US1949529A - Refining of steel - Google Patents

Refining of steel Download PDF

Info

Publication number
US1949529A
US1949529A US447770A US44777030A US1949529A US 1949529 A US1949529 A US 1949529A US 447770 A US447770 A US 447770A US 44777030 A US44777030 A US 44777030A US 1949529 A US1949529 A US 1949529A
Authority
US
United States
Prior art keywords
slag
oxids
steel
dissolved
radical
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
Application number
US447770A
Inventor
Vere B Browne
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Allegheny Ludlum Corp
Original Assignee
Allegheny Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Allegheny Steel Corp filed Critical Allegheny Steel Corp
Priority to US447770A priority Critical patent/US1949529A/en
Application granted granted Critical
Publication of US1949529A publication Critical patent/US1949529A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/0087Treatment of slags covering the steel bath, e.g. for separating slag from the molten metal

Definitions

  • This invention relates to the refining of steel and especially to a new and'novel method of effecting such refining by invoking and utilizing the principles of physical chemistry.
  • Another object of my invention is to refine steel of any type having a supernatant slag by causing the oxids dissolved in the steel to migrate to the slag.
  • a further object of my invention is the conversion of oxids to silicates in the Slag by adding in effect the SiOz radical to the slag in excess.
  • oxids can be removed by changing the composition of the slag and so changing the solution pressures of the two'liquids, thus causing the oxids to migrate to the slag instead of remaining in the metal.
  • This phenomenon may be termed mass action equilibrium.
  • a slag consisting of CaO MnSiOa xFeO FeSiOa' will have a relation to the metal which will cause the FeO to migrate to the slag, where it chemically unites with the SiOz.
  • a process of removing dissolved basic oxids from low carbon steels containing the same and having a supernatant slag comprising adding sand to the slag at the end of the steel-making operations in an amount more than sufiicient to combine with said dissolved oxids.
  • a process of removing basic oxids entrapped in molten steel containing the same and having a supernatant slag comprising liberating said oxids from said steel and causing them to migrate to said slag where they are chemically combined by adding in efiect to said slag the SiOz radical in excess of the combining equivalent of said oxids.
  • a physico-chemical method of treating steel containing dissolved or entrapped oxids and having a supernatant slag involving causing said oxids to physically pass from said steel to said slag by an adjustment of solution pressures of steel and slag to bring about such transference by adding SiO2 in excess of the combining equivalents of the oxids and causing said so-transferred oxids to chemically unite with a portion of said slag specially added for such purposes.
  • a physico-chemical process of refining molten steel which has a supernatant molten slag thereon, both steel and slag containing dissolved and entrapped oxids, comprising adding available SiOz to the slag in an amount more than sufiicient to combine with all such oxids, thus converting oxids in the slag to corresponding silicates, setting up a physical migration of oxids from steel to slag, converting to corresponding silicates such migrated oxids, and preventing premature equilibrium or reversal of the aforesaid action.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Steel In Its Molten State (AREA)

Description

Patented Mar. 6, i934 1 I nsrmmc OF STEEL Vere B.- Browne, Brackenridge, Pa., assignor to Allegheny Steel Company, Brackenridge, Pa., a corporation of Pennsylvania No Drawing. Application April 26, 1930 Serial No. 447,770
' 9 Claims.
This invention relates to the refining of steel and especially to a new and'novel method of effecting such refining by invoking and utilizing the principles of physical chemistry.
It has been generally considered that the reactions taking place in a furnace are purely chemical and that in order to remove impurities from the steel it has been assumed that a chemical union must take place so that theimpurities are 10 either oxidized or reduced and thus put in a condition in which they can be isolated or collected and removed. 7 While this is true as far as it goes, I have discovered that certain impurities can be removed without depending solely on a chemicalunion, but rather by changing the solution pressures of the two liquids (steel and slag) so that the utilized tendency or effect is a physical rather than a chemical onel is the refining of steel by a change of solution pressure, thus utilizing the principles of physical chemistry.
Another object of my invention is to refine steel of any type having a supernatant slag by causing the oxids dissolved in the steel to migrate to the slag.
A further object of my invention is the conversion of oxids to silicates in the Slag by adding in effect the SiOz radical to the slag in excess.
Other and further objects will be understood by those skilled in this particular art.
I have discovered. that steel can be produced free from oxids, such as FeO and MnO and the like, even under a slag extremely high in oxids provided that the solution pressure can be changed so that the oxids migrate or tend to ,migrate from the-metal to the slag and provided that there is an acid radical present' to combine 40 with the oxids. This is, I believe, a logical explanation-ofthe difference between acid and basic steel; e
Forexample, in the making of silicon steel in an electric or open hearth furnace, it isdesired to have the carbon content as low as possible, but when the carbon content has been reduced to say about 102% the slag will contain, many times, as much as about 35% FeO and the metal fwill be practically saturated with oxids. When silicon is added to such steel the silicon reduces, the FeO and is itself oxidized to silica (SiOz) which 'is entrapped in the metal in the form of an emulsion. Even the removal of the slag does not help materially under such con- 5 ditions as the metal still contains dissolved oxids.
One of the objects of my invention, therefore,
I have discovered further that these oxids can be removed by changing the composition of the slag and so changing the solution pressures of the two'liquids, thus causing the oxids to migrate to the slag instead of remaining in the metal. This phenomenon may be termed mass action equilibrium. For example, a slag consisting of CaO MnSiOa xFeO FeSiOa' will have a relation to the metal which will cause the FeO to migrate to the slag, where it chemically unites with the SiOz.
I have discovered, therefore, that it is possible to remove oxids completely from low carbon steels such as are used, for example, in the manufacture of transformer sheets by adding sand to the slag at the end of the operation in an amount sufficient to more than combine with all the MnO and FeO present. This will effect a change in the solution pressure and the dissolved oxids will be liberated from the metal to combine with the excess silica. It is known that metallic silicates dissolve in each otherwhen melted and also that they dissolve oxids of metals, but they do not dissolve metals or reduced substances.
In case one prefers to remove the slag entirely the same result can be obtained by replacing the original slag with a slag composed of CaO and SiOz butwith a liberal excess of SiO2 over and above that amount calculated to combine with the amount of dissolved oxids estimated to be present.
Experimentation has proved not only the accuracy of the above considerations, but that valuable results are secured economically and eniciently.
In general, when acid .radical is present in suflicient quantities all the basic substances in the slag are satisfied and hence the slag has a further capacity for attracting to itself additional oxids, which are likewise satisfied, and the migration continues.- If the slag has an excess of cid radical it is understood that all the oxids wil be removed from the steel.
(vSiOz The process is applicable to any kind of steel and may be used, for example, in connection with silicon steel or chrome alloys, but it is not limited thereto.
What I claim as new and desire to secure by Letters Patent is:
1. In the process of refining steel containing dissolved basic oxids and having a surface slag thereon, adding in eiTect the SiOz radical in excess of that theoretically necessary to convert all said dissolved oxids into silicates, bringing about a change in the relative solution pressures of steel and slag so as to set up a migratory tendency of the dissolved oxids from the steel to the slag, said oxids being converted in said slag into corresponding silicates, said excess SiOz radical in said slag maintaining said slag free from uncombined oxids other than SiOz and hence preventing a premature equilibrium or a reversal of the migration. I
2. In the process of refining steel containing dissolved basic oxids and having a slag thereon, causing the dissolved oxids to migrate from said steel to said slag by adding in effect to said slag an amount of acid radical over and above the combining equivalent of the oxids, said oxids there combining with the chemical equivalent of acid radical and maintaining said slag free from uncombined oxids other than those of the acid radical itself.
3. In the process of refining steel containing dissolved basic oxids and having a slag thereon, causing all the dissolved oxids to migrate from said steel to said slag by adding to said slag in effect the S102 radical in excess of the combining equivalent of said oxids, said oxids there combining with an equivalent amount of said S102 radical.
4. In the process of refining steel containing dissolved basic oxids and having a slag thereon, causing all the dissolved oxids to migrate from said steel to said slag by adding to said slag in effect the SiOz radical in excess of the combining equivalent of said oxids, said oxids there combining with an equivalent amount of said Si02 radical producing corresponding silicates and maintaining said slag free from uncombined oxids other than those of the acid radical itself.
5. A process of removing dissolved basic oxids from low carbon steels containing the same and having a supernatant slag, comprising adding sand to the slag at the end of the steel-making operations in an amount more than sufiicient to combine with said dissolved oxids.
6. A process of removing basic oxids entrapped in molten steel containing the same and having a supernatant slag, comprising liberating said oxids from said steel and causing them to migrate to said slag where they are chemically combined by adding in efiect to said slag the SiOz radical in excess of the combining equivalent of said oxids.
7. In the manufacture of steel containing dissolved iron and manganese oxids and having a supernatant slag, the steps of adding acid radical S102 in effect in excess of the combining equivalent of said oxids to said slag, causing said iron and manganese oxids to migrate to said slag and to combine with a portion of said acid radical SiO2 to form iron and manganese silicates which remain in and become a part of said slag.
8. A physico-chemical method of treating steel containing dissolved or entrapped oxids and having a supernatant slag involving causing said oxids to physically pass from said steel to said slag by an adjustment of solution pressures of steel and slag to bring about such transference by adding SiO2 in excess of the combining equivalents of the oxids and causing said so-transferred oxids to chemically unite with a portion of said slag specially added for such purposes.
9. A physico-chemical process of refining molten steel which has a supernatant molten slag thereon, both steel and slag containing dissolved and entrapped oxids, comprising adding available SiOz to the slag in an amount more than sufiicient to combine with all such oxids, thus converting oxids in the slag to corresponding silicates, setting up a physical migration of oxids from steel to slag, converting to corresponding silicates such migrated oxids, and preventing premature equilibrium or reversal of the aforesaid action.
VERE B. BROWNE.
US447770A 1930-04-26 1930-04-26 Refining of steel Expired - Lifetime US1949529A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US447770A US1949529A (en) 1930-04-26 1930-04-26 Refining of steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US447770A US1949529A (en) 1930-04-26 1930-04-26 Refining of steel

Publications (1)

Publication Number Publication Date
US1949529A true US1949529A (en) 1934-03-06

Family

ID=23777675

Family Applications (1)

Application Number Title Priority Date Filing Date
US447770A Expired - Lifetime US1949529A (en) 1930-04-26 1930-04-26 Refining of steel

Country Status (1)

Country Link
US (1) US1949529A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2416179A (en) * 1944-12-16 1947-02-18 Reynolds Metals Co Method of fluidizing slag
US3151973A (en) * 1962-02-23 1964-10-06 Inland Steel Co Production of low sulfur iron
US3318691A (en) * 1965-07-06 1967-05-09 Jellinghaus Rudolf Process for producing castings from an iron alloy containing silicon
EP0284694A2 (en) * 1987-04-03 1988-10-05 Inland Steel Company Controlling dissolved oxygen content in molten steel

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2416179A (en) * 1944-12-16 1947-02-18 Reynolds Metals Co Method of fluidizing slag
US3151973A (en) * 1962-02-23 1964-10-06 Inland Steel Co Production of low sulfur iron
US3318691A (en) * 1965-07-06 1967-05-09 Jellinghaus Rudolf Process for producing castings from an iron alloy containing silicon
EP0284694A2 (en) * 1987-04-03 1988-10-05 Inland Steel Company Controlling dissolved oxygen content in molten steel
EP0284694A3 (en) * 1987-04-03 1990-01-31 Inland Steel Company Controlling dissolved oxygen content in molten steel

Similar Documents

Publication Publication Date Title
US1949529A (en) Refining of steel
US1890485A (en) Method of treating metal
US3099552A (en) Method of making low sulfur steel
US2448882A (en) Method for deironing chromium ore
US2301360A (en) Purification of high silicon iron alloys
US2049004A (en) Art of refining metals
US2054427A (en) Process for the reduction of silicates other than alkaline earth metal silicates and the production of alloys of aluminium
US1743885A (en) Extraction of iron and titanium compounds from titanium ores
US2512578A (en) Method of desulfurizing and decopperizing ferrous metal
US1582318A (en) Colored granulated slag and method of making same
US1825463A (en) Method of reclaiming stainless steel scrap
US2501832A (en) Bessemerizing of ferrous metal
US800130A (en) Process of separating nickel from mattes.
US1187623A (en) Making steel.
US2233726A (en) Method of treating low carbon open hearth steel
US2207282A (en) Method of treating alloys
US2345222A (en) Production of steel
ES8205871A1 (en) Copper refining and novel flux therefor
US2462871A (en) Treating agent
US1686277A (en) Metallic composition and process for making the same
US2092621A (en) Recovery of beryllium from siliceous ores
US943192A (en) Refining-steel.
US771645A (en) Method of decarburizing metals or alloys.
US1777081A (en) Manufacture of steel
US2111032A (en) Method of purifying fused metals