US1081532A - Purifying steel. - Google Patents

Purifying steel. Download PDF

Info

Publication number
US1081532A
US1081532A US73996313A US1913739963A US1081532A US 1081532 A US1081532 A US 1081532A US 73996313 A US73996313 A US 73996313A US 1913739963 A US1913739963 A US 1913739963A US 1081532 A US1081532 A US 1081532A
Authority
US
United States
Prior art keywords
steel
manganese
slag
silicate
lime
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
US73996313A
Inventor
Ernest Humbert
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to US73996313A priority Critical patent/US1081532A/en
Application granted granted Critical
Publication of US1081532A publication Critical patent/US1081532A/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
    • C21C7/0025Adding carbon material

Definitions

  • the principal processes of making steel are first, the converter, acid or basic, and second, the open-hearth process, acid or basic.
  • the acid converter process air is blown through a molten mass of pig iron so as to oxidize the silicon, carbon and manganese.
  • the basic converter process there is a similar oxidation of carbon, silicon, manganese and phosphorus.
  • the carbon is burned to carbon monoxid and carbon dioXid (CO and C0
  • the oXids of carbon escape as gases, but the silicon and manganese (and part of the iron) are oxidized and form the silicate or silicates of manganese and iron. A part of this silicate rises to the top of the vessel and forms the slag.
  • a certain amount of silicon and manganese are added in order to deoXidize the metal according to the following reactions:
  • rateiiteanee. is, rare.
  • silicate impurities In order to eliminate these impurities I use a special slag which I place in the finishing ladle and upon which I pour the steel from the converter or open-hearth or other vessel in which it has been formed. From this finishing ladle the metal thus purified is then poured into ingot molds or sand molds.
  • the slag is composed of from ten to thirty (10% to 30%) per cent. silica, five to fifty (5% to 50%) per cent. calcium carbid (CaC and the balance lime. This slag has several points of advantage.
  • the manganese and iron are incorporated in the metal.
  • the oXid of carbon escapes as a gas as fast as the metal comes into contact with the slag.
  • the reaction is instantaneous.
  • the slag which may be called a silico-calcium-carbid, is converted as the equation shows into the metals and the oXid of carbon and a silicate of lime.
  • the silicate of lime is very fusible and floats on the top of the ladle with the excess (which is necessarily provided) of the silico-calciunicarbid.
  • the maintenance of a high temperature and the liquidity of the slag is assisted by the strong chemical reaction and the evolution of heat produced by the breaking up of the calcium carbid (about 5700 calories per kilo of the carbid). This heat assists in keeping the silicate of lime very fluid and in keeping the entire mass very fluid until it is poured.
  • the slag should be put into the ladle in liquid form. It is made by melting a mixture of silica sand (10% to 30%) lime (70% to 90%) and adding carbon in the form of coke or anthracite or otherwise (10% to 30% of the total lime and silica). The quantity of carbon will vary according to the percentage of calcium carbid desired in the finished slag.
  • What I claim is- L The method of purifying steel which consists in pouring it into a finishing vessel containing a molten silico-calcium-carbid slag so as to convert the silicates of iron and manganese therein into a readily fusible silicate of lime.
  • the method of purifying steel which consists in melting a mixture of silica sand (10% to 30%) and lime (70% to 90%) adding carbon thereto (about 10% to 30% of the total lime and sand) and pouring the steel to be purified upon saidmelted mixture so as to convert the silicates of manganese and iron therein into a readily fusible silicate of lime.

Landscapes

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

Description

UNITED .PATEENT @IWIQE.
ERNEST HUMBEHI, OE SOUTH CHICAGO, ILLINOIS.
PURIFYING STEEL.
No Drawing.
To all whom it may concern Be it known that I, ERNEST I-IUMBERT, a citizen of France, residing at South Ohicago, Illinois, have invented certain new and useful Improvements in Purifying Steel, of which the following is a specification.
The principal processes of making steel are first, the converter, acid or basic, and second, the open-hearth process, acid or basic. In the acid converter process air is blown through a molten mass of pig iron so as to oxidize the silicon, carbon and manganese. In the basic converter process there is a similar oxidation of carbon, silicon, manganese and phosphorus. In both these cases the carbon is burned to carbon monoxid and carbon dioXid (CO and C0 The oXids of carbon escape as gases, but the silicon and manganese (and part of the iron) are oxidized and form the silicate or silicates of manganese and iron. A part of this silicate rises to the top of the vessel and forms the slag. When the carbon is reduced to the point desired a certain amount of silicon and manganese are added in order to deoXidize the metal according to the following reactions:
In the final combination there is always a certain amount of FeO present and the slag may be expressed by the formula In the acid open-hearth process the same reactions are used for deoXidizing the metal. In the basic open-hearth some manganese is generally added in the furnace to deoXidize the metal, part of which manganese forms MnO. Silicon is then added in the ladle to kill the metal and a silicate or silicates of iron and manganese are formed as in the converter process. This silicate or silicates constitute non-metallic impurities, and part of these are retained in suspension in the metal. Their association with the metal is a mechanical one like that of small pebbles in a mass of clay; as is shown by a microscope. These impurities do not alloy with the metal and their presence is the cause of many troubles heretofore found in finished steel, especially Bessemer rails. I propose to substantially eliminate these impurities from the steel after finishing it in the usual Specification of Letters Patent.
rateiiteanee. is, rare.
Application fi1ed. January 3, 1913. Serial No. 739,963.
way in the Bessemer or 0penhearth furnaces or indeed after finishing it in any way which results in the existence of these silicate impurities. In order to eliminate these impurities I use a special slag which I place in the finishing ladle and upon which I pour the steel from the converter or open-hearth or other vessel in which it has been formed. From this finishing ladle the metal thus purified is then poured into ingot molds or sand molds. The slag is composed of from ten to thirty (10% to 30%) per cent. silica, five to fifty (5% to 50%) per cent. calcium carbid (CaC and the balance lime. This slag has several points of advantage. It is easily fusible and remains liquid for a comparatively long time in the ladle so that it elfects a thorough purification. As'the metal is poured into the ladle the silicate of iron and manganese on coming into contact with the slag is reduced according to the following reaction:
The manganese and iron are incorporated in the metal. The oXid of carbon escapes as a gas as fast as the metal comes into contact with the slag. The reaction is instantaneous. The slag, which may be called a silico-calcium-carbid, is converted as the equation shows into the metals and the oXid of carbon and a silicate of lime. The silicate of lime is very fusible and floats on the top of the ladle with the excess (which is necessarily provided) of the silico-calciunicarbid. The maintenance of a high temperature and the liquidity of the slag is assisted by the strong chemical reaction and the evolution of heat produced by the breaking up of the calcium carbid (about 5700 calories per kilo of the carbid). This heat assists in keeping the silicate of lime very fluid and in keeping the entire mass very fluid until it is poured.
The slag should be put into the ladle in liquid form. It is made by melting a mixture of silica sand (10% to 30%) lime (70% to 90%) and adding carbon in the form of coke or anthracite or otherwise (10% to 30% of the total lime and silica). The quantity of carbon will vary according to the percentage of calcium carbid desired in the finished slag.
What I claim is- L The method of purifying steel which consists in pouring it into a finishing vessel containing a molten silico-calcium-carbid slag so as to convert the silicates of iron and manganese therein into a readily fusible silicate of lime.
2. The method of purifying steel Which consists in melting a mixture of silica and lime, adding carbon thereto pouring the steel upon the same and thereby converting the silicates of manganese and iron in the steel into a readily fusible silicate of lime.
8. The method of purifying steel which consists in melting a mixture of silica sand (10% to 30%) and lime (70% to 90%) adding carbon thereto (about 10% to 30% of the total lime and sand) and pouring the steel to be purified upon saidmelted mixture so as to convert the silicates of manganese and iron therein into a readily fusible silicate of lime.
In Witness whereof, I have hereunto signed my name in the presence of two subscribing Witnesses.
ERNEST HUMBERT.
Witnesses:
JULIUs ISRAEL, FREDERICK P. LILLEY.
Copies of this patent may be obtained for five cents each, by addressing the Commissioner of Patents, Washington, I). G.
US73996313A 1913-01-03 1913-01-03 Purifying steel. Expired - Lifetime US1081532A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US73996313A US1081532A (en) 1913-01-03 1913-01-03 Purifying steel.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US73996313A US1081532A (en) 1913-01-03 1913-01-03 Purifying steel.

Publications (1)

Publication Number Publication Date
US1081532A true US1081532A (en) 1913-12-16

Family

ID=3149765

Family Applications (1)

Application Number Title Priority Date Filing Date
US73996313A Expired - Lifetime US1081532A (en) 1913-01-03 1913-01-03 Purifying steel.

Country Status (1)

Country Link
US (1) US1081532A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2865735A (en) * 1956-08-24 1958-12-23 Knorr Bremse Gmbh Processes for reducing the sulphur content in iron and for economizing in coke in cupola furnaces

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2865735A (en) * 1956-08-24 1958-12-23 Knorr Bremse Gmbh Processes for reducing the sulphur content in iron and for economizing in coke in cupola furnaces

Similar Documents

Publication Publication Date Title
US4695318A (en) Method of making steel
JPH07504230A (en) Method for desulfurizing molten iron with minimal slag formation and equipment for carrying out the process
US3791819A (en) Production of stainless steels
RU2059731C1 (en) Steel continuous melting method
US3615348A (en) Stainless steel melting practice
US2906616A (en) Method for desulfurizing molten metal and in particular liquid pig iron
US1081532A (en) Purifying steel.
US2800631A (en) Method of carrying out melting processes
CA1321075C (en) Additive for promoting slag formation in steel refining ladle
JPS587691B2 (en) Steel manufacturing method
Steenkamp et al. Introduction to the production of clean steel
US2811436A (en) Process of producing steel
US2079848A (en) Making steel
US724770A (en) Art of making steel.
RU2786789C1 (en) Active deoxidizer of liquid and refractory hot and cold slags
US1532052A (en) Treatment of iron or steel in electric furnaces
JPS6123243B2 (en)
US318067A (en) Assig-nob to pittsbtjeg
US1365091A (en) Allot
US128088A (en) Improvement in processes of purifying iron and copper
GB460138A (en) Improvements in and relating to the manufacture of iron
Sims et al. Experimental operation of a basic-lined surface-blown hearth for steel production
WO2022054553A1 (en) Method for producing chromium-containing molten iron
SU779407A1 (en) Powdered mixture for liquid steel straining
US801656A (en) Process for the deoxidation of ingot-iron, ingot-steel, &c.