[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

EP0259772B1 - Apparatus and method for manufacturing copper-base alloy - Google Patents

Apparatus and method for manufacturing copper-base alloy Download PDF

Info

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
Application number
EP87112809A
Other languages
German (de)
French (fr)
Other versions
EP0259772A3 (en
EP0259772A2 (en
Inventor
Izumi Sukekawa
Haruhiko Asao
Hiroshi Kohno
Yukio Sugawara
Keiji Nogami
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.)
Mitsubishi Materials Corp
Original Assignee
Mitsubishi Materials 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
Priority claimed from JP61206134A external-priority patent/JPS6362830A/en
Priority claimed from JP61206133A external-priority patent/JPS6362829A/en
Application filed by Mitsubishi Materials Corp filed Critical Mitsubishi Materials Corp
Publication of EP0259772A2 publication Critical patent/EP0259772A2/en
Publication of EP0259772A3 publication Critical patent/EP0259772A3/en
Application granted granted Critical
Publication of EP0259772B1 publication Critical patent/EP0259772B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B9/00General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/10Supplying or treating molten metal
    • B22D11/11Treating 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.

Landscapes

  • 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)

Description

  • The present invention relates to an apparatus and a method for manufacturing a copper-base alloy having a quite uniform chemical composition.
  • Prior Art
  • In manufacturing a copper-base alloy, there has conventionally been employed a batch process, in which solute metals are alloyed with copper in a melting furnace.
  • The batch process, however, 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. In the 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.
  • SUMMARY OF THE INVENTION
  • It is therefore an object of the present invention to provide a copper alloy manufacturing apparatus which can melt a solute constituent in a molten copper uniformly to continuously produce a copper alloy having a uniform chemical composition with a reduced cost.
  • Another object is to provide a method of manufacturing a copper alloy by using such an apparatus.
  • According to a first aspect of the present invention, there is provided 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, and the downstream feed means being arranged to introduce at least one solid solute constituent having a lower melting point than copper into said passageway, said first and second feed means being arranged to enable said at least two solute constituents to become mixed with said molten copper.
    According to a second aspect of the present invention, there is provided 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 of said alloying spout ; and tapping the molten copper-base alloy into said tundish from said alloying spout.
  • BRIEF DESCRIPTION OF THE DRAWINGS
    • Fig. 1 is a schematic cross-sectional view showing an apparatus in accordance with the present invention;
    • Fig. 2 is a schematic transverse cross-sectional view of an alloying spout mounted in the apparatus of Fig. 1;
    • Fig. 3 is a schematic cross-sectional view showing a part of a modified apparatus in accordance with the present invention; and
    • Fig. 4 is a schematic cross-sectional view showing a part of another modified apparatus in accordance with the present invention.
    DESCRIPTION OF THE PREFERRED EMBODIMENTS OF THE INVENTION
  • Referring to 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. As shown in Fig. 2, 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. As is the case with the pouring spout 12, the alloying spout 16 is accommodated in a refractory brick-lined housing 13. A pouring basin or tundish 18, which is also comprised of a hermetically sealable casing, is disposed at the other end of the alloying spout 16 for receiving the molten metal tapped from the alloying spout 16, and graphite powder is contained in the tundish to cover the surface of the molten metal for sealing purposes. 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. As such 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. With respect to an element having a higher melting point as compared with copper, such as Cr, Zr, Ti, Si, Ni and Fe, 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 operation of the copper alloy manufacturing apparatus will now be described.
  • First, 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. When 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. In the pouring spout 12, 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.
  • Subsequently, 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. During the passage of the copper through the alloying spout 16, 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, and second solute constituents, which have low melting points compared with copper, are added through the second feeder 22 into the passageway 16c of the spout 16. In this step, inasmuch as the molten copper is flowing through the passageway 16c at a sufficient flow rate, 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. In addition, although 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. With respect to 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.
  • Although in the foregoing, 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. However, if 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. In such a case, 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.
  • Further, although in the above embodiments, two feeders are connected to the alloying spout 16, only one feeder may be enough if only a few solute constituents are to be added, or the solubilities of the solute constituents are almost equivalent to each other. In addition, 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.
  • As described above, in the apparatus in accordance with the present invention, 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. In addition, by changing the quantity of the solute constituents to be added in the alloying spout, the quantity of the alloy to be produced 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.
  • The invention will now be illustrated by way of the following EXAMPLES.
  • EXAMPLE 1
  • 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. For comparison purposes, 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.
  • As seen from 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. On the other hand, 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.
    Figure imgb0001
  • EXAMPLE 2
  • 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.
  • As seen from 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. On the other hand, 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.
    Figure imgb0002
  • EXAMPLE 3
  • 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.
  • As seen from 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. On the other hand, Mg contents of the alloys obtained by the conventional batch process vary widely, and besides there is an alloy which does not meet requirements. Further, as is the case with EXAMPLE 2, although Mg is reactive and is liable to oxidation, 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.
    Figure imgb0003
  • EXAMPLE 4
  • 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. For comparison purposes, 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.
  • As seen from 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. On the other hand, Cr contents of the alloys obtained by the conventional batch process vary widely, and besides there are alloys which do not meet requirements.
    Figure imgb0004
  • EXAMPLE 5
  • 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. Similarly, 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, and 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 were alloyed with copper, respectively, and 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, were obtained.
  • EXAMPLE 6
  • 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.

Claims (12)

  1. An apparatus for manufacturing a copper-base alloy comprising
       an alloying spout (16) inclined downwardly from one end towards the other end for flowing molten copper therethrough, said alloying spout (16) including an inlet (16a) at said one end and an outlet (16b) at said other end and having an elongated passageway (16c) through which said inlet (16a) communicates with said outlet (16b), whereby the molten copper introduced from said inlet (16a) can flow downwardly through said passageway (16c) to said outlet (16b);
       characterized in that
       a tundish (18) is disposed at said other end of said alloying spout (16) for receiving said molten copper-base alloy tapped from said alloying spout (16);
       said alloying spout (16) and said tundish (18) are respectively comprised of hermetically sealable casings: and
    said alloying spout (16) includes first and second spaced-apart feed means (20, 22) provided at relatively upstream and downstream portions of said alloying spout (16), the upstream feed means (20) being arranged to introduce at least one solid solute constituent having a higher melting point than copper into said passageway (16c), and the downstream feed means (22) being arranged to introduce at least one solid solute constituent having a lower melting point than copper into said passageway (16c), said first and second feed means (20, 22) being arranged to enable said at least two solute constituents to become mixed with said molten copper.
  2. An apparatus according to claim 1, further comprising a heat furnace (32) interposed between said alloying spout (16) and said tundish (18) for heating the molten copper-base alloy tapped from said alloying spout (16).
  3. An apparatus according to claim 2, wherein said heating furnace (32) is an induction furnace.
  4. An apparatus according to any preceding claim, further comprising a melting furnace (10) for melting solid copper to produce the molten copper, a pouring spout (12) for causing the molten copper produced in said melting furnace (10) to flow therethrough, a holding furnace (14) interposed between said pouring spout (12) and said alloying spout (16) for receiving said molten copper therein and for keeping the molten copper at a prescribed temperature, and a mould (26) disposed adjacent to said tundish (18) for casting said molten copper-base alloy to produce a cast product of the copper-base alloy.
  5. An apparatus according to any preceding claim, wherein said alloying spout (16) includes heating means (36) attached thereto for heating the molten copper passing through said passageway (16c).
  6. A method of manufacturing a copper-base alloy, comprising the steps of:
    (a) providing an alloying spout (16) inclined downwardly from an inlet (16a) towards an outlet (16b) and having an elongated passageway (16c) through which said inlet (16a) communicates with said outlet (16b); and
    (b) continuously introducing molten copper from said inlet (16a) into said passageway (16c) of said alloying spout (16) and causing the molten copper to flow downwardly through said passageway (16c) to said outlet (16b);
       characterized by continuously introducing at least one solid solute constituent having a higher melting point than copper through a first feed means (20) into an upstream portion of said passageway (16c) of said alloying spout (16) and continuously introducing at least one solid solute constituent having a lower melting point than copper through a second feed means (22) into a downstream portion of said passageway (16c), the first and second feed means (20, 22) 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 (16)and providing a hermetically sealable tundish (18) at the outlet (16b) of said alloying spout (16); and
       tapping the molten copper-base alloy into said tundish (18) from said alloying spout (16).
  7. A method according to claim 6, wherein said molten copper is an oxygen free copper.
  8. A method according to claim 6, wherein said molten copper is low oxygen copper.
  9. A method according to claim 6, wherein said molten copper and said solute constituents are mixed in a non-oxidizing atmosphere.
  10. A method according to claim 9, in which said non-oxidizing atmosphere is an inert gas atmosphere.
  11. A method according to claim 10, in which said non-oxidizing atmosphere is a reducing gas atmosphere.
  12. A method according to claim 6, wherein at least one of said solid solute constituents is a reactive element which is susceptible to oxidation.
EP87112809A 1986-09-02 1987-09-02 Apparatus and method for manufacturing copper-base alloy Expired - Lifetime EP0259772B1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP206133/86 1986-09-02
JP61206134A JPS6362830A (en) 1986-09-02 1986-09-02 Apparatus for producing alloy melt
JP61206133A JPS6362829A (en) 1986-09-02 1986-09-02 Apparatus for producing alloy melt
JP206134/86 1986-09-02

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 (en)
KR (1) KR940006287B1 (en)
DE (1) DE3780887T2 (en)
FI (1) FI88730C (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2679162A1 (en) * 1991-07-18 1993-01-22 Siderurgie Fse Inst Rech Device for jet (stream, runner) transfer of liquid metal, particularly from a continuous casting ladle towards a distributor
DE10112621A1 (en) 2001-03-14 2002-09-19 Km Europa Metal Ag Arrangement for pouring a casting melt consisting of a copper alloy
JP5053242B2 (en) 2007-11-30 2012-10-17 古河電気工業株式会社 Method and apparatus for producing copper alloy material
CN104357698B (en) * 2014-09-28 2016-06-22 江苏中容铜业有限公司 Production system for copper strip substrate of lead frame
CN111618291A (en) * 2020-06-02 2020-09-04 中国重型机械研究院股份公司 Steelmaking continuous casting anaerobic pipeline conveying device and method

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1433570A1 (en) * 1964-05-20 1968-11-07 Kaiser Ind Corp Continuous process and device for the production of cast bodies from oxidizable metals
GB1181518A (en) * 1966-08-15 1970-02-18 Ass Elect Ind Improvements relating to Production of Cast Metal.
SE384805B (en) * 1971-06-03 1976-05-24 I Properzi PROCEDURE AND DEVICE FOR DEGASING AND TRANSMISSION OF MELTED METAL
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 (en) * 1983-12-05 1985-06-28 Furukawa Electric Co Ltd:The Method for controlling amount of oxygen in molten copper for continuous casting

Also Published As

Publication number Publication date
KR880004113A (en) 1988-06-01
EP0259772A3 (en) 1988-09-14
FI873791A (en) 1988-03-03
EP0259772A2 (en) 1988-03-16
DE3780887T2 (en) 1993-01-14
FI88730C (en) 1993-06-28
FI873791A0 (en) 1987-09-01
FI88730B (en) 1993-03-15
KR940006287B1 (en) 1994-07-14
DE3780887D1 (en) 1992-09-10

Similar Documents

Publication Publication Date Title
US4248630A (en) Method of adding alloy additions in melting aluminum base alloys for ingot casting
EP1018383B1 (en) Die casting method
EP2039444A1 (en) Process for manufacturing copper alloy wire rod and copper alloy wire rod
US5391348A (en) Apparatus and method for making steel alloys in a tundish
US4832911A (en) Method of alloying aluminium
US4524819A (en) Method of manufacturing leaded free-cutting steel by continuous casting process
US3490897A (en) Process for producing low oxygen,high conductivity copper
EP0259772B1 (en) Apparatus and method for manufacturing copper-base alloy
US5062614A (en) Apparatus and method for manufacturing copper-base alloy
CN106048335B (en) Large-scale thick casting aluminum alloy materials of space flight and preparation method thereof
US4981514A (en) Method for manufacturing copper-base alloy
US4088475A (en) Addition of reactive elements in powder wire form to copper base alloys
GB2299099A (en) Process for producing grain refining master alloys.
US4459154A (en) Alloy and process for producing and casting ductile and compacted graphite cast irons
US3528803A (en) Method for manufacturing oxygen-free copper by casting
EP0185540A2 (en) Method of refining grains fo primary silicon in hypereutectic Al-Si alloys
KR940010770B1 (en) Method of manufacturing copper-base alloy
JPH07179926A (en) Metallic capsule additive
US3459540A (en) Production of clean fine grain steels
US4367784A (en) Method for adding cooling powders to steel during continuous casting
EP0720967A1 (en) Metallurgical silicon and ferrosilicon of low oxygen content
US3849123A (en) Incorporation of solid additives into molten aluminum
US4203763A (en) Method of manufacturing a lead alloy steel and a steel made according to the method
JP2000317580A (en) Method for casting copper alloy
EP0142585B1 (en) Alloy and process for producing ductile and compacted graphite cast irons

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): DE FR GB SE

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): DE FR GB SE

17P Request for examination filed

Effective date: 19881114

17Q First examination report despatched

Effective date: 19890630

RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: MITSUBISHI MATERIALS CORPORATION

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): DE FR GB SE

ET Fr: translation filed
REF Corresponds to:

Ref document number: 3780887

Country of ref document: DE

Date of ref document: 19920910

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
EAL Se: european patent in force in sweden

Ref document number: 87112809.6

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 19980814

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 19980821

Year of fee payment: 12

Ref country code: DE

Payment date: 19980821

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 19980824

Year of fee payment: 12

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19990902

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: THE PATENT HAS BEEN ANNULLED BY A DECISION OF A NATIONAL AUTHORITY

Effective date: 19990929

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 19990902

EUG Se: european patent has lapsed

Ref document number: 87112809.6

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20000531

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20000701

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST