EP0259772B1 - Apparatus and method for manufacturing copper-base alloy - Google Patents
Apparatus and method for manufacturing copper-base alloy Download PDFInfo
- Publication number
- EP0259772B1 EP0259772B1 EP87112809A EP87112809A EP0259772B1 EP 0259772 B1 EP0259772 B1 EP 0259772B1 EP 87112809 A EP87112809 A EP 87112809A EP 87112809 A EP87112809 A EP 87112809A EP 0259772 B1 EP0259772 B1 EP 0259772B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- spout
- copper
- alloying
- molten copper
- passageway
- 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
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/10—Supplying or treating molten metal
- B22D11/11—Treating the molten metal
Definitions
- the present invention relates to an apparatus and a method for manufacturing a copper-base alloy having a quite uniform chemical composition.
- the batch process has been disadvantageous in that every time the kinds of copper-base alloys to be manufactured are changed, the inside of the melting furnace has to be washed. As a result, a large quantity of a melt has been required for washing, and it is laborious to carry out such washing. In addition, inasmuch as the intermittent operation deteriorates the rate of operation of the melting furnace, the productivity has been lowered, resulting in a high production cost. Besides, since the solute constituents are difficult to be mixed uniformly with copper, the alloy thus produced has not complied with a desired quality.
- US-A-3836360 discloses an apparatus for manufacturing a copper-base alloy which comprises a furnace for heating pure copper which is then released at a controlled rate into a launder.
- the melted copper flows through a relatively narrow channel formed in the launder to a discharge end.
- the alloyed metal is continuously discharged from this end into the entrance of a direct chill casting mould.
- a wire coil comprising a master alloy is fed into the alloy as it flows along the narrow channel of the launder.
- GB-A-1181518 discloses a process for producing oxygen-free cast metal by maintaining an inert atmosphere containing carbon monoxide and hydrogen above a molten alloy whilst it is flowing through a furnace system.
- a pouring spout of a holding furnace is joined in a gas tight manner to a closed casting head formed as a launder which the holding furnace spout enters at one end and which at the other end has a bottom pouring discharge port which is controlled by a plunger.
- Another object is to provide a method of manufacturing a copper alloy by using such an apparatus.
- an apparatus for manufacturing a copper-base alloy comprising an alloying spout inclined downwardly from one end towards the other end for flowing molten copper therethrough, said alloying spout including an inlet at said one end and an outlet at said other end and having an elongated passageway through which said inlet communicates with said outlet, whereby the molten copper introduced from said inlet can flow downwardly through said passageway to said outlet; characterised in that a tundish is disposed at said other end of said alloying spout for receiving said molten copper-base alloy tapped from said alloying spout; said alloying spout and said tundish are respectively comprised of hermetically sealable casings; and said alloying spout includes first and second spaced-apart feed means provided at relatively upstream and downstream portions of said alloying spout, the upstream feed means being arranged to introduce at least one solid solute constituent having a higher melting point than copper into said passageway,
- a method of manufacturing a copper-base alloy comprising the steps of providing an alloying spout inclined downwardly from an inlet towards an outlet and having an elongated passageway through which said inlet communicates with said outlet; and continuously introducing molten copper from said inlet into said passageway of said alloying spout and causing the molten copper to flow downwardly through said passageway to said outlet ; characterized by continuously introducing at least one solid solute constituent having a higher melting point than copper through a first feed means into an upstream portion of said passageway of said alloying spout and continuously introducing at least one solid solute constituent having a lower melting point than copper through a second feed means into a downstream portion of said passageway, the first and second feed means being arranged to enable the mixing of said at least two solute constituents with said molten copper; imparting a hermetically sealable structure to said alloying spout and providing a hermetically sealable tundish at the outlet
- FIGs. 1 and 2 there is illustrated an apparatus for manufacturing a copper-base alloy, which comprises a melting crucible furnace 10 for melting a solid copper material to produce a molten copper.
- a pouring spout 12 which is inclined downwardly from one end toward the other end and has an inlet 12a at the one end and an outlet 12b at the other end, is connected at the one end to the melting furnace 10, and a holding furnace 14 is disposed at the other end of the pouring spout 12 for holding the molten copper tapped from the pouring spout 12 in an oxygen-free state and keeping the temperature of the molten copper at a prescribed level.
- the pouring spout 12 is accommodated in a refractory brick-lined housing 13, and a reducing gas, which consists of a mixture of carbon monoxide gas and nitrogen gas, is contained in the spout 12.
- An alloying spout 16 which is inclined downwardly from one end toward the other end, is connected at the one end to the holding furnace 14 for causing the molten copper tapped from the holding furnace 14 to flow downwardly therethrough.
- the alloying spout 16 is comprised of a hermetically sealable casing having an inlet 16a at the one end and an outlet 16b at the other end and an elongated passageway 16c through which the inlet 16a communicates with the outlet 16b, and an inert gas or a reducing gas is filled in the passageway 16c.
- the alloying spout 16 is accommodated in a refractory brick-lined housing 13.
- First and second feeders 20 and 22 are respectively connected to the alloying spout 16 for introducing solid solute constituents into the passageway 16c of the alloying spout 16, the first feeder 20 being connected to an upstream portion of the spout 16 adjacent to the one end thereof while the second feeder 22 is connected to a downstream portion of the spout 16 adjacent to the other end thereof.
- the passageway 16c of the alloying spout 16 should be long enough to melt the solute constituents to mix them with the molten copper during the passage of the molten copper through the passageway 16c.
- the solute constituents to be alloyed with copper are different depending upon the kinds of the copper alloys to be produced.
- solute constituents many elements such as chromium (Cr), zirconium (Zr), titanium (Ti), silicon (Si), nickel (Ni), iron (Fe), magnesium (Mg), tin (Sn), tellurium (Te), arsenic (As), phosphorus (P), aluminium (Al), zinc (Zn), beryllium (Be), W (tungsten) and the like may be alloyed with copper.
- a solid material of a high purity should preferably be used. Such pure solid material may be in the form of granules, grains, wires, pieces, powders or the like.
- the outer shell of the tundish 18 has an opening in the bottom, in which is fitted a nozzle 18a with a stopper 24. By raising and lowering the stopper 24, the quantity of the molten copper alloy to be tapped from the tundish 18 can be controlled.
- a mould 26 is disposed under the tundish 18 for continuously casting the molten alloy tapped from the nozzle 18a of the tundish 18 to produce a cast copper alloy.
- a sealing shell 28 is mounted between the tundish 18 and the mould 26 for hermetically sealing the inside of the mould and the tundish, and an inert gas is supplied thereinto.
- the melting furnace 10 is charged with the solid copper, and the copper is melted. Specifically, in this melting furnace 10, pieces of charcoal are added to prevent the molten copper from being exposed to the air, so that low oxygen molten copper, which contains an oxygen content of not greater than 50 ppm, is produced in it.
- the molten copper in the melting furnace 10 exceeds a prescribed level, it overflows into the pouring spout 12 and passes therethrough to the holding furnace 14.
- the low oxygen molten copper is reduced by the reducing gas contained therein to an oxygen free molten copper, an oxygen content of which is not greater than 10 ppm.
- the oxygen-free molten copper is tapped into the holding furnace 14 and kept at a prescribed temperature. Then, the molten copper overflows into the alloying spout 16 and passes through the passageway 16c thereof to flow into the tundish 18.
- first solid solute constituents which have high melting points compared with copper and are difficult to be melted, are added through the first feeder 20 into the passageway 16c of the alloying spout 16
- second solute constituents which have low melting points compared with copper
- the solute constituents introduced into the passageway 16c are mixed with the molten copper uniformly and melted quickly, and thus a molten copper-base alloy of a uniform chemical composition is produced.
- the first solute constituents have high melting points and are difficult to be melted, they are added in the alloying spout 16 at its upstream portion, and therefore they can be sufficiently alloyed with the copper during the passage through the elongated passageway 16c.
- the second solute constituents having low melting points they are added in the spout 16 at its downstream portion, but are easily mixed with and alloyed with the copper.
- Some solute constituents having higher solubilities may be added in the tundish 18. Further, the solute constituents may preferably be preheated to temperatures near to their melting points before they are added.
- the molten copper alloy thus produced is tapped from the alloying spout 16 into the tundish 18, and teemed from the tundish 18 into the mould 26 through the nozzle 18a, so that a cast product 30 of copper alloy is manufactured.
- the solute constituents are alloyed with the oxygen free copper in the alloying spout 16, they may be alloyed with low oxygen copper or deoxidized copper.
- the solute constituent to be added is an active or reactive element such as Cr, Ti, Zr, Si, Mg, Ca, Al and the like, which has a great affinity for oxygen, such element combines with oxygen to thereby lower the yield of the alloy.
- the low oxygen copper may be preferably used.
- Fig. 3 shows a modified apparatus in accordance with the present invention which differs from the apparatus of Figs. 1 and 2 only in that there is provided a heating furnace 32 between the alloying spout 16 and the tundish 18 for heating the molten alloy tapped from the spout 16.
- the heating furnace 32 is a high frequency induction furnace, to which is attached a bubbling apparatus 34 for blowing an inert gas such as argon into the molten alloy to stir it up.
- An alloy produced by the apparatus of this embodiment contains a high content of solute elements.
- Fig. 4 shows another modified apparatus in accordance with the present invention which differs from the apparatus of Figs. 1 and 2 only in that heating means 36 is attached to the alloying spout 16 for heating the molten copper and the solute elements passing through the passageway 16c.
- each of the spouts 12 and 16 may be a spout of a U-shaped cross section housed in a hermetically sealable refractory brick-lined housing.
- the solute constituents are continuously added in the molten copper which is flowing at a sufficient flow rate. Accordingly, the solute constituents added are stirred by the flow of the molten copper and mixed therewith uniformly and melted quickly, and thus the copper-base alloy of a uniform chemical composition is produced continuously.
- the quantity of the solute constituents to be added in the alloying spout is changed, and besides different kinds of alloys can easily be manufactured. Further, since the alloying is carried out in the alloying spout, there is no need to wash the inside of the melting furnace when changing the kinds of alloys to be manufactured, thus increasing the operating rate of the apparatus substantially.
- Cr-Cu alloys of a desired Cr content ranging from 0.25 to 0.40 % by weight were manufactured using the apparatus of Figs. 1 and 2.
- Cr-Cu alloys of the same desired Cr content were produced by the conventional batch process. The data on Cr contents and the like for such alloys are shown in TABLE 1.
- the alloys obtained by the apparatus in accordance with the present invention exhibits generally uniform Cr contents and complies with the desired specification.
- Cr contents of the alloys obtained by the conventional batch process vary widely, and besides there is an alloy which does not meet the specification.
- Zr-Cu alloys of a desired Zr content ranging from 0.07 to 0.13 % by weight were manufactured by using the apparatus of Figs. 1 and 2, and by the conventional batch process for comparison purposes.
- the data on Zr contents and the like for such alloys are shown in TABLE 2.
- the alloys obtained by the apparatus in accordance with the present invention exhibits a generally uniform Zr content and complies with the desired specification.
- Zr contents of the alloys obtained by the conventional batch process vary widely, and besides there is an alloy which does not meet requirements. Further, although Zr is reactive and is liable to oxidation, Zr contents of the alloys obtained by the apparatus of the invention are relatively higher as compared with the alloys obtained by the conventional process.
- Mg-Cu alloys of a desired Mg content ranging from 0.02 to 0.08 % by weight were manufactured by using the apparatus of Figs. 1 and 2, and by the conventional batch process for comparison purposes.
- the data on Mg contents and the like for such alloys are shown in TABLE 3.
- the alloys obtained by the apparatus in accordance with the present invention exhibits a generally uniform Mg content and complies with the desired specification.
- Mg contents of the alloys obtained by the conventional batch process vary widely, and besides there is an alloy which does not meet requirements.
- Mg contents of the alloys obtained by the apparatus of the invention are relatively higher as compared with the alloys obtained by the conventional process.
- Cr-Cu alloys of a desired Cr content ranging from 0.75 to 0.90 % by weight were manufactured using the apparatus of Fig. 3 which includes the heating furnace 32.
- Cr-Cu alloys of the same desired Cr content were produced by the conventional batch process. The data on Cr contents and the like for such alloys are shown in TABLE 4.
- the alloys produced by the apparatus in accordance with the present invention exhibits a generally uniform Cr content and complies with the desired specification.
- Cr contents of the alloys obtained by the conventional batch process vary widely, and besides there are alloys which do not meet requirements.
- Granules of a pure Cr metal each of which had a high melting point and had a purity of not less than 99.7 % by weight and a granular size of 0.1 mm to 1.5 mm, were alloyed with copper using the apparatus of Figs. 1 and 2, and a copper alloy which had a uniform chemical composition containing a Cr content of 1.1 % by weight was successfully obtained.
- smashed pieces of Ti each having a purity of not less than 99.6 % by weight and a size of 3.0 mm to 5.0 mm
- pieces of Zr each having a purity of not less than 98.0 % by weight and a size of 1.0 mm ⁇ 5.0 mm ⁇ 10.0 mm
- smashed pieces of Si each having a purity of not less than 99.9 % by weight and a size of 3.0 mm ⁇ 5.0 mm
- spherical pieces of Ni each having a purity of not less than 99.8 % by weight and a size of 8 mm
- pieces of Fe each having a purity of not less than 99.9 % by weight and a size of 1 mm ⁇ 2 mm to 5 mm
- copper alloys which contain Ti content of 2.5 % by weight, Zr content of 0.2 % by weight, Si content of 1.7 % by weight, Ni content of 2.5 % by weight, and Fe content of 2.3 % by weight, respectively
- a Cu-Cr-Ti-Si-Ni-Sn alloy was produced by the apparatus of Figs. 1 and 2. In this case, by adding the alloying elements in the order of Cu-Cr-Ti-Si-Ni-Sn, an alloy having Cr content of 0.3 % was obtained.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Continuous Casting (AREA)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP206134/86 | 1986-09-02 | ||
JP61206133A JPS6362829A (ja) | 1986-09-02 | 1986-09-02 | 合金溶体の製造装置 |
JP206133/86 | 1986-09-02 | ||
JP61206134A JPS6362830A (ja) | 1986-09-02 | 1986-09-02 | 合金溶体の製造装置 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0259772A2 EP0259772A2 (en) | 1988-03-16 |
EP0259772A3 EP0259772A3 (en) | 1988-09-14 |
EP0259772B1 true EP0259772B1 (en) | 1992-08-05 |
Family
ID=26515465
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP87112809A Expired - Lifetime EP0259772B1 (en) | 1986-09-02 | 1987-09-02 | Apparatus and method for manufacturing copper-base alloy |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0259772B1 (fi) |
KR (1) | KR940006287B1 (fi) |
DE (1) | DE3780887T2 (fi) |
FI (1) | FI88730C (fi) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2679162A1 (fr) * | 1991-07-18 | 1993-01-22 | Siderurgie Fse Inst Rech | Dispositif de transfert par jet de metal liquide, notamment d'une poche de coulee continue vers un repartiteur. |
DE10112621A1 (de) * | 2001-03-14 | 2002-09-19 | Km Europa Metal Ag | Anordnung zum Abgießen einer aus einer Kupferlegierung bestehenden Gießschmelze |
JP5053242B2 (ja) | 2007-11-30 | 2012-10-17 | 古河電気工業株式会社 | 銅合金材の製造方法及びその装置 |
CN104357698B (zh) * | 2014-09-28 | 2016-06-22 | 江苏中容铜业有限公司 | 一种引线框架铜带基材生产系统 |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1433570A1 (de) * | 1964-05-20 | 1968-11-07 | Kaiser Ind Corp | Kontinuierliches Verfahren und Vorrichtung zur Erzeugung von Gusskoerpern aus oxydierbaren Metallen |
GB1181518A (en) * | 1966-08-15 | 1970-02-18 | Ass Elect Ind | Improvements relating to Production of Cast Metal. |
SE384805B (sv) * | 1971-06-03 | 1976-05-24 | I Properzi | Forfarande och anordning for avgasning och overforing av smelt metall |
US3836360A (en) * | 1972-07-10 | 1974-09-17 | Anaconda Co | Method and apparatus for pre-heating and adding master alloy to a copper melt |
US3785427A (en) * | 1972-08-15 | 1974-01-15 | Metallurg Hoboken Overpett | Casting of deoxidized copper |
JPS60121056A (ja) * | 1983-12-05 | 1985-06-28 | Furukawa Electric Co Ltd:The | 連続鋳造用溶銅の酸素量制御方法 |
-
1987
- 1987-09-01 KR KR1019870009673A patent/KR940006287B1/ko not_active IP Right Cessation
- 1987-09-01 FI FI873791A patent/FI88730C/fi not_active IP Right Cessation
- 1987-09-02 EP EP87112809A patent/EP0259772B1/en not_active Expired - Lifetime
- 1987-09-02 DE DE8787112809T patent/DE3780887T2/de not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP0259772A3 (en) | 1988-09-14 |
FI88730C (fi) | 1993-06-28 |
EP0259772A2 (en) | 1988-03-16 |
FI88730B (fi) | 1993-03-15 |
FI873791A (fi) | 1988-03-03 |
DE3780887T2 (de) | 1993-01-14 |
FI873791A0 (fi) | 1987-09-01 |
DE3780887D1 (de) | 1992-09-10 |
KR940006287B1 (ko) | 1994-07-14 |
KR880004113A (ko) | 1988-06-01 |
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