US3325278A - Alloy purification process - Google Patents

Alloy purification process Download PDF

Info

Publication number
US3325278A
US3325278A US365778A US36577864A US3325278A US 3325278 A US3325278 A US 3325278A US 365778 A US365778 A US 365778A US 36577864 A US36577864 A US 36577864A US 3325278 A US3325278 A US 3325278A
Authority
US
United States
Prior art keywords
molten
ferrosilicon
calcium
impurities
aluminum
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
US365778A
Inventor
Melvin L Mcclellan
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.)
Elkem Metals Co LP
Original Assignee
Union Carbide 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 Union Carbide Corp filed Critical Union Carbide Corp
Priority to US365778A priority Critical patent/US3325278A/en
Application granted granted Critical
Publication of US3325278A publication Critical patent/US3325278A/en
Assigned to ELKEM METALS COMPANY, A NEW YORK GENERAL PARTNERSHIP reassignment ELKEM METALS COMPANY, A NEW YORK GENERAL PARTNERSHIP ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: UNION CARBIDE CORPORATION, A NY CORP.
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
    • C21C7/04Removing impurities by adding a treating agent

Definitions

  • the present invention relates to the purification of alloys. More particularly, the present invention relates to a process for the removal of impurities from molten metals by the oxidation of the impurities.
  • ferrosilicon which is used in the treatment of steel often contains small percentages, e.g. up to 2 percent each of aluminum and calcium.
  • the silicon As the silicon is oxidized, it forms a fluid slag on the surface of the molten metal which has the effect of retarding further oxidation of the calcium and aluminum impurities and results in the inefiicient usage of oxygen and also causes slag separation problems.
  • a process in accordance with the present invention comprises providing a molten bath of the metal to be purified; contacting the surface of the molten metal with a stream of gaseous oxygen; and introducing inert gas into the lower portion of the molten metal bath to provide agitation thereof to thereby promote oxidation of the oxidizable impurities therein.
  • impurity-containing metal for example ferrosilicon (74 to 76 percent Si) containing 0.45 percent Al and 0.20 percent Ca is provided in the molten state.
  • Molten ferrosilicon or other metal can be concurrently obtained by .tapping from the furnace in which it is produced into a ladle or similar device.
  • a stream of oxygen is directed at the surface of the molten metal while concurrently an inert gas, e.g. argon is introduced into the lower portion of the bath.
  • an inert gas e.g. argon
  • the argon introduction can suitably be accomplished by means of a tuyere located in the bottom of the ladle containing the molten ferrosilicon. It has been found that the rate of argon introduction is preferably no greater than the rate of oxygen flow, in order to permit effective removal of aluminum and calcium. For best results, the oxygen flow should be about 1 to 2 times the rate of argon flow.
  • the oxygen flow should be limited to a value which avoids the oxidation of metal other than the impurities to be removed. That is to say, the oxygen rate is limited so that there is no substantial slag formation on the surface of the metal.
  • molten ferrosilicon 75.8% Si, 0.20% Ca, 0.45% Al bal. Fe
  • the oxygen flow rate is suit-.
  • the inert gas cannot be merely mixed with the oxygen since under these circumstances only dilution is achieved and little if any improvement in impurity removal is obtained.
  • melts of percent ferrosilicon were produced under lime-alumina slag.
  • the slag was frozen in place and the metal was poured into a ladle having a 30 inch ID. and equipped with a tuyere inch in diameter centrally located at the bottom.
  • the depth of the alloy in each case was about 22 inches.
  • Argon was introduced through the tuyere and bubbled through the melt and a stream of oxygen was blow onto the surface of the molten metal through a water cooled lance. This treatment was continued in each instance until the aluminum content of the alloy was decreased to about 1.0 percent and the calcium content to about 0.5 percent.
  • the calcium and aluminum contents of the starting alloy were about 1.7 percent and 1.6 percent, respectively.
  • a process for removing aluminum and calcium impurities from ferrosilicon which comprises:
  • a process for removing aluminum and calcium impurities from ferrosilicon which comprises:

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 States Patent 3,325,278 ALLOY PURIFICATION PROCESS Melvin L. McClellan, Grand Island, N.Y., assignor to Union Carbide Corporation, a corporation of New York No Drawing. Filed May 7, 1964, Ser. No. 365,778 2 Claims. (Cl. 7560) The present invention relates to the purification of alloys. More particularly, the present invention relates to a process for the removal of impurities from molten metals by the oxidation of the impurities.
Many metals and alloys, by virtue of their method of manufacture, contain minor amounts of impurities which detrimentally affect their performance in. their intended use. 1
For example, ferrosilicon which is used in the treatment of steel, often contains small percentages, e.g. up to 2 percent each of aluminum and calcium.
In many instances, for example in the production of special electrical steels containing silicon the presence of such amounts of aluminum and calcium is highly undesirable since these elements interfere with the electrical properties of the steel.
It has been proposed to remove these impurities by melting the alloy under a high silica slag or holding the alloy molten under such a slag in an arc furnace. However .this type of procedure is costly and requires relatively expensive equipment.
It has also been proposed to treat aluminum and calcium containing ferrosilicon with gaseous oxygen while in the molten state to oxidize and thus remove these materials.
This approach has not been entirely successful due .to the fact that as the aluminum and/or calcium contents are lowered, substantial oxidation of silicon begins and relatively large amounts of silicon, e.g. up to 5 percent and more are lost.
Moreover, as the silicon is oxidized, it forms a fluid slag on the surface of the molten metal which has the effect of retarding further oxidation of the calcium and aluminum impurities and results in the inefiicient usage of oxygen and also causes slag separation problems.
It is therefore an object of the present invention to provide an improved process for removing impurities from molten metal through the use of gaseous oxygen.
Other objects will be apparent from the following description and claims.
A process in accordance with the present invention comprises providing a molten bath of the metal to be purified; contacting the surface of the molten metal with a stream of gaseous oxygen; and introducing inert gas into the lower portion of the molten metal bath to provide agitation thereof to thereby promote oxidation of the oxidizable impurities therein.
In the practice of the present invention impurity-containing metal for example ferrosilicon (74 to 76 percent Si) containing 0.45 percent Al and 0.20 percent Ca is provided in the molten state.
Molten ferrosilicon or other metal can be concurrently obtained by .tapping from the furnace in which it is produced into a ladle or similar device.
With the metal bath at a convenient temperature, e.g. 1350 to 1700 C. a stream of oxygen is directed at the surface of the molten metal while concurrently an inert gas, e.g. argon is introduced into the lower portion of the bath. The argon introduction can suitably be accomplished by means of a tuyere located in the bottom of the ladle containing the molten ferrosilicon. It has been found that the rate of argon introduction is preferably no greater than the rate of oxygen flow, in order to permit effective removal of aluminum and calcium. For best results, the oxygen flow should be about 1 to 2 times the rate of argon flow.
Also, the oxygen flow should be limited to a value which avoids the oxidation of metal other than the impurities to be removed. That is to say, the oxygen rate is limited so that there is no substantial slag formation on the surface of the metal.
By way of a more specific description of an embodiment of the presentinvention, a batch of molten ferrosilicon (75.8% Si, 0.20% Ca, 0.45% Al bal. Fe) is placed in a If a slag begins to form, the oxygen flow rate is suit-.
ably decreased to avoid further oxidation of silicon. It has been found that with the equipment and materials aforedescribed an oxygen flow rate of about 360 c.f.h. and an argon flow rate of about 225 c.f.h. can provide a reduction of the aluminium and calcium content to below about 25% and .06% respectively, without any significant loss of silicon, i.e. the silicon loss is less than 1 percent.
It is to be noted that in the present invention, the inert gas cannot be merely mixed with the oxygen since under these circumstances only dilution is achieved and little if any improvement in impurity removal is obtained.
In order to determine the effectiveness of the deoxidizing process of the present invention, melts of percent ferrosilicon were produced under lime-alumina slag. The slag was frozen in place and the metal was poured into a ladle having a 30 inch ID. and equipped with a tuyere inch in diameter centrally located at the bottom. The depth of the alloy in each case was about 22 inches. Argon was introduced through the tuyere and bubbled through the melt and a stream of oxygen was blow onto the surface of the molten metal through a water cooled lance. This treatment was continued in each instance until the aluminum content of the alloy was decreased to about 1.0 percent and the calcium content to about 0.5 percent. The calcium and aluminum contents of the starting alloy were about 1.7 percent and 1.6 percent, respectively.
The results obtained are shown in Table I.
TABLE I Weight of O2 Argon Slag Temp. at Starting Rate, Rate, Time, Forma- End of Alloy, lbs. c.f.h. c.i.h. minutes tion Treatpient,
I 1,590 720 225 15 Heavy 2,880 II, 1,750 360 225 25 None 2, 685
1 Silicon oxidation.
treatment of manganese, chromium, and iron base alloys.
What is claimed is:
1. A process for removing aluminum and calcium impurities from ferrosilicon which comprises:
(1) providing a molten bath of ferrosilicon (2) contacting the surface of the molten metal with a stream of gaseous oxygen and (3) introducing inert gas into the lower portion of the molten ferrosilicon bath .to provide agitation thereof to thereby promote oxidation of the calcium and aluminum impurities therein.
2. A process for removing aluminum and calcium impurities from ferrosilicon which comprises:
(1) providing a molten bath of ferrosilicon at a temperature in the range of about 1350 C. to about 1700 C.; l
(2) contacting the surface of the molten ferrosilicon with gaseous oxygen by directing a stream of oxygen at the surface of the molten ferrosilicon;
(3) introducing inert gas into the molten ferrosilicon below the surface of the molten bath and at the lower portion thereof, the rate of flow of inert gas being sufficient to cause vigorous agitation of the molten bath by bubbles of inert gas; and
(4) adjusting the rate of How of oxygen and inert gas so that the oxygen flow rate is between about 1 and 2 times the inert gas flow rate and so that there is no substantial formation of slag on the surface of the molten ferrosilicon.
References Cited UNITED STATES PATENTS 1,968,917 8/ 1934 Soldatoff 7560 2,866,701 12/1958 Strauss 7560 3,169,058 2/1965 Nelson 75-59 3,201,226 8/1965 Spolders et al 7560 FOREIGN PATENTS 872,995 7/1196 1 Great Britain. 878,386 9/ 1961 Great Britain.
BENJAMIN HENKIN, Primary Examiner.

Claims (1)

1. A PROCESS FOR REMOVING ALUMINUM AND CALCIUM IMPURITIES FROM FERROSILICON WHICH COMPRISES: (1) PROVIDING A MOLTEN BATH OF FERROSILICON (2) CONTACTING THE SURFACE OF THE MOLTEN METAL WITH A STREAM OF GASEOUS OXYGEN AND (3) INTRODUCING INERT GAS INTO THE LOWER PORTION OF THE MOLTEN FERROSILICON BATH TO PROVIDE AGITATION THEREOF TO THEREBY PROMOTE OXIDATION OF THE CALCIUM AND ALUMINUM IMPURITIES THEREIN.
US365778A 1964-05-07 1964-05-07 Alloy purification process Expired - Lifetime US3325278A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US365778A US3325278A (en) 1964-05-07 1964-05-07 Alloy purification process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US365778A US3325278A (en) 1964-05-07 1964-05-07 Alloy purification process

Publications (1)

Publication Number Publication Date
US3325278A true US3325278A (en) 1967-06-13

Family

ID=23440319

Family Applications (1)

Application Number Title Priority Date Filing Date
US365778A Expired - Lifetime US3325278A (en) 1964-05-07 1964-05-07 Alloy purification process

Country Status (1)

Country Link
US (1) US3325278A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3839018A (en) * 1968-06-03 1974-10-01 British Iron Steel Research Production of low carbon ferroalloys
EP0100869A1 (en) * 1982-07-19 1984-02-22 Hoechst Aktiengesellschaft Method of lowering the titanium and aluminium content of block iron
US4529442A (en) * 1984-04-26 1985-07-16 Allegheny Ludlum Steel Corporation Method for producing steel in a top oxygen blown vessel

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1968917A (en) * 1933-06-30 1934-08-07 Vassily V Soldatoff Process of making steel
US2866701A (en) * 1956-05-10 1958-12-30 Vanadium Corp Of America Method of purifying silicon and ferrosilicon
GB872995A (en) * 1956-11-05 1961-07-19 Pechiney Prod Chimiques Sa Process for purifying silicon or a ferro-silicon alloy
GB878386A (en) * 1959-03-13 1961-09-27 British Oxygen Co Ltd Treatment of molten ferrous metal
US3169058A (en) * 1960-11-18 1965-02-09 Union Carbide Corp Decarburization, deoxidation, and alloy addition
US3201226A (en) * 1957-02-27 1965-08-17 Ruhrstahl Huttenwerke Ag Steel purification vacuum method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1968917A (en) * 1933-06-30 1934-08-07 Vassily V Soldatoff Process of making steel
US2866701A (en) * 1956-05-10 1958-12-30 Vanadium Corp Of America Method of purifying silicon and ferrosilicon
GB872995A (en) * 1956-11-05 1961-07-19 Pechiney Prod Chimiques Sa Process for purifying silicon or a ferro-silicon alloy
US3201226A (en) * 1957-02-27 1965-08-17 Ruhrstahl Huttenwerke Ag Steel purification vacuum method
GB878386A (en) * 1959-03-13 1961-09-27 British Oxygen Co Ltd Treatment of molten ferrous metal
US3169058A (en) * 1960-11-18 1965-02-09 Union Carbide Corp Decarburization, deoxidation, and alloy addition

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3839018A (en) * 1968-06-03 1974-10-01 British Iron Steel Research Production of low carbon ferroalloys
EP0100869A1 (en) * 1982-07-19 1984-02-22 Hoechst Aktiengesellschaft Method of lowering the titanium and aluminium content of block iron
US4529442A (en) * 1984-04-26 1985-07-16 Allegheny Ludlum Steel Corporation Method for producing steel in a top oxygen blown vessel
EP0160376A2 (en) * 1984-04-26 1985-11-06 Allegheny Ludlum Corporation Method for producing steel in a top oxygen blown vessel
EP0160376A3 (en) * 1984-04-26 1989-07-26 Allegheny Ludlum Steel Corporation Method for producing steel in a top oxygen blown vessel

Similar Documents

Publication Publication Date Title
US3325278A (en) Alloy purification process
US3212881A (en) Purification of alloys
US3537842A (en) Treatment of molten metal
US3615348A (en) Stainless steel melting practice
US3172758A (en) Oxygen process for producing high
US3305352A (en) Process of producing alloys
US3318687A (en) Treatment of slag in the process of making steel
JPH10130714A (en) Production of steel for wire rod excellent in wire drawability and cleanliness
US3210183A (en) Method of manufacturing nodular graphite-cast steel and-cast iron having excellent castability
US2301360A (en) Purification of high silicon iron alloys
US2458651A (en) Processes for producing low carbon chromium steels
US3374088A (en) Method for producing low silicon ferromanganese alloys
US3063831A (en) Method of making titaniumcontaining alloys
KR940004821B1 (en) Making method of high carbon steel
JPH07103416B2 (en) High carbon steel wire manufacturing method
KR100224635B1 (en) Slag deoxidation material for high purity steel making
SU1044641A1 (en) Method for alloying steel with manganese
EP0163784B1 (en) Two stage deoxidation process in steel-making
US1858386A (en) Process for preparing and purifying alloys
US1535311A (en) Process of producing substantially pure iron
US1925916A (en) Process of producing alloys
SU1035079A1 (en) Manganese slag
US3244510A (en) Method of making electrical steel having superior magnetic properties
US1786806A (en) Process of refining iron and steel
US3024105A (en) Process for low-phosphorus ferromanganese alloys

Legal Events

Date Code Title Description
AS Assignment

Owner name: ELKEM METALS COMPANY, 270 PARK AVENUE, NEW YORK, N

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:UNION CARBIDE CORPORATION, A NY CORP.;REEL/FRAME:003882/0761

Effective date: 19810626

Owner name: ELKEM METALS COMPANY, A NEW YORK GENERAL PARTNERSH

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:UNION CARBIDE CORPORATION, A NY CORP.;REEL/FRAME:003882/0761

Effective date: 19810626