 | 1988-11-22 | The Dow Chemical Company | Magnesium and calcium composite |
| EP0257718A1 (en) * | 1986-08-25 | 1988-03-02 | The Dow Chemical Company | Injectable reagents for molten metals |
| US4765830A (en) * | 1986-08-25 | 1988-08-23 | The Dow Chemical Company | Injectable reagents for molten metals |
| US4988387A (en) * | 1989-03-13 | 1991-01-29 | Hoechst Aktiengesellschaft | Agent and process for desulfurizing molten metals |
| US5720830A (en) * | 1992-11-19 | 1998-02-24 | Sheffield Forgemasters Limited | Engineering ferrous metals and method of making thereof |
| US5480127A (en) * | 1994-02-11 | 1996-01-02 | Leybold Durferrit Gmbh | Apparatus for the melting and treatment of metal |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3885956A (en) | Method and composition for the treatment of ferrous melts and process for making the treating composition | |
| AU579275B2 (en) | Magnesium calcium oxide composite | |
| US4139369A (en) | Desulphurization of an iron melt | |
| US4364771A (en) | Product for the desulphurization of cast irons and steels | |
| GB2160896A (en) | Agents for the removal of impurities from a molten metal and a process for producing same | |
| US2874038A (en) | Method of treating molten metals | |
| US4084960A (en) | Methods of desulphurizing iron and steel and gases, such as stack gases and the like | |
| US3058822A (en) | Method of making additions to molten metal | |
| CN113056566B (en) | Carburant and carburant method using same | |
| US3666445A (en) | Auxiliary composition for steel-making furnaces | |
| SU789619A1 (en) | Method of processing zinc-containing dust in blast furnace and steel smelting production | |
| US4099964A (en) | Recycling of iron values | |
| JP2007009240A (en) | Method for reusing converter dust | |
| RU2107738C1 (en) | Method of steel melting from metal scrap in electric-arc furnace | |
| US4131451A (en) | Method for removing zinc from zinc-containing slags | |
| US2793111A (en) | Method for the recovery of cobalt from impure cobalt oxide | |
| KR910010056B1 (en) | Making process for the pellet of cr ore | |
| CA1099523A (en) | Method for removing zinc from zinc-containing slags | |
| US3811870A (en) | Basic oxygen process using a sodium hydroxide reaction product flux | |
| RU2352645C1 (en) | Method of steel smelting in arc electric steel-making furnace | |
| GB2199025A (en) | Modifying metallurgical slag | |
| KR100325103B1 (en) | Desulfurizing agent made by waste sludge from continuous casting | |
| JPH1036148A (en) | Treatment of molten iron dephosphorized slag and slag | |
| CA1074533A (en) | Methods of desulphurizing iron and steel and gases, such as stack gases and the like | |
| CN112011721A (en) | Pig iron for directly producing low-silicon low-titanium low-trace-element nodular cast iron and preparation method thereof |