US2805933A - Process for the preparation of ferroalloys - Google Patents

Process for the preparation of ferroalloys Download PDF

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US2805933A
US2805933A US475577A US47557754A US2805933A US 2805933 A US2805933 A US 2805933A US 475577 A US475577 A US 475577A US 47557754 A US47557754 A US 47557754A US 2805933 A US2805933 A US 2805933A
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silicon
content
alloy
oxygen
carbon content
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US475577A
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Mcyer Oskar
Ebert Hans
Frank Klaus
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Knapsack AG
Knapsack Griesheim AG
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Knapsack AG
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C35/00Master alloys for iron or steel
    • C22C35/005Master alloys for iron or steel based on iron, e.g. ferro-alloys

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  • Patent PRQtZESS FOR THE PREEARATION F FERRGALLOY Oskar Meyer, Aachen, and Hans Ebert and Hans Frank,
  • the present invention relates to a process for the preparation of low-carbon ferroalloys, especially of ferrochromium with a carbon content not exceeding 0.08%, preferably ranging between 0.02% and 0.04%, and of terromanganese with a carbon content of about 0.2%.
  • ferrochromium and iron-silico-alloy with a medium silicon content and a carbon content of about 0.1% In the preparation of ferrochromium and iron-silico-alloy with a medium silicon content and a carbon content of about 0.1% andin the preparation of ferromanganese an iron-silico-alloy with more than 0.1% of carbon are treated with oxygen or oxygen-containing gases and are refined by means of a mixture consisting of chromium ore and lime or of manganese ore and lime. The slag is then separated and the ferroalloy is further treated with oxy gen or oxygen-containing gases.
  • the major part of the silicon is slagged 0E from low-carbon silicon alloys by means of lime and ores or metal oxides.
  • the further elimination of silicon is then effected by oxidation with gaseous oxygen.
  • the aluminum content of the silicoalloy can be increased to at least 1% by addition of alumina-containing materials.
  • Alurnina-containing quartzite is particularly suitable for this purpose.
  • titanium or zirconium in the form of titaniumor .zirconium-containing additions and thus to raise the content of titanium or zirconium in the silicoalloy to at least 1%.
  • This alloy containing 35-45% of silicon is treated, in a vessel with an acid lining, for instance a converter, an electroconverter or in a similar device, with oxygen or oxygen-containing gases, whereby the original carbon content of about 0.05O.l% is reduced to 0.008% at least, however, to 0.04%. At the same time 12% of the silicon content are burnt and form a silicon slag.
  • the silicochromium so treated is desiliconized in known manner in the same vessel or after transferring it into another vessel with a mixture consisting of chromium ore and lime.
  • the desiliconization process is retarded in accordance with the falling silicon content. For this reason, the refining process is broken oif when a residual content of about 5-10% of silicon is left.
  • the slag obtained which contains about 5% of chromium oxide is drawn off or poured out. .It is discarded since it containsonly little chromium oxide.
  • the ferrochromium which still contains 35% of silicon is treated with gaseous oxygen while adding such a quantity of lime that a lime silica slag formshaving a basicity of at least 1.2- 2.0.
  • the content of chromium oxide of this slag is very low.
  • the slag can likewise be discarded.
  • the advantage of the new method of working resides in the fact that by the treatment with gaseous oxygen the speed of oxidation of the silicon is considerably increased.
  • a further advantage resides in the fact that the nitrogen content of the ferrochromium alloy is reduced at the same time.
  • the aluminum content of the alloy can be raised to l2% or more.
  • the decarbonization to the desired lowest content is accelerated by the initial content of aluminum, since the oxidation of aluminum produces a desired increase in the temperature.
  • a silicoalloy with 22% of silicon and a ratio of manganese to iron of about 2.2:1 is prepared in known manner. The. same operations are carried out as described in Example 1.
  • the oxidizing refining process of the silicoalloy leads to a reduction of the carbon content from about 1% to 0.5% max.
  • the silicon content has been reduced to about 3-5%, the refining process is broken off and the residual silicon is eliminated by means of oxygen.
  • the silicon content of the initial alloy that is to sayof the silicoalloy,must be raised to 30% if the same ratio of manganese to iron applies.
  • the process of preparing a ferrochromium alloy containing a maximum carbon content of 0.08% comprising the steps of treating, at a temperature above 1600 C., a member of a group consisting-of an ironsilico-alloy of medium silicon content containing at least 1% by weight of a reducing metal, anda mixture of an iron-silico-alloy and at least 1% by weight of a reducing metal, said reducing metal being selected from the group consisting of aluminum, titanium and zirconium, said member having a carbon content of less than 0.1% with oxygen to obtain the desired carbon content, refining the 4 resulting alloy with a mixture consisting of lime and chromium ore, separating resulting slag and treating resulting ferroalloy with oxygen to lower the silicon, nitrogen and other impurity content.
  • the process of preparing a ferromanganese alloy containing a maximum carbon content of 0.2% comprising the steps of treating, at a temperature above 1600 C., a member of a group consisting of an iron-silicoalloy of medium silicon content containing at least 1% by weight of a reducing metal, and a mixture of an ironsilico-alloy and at least 1% by weight of a reducing metal, said reducing metal being selected from the group consisting of aluminum, titanium and zirconium, said member having a carbon content of more than 0.1% with oxygen to obtain the desired carbon content, refining the resulting alloy with a mixture consisting of lime and manganese ore, separating resulting slag and treating resulting ferroalloy with oxygen to lower the silicon, nitrogen and other impurity content.
  • a maximumcarbon content of approximately 0.2% comprising the steps of treating, at a temperature above 1600 C., a member of the group consisting of an iron-manganese-silicon-alloy of a medium silicon content containing at least 1% by weight of a reducing metal,
  • a reducing metal being selected from the group consisting of aluminum, titanium and zirconium, having a carbon content of from 0.5% to 1.5% and a maximum ratio of manganese to iron of from 2.2 to l with oxygen to obtain the desired carbon content, refining the resulting alloy with a mixture consisting of lime and manganese ore, separating resulting slag and treating resulting ferroalloy with oxygen to lower the silicon, nitrogen and other purity content.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Description

United grates Patent PRQtZESS FOR THE PREEARATION F FERRGALLOY Oskar Meyer, Aachen, and Hans Ebert and Hans Frank,
Knapsack, near Koln, Germany, assignors to Knapsack- Griesheirn Aktiengeseiischaft, Knapsaek, near Kain, Germany, a corporation of Germany No Drawing. Application December 15, 1954,
Serial No. 475,577
' SCiaim s. ems-es The present invention relates to a process for the preparation of low-carbon ferroalloys, especially of ferrochromium with a carbon content not exceeding 0.08%, preferably ranging between 0.02% and 0.04%, and of terromanganese with a carbon content of about 0.2%. In the preparation of ferrochromium and iron-silico-alloy with a medium silicon content and a carbon content of about 0.1% andin the preparation of ferromanganese an iron-silico-alloy with more than 0.1% of carbon are treated with oxygen or oxygen-containing gases and are refined by means of a mixture consisting of chromium ore and lime or of manganese ore and lime. The slag is then separated and the ferroalloy is further treated with oxy gen or oxygen-containing gases.
The processes employed at present for the production of low-carbon ferroalloys, especially of ferrochromium and ferromanganese, are customarily carried out either in one step or in two steps and lead to a silicon-containing alloy of a varying silicon content ranging from 15 to 60% through a carbon-containing prealloy. The carbon content remaining in the alloy depends on the amount of the silicon content. This alloy known as silicoalloy is then reacted with mixtures consisting of chromium ore or manganese ore and slag formers to yield a ferroalloy. In this process the silicon is used for reduction of the heavy metal oxides. I 7
Other processes are carried out in asolid phase and the carbon is removed by oxidation under a very reduced pressure.
There are also known processes for the elimination of impurities from silicon alloys, wherein the proportions of aluminum, carbon, hydrogen, nitrogen, and phosphorus in the alloys are reduced by blowing oxygen or oxygencontaining gases on to the surface or" the melt or by passing or blowing them through the melt, without the silicon being essentially oxidized.
According to another process the major part of the silicon is slagged 0E from low-carbon silicon alloys by means of lime and ores or metal oxides. The further elimination of silicon is then effected by oxidation with gaseous oxygen.
Now we have found that a combination of the two lastnamed processes results in a considerable improvement of the hitherto used methods for the preparation of ferroalloys with a low carbon content.
Thus it is possible to prepare especially low-carbon ferroalloys, in particular ferrochromium with a carbon content not exceeding 0.08%, preferably between 0.02 and 0.04%, and ferromanganese with a carbon content of about 0.2% in the following way: An iron-sihco-alloy with a medium silicon content and a carbon content not exceeding 0.1% in the case of ferrochromium and with a carbon content of above 0.1% in the case of ferromanganese is treated with oxygen or oxygen-containing gases, is thus reduced to the desired low contents and refined by means of a mixture consisting of chromium ore and lime or manganese ore and lime. After the desiliconization is thus attained, the slag is separated and the ferro- 2 alloy is further treated with oxygen or oxygen-containing gases in order to obtain lower proportions of silicon, nitrogen, and other impurities. a
In an especially advantageous modification of the process for the preparation of ferromanganese, and ironmanganese-silicon-alloy with a medium silicon content of preferably 20-30% is used. The ratio of manganese to iron in this alloy is 2.2:1 and the carbon content ranges between 05-15% in correspondence with the silicon con tent.
' When using raw materials which are poor in aluminum, the aluminum content of the silicoalloy can be increased to at least 1% by addition of alumina-containing materials. Alurnina-containing quartzite is particularly suitable for this purpose.
Finally, it is also possible to use, instead of aluminum, titanium or zirconium in the form of titaniumor .zirconium-containing additions and thus to raise the content of titanium or zirconium in the silicoalloy to at least 1%.
The process of the present invention will be illustrated by means of the following examples:
1. Preparation of ferrochromium A silicochromium which contains between and of silicon is prepared .in the usual manner, whilst the processes hitherto known require 55% of silicon.
This alloy containing 35-45% of silicon is treated, in a vessel with an acid lining, for instance a converter, an electroconverter or in a similar device, with oxygen or oxygen-containing gases, whereby the original carbon content of about 0.05O.l% is reduced to 0.008% at least, however, to 0.04%. At the same time 12% of the silicon content are burnt and form a silicon slag.
This process is best carried out at temperatures above 1600 C. The silicochromium so treated is desiliconized in known manner in the same vessel or after transferring it into another vessel with a mixture consisting of chromium ore and lime. The desiliconization process is retarded in accordance with the falling silicon content. For this reason, the refining process is broken oif when a residual content of about 5-10% of silicon is left. The slag obtained which contains about 5% of chromium oxide is drawn off or poured out. .It is discarded since it containsonly little chromium oxide.
After having drawn off the slag, the ferrochromium which still contains 35% of silicon is treated with gaseous oxygen while adding such a quantity of lime that a lime silica slag formshaving a basicity of at least 1.2- 2.0. The content of chromium oxide of this slag is very low. Thus, the slag can likewise be discarded.
The advantage of the new method of working resides in the fact that by the treatment with gaseous oxygen the speed of oxidation of the silicon is considerably increased. A further advantage resides in the fact that the nitrogen content of the ferrochromium alloy is reduced at the same time.
If, in the preparation of the silicochromium, aluminacontaining quartzite is used, the aluminum content of the alloy can be raised to l2% or more. Thus, it is achieved that, instead of silicon, aluminum is oxidized in the first step of the treatment. In addition, the decarbonization to the desired lowest content is accelerated by the initial content of aluminum, since the oxidation of aluminum produces a desired increase in the temperature.
The same eiiect can be attained if titanium or zirconium are contained in the silicoalloy in similar quantities.
2. Preparation of ferromanganese The same conditions apply as in Example 1. However, the reduced carbon content in the finished alloy need only amount to 0.5% max. and, in exceptional cases, to 0.1%. Therefore, the initial contents of silicon in the silicoalloy PatentedSept. 10, 1957:
need not be so high since the carbon content in ferroalloys depends on the silicon content of the alloy.
A silicoalloy with 22% of silicon and a ratio of manganese to iron of about 2.2:1 is prepared in known manner. The. same operations are carried out as described in Example 1. The oxidizing refining process of the silicoalloy leads to a reduction of the carbon content from about 1% to 0.5% max. When the silicon content has been reduced to about 3-5%, the refining process is broken off and the residual silicon is eliminated by means of oxygen.
If the ferromanganese is to contain 0.1% of carbon, the silicon content of the initial alloy, that is to sayof the silicoalloy,,must be raised to 30% if the same ratio of manganese to iron applies.
In order to meet the present-day requirements it is obvious that the desiliconization ofthe silicomanganese must be carried out with a high-grade manganese ore. The residual silicon is removed by means of oxygen as described above. 1
The advantage of the process according to the present invention resides in the fact that the desired carbon mum carbon content of 0.08% and ferromanganese con-' taining a maximum carbon content of approximately 0.2% comprising the steps 'of treating, at a temperatureabove 1600 C., a member of the group consisting of an iron-silico-alloy of medium silicon content containing at least 1% by weight of a reducing metal, and a mixture of an iron-silico-alloy of medium silicon content and at least 1% by weight of a reducing metal, said reducing metal being selected from the group consisting of aluminum, titanium and zirconium, with oxygen to obtain the desired carbon content, refining the resulting alloy with a mixture consisting of lime and an ore of the selected alloying metal, separating resulting slag and treating resulting ferroalloy with oxygen to lower the silicon, nitrogen and other impurity content.
2. The process of preparing a ferrochromium alloy containing a maximum carbon content of 0.08% comprising the steps of treating, at a temperature above 1600 C., a member of a group consisting-of an ironsilico-alloy of medium silicon content containing at least 1% by weight of a reducing metal, anda mixture of an iron-silico-alloy and at least 1% by weight of a reducing metal, said reducing metal being selected from the group consisting of aluminum, titanium and zirconium, said member having a carbon content of less than 0.1% with oxygen to obtain the desired carbon content, refining the 4 resulting alloy with a mixture consisting of lime and chromium ore, separating resulting slag and treating resulting ferroalloy with oxygen to lower the silicon, nitrogen and other impurity content.
3. The process of preparing a ferromanganese alloy containing a maximum carbon content of 0.2% comprising the steps of treating, at a temperature above 1600 C., a member of a group consisting of an iron-silicoalloy of medium silicon content containing at least 1% by weight of a reducing metal, and a mixture of an ironsilico-alloy and at least 1% by weight of a reducing metal, said reducing metal being selected from the group consisting of aluminum, titanium and zirconium, said member having a carbon content of more than 0.1% with oxygen to obtain the desired carbon content, refining the resulting alloy with a mixture consisting of lime and manganese ore, separating resulting slag and treating resulting ferroalloy with oxygen to lower the silicon, nitrogen and other impurity content.)
4. The process of preparing a ferromanganese alloy.
containing a maximumcarbon content of approximately 0.2% comprising the steps of treating, at a temperature above 1600 C., a member of the group consisting of an iron-manganese-silicon-alloy of a medium silicon content containing at least 1% by weight of a reducing metal,
and a mixture of an iron-manganese-silicon-alloy of me.
dium' silicon content and at least 1% by weight of a reducing metal, said reducing metal being selected from the group consisting of aluminum, titanium and zirconium, having a carbon content of from 0.5% to 1.5% and a maximum ratio of manganese to iron of from 2.2 to l with oxygen to obtain the desired carbon content, refining the resulting alloy with a mixture consisting of lime and manganese ore, separating resulting slag and treating resulting ferroalloy with oxygen to lower the silicon, nitrogen and other purity content.
5. The process of claim 4 wherein the silicon content of the iron-manganese-silicon-alloy is from 20 to 30%.
References Cited in the file of this patent UNITED STATES PATENTS OTHER REFERENCES Camp and Francis, The Making, Shaping, and Treating of Steel, 6th Edition, pages 446-447.

Claims (1)

1. THE PROCESS OF PREPARING A FERROALLOY SELECTED FROM THE GROUP CONSISTING OF FERROCHROMIUM CONTAINING A MAXIMUM CARBON CONTENT OF 0.08% AND FERROMANGANESE CONTAINING A MAXIMUM CARBON CONTENT OF APPROXIMATELY 0.2% COMPRISING THE STEPS OF TREATING, AT A TEMPERATURE ABOVE 1600*C., A MEMBER OF THE GROUP CONSISTING AN IRON-SILICO-ALLOY OF MEDIUM SILICON CONTENT CONTAINING AT LEAST 1% BY WEIGHT OF A REDUCING METAL, AND A MIXTURE OF AN IRON-SILICO-ALLOY OF MEDIUM SILICON CONTENT AND AT LEAST 1% BY WEIGHT OF A REDUCING METAL, SAID REDUCING METAL BEING SELECTED FROM THE GROUP CONSISTING OF ALUMINUM, TITANIUM AND ZIRCONIUM, WITH OXYGEN TO OBTAIN THE DESIRE CARBON CONTENT, REFINING THE RESULTING ALLOY WITH A MIXTURE CONSISTING OF LIME AND AN ORE OF THE SELECTED ALLOYING METAL, SEPARATING RESULTING SLAG AND TREATING RESULTING FERROALLY WITH OXYGEN TO LOWER THE SILICON, NITROGEN AND OTHER IMPURITY CONTENT.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3305352A (en) * 1964-01-03 1967-02-21 Union Carbide Corp Process of producing alloys
US3369887A (en) * 1964-12-11 1968-02-20 Interlake Steel Corp Process for the production of manganese-silicon alloys
US3839018A (en) * 1968-06-03 1974-10-01 British Iron Steel Research Production of low carbon ferroalloys

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1508557A (en) * 1921-05-04 1924-09-16 Ferrolegeringar Ab Method for producing chromium or alloys of chromium
US1748750A (en) * 1927-02-25 1930-02-25 Electro Metallurg Co Process of making low-carbon ferro-alloys
US1793153A (en) * 1927-07-20 1931-02-17 Electro Metallurg Co Process of making rustless iron alloys
US2049081A (en) * 1922-02-23 1936-07-28 Robert Wickersham Stimson Alloys
US2227287A (en) * 1937-09-24 1940-12-31 Marvin J Udy Chromium metallurgy
GB533703A (en) * 1938-03-30 1941-02-19 Electro Chimie Metal Improvements in or relating to the manufacture of steel or alloy steels
US2557458A (en) * 1950-03-31 1951-06-19 United States Steel Corp Method of fusing alloy additions to a steel bath

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1508557A (en) * 1921-05-04 1924-09-16 Ferrolegeringar Ab Method for producing chromium or alloys of chromium
US2049081A (en) * 1922-02-23 1936-07-28 Robert Wickersham Stimson Alloys
US1748750A (en) * 1927-02-25 1930-02-25 Electro Metallurg Co Process of making low-carbon ferro-alloys
US1793153A (en) * 1927-07-20 1931-02-17 Electro Metallurg Co Process of making rustless iron alloys
US2227287A (en) * 1937-09-24 1940-12-31 Marvin J Udy Chromium metallurgy
GB533703A (en) * 1938-03-30 1941-02-19 Electro Chimie Metal Improvements in or relating to the manufacture of steel or alloy steels
US2557458A (en) * 1950-03-31 1951-06-19 United States Steel Corp Method of fusing alloy additions to a steel bath

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3305352A (en) * 1964-01-03 1967-02-21 Union Carbide Corp Process of producing alloys
US3369887A (en) * 1964-12-11 1968-02-20 Interlake Steel Corp Process for the production of manganese-silicon alloys
US3839018A (en) * 1968-06-03 1974-10-01 British Iron Steel Research Production of low carbon ferroalloys

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