WO2018155658A1 - Method for producing ti-al alloy - Google Patents

Method for producing ti-al alloy Download PDF

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Publication number
WO2018155658A1
WO2018155658A1 PCT/JP2018/006823 JP2018006823W WO2018155658A1 WO 2018155658 A1 WO2018155658 A1 WO 2018155658A1 JP 2018006823 W JP2018006823 W JP 2018006823W WO 2018155658 A1 WO2018155658 A1 WO 2018155658A1
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WIPO (PCT)
Prior art keywords
ingot
mass
alloy
flux
melting
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PCT/JP2018/006823
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French (fr)
Japanese (ja)
Inventor
史晃 工藤
大介 松若
石田 斉
哲史 出浦
Original Assignee
株式会社神戸製鋼所
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Priority claimed from JP2017032273A external-priority patent/JP6794598B2/en
Priority claimed from JP2017197905A external-priority patent/JP6756078B2/en
Application filed by 株式会社神戸製鋼所 filed Critical 株式会社神戸製鋼所
Priority to US16/487,182 priority Critical patent/US11377714B2/en
Priority to EP18756604.7A priority patent/EP3586998B1/en
Publication of WO2018155658A1 publication Critical patent/WO2018155658A1/en

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    • 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
    • B22D11/04Continuous casting of metals, i.e. casting in indefinite lengths into open-ended moulds
    • B22D11/041Continuous casting of metals, i.e. casting in indefinite lengths into open-ended moulds for vertical casting
    • 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
    • B22D11/04Continuous casting of metals, i.e. casting in indefinite lengths into open-ended moulds
    • B22D11/059Mould materials or platings
    • 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
    • B22D11/108Feeding additives, powders, or the like
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D21/00Casting non-ferrous metals or metallic compounds so far as their metallurgical properties are of importance for the casting procedure; Selection of compositions therefor
    • B22D21/02Casting exceedingly oxidisable non-ferrous metals, e.g. in inert atmosphere
    • B22D21/04Casting aluminium or magnesium
    • 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
    • C22B9/04Refining by applying a vacuum
    • 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
    • C22B9/16Remelting metals
    • C22B9/20Arc remelting
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C14/00Alloys based on titanium
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C21/00Alloys based on aluminium

Definitions

  • the present invention provides a high-grade or low-oxygen Ti—Al alloy by adding an aluminum raw material and a flux to a low-grade titanium raw material such as titanium oxide (TiO 2 ) such as lower sponge titanium, scrap titanium, and rutile ore.
  • a low-grade titanium raw material such as titanium oxide (TiO 2 ) such as lower sponge titanium, scrap titanium, and rutile ore.
  • TiO 2 titanium oxide
  • the present invention relates to a method for producing a Ti—Al-based alloy.
  • VAR vacuum arc melting method
  • EB electron beam melting method
  • PAM plasma arc melting method
  • VAR vacuum arc melting method
  • VIM vacuum induction melting
  • CCIM water-cooled copper induction melting
  • high-quality raw materials with low oxygen content are used as titanium raw materials for melting Ti-Al alloys.
  • the price of high-grade titanium raw materials has risen. Therefore, there is a growing need to obtain a high-quality, that is, low-oxygen Ti—Al alloy even when using titanium raw materials such as low-grade ores and scraps with a high oxygen content.
  • Patent Document 1 when PAM or CCIM is used and dissolved and held by adding 40% by mass or more of Al to high oxygen content Ti in an atmosphere of 1.33 Pa or higher, oxygen in the Ti—Al based alloy is reduced. combines with Al Al 2 in the form of O 3 is discharged from in Ti-Al deoxidation progresses, and that the addition of flux CaO-CaF 2 based, activity of Al 2 O 3 is reduced Further, it is described that deoxidation further proceeds.
  • low-grade Ti in other words, high-grade Ti such as pure Ti is added to a Ti—Al-based alloy in which Al 2 O 3 or CaO—CaF 2 -based flux is partially left. It is also described that if Al is diluted, a Ti—Al based alloy having an Al content of less than 40% by mass and a low oxygen content can be produced.
  • the Ti-Al-based alloy has parts which as Al 2 O 3 and flux remaining, melting it in Ti-Al alloy of the Al content by adding pure Ti is less than 40 wt%
  • Al 2 O 3 and the like inside the flux are decomposed / re-dissolved, and the oxygen concentration and the like are increased. Therefore, with the production method of Patent Document 1, it is not easy to obtain a high-quality, that is, low-oxygen Ti—Al-based alloy with an Al content of less than 40% by mass.
  • the portion where Al 2 O 3 or the like remains is mechanically removed by cutting or the like and then dissolved by adding high-grade, that is, low-oxygen Ti, the low oxygen content of less than 40% by mass is obtained.
  • a Ti-Al alloy can be obtained, but a part of the metal Ti is also removed at the time of mechanical removal of Al 2 O 3 etc., so the yield of the Ti-Al alloy becomes very poor. This leads to an increase in cost.
  • Patent Documents 2 to 5 disclose techniques useful for separating / removing substances such as residual flux from Ti—Al based alloys.
  • Patent Document 2 when an active metal is continuously melted and solidified to cast an ingot by using a plasma arc as a heat source, a flux such as CaF 2 is heated and melted in advance and then the active metal is charged. Alternatively, it is put together with the active metal, and a flux is contained between the water-cooled copper crucible and the ingot to slowly cool and solidify the surface of the ingot, thereby melting the ingot with a smooth ingot surface. Is described.
  • Patent Document 3 discloses a flux such as CaF 2 when casting an ingot by continuously melting and solidifying titanium or a titanium alloy using a plasma-cooled water-cooled copper mold with a plasma arc as a heat source. By changing the addition amount according to the mold position, the effect of slowly cooling the interface between the water-cooled copper mold and the molten metal is developed, and as a result, casting a slab with a good casting surface condition Is described as being possible.
  • a cold-crucible levitation and dissolution apparatus (CCIM) is used to add rare earth metal (cerium or misch metal in the examples) to Ti and calcium fluoride (CaF 2 ) as a flux to Ti.
  • rare earth metal cerium or misch metal in the examples
  • CaF 2 calcium fluoride
  • a molten flux can be present between the molten metal and the water-cooled copper crucible, and by transferring solid or liquid non-metallic inclusions to the molten flux layer, the molten metal improves the cleanliness of the molten metal.
  • a purification method is described.
  • non-metallic inclusions when a metal containing non-metallic inclusions is melted using a high-frequency induction furnace such as CCIM, the non-metallic inclusions have a lower electrical conductivity than metals such as Ti. It is known that there is a tendency to gather outside (water-cooled copper crucible side). Therefore, if the method of Patent Document 4 is used, non-metallic inclusions such as Al 2 O 3 may be localized and physically removed from the Ti—Al-based alloy.
  • Patent Document 5 discloses an induction melting furnace provided with a water-cooled copper crucible in which a crucible main body is movable in the vertical direction relative to the contents accommodated in the furnace. This Patent Document 5 also describes that a long active metal ingot is produced by repeatedly dissolving a metal raw material and lowering a water-cooled copper crucible. This Patent Document 5 is also similar to Patent Document 4 in that a high-frequency induction furnace equipped with a water-cooled copper crucible is used. In principle, non-metallic inclusions tend to gather outside the metal ingot. Therefore, there is a possibility that non-metallic inclusions such as Al 2 O 3 can be physically removed from the Ti—Al based alloy as in Patent Document 4.
  • Patent Document 2 Al 2 O 3 and CaO—CaF 2 flux remaining in the Ti—Al based alloy, which is a problem in Patent Document 1, can be mechanically removed on the ingot surface. Although it can be discharged, the method of Patent Document 2 uses a flux such as CaF 2 for the purpose of smoothing the cast surface of the ingot, and cannot be expected to have an effect of deoxidation or inclusion removal.
  • a plasma arc is used as a heat source, and high oxygen Ti, Al, and CaO—CaF 2 fluxes are continuously added to a bottomless water-cooled copper mold and melted downward. If withdrawn, the flux remains solid, or to coagulate migrate between the molten metal dissolves immediately after a water-cooled copper mold and Ti-Al alloy, it is dissolved Al 2 O 3 in the flux Al 2 O Solidification is performed before the activity of 3 is sufficiently reduced, and it is considered that the deoxidation promoting effect and inclusion removal effect due to the decrease in the activity of Al 2 O 3 can hardly be expected.
  • Patent Document 4 simply dissolves a metal containing non-metallic inclusions using a cold-crucible levitation and dissolution apparatus (CCIM), and a non-metal such as Al 2 O 3. It is not a suitable condition for inclusions to migrate into the flux. Therefore, even if the transition of non-metallic inclusions to the flux occurs, the possibility that a sufficient amount of transition is performed is low, and there is a high possibility that the non-metallic inclusions remain in the molten metal (described later). In the comparative example 1 and the comparative example 2 of the example according to the second embodiment, the result that the nonmetallic inclusion remains is actually obtained).
  • CCIM cold-crucible levitation and dissolution apparatus
  • Patent Document 4 does not describe how to treat the flux remaining in the molten metal. . In other words, if the flux remaining in the molten metal cannot be removed from the molten metal by any method, a Ti—Al alloy with high cleanliness cannot be obtained even using the technique of Patent Document 4.
  • the method for producing an active metal ingot of Patent Document 5 can in principle collect non-metallic inclusions on the outside of the metal ingot, as in Patent Document 4, but non-metallic inclusions. Since it is not a condition suitable for transferring to the flux, there is a possibility that non-metallic inclusions such as Al 2 O 3 in the Ti—Al alloy cannot be actually removed (second embodiment described later). In Comparative Example 3 of the example, a result in which nonmetallic inclusions remain is actually obtained).
  • Patent Document 5 does not assume dissolution with addition of flux, and there is no description regarding deoxidation and inclusion removal. Therefore, it is unclear whether deoxidation or inclusion removal can be performed without any problems when the pulling-down is performed at the pulling-down rate specified in Patent Document 5.
  • the speed at the time of lowering is set to 30 mm or less per minute.
  • the flux layer breaks and the molten metal leaks out, so that deoxidation is ensured. It may not be done.
  • the present invention has been made in view of the above-mentioned problems. From a low-grade titanium material containing a high concentration of oxygen, a high-grade and low-oxygen Ti—Al alloy is efficiently produced with a high yield. It is an object of the present invention to provide a method for producing a Ti—Al based alloy that can be produced.
  • the manufacturing method of the Ti—Al based alloy of the present invention takes the following technical means. That is, the method for producing a Ti—Al based alloy of the present invention is based on a Ti—Al based alloy comprising a titanium material and an aluminum material and containing a total of 0.1 mass% or more of oxygen and 40 mass% or more of Al. A dissolved raw material obtained by adding a CaO—CaF 2 -based flux in which 35 to 95% by mass of calcium fluoride is mixed with calcium oxide to 3 to 20% by mass with respect to the Ti—Al-based alloy is added to 1.33 Pa.
  • a primary ingot manufacturing process in which the primary ingot is melted by melting and holding by a melting method using a water-cooled copper container in the above atmosphere, and the primary ingot is bottomless in an atmosphere of 1.33 Pa or more
  • a secondary ingot manufacturing step for continuously drawing a secondary ingot while being melted by a melting method using a water-cooled copper mold, and a flux for mechanically removing the surface adhering flux layer of the secondary ingot A layer removal step, Characterized by (hereinafter sometimes referred to this embodiment the first embodiment).
  • Ti—Al based alloy production method of the present invention is a Ti—Al based alloy comprising a titanium material and an aluminum material and containing a total of 0.1 mass% or more of oxygen and 40 mass% or more of Al.
  • a melting raw material in which CaO—CaF 2 flux containing 35 to 95% by mass of calcium fluoride and calcium oxide is mixed to 3 to 20% by mass with respect to the Ti—Al alloy is cast.
  • the first divided body is charged into a bottomless water-cooled copper mold, dissolved in an inert gas atmosphere of 1.33 Pa or higher, and the bottom of the water-cooled copper mold is pulled down at a rate of 15 mm or less per minute.
  • the melted raw material second divided body divided in the raw material dividing step is charged into the water-cooled copper mold and dissolved in an inert gas atmosphere of 1.33 Pa or more, and the water-cooled copper mold is 15 mm or less per minute.
  • a titanium material is added to the ingot after the flux layer removing step and dissolved by a melting method using a water-cooled copper container in an atmosphere of about 1.33 Pa (hereinafter referred to as titanium material adding / dissolving step). Therefore, it is preferable to obtain a Ti—Al alloy having an Al content of less than 40% by mass.
  • the melting method using the water-cooled copper container in the primary ingot manufacturing process is any one of an arc melting method, a plasma arc melting method, and an induction melting method.
  • the melting method using a bottomless water-cooled copper mold in the secondary ingot manufacturing step and the divided body base ingot manufacturing step may use plasma arc or induction heating as a heat source.
  • a high quality and low oxygen Ti—Al based alloy is efficiently produced from a low quality titanium material containing a high concentration of oxygen with a high yield. can do.
  • FIG. 3 is a diagram showing a Ti—Al-based alloy manufacturing method according to the first embodiment of the present invention divided into processes.
  • FIG. 5 is a diagram schematically showing a Ti—Al-based alloy manufacturing method according to a second embodiment of the present invention, divided into processes. It is a figure which shows the SEM image of the cross section of the secondary ingot obtained by the manufacturing method of this invention.
  • the Ti—Al-based alloy manufacturing method of the present embodiment has three steps of a primary ingot manufacturing process to a flux layer removing process, preferably a primary ingot manufacturing process to a flux.
  • a titanium material addition / dissolution step is further performed to increase the oxygen content to less than 0.1% by mass from the Ti-Al alloy material W containing 0.1% by mass or more of oxygen.
  • a high-quality Ti—Al-based alloy Z is manufactured.
  • the alloy material W used in the manufacturing method of the Ti—Al-based alloy Z is a mixture of a titanium material and an aluminum material, and during the melting, deoxidation is caused by the action of aluminum contained in the aluminum material. It is to do. Further, in the manufacturing method of the present invention, CaO—CaF 2 flux ⁇ is further added to the alloy material W to promote deoxidation. According to such a production method of the present invention, from an alloy material W containing 0.1% by mass or more of oxygen, finally, a high-grade Ti—Al based alloy Z having less than 0.1% by mass of oxygen. Can be obtained.
  • an aluminum material is added to the titanium material, the Ti-Al alloy alloy material W is deoxidized, and the deoxidized alloy material is melted as the primary ingot X. It is a process.
  • the alloy material W described above contains oxygen (O) in a total amount of 0.1% by mass or more and aluminum (Al) in an amount of 40% by mass or more. That is, the titanium material constituting the alloy material W includes titanium oxide (TiO 2 ) such as low-quality and high-oxygen sponge titanium, scrap raw material, and rutile ore. The reason why low-grade titanium materials are used for the alloy material W is that these titanium materials are inexpensive and easy to procure.
  • the alloy material W described above has a total oxygen content of 0.1% by mass or more.
  • the total content of oxygen in the alloy material W is less than 0.1% by mass, the content of oxygen is small and deoxidation itself is not necessary.
  • the upper limit of the oxygen content is not specified, but the upper limit of the total content of oxygen actually contained in the alloy material W is considered to be about 25% by mass.
  • the reason why the Ti—Al-based alloy containing 40% by mass or more of Al is used for the alloy material W to be deoxidized in the primary ingot manufacturing process is as follows.
  • the maximum amount of oxygen dissolved in a Ti—Al alloy is Ti—Al
  • the solid solution oxygen concentration tends to decrease.
  • the Al content in the alloy Z increases, the solid solution oxygen concentration tends to decrease.
  • the Al content is increased to 40% by mass or more, the alloy material W in the alloy material when deoxidation is performed.
  • the present inventors have completed the present invention, thinking that oxygen can be lowered.
  • the flux ⁇ described above has a function of reducing the activity of Al 2 O 3 in the alloy material W by being added to the alloy material W and promoting the deoxidation reaction. That is, the flux ⁇ dissolves Al 2 O 3 which is a deoxidation product of the Ti—Al alloy, thereby reducing the activity of Al 2 O 3 which is a generated species in the deoxidation reaction, and deoxidizing the flux ⁇ . Has the effect of promoting the reaction.
  • the content of CaF 2 in the flux ⁇ is set to 35% by mass or more so that the melting point of the flux ⁇ is 1800K or less.
  • Ti-Al alloy Z obtained as a product so as not to be contaminated with fluorine in CaF 2 the content of CaF 2 in the flux ⁇ is set to 95 wt% or less.
  • the amount of the CaO—CaF 2 -based flux ⁇ added to the alloy material W is 3% by mass to 20% by mass with respect to the Ti—Al-based alloy Z. If the amount added to the Ti—Al-based alloy Z is less than 3% by mass, the Al 2 O 3 activity is not significantly reduced, and the deoxidation promoting effect is hardly obtained. If the amount added to the Ti—Al-based alloy Z is more than 20% by mass, the risk that the added flux ⁇ remains in the manufactured Ti—Al-based alloy Z increases.
  • the atmosphere in which the deoxidation is performed does not necessarily have to be a high vacuum. That is, it is possible to sufficiently perform deoxidation even when dissolution is performed using a water-cooled copper container prepared in an atmosphere that is not a high vacuum atmosphere, specifically, an atmosphere of 1.33 Pa or higher. is there.
  • the loss of volatilization of Al or Ti as in the case of deoxidation in a high vacuum atmosphere is eliminated.
  • a low-oxygen Ti—Al alloy (high-grade Ti—) having a target composition is obtained while reducing the volatilization loss of Al and Ti (without substantially reducing the Ti content).
  • Al-based alloy can be easily manufactured.
  • the inside of the water-cooled copper container 1 is in an atmosphere of 1.33 Pa or more, more preferably 1.33 Pa to 5.33 ⁇ 10 5 Pa. It is carried out by adjusting to an atmosphere of ( ⁇ 5 atm).
  • agitation using a stirrer may be considered, but after the ingot is solidified in the container 1 (mold) as in the present embodiment, the top and bottom are inverted to pull the ingot.
  • the operation of repeating and re-dissolving may be performed a plurality of times.
  • the stirring operation by turning the ingot (primary ingot F) upside down can be performed more preferably 2 to 5 times. In this way, if the ingot is cast several times while reversing the top and bottom, the added flux ⁇ can be reliably mixed with the alloy material to promote the deoxidation reaction, and the deoxidation is sufficiently performed.
  • the primary ingot X can be melted.
  • the alloy material in the portion near the container wall of the water-cooled copper container 1 is not melted due to the effect of heat removal. Therefore, there is an undissolved (unreacted) portion in one dissolution, and a reaction for promoting deoxidation (deoxidation products Al 2 O 3 and CaO—CaF 2 flux ⁇ ) in the undissolved portion. Reaction) may not proceed sufficiently. Therefore, in the manufacturing method of the present embodiment, the operation of inverting the top of the primary ingot X and melting again is repeated a plurality of times.
  • the flux ⁇ is ingot (secondary ingot Y) so that Al 2 O 3 generated in the primary ingot manufacturing process is easily removed mechanically in the flux layer removing process described later.
  • the ingot in which the fluxes are biased in this way is the secondary ingot Y.
  • the primary ingot X is continuously drawn out downward while being melted by a melting method using a bottomless water-cooled copper mold 2 in an atmosphere of 1.33 Pa or higher.
  • the ingot Y is obtained.
  • a method of melting using a plasma arc or induction heating as a heat source can be used, but a method of melting using a plasma arc as a heat source is preferably used.
  • a flux ⁇ in which Al 2 O 3 is dissolved On the surface of the molten metal supplied to the inside of the water-cooled copper mold 2, a flux ⁇ in which Al 2 O 3 is dissolved floats. If a plasma arc is used as a heat source, the flux ⁇ is generated by the arc sprayed on the surface.
  • Coagulation is performed in a state of being concentrated in the vicinity of the inner peripheral surface and being concentrated in the vicinity.
  • the flux ⁇ is biased to exist on the outer peripheral side of the secondary ingot Y that is drawn downward.
  • the surface adhering flux layer ⁇ formed on the outer peripheral surface of the secondary ingot Y is shot blasted or ground in the flux layer removing process. If the mechanical means 3 is used, the Al 2 O 3 together with the flux can be removed.
  • the flux layer removing step is a step of scraping off the surface-adhered flux layer ⁇ formed on the outer peripheral surface of the secondary ingot in the secondary ingot manufacturing step by mechanical means 3 such as shot blasting or grinding. By performing this flux layer removal step, the oxygen concentration of the secondary ingot Y can be lowered as a whole.
  • the oxygen content contained in the Ti—Al based alloy Z is totaled by setting the Al content in the alloy material W to 40 mass% or more. Therefore, the Ti-Al alloy Z to be manufactured necessarily has an Al content of 40% by mass or more. However, when the obtained Ti—Al-based alloy Z is used, there is a desire to reduce the Al content to less than 40% by mass.
  • the titanium material addition / dissolution process described below may be performed.
  • the titanium material addition / dissolution step is performed by adding the titanium material V to the secondary ingot Y and dissolving it by a melting method using a water-cooled copper mold 4 (water-cooled copper container) in an atmosphere of 1.33 Pa or more.
  • a Ti—Al based alloy Z2 having an Al content of less than 40% by mass is obtained.
  • the melting method shown in the figure uses a water-cooled copper container, but the melting method used in this titanium material addition / dissolution step is a melting method other than water-cooled copper induction melting (CCIM), such as a vacuum arc melting method. (VAR) or vacuum induction melting (VIM) may be used.
  • CCIM water-cooled copper induction melting
  • VAR vacuum arc melting method
  • VIM vacuum induction melting
  • the titanium material V added to the secondary ingot Y in the titanium material addition / melting step is a Ti-Al alloy Z2 having an Al content of less than 40% by mass after the titanium material addition / melting step.
  • the Al content is preferably less than 40% by mass.
  • a titanium material V having an Al content of less than 40% by mass such as pure Ti that does not contain aluminum as an impurity, is added, the Al content contained in the secondary ingot Y is reduced by dilution.
  • a Ti—Al-based alloy Z2 whose amount is less than 40% by mass can be obtained.
  • the titanium material V added in the titanium material addition / dissolution process varies depending on the required quality of the Ti—Al alloy Z2 to be manufactured, components other than aluminum in the titanium material V (Sn, V, Mn The concentration of such metals other than aluminum cannot be specified.
  • the titanium material addition / dissolution process is performed in addition to the primary ingot manufacturing process to the flux layer removal process described above, a Ti-Al alloy Z2 that meets the required quality can be obtained for the composition other than oxygen and aluminum.
  • the convenience of the production method of the present invention can be further enhanced.
  • the manufacturing method of the Ti—Al-based alloy 101 has three steps of a raw material dividing step to a flux layer removing step, preferably after the raw material dividing step to the flux layer removing step. Further, a titanium material addition / dissolution step is performed to obtain a high-grade Ti—Al in which the oxygen content is less than 0.1% by mass from the alloy material of the Ti—Al alloy 101 containing 0.1% by mass or more of oxygen.
  • the system alloy 101 is manufactured.
  • the alloy material used in the manufacturing method of the Ti—Al alloy 101 is a mixture of a titanium material and an aluminum material.
  • the melting raw material 102 mixed with aluminum is melted in the divided body base ingot manufacturing process in this way, the aluminum reacts with oxygen in the alloy material to perform deoxidation.
  • CaO—CaF 2 -based flux 103 is added to the alloy material for the purpose of promoting deoxidation in the raw material dividing step.
  • a flux 103 is added in the raw material dividing step, deoxidation in the divided base ingot manufacturing step is further promoted, and oxygen is finally reduced from an alloy material containing 0.1% by mass or more of oxygen. It is possible to obtain a high-grade Ti—Al-based alloy 101 of less than 1 mass%.
  • the melted raw material 102 to which the flux 103 is added is divided into a plurality of pieces to form divided bodies.
  • the lowering operation is performed on all the divided bodies following the melting operation of the divided body of the melting raw material 102, and non-metallic inclusions such as Al 2 O 3 are added to the flux 103.
  • the flux 103 to which the non-metallic inclusions are transferred can be unevenly distributed (localized) on the outer peripheral surface of the ingot.
  • the non-metallic inclusions and the flux 103 that are unevenly distributed in this way are mechanically removed in the flux layer removing step, or preferably the component adjustment is further performed in the titanium material adding / dissolving step, so that the Ti—Al of the present invention A system alloy 101 is manufactured.
  • the flux 103 is added to the alloy material of the Ti—Al-based alloy 101 to produce the molten raw material 102, the produced molten raw material 102 is divided into n pieces, and the first divided body 141 ⁇ The n-th divided body is formed.
  • This dividing operation of the melting raw material 102 is a feature of the manufacturing method of the present invention.
  • the alloy material of the Ti—Al based alloy 101 used for the melting raw material 102 is made of a titanium material and an aluminum material, and the total amount of oxygen is 0.1 mass% or more and Al is 40 mass%. Contains above.
  • the flux 103 blended in the alloy material is a CaO—CaF 2 -based flux 103 in which 35 to 95 mass% of calcium fluoride is blended with calcium oxide. The alloy material described above is blended with the flux 103 in an amount of 3 to 20% by mass to form the melting raw material 102 of this embodiment.
  • the titanium material constituting the above-mentioned alloy material is one containing a sponge titanium containing much oxygen in low-grade scrap material, titanium oxide such as rutile ore (TiO 2).
  • titanium oxide such as rutile ore (TiO 2).
  • the above-described alloy material has a total oxygen content of 0.1% by mass or more.
  • the total content of oxygen in the alloy material is less than 0.1% by mass, the content of oxygen is small and deoxidation itself is not necessary.
  • the upper limit of the oxygen content is not specified, but the upper limit of the total content of oxygen actually contained in the alloy material is considered to be about 25% by mass.
  • the reason why the Ti—Al alloy 101 containing 40% by mass or more of Al is used as the alloy material used for the melting raw material 102 in the raw material dividing step is based on the following reason.
  • the maximum amount of oxygen dissolved in the Ti—Al alloy 101 is Ti—
  • the Al content in the Al-based alloy 101 is increased, the dissolved oxygen concentration tends to decrease.
  • the melting raw material 102 containing the Ti—Al alloy 101 produced using a low-grade titanium material can be removed in the divided base ingot manufacturing process if the Al content is increased to 40% by mass or more.
  • the inventors have thought that oxygen in the alloy material can be lowered when acid is performed, and the present inventors have completed the present invention.
  • the flux 103 described above has the function of reducing the activity of Al 2 O 3 in the melting raw material 102 by being added to the melting raw material 102 and promoting the deoxidation reaction in the divided body ingot manufacturing process described later. is doing. That is, the flux 103 dissolves Al 2 O 3 which is a deoxidation product of the Ti—Al-based alloy 101, thereby reducing the activity of Al 2 O 3 which is a generated species in the deoxidation reaction. Has the effect of promoting acid reaction.
  • the dissolution of Al 2 O 3 in the flux 103 occurs only when the flux 3 is melted. Therefore, if the melting point of the flux 103 becomes too high, the flux 103 does not melt and Al 2 O 3 does not dissolve. That is, in the case of the CaO—CaF 2 based flux 103, it is necessary to decrease the melting point of the flux 103 itself by increasing the content of CaF 2 having a low melting point. Specifically, in the deoxidation of the present embodiment, the content of CaF 2 in the flux 103 is set to 35% by mass or more so that the melting point of the flux 103 is 1800K or less.
  • the content of CaF 2 in the flux 103 It is 95 mass% or less.
  • the addition amount of the CaO—CaF 2 -based flux 103 to the melting raw material 102 is 3% by mass to 20% by mass with respect to the Ti—Al-based alloy 101 as a product. If the addition amount relative to Ti-Al alloy 101 is less than 3 wt%, Al 2 O 3 does not occur reduction in the activity of so much, no deoxidation promoting effect is hardly obtained. If the amount added to the Ti—Al based alloy 101 is more than 20 mass%, the risk that the added flux 103 remains in the manufactured Ti—Al based alloy 101 increases.
  • the melting raw material 102 is first prepared by blending the flux 103 with the alloy material.
  • the melting raw material 102 in which the flux 103 is mixed with the alloy material of the Ti—Al alloy 101 in the above-described raw material dividing step is charged into the water-cooled copper crucible 105 and melted (the solidification method in the crucible is performed).
  • Non-metallic inclusions such as Al 2 O 3 cannot be sufficiently removed. In order to sufficiently remove the non-metallic inclusions, it is necessary to perform an operation of a divided body base ingot manufacturing process as described below.
  • the prepared dissolving raw material 102 is divided into n pieces to form the first divided body 141 to the n-th divided body.
  • N which is the number of divisions of the melting raw material 102, is an integer of 2 or more, and the melting raw material 102 is divided into a plurality of divided bodies in the raw material dividing step.
  • the weight of each divided body is the maximum with respect to the final target ingot weight at the end of casting.
  • the melted raw material 2 after adjustment is divided into n so as to be 4/5 or less.
  • the divided body is preferably equally divided (in this case, 33.3 ton), but the present invention is not limited to equally dividing the divided body.
  • none of the first divided body 141 to the n-th divided body obtained in the raw material dividing step will exceed 4/5 of the final target ingot weight at the end of casting. Heat removal from the bottom 107 of the copper crucible 105 can be suppressed, and the deoxidation reaction can be sufficiently promoted.
  • the raw material weight of each divided body after dividing the molten raw material 102 is divided so as to be 4/5 or less of the whole at the maximum with respect to the final ingot weight. That is, at least two melting operations and two lowering operations (partition body charging / dissolution ⁇ lowering ⁇ partition body charging / dissolution ⁇ lowering) are required. This is because the portion close to the water-cooled copper crucible 105 at the bottom 107 is strongly cooled by only one melting operation, and solidification proceeds before the charged flux 103 is sufficiently melted. Therefore, Al 2 O 3 It is difficult for non-metallic inclusions such as these to react with the flux 103. In this regard, since the heat removal from the bottom 107 is suppressed in the second and subsequent melting operations, the flux 103 and the non-metallic inclusions sufficiently react with each other during the second and subsequent melting, thereby promoting deoxidation. To do.
  • the separation efficiency between the metal and the flux 103 can be lowered even if the second and subsequent melting operations are performed.
  • the weight of the first divided body 141 exceeds 4/5 of the final target weight, the non-metallic inclusions and the flux can be dissolved even if the amount less than the remaining 1 / V is dissolved in the second and subsequent dissolutions. Reaction with 103 is less likely to occur. For this reason, it is desirable to divide the divided body into a maximum of 4/5 or less, preferably 2/3 or less of the whole, more preferably I / 2 or less of the whole.
  • the present invention has been described by giving an example in which the dissolved raw material 102 is divided into three parts and deoxidized in the raw material dividing step, but the number of divisions is five. Even if it is 11 divisions, there is no problem.
  • the first divided body 141 of the melted raw material 102 divided in the raw material dividing process is charged into a water-cooled copper crucible 105 (bottomed water-cooled copper crucible 105) to be inactive at 1.33 Pa or more.
  • An operation of melting under a gas atmosphere and pulling down the water-cooled copper crucible 105 at a speed of 15 mm or less per minute is performed, and then the second divided body 142 of the melted raw material 102 divided in the raw material dividing step is bottomed out.
  • the ingot is formed by repeating.
  • the divided body base ingot manufacturing process includes a melting operation in which a divided body of the melting raw material 102 is charged into a water-cooled copper crucible 105 and melted in an inert gas atmosphere of 1.33 Pa or more, and this melting operation is followed. Then, the operation of continuously lowering the water-cooled copper crucible 105 downward at a speed of 15 mm / min or less is performed as “basic operation”. And this basic operation is performed once in order about each of the 1st division body 141, the 2nd division body 142, ..., and the nth division body.
  • the reason why the inert gas atmosphere is 1.33 Pa or more is that no volatilization loss of Al or Ti occurs as in the case of melting in a high vacuum atmosphere. More preferably, it is dissolved in an inert gas atmosphere of 1.33 Pa to 5.33 ⁇ 10 5 Pa ( ⁇ 5 atm).
  • the divided body base ingot manufacturing process proceeds by processing the melting raw material 102 in the order of the lowering operation of the divided body 142, the melting operation of the third divided body 143, and the lowering operation of the third divided body 143.
  • each divided body of the melting raw material 102 is charged into a water-cooled copper crucible 105 (water-cooled copper mold) prepared in an inert gas atmosphere of 1.33 Pa or more, and water-cooled.
  • the ingot is cast by melting each divided body of the melting raw material 102 in the copper crucible 105 using a plasma arc or induction heating as a heat source.
  • the melting is preferably performed using induction heating as a heat source.
  • the non-metallic inclusions gather outside the molten metal due to the difference in electrical conductivity between the non-metallic inclusions and the metal. It is known. That is, the flux 103 in which the Al 2 O 3 in the molten metal supplied into the water-cooled copper crucible 105 is concentrated in the vicinity of the inner peripheral surface of the mold due to induction heating, and solidification is performed in the state of being concentrated. As a result, the surface-attached flux layer 108 in which the flux 103 is biased and present on the outer peripheral side of the ingot drawn downward is formed in the ingot melted in the divided body base ingot manufacturing process.
  • the surface-attached flux layer 108 can be scraped off by mechanical means such as shot blasting or grinding in the flux layer removing process. This is because non-metallic inclusions such as Al 2 O 3 can be removed.
  • the pulling-down operation performed following the melting operation of the divided body of the melting raw material 102 in the divided body base ingot manufacturing process is the surface adhesion formed on the surface of the ingot by melting the flux 103 by the above-described melting operation.
  • the flux layer 108 is unevenly distributed between the mold and the ingot.
  • the above-described water-cooled copper crucible 105 has a structure in which a cylindrical crucible body 106 that opens both upward and downward and a bottom portion 107 that is disposed on the bottom side of the crucible body 106 are combined. It has become.
  • the bottom 107 of the water-cooled copper crucible 105 is attached to the crucible main body 106 so as to be movable in the vertical direction.
  • the cast placed on the upper side of the bottom 107 is performed.
  • the lump can also be lowered.
  • the surface adhering flux layer 108 is unevenly distributed between the outer periphery side of the ingot, in other words, between the mold and the ingot.
  • the ingot lowering speed in other words, the lowering speed of the bottom 107 of the water-cooled copper crucible 105 is set to 15 mm / min or less, preferably 10 mm / min or less. If the ingot lowering speed exceeds 15 mm / min, the surface-adhered flux layer 108 formed on the outer peripheral surface of the ingot in the above-described divided body base ingot manufacturing process is broken, and the surface-adhered flux layer 108 is used as a mold. This is because it is difficult to make it unevenly distributed between the steel and the ingot.
  • the one that performs the above-described dissolving operation and pulling-down operation once at a time is the “basic operation” for a certain divided body. This “basic operation” is performed once for each of the first divided body 141, the second divided body 142,.
  • the melting raw material 102 is divided into three, and the first divided body 141, the second divided body 142, and the third divided body 143 exist, Melting operation of first divided body 141 ⁇ Lowering operation of first divided body 141 ⁇ Melting operation of second divided body 142 ⁇ Lowering operation of second divided body 142 ⁇ Melting operation of third divided body 143 ⁇ Third divided body 143 In the end, a cylindrical ingot that is long in the vertical direction is melted (cast) in the divided base ingot manufacturing process.
  • the outer peripheral surface of the ingot was cast with the above-mentioned divided body based ingot manufacturing process and surface deposition flux layer 108 solidified in a state where the flux 103 is biased is formed on the surface adhering flux layer 108 Al 2
  • Non-metallic inclusions such as O 3 are also contained at a high concentration. Therefore, if the surface adhering flux layer 108 formed on the outer peripheral surface of the ingot is scraped by mechanical means such as shot blasting or grinding in the flux layer removing step, the non-metallic inclusions such as Al 2 O 3 together with the flux 103 The oxygen concentration contained in the ingot can be lowered as a whole.
  • the Ti—Al-based alloy 101 obtained from the raw material dividing step through the flux layer removing step has the surface-attached flux layer 108 formed on the outer peripheral surface of the ingot in the divided body base ingot manufacturing step. Since it is removed by mechanical means such as shot blasting and grinding in the process, the oxygen content contained in the Ti-Al alloy 101 is greatly reduced, and the oxygen originally contained in the alloy material is reliably deoxidized. Has been reduced. That is, according to the manufacturing method of the Ti—Al based alloy 101 of the present embodiment, the high quality, that is, the low oxygen Ti—Al based alloy 101 is efficiently produced from the low quality titanium containing a high concentration of oxygen with a high yield. Can be manufactured.
  • the oxygen content contained in the Ti—Al based alloy 101 is totaled by setting the Al content in the alloy material to 40% by mass or more. Since the Ti content is less than 0.1% by mass, the produced Ti—Al-based alloy 101 inevitably has an Al content of 40% by mass or more. However, when the obtained Ti—Al-based alloy 101 is used, there is a desire to reduce the Al content to less than 40% by mass.
  • the titanium material addition / dissolution step described below may be performed.
  • the titanium content is added to the ingot and melted by a melting method using a water-cooled copper mold (water-cooled copper container 109) in an atmosphere of 1.33 Pa or higher, so that the Al content is increased.
  • a Ti—Al alloy 101 of less than 40% by mass is obtained.
  • the melting method illustrated in FIG. 2 uses a water-cooled copper container, but the melting method used in this titanium material addition / dissolution step is a melting method other than water-cooled copper induction melting (CCIM), such as a vacuum arc.
  • CCIM water-cooled copper induction melting
  • VAR vacuum induction melting
  • VIM vacuum induction melting
  • the titanium material added to the ingot in the titanium material addition / melting step is to obtain a Ti—Al alloy 101 having an Al content of less than 40 mass% after the titanium material addition / melting step.
  • the titanium content is preferably less than 40% by mass.
  • a titanium material with an Al content of less than 40% by mass such as pure Ti that does not contain aluminum as an impurity, is added, the Al content contained in the ingot is reduced by dilution, so the Al content is 40% by mass.
  • a Ti—Al alloy 101 that is less than 1% can be obtained.
  • the titanium material added in the titanium material addition / dissolution step varies depending on the required quality of the Ti—Al alloy 101 to be manufactured. Therefore, components other than aluminum (such as Sn, V, Mn, etc.) in the titanium material. The concentration of the metal other than aluminum cannot be specified and can be arbitrarily changed.
  • the ratio (H / D) between the final ingot height H (final target ingot height) and the ingot diameter D is not particularly limited. From the viewpoint, it is preferably 1 or more.
  • the Ti—Al alloy 101 that matches the required quality can be obtained for the composition other than oxygen and aluminum. The convenience of the manufacturing method can be further enhanced.
  • Example 1 the alloy material W containing 40% by mass of Al and 0.8% by mass of O was processed from the primary ingot manufacturing process to the titanium material adding / dissolving process. Is an alloy material W containing 50% by mass of Al and 0.8% by mass of O as compared with Example 1 and subjected to the treatment from the primary ingot manufacturing process to the titanium material addition / dissolution process. is there.
  • the comparative example 1 and the comparative example 2 do not perform a secondary ingot manufacturing process and a flux layer removal process after a primary ingot manufacturing process among four processes which comprise the manufacturing method of this invention, The titanium material is directly added and dissolved.
  • Comparative Example 1 the inclusions that were confirmed to be generated after the primary ingot manufacturing step were left without being removed, and Comparative Example 2 was obtained by removing inclusions as much as possible.
  • the primary ingot manufacturing process scrap Ti, titanium oxide (TiO 2), pure Al, the CaO-CaF 2 as a raw material by a plasma arc melting method, intermediate material (Ti-40, 50 wt% Al-0 .8 mass% O), the secondary ingot manufacturing step, the ingot manufactured in the primary ingot manufacturing step is remelted by the plasma arc drawing melting method, and the flux layer removing step is The step of mechanically removing the flux layer (containing Al 2 O 3 ) adhering to the ingot surface after the secondary ingot manufacturing step and the titanium material addition / dissolution step are the primary ingot manufacturing step (Comparative Example 1).
  • Comparative Example 2 Ti—Al ingot produced in the primary ingot production process + secondary ingot production process + flux layer removal process (Examples 1 and 2), pure Ti (O: 0.
  • a plasma arc melting method A step of melting the -30 wt% Al ingot.
  • TiO 2 titanium oxide
  • Comparative Example 1 a Ti-Al alloy is melted by directly adding and melting a titanium material after the primary ingot manufacturing process. That is, in Comparative Example 1, the primary ingot is not subjected to the secondary ingot manufacturing process in which the primary ingot is continuously drawn while being melted by a melting method using a bottomless water-cooled copper mold. internal and remains from entrapment as Al 2 O 3 or flux, not performed the flux layer removing step.
  • the oxygen concentration was measured by the inert gas melting method for both the portion where the inclusion was confirmed and the portion where the inclusion was not confirmed, the inclusion was confirmed as shown in Table 1. At the position where the oxygen concentration was 1.82% by mass, and at the position where no inclusion was confirmed, the oxygen concentration was 0.24% by mass. From this, it can be seen that the inclusions confirmed by SEM observation are inclusions such as flux and Al 2 O 3 .
  • a titanium material (pure Ti) containing 0.05% by mass of oxygen is added to the ingot after the primary ingot manufacturing process, so that the Al content becomes 30% by mass.
  • a Ti—Al alloy having an oxygen concentration of 0.79% by mass was obtained.
  • Comparative Example 1 pure Ti (0.05% by mass of O is contained in the titanium material addition / dissolution step with respect to the alloy material in which oxide inclusions remain after the flux layer removal step.
  • oxides such as Al 2 O 3 are decomposed and redissolved in the molten metal, and the oxygen concentration is increased.
  • Comparative Example 2 In contrast to Comparative Example 1 described above, Comparative Example 2 is obtained by mechanically removing the Ti—Al alloy region containing oxide inclusions that was confirmed after the primary ingot manufacturing process. That is, since oxygen is removed from the Ti—Al based alloy by removing inclusions, the oxygen content of Comparative Example 2 is comparative when the Al content is 30% by mass. The oxygen content is 0.21% by mass, which is smaller than in Example 1. However, when removing the oxide inclusions, not only the inclusions contained in the ingot but also the metal (Ti—Al alloy) is lost. Therefore, the “intermediate material use amount” indicating how much of the alloy material has become a Ti—Al alloy, in other words, “yield” is 50%, which is about half of Comparative Example 1. Yes.
  • Example 1 In contrast to Comparative Example 1 and Comparative Example 2 described above, Example 1 is prepared by mixing the same raw materials as Comparative Example 1 and Comparative Example 2 to adjust the alloy material W, and further adding CaO—CaF 2 flux to the alloy material W.
  • the processing conditions for melting the primary ingot X are also the same as in the comparative example, using a 100 kW plasma arc furnace and melting at a pressure of 1.20 ⁇ 10 5 Pa.
  • Example 1 differs from the comparative example in that the upside down and remelting, which was not the comparative example, is repeated three times.
  • the secondary ingot Y is melted while being drawn downward by a melting method using a plasma arc as a heat source. did.
  • CaO—CaF 2 -based flux ⁇ containing Al 2 O 3 was discharged and adhered to the surface of the secondary ingot Y.
  • the secondary ingot Y was subjected to shot blasting (mechanical means 3) in the flux layer removing step to remove the flux layer ⁇ on the surface of the secondary ingot Y.
  • pure Ti oxygen concentration 0.05 mass% is further added as a titanium material addition / dissolution step, and Ti-30 mass% Al alloy Z2 is melted to reduce the oxygen concentration. analyzed.
  • Example 2 In addition, the knowledge as obtained in Example 1 described above can also be obtained for the alloy material W of Example 2 in which the Al content is 50 mass% higher than in Example 1.
  • CaO—CaF 2 flux 103 is added to an alloy material prepared by mixing an aluminum material with a titanium material to deoxidize O (oxygen) contained in the alloy material. It is a thing.
  • Example 1 the alloy material containing 40% by mass of Al and 0.8% by mass of O was processed from the raw material dividing step to the titanium material adding / dissolving step.
  • Example 2 the alloy material containing 60% by mass of Al and 0.8% by mass of O was processed from the raw material dividing step to the titanium material adding / dissolving step.
  • Example 3 the alloy material containing 45% by mass of Al and 0.8% by mass of O was subjected to the raw material dividing step to the titanium material adding / dissolving step.
  • Example 4 the alloy material containing 52% by mass of Al and 0.8% by mass of O is subjected to the raw material dividing step to the titanium material adding / dissolving step.
  • the number of divisions of the melting raw material 2 in Examples 1 to 4 is “11”, and one melting operation and one time are performed for each of the first divided body 141 to the eleventh divided body (not shown).
  • the "basic operation” consists of a pull-down operation.
  • Comparative Example 1 uses an alloy material having the same composition as Example 1, but the melting raw material 102 is not divided during the raw material dividing step, and only the melting operation is performed in the divided body base ingot manufacturing step. The ingot is obtained by performing. In Comparative Example 1, the obtained ingot was further subjected to a titanium material addition / dissolution step to obtain a Ti-30Al ingot.
  • Comparative Example 2 was obtained by performing the same process as Comparative Example 1 to obtain an ingot, and the titanium material addition / dissolution step was performed using only a specific part of the obtained ingot.
  • Comparative Example 3 As in Example 1, the alloy material containing 40% by mass of Al and 0.8% by mass of O was processed from the raw material dividing step to the titanium material adding / dissolving step. . Comparative Example 3 is different from Example 1 in that the flux 103 is not blended with the melting raw material 102.
  • scrap Ti, titanium oxide (TiO 2 ), and pure Al are used as alloy materials.
  • a CaO—CaF 2 flux 103 is used as a Ti—Al system. 10% of the weight of the alloy 101 was blended, and in Comparative Example 3, the melting raw material 102 was produced without blending the flux 103.
  • the melted raw material 102 prepared in the raw material splitting process is charged into a water-cooled copper crucible 105 (inner diameter 80 mm) having no bottom, and argon as an inert gas is introduced. It melt
  • the melting raw material 102 is divided into 11 parts in the raw material dividing process, and the first divided body 141 to the 11th divided body (not shown) are preliminarily formed.
  • the dissolution operation and the pull-down operation were performed once for each of the divided bodies, and the dissolution raw material 102 was dissolved to proceed with deoxidation. Moreover, about the comparative example 1 and the comparative example 2, as above-mentioned, the division body base ingot manufacturing process itself is not implemented.
  • the surface-attached flux layer adhered to the surface of the ingot by performing shot blasting as a mechanical means on the surface of the ingot with respect to the ingot cast in the divided body base ingot manufacturing step 108 was removed.
  • the oxygen concentration contained in the ingot was analyzed by an inert gas melting method.
  • pure Ti having an oxygen concentration of 0.05 mass% is added to the ingot from which the surface adhering flux layer 108 has been removed in the flux layer removing step using a plasma arc melting furnace.
  • Ti-30 mass% Al alloy was melted.
  • the oxygen concentration was analyzed by an inert gas melting method in the same manner as the ingot after the flux layer removal step.
  • Table 2 shows the analysis results of Examples and Comparative Examples.
  • Comparative Example 1 In Comparative Example 1, as described above, the melting raw material 102 is not divided in the raw material dividing step, and only the melting operation without the pulling-down operation is performed on the molten raw material 102 that is not divided in the divided body base ingot manufacturing process. Thus, an ingot is obtained.
  • oxygen was 0.50% by mass in a site where no inclusion was present, and in a site where an inclusion was present 1.16% by mass of oxygen was detected.
  • the ingot described above is melted using a plasma arc melting furnace in the titanium material addition / melting step, and pure Ti (oxygen concentration 0.05 mass%) is added to the ingot to obtain a Ti-30 mass% Al alloy.
  • the oxygen concentration of the resulting Ti-30 mass% Al alloy ingot was analyzed by an inert gas melting method. As a result of the analysis, 0.79% by mass of oxygen was detected. Furthermore, when the inside of an ingot of Ti-30 mass% Al alloy was observed with an SEM, the presence of oxide inclusions such as Al 2 O 3 was not confirmed.
  • the oxygen concentration increased from 0.50% by mass to 0.79% by mass in the portion where no inclusion was present. This is because, when pure Ti110 is added to the ingot in the titanium material addition / melting step and the components are adjusted, the oxide inclusions remaining in the ingot are decomposed by pure Ti and become Ti-Al. It is considered that the oxygen concentration has increased due to re-dissolution.
  • Comparative Example 2 In Comparative Example 2, the ingot is melted by the same melting raw material 102 and melting method as in Comparative Example 1. Therefore, the oxygen concentration of the site where the melted ingot inclusions are not present is 0.51% by mass, and the site where the inclusions are present is 1.12% by mass. Of the ingot of Comparative Example 2, a portion where no inclusions were present was selected and melted using a plasma arc melting furnace, and pure Ti110 (oxygen concentration 0.05 mass%) was added to obtain Ti-30. An ingot of mass% Al alloy was melted. As a result of analyzing the oxygen concentration of the molten ingot, the oxygen concentration was 0.42% by mass, which was lower than that of Comparative Example 1.
  • Comparative Example 3 In the same manner as in Comparative Example 1 and Comparative Example 2, the melting raw material 102 was prepared so as to be Ti-40 mass% Al-0.8 mass% O, and an ingot (2800 g) was melted. Unlike the comparative example 1 and the comparative example 2, the melting raw material 102 of the comparative example 3 was prepared by dissolving the raw material 102 without adding the flux 103 to the alloy material in the raw material dividing step. It is divided into 11 pieces. Specifically, the first divided body 141 initially charged in the water-cooled copper crucible 105 has a raw material weight of 800 g (excluding the flux 103), and thereafter the second divided body 142 to the eleventh divided portion to be additionally charged. The body 151 has a raw material weight of 200 g.
  • the raw material (800 g) of the first divided body 141 was charged on a starting block made of pure Ti (the bottom 107 of the water-cooled copper crucible 105), and the pressure was 6.6 ⁇ 10 4 Pa in an Ar atmosphere. Dissolved in the crucible. After the 1st division body 141 melt
  • Example 1 In Example 1, as in Comparative Example 3, the melting raw material 102 was divided into 11 pieces and the ingot was melted. The difference between Example 1 and Comparative Example 3 is that 10% by mass of the flux 103 is blended with respect to the weight of the Ti—Al alloy 101.
  • the flux layer on the surface of the ingot could be easily removed by shot blasting.
  • the oxygen concentration in the portion where Al 2 O 3 does not exist is 0.30% by mass. Even at a site where oxide inclusions such as Al 2 O 3 were slightly observed, the oxygen concentration was as very low as 0.40% by mass. Therefore, in Example 1 in which the flux 103 was blended in the raw material dividing step and the melting raw material 102 was divided, and the melting operation and the lowering operation were repeated for each divided body in the divided body base ingot manufacturing step. It can be seen that the oxygen concentration inside can be greatly reduced.
  • Example 2 In Example 2, as in Comparative Example 3, the melting raw material 102 was divided into 11 pieces and the ingot was melted. The difference between Example 2 and Comparative Example 3 is that 10% by mass of the flux 103 is blended with respect to the weight of the Ti—Al-based alloy 101.
  • the flux layer on the surface of the ingot could be easily removed by shot blasting.
  • the oxygen concentration of the portion where Al 2 O 3 does not exist is 0.045% by mass. Even at a site where oxide inclusions such as Al 2 O 3 were slightly observed, the oxygen concentration was as very low as 0.065% by mass. Therefore, in Example 2 in which the flux 103 was blended in the raw material dividing step and the melting raw material 102 was divided, and the melting operation and the lowering operation were repeated for each divided body in the divided body base ingot manufacturing step. It can be seen that the oxygen concentration inside can be greatly reduced.
  • the oxide material inclusions in the ingot were hardly present in the titanium material addition / dissolution step of Example 2, so that even when remelted, oxygen It was found that the concentration did not increase and there was no yield reduction. Therefore, by using the production method of the present invention, it is possible to efficiently produce a low-oxygen Ti—Al-based alloy 101 having an Al content of less than 60 mass% with a high yield using low-grade raw materials. It is judged that.
  • Example 3 In Example 3, as in Comparative Example 3, the melting raw material 102 was divided into 11 pieces and the ingot was melted. Example 3 is different from Comparative Example 3 in that the flux 103 is blended by 10 mass% with respect to the weight of the Ti—Al alloy 101.
  • the flux layer on the surface of the ingot (surface-adhered flux layer 108) could be easily removed by shot blasting.
  • the oxygen concentration in the portion where Al 2 O 3 does not exist is 0.16% by mass. Even at a site where oxide inclusions such as Al 2 O 3 were slightly observed, the oxygen concentration was as low as 0.20% by mass. Therefore, in Example 3 in which the flux 103 was blended in the raw material dividing step and the melting raw material 102 was divided, and the melting operation and the lowering operation were repeatedly performed for each divided body in the divided body base ingot manufacturing step. It can be seen that the oxygen concentration inside can be greatly reduced.
  • Example 4 In Example 4, as in Comparative Example 3, the melting raw material 102 was divided into 11 pieces and the ingot was melted. The difference between Example 4 and Comparative Example 3 is that 10% by mass of the flux 103 is blended with respect to the weight of the Ti—Al-based alloy 101.
  • the flux layer on the surface of the ingot could be easily removed by shot blasting.
  • the oxygen concentration in the portion where Al 2 O 3 does not exist is 0.042% by mass. Even at a site where oxide inclusions such as Al 2 O 3 were slightly confirmed, the oxygen concentration was as very low as 0.060% by mass.
  • Example 4 where the flux 103 was blended in the raw material dividing step and the melting raw material 102 was divided, and the melting operation and the lowering operation were repeated for each divided body in the divided body base ingot manufacturing step, the ingot It can be seen that the oxygen concentration inside can be greatly reduced.
  • embodiment disclosed this time is an illustration and restrictive at no points.
  • matters that are not explicitly disclosed, for example, operating conditions and operating conditions, various parameters, dimensions, weights, volumes, and the like of a component deviate from a range that a person skilled in the art normally performs. Instead, values that can be easily assumed by those skilled in the art are employed.
  • Japanese Patent Application No. 2017-032273 Japanese patent application filed on April 13, 2017
  • Japanese Patent Application No. 2017-079928 Japanese patent application filed on October 11, 2017. This is based on a Japanese patent application (Japanese Patent Application No. 2017-197905), the contents of which are incorporated herein by reference.
  • a high-grade and low-oxygen Ti—Al alloy can be efficiently produced from a low-grade titanium material containing oxygen at a high concentration with a high yield, and it is a material for aircraft and automobiles. It is particularly useful in the production of

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Abstract

The present invention is provided with: a primary ingot production step in which 3-20 mass% of a CaO-CaF2 flux obtained by mixing 35-95 mass% of calcium fluoride with calcium oxide, is added to a Ti-Al alloy material including a total of at least 0.1 mass% of oxygen, and at least 40 mass% of Al, and the resultant substance is melted by way of a melting method using a water-cooled copper container in an atmosphere having a pressure of 1.33 Pa or higher, and held, to produce a primary ingot; a secondary ingot production step in which the primary ingot is continuously drawn downwards while being melted by way of a melting method using a bottomless water-cooled copper casting mould in an atmosphere having a pressure of 1.33 Pa or higher, to obtain a secondary ingot Y; and a flux layer removal step in which a flux layer deposited on the surface of the secondary ingot Y is mechanically removed.

Description

Ti-Al系合金の製造方法Method for producing Ti-Al alloy
 本発明は、低級スポンジチタン、スクラップチタン、ルチル鉱石などの酸化チタン(TiO)のような低品位のチタン原料にアルミ原料およびフラックスを加えることで、高品位すなわち低酸素なTi-Al系合金を製造するTi-Al系合金の製造方法に関するものである。 The present invention provides a high-grade or low-oxygen Ti—Al alloy by adding an aluminum raw material and a flux to a low-grade titanium raw material such as titanium oxide (TiO 2 ) such as lower sponge titanium, scrap titanium, and rutile ore. The present invention relates to a method for producing a Ti—Al-based alloy.
 近年、航空機及び自動車向け素材としてTi-Al系合金の需要が増加している。従来、Ti-Al系合金は酸素に対して非常に活性であるため、酸素の影響を低減可能な真空アーク溶解法(VAR)、電子ビーム溶解法(EB)、プラズマアーク溶解法(PAM)、真空誘導溶解(VIM)、水冷銅式誘導溶解(CCIM)などの手法を用いて溶解・鋳造が行われている。 In recent years, demand for Ti-Al alloys as materials for aircraft and automobiles has increased. Conventionally, Ti—Al alloys are very active against oxygen, so that the vacuum arc melting method (VAR), electron beam melting method (EB), plasma arc melting method (PAM), which can reduce the influence of oxygen, Melting and casting are performed using techniques such as vacuum induction melting (VIM) and water-cooled copper induction melting (CCIM).
 上述した溶解・鋳造の手法の中でも、真空雰囲気下で行われるVAR、EB、VIMなどの手法に基づく溶解プロセスでは、合金元素のAlだけでなく、Tiも揮発によって失われるため、工業プロセスにおいては溶解後の組成を制御することが困難であり、製造コストの増加を招くことが危惧される。 Among the melting and casting methods described above, in the melting process based on a method such as VAR, EB, and VIM performed in a vacuum atmosphere, not only the alloy element Al but also Ti is lost due to volatilization. It is difficult to control the composition after dissolution, and there is a concern that the manufacturing cost will increase.
 また、Ti-Al系合金を溶製する際のチタン原料として、一般的には、酸素含有量が少ない高品位な原料を用いているが、昨今は高品位なチタン原料の価格が高騰しており、酸素含有量の多い低品位な鉱石やスクラップなどのチタン原料を用いても高品位すなわち低酸素なTi-Al系合金を得たいというニーズが高まっている。 In general, high-quality raw materials with low oxygen content are used as titanium raw materials for melting Ti-Al alloys. Recently, however, the price of high-grade titanium raw materials has soared. Therefore, there is a growing need to obtain a high-quality, that is, low-oxygen Ti—Al alloy even when using titanium raw materials such as low-grade ores and scraps with a high oxygen content.
 そこで、揮発によるTiのロスが起こりやすいVAR、EB、VIMなどの溶解法を用いるのではなく、PAMやCCIMなどの溶解法を用い、低品位な原料(酸素含有量の0.1質量%以上と多いチタン原料)から、AlやTiの揮発ロスを抑えつつ脱酸を行って、Ti-Al系合金を製造する技術が提案されている。 Therefore, instead of using melting methods such as VAR, EB, and VIM, where Ti loss is likely to occur due to volatilization, low-quality raw materials (over 0.1% by mass of oxygen content) are used by using melting methods such as PAM and CCIM. A technology for producing a Ti—Al-based alloy by deoxidation from a large amount of titanium raw material) while suppressing volatilization loss of Al and Ti has been proposed.
 例えば、特許文献1には、PAMやCCIMを用い、1.33Pa以上の雰囲気下で高酸素含有TiにAlを40質量%以上添加して溶解・保持すると、Ti-Al系合金中の酸素がAlと結合してAlの形でTi-Al中から排出されて脱酸が進行し、且つ、CaO-CaF系のフラックスを添加すると、Alの活量が低下して、更に脱酸が進行すると記載されている。 For example, in Patent Document 1, when PAM or CCIM is used and dissolved and held by adding 40% by mass or more of Al to high oxygen content Ti in an atmosphere of 1.33 Pa or higher, oxygen in the Ti—Al based alloy is reduced. combines with Al Al 2 in the form of O 3 is discharged from in Ti-Al deoxidation progresses, and that the addition of flux CaO-CaF 2 based, activity of Al 2 O 3 is reduced Further, it is described that deoxidation further proceeds.
 上述した特許文献1の製造方法では、確かにTi-Al系合金中の酸素はAlの形で排出されて脱酸される。しかし、単純にPAMやCCIMを用いて溶解・保持しただけでは、脱酸の副生成物であるAlや脱酸促進のために添加するCaO-CaF系のフラックスがTi-Al合金の特定部位に残留してしまう可能性があり、Ti-Al系合金中に脱酸が進行している部位と脱酸が進行していない部位(Alが残留している部位)とが混在することとなってしまう。 In the manufacturing method of Patent Document 1 described above, oxygen in the Ti—Al alloy is certainly discharged in the form of Al 2 O 3 and deoxidized. However, by simply dissolving and holding using PAM or CCIM, Al 2 O 3 which is a by-product of deoxidation and CaO—CaF 2 flux added to promote deoxidation are Ti—Al alloys. In the Ti-Al alloy, the site where deoxidation has progressed and the site where deoxidation has not progressed (site where Al 2 O 3 remains) Will be mixed.
 また、特許文献1には、AlやCaO-CaF系のフラックスが部分的に残留したTi-Al系合金に、低酸素Ti、言い換えれば純Tiなどの高品位のTiを添加してAlを希釈すれば、Al含有量が40質量%未満で且つ酸素含有量の少ないTi-Al系合金を製造することができるとも記載されている。 In Patent Document 1, low-grade Ti, in other words, high-grade Ti such as pure Ti is added to a Ti—Al-based alloy in which Al 2 O 3 or CaO—CaF 2 -based flux is partially left. It is also described that if Al is diluted, a Ti—Al based alloy having an Al content of less than 40% by mass and a low oxygen content can be produced.
 しかし、Ti-Al系合金中にはAlやフラックスが残留している部位があり、これに純Tiを添加してAl含有量が40質量%未満のTi-Al系合金を溶製しようとすると、フラックスの内部のAl等が分解/再溶解して、酸素濃度等がかえって上昇してしまう。それゆえ、特許文献1の製造方法では、Al含有量が40質量%未満となるような高品位すなわち低酸素のTi-Al系合金を得ることは容易ではない。 However, the Ti-Al-based alloy has parts which as Al 2 O 3 and flux remaining, melting it in Ti-Al alloy of the Al content by adding pure Ti is less than 40 wt% When trying to do so, Al 2 O 3 and the like inside the flux are decomposed / re-dissolved, and the oxygen concentration and the like are increased. Therefore, with the production method of Patent Document 1, it is not easy to obtain a high-quality, that is, low-oxygen Ti—Al-based alloy with an Al content of less than 40% by mass.
 なお、Al等が残留した部位を切断等により機械的に除去した上で、高品位すなわち低酸素のTiを添加して溶解すれば、Al含有量が40質量%未満の低酸素のTi-Al系合金が得られるが、Al等の機械的除去の際には金属Tiの一部も一緒に除かれてしまうため、Ti-Al系合金の歩留が非常に悪くなり、コストアップに繋がってしまう。 In addition, if the portion where Al 2 O 3 or the like remains is mechanically removed by cutting or the like and then dissolved by adding high-grade, that is, low-oxygen Ti, the low oxygen content of less than 40% by mass is obtained. A Ti-Al alloy can be obtained, but a part of the metal Ti is also removed at the time of mechanical removal of Al 2 O 3 etc., so the yield of the Ti-Al alloy becomes very poor. This leads to an increase in cost.
 つまり、特許文献1の脱酸方法では、Alを40質量%以上含有するTi-Al系合金に対しては、AlやCaO-CaF系のフラックスをいかにTi-Al系合金中に残さないか、言い換えればAlやCaO-CaF系フラックスが残留した場合には、残留したフラックスなどの物質をいかにTi-Al系合金中から分離/除去するかが重要となる。 That is, in the deoxidation method of Patent Document 1, for a Ti—Al alloy containing 40 mass% or more of Al, how to use Al 2 O 3 or CaO—CaF 2 flux in the Ti—Al alloy. If the Al 2 O 3 or CaO—CaF 2 flux remains, it is important how to separate / remove the remaining flux and other substances from the Ti—Al alloy.
 この点、特許文献2~5には、残留したフラックスなどの物質をTi-Al系合金中から分離/除去する際に有用な技術が開示されている。 In this regard, Patent Documents 2 to 5 disclose techniques useful for separating / removing substances such as residual flux from Ti—Al based alloys.
 例えば、特許文献2には、プラズマアークを熱源とし、活性金属を連続的に溶解・凝固して鋳塊を鋳造する際に、CaFなどのフラックスを予め加熱溶解させた後に活性金属を投入するか、あるいは、活性金属と伴に投入し、水冷銅るつぼと鋳塊との間にフラックスを内在させて鋳塊の表面を緩徐冷凝固させて、平滑な鋳塊肌を持つ鋳塊を溶製させることが記載されている。 For example, in Patent Document 2, when an active metal is continuously melted and solidified to cast an ingot by using a plasma arc as a heat source, a flux such as CaF 2 is heated and melted in advance and then the active metal is charged. Alternatively, it is put together with the active metal, and a flux is contained between the water-cooled copper crucible and the ingot to slowly cool and solidify the surface of the ingot, thereby melting the ingot with a smooth ingot surface. Is described.
 また、特許文献3には、プラズマアークを熱源とし、断面直方形状の水冷銅鋳型を用い、チタンまたはチタン合金を連続的に溶解・凝固して鋳塊を鋳造する際に、CaF2等のフラックスを鋳型位置に応じて添加量を変えて投入することで、水冷銅鋳型と溶湯との界面を緩冷却する効果を発現させて、結果的に、鋳肌の状態が良好なスラブを鋳造することが可能になると記載されている。 Patent Document 3 discloses a flux such as CaF 2 when casting an ingot by continuously melting and solidifying titanium or a titanium alloy using a plasma-cooled water-cooled copper mold with a plasma arc as a heat source. By changing the addition amount according to the mold position, the effect of slowly cooling the interface between the water-cooled copper mold and the molten metal is developed, and as a result, casting a slab with a good casting surface condition Is described as being possible.
 特許文献4には、コールドクルーシブル型浮揚溶解装置(CCIM)を用いて、Tiに脱酸剤として希土類金属(実施例ではセリウムやミッシュメタル)、フラックスとしてフッ化カルシウム(CaF)を添加して溶解すると、溶湯と水冷銅るつぼの間に溶融フラックスを存在させることができ、この溶融フラックス層に固体あるいは液体の非金属介在物を移行させることで、溶融金属の清浄度を向上させる溶融金属の精製方法が記載されている。 In Patent Document 4, a cold-crucible levitation and dissolution apparatus (CCIM) is used to add rare earth metal (cerium or misch metal in the examples) to Ti and calcium fluoride (CaF 2 ) as a flux to Ti. Once melted, a molten flux can be present between the molten metal and the water-cooled copper crucible, and by transferring solid or liquid non-metallic inclusions to the molten flux layer, the molten metal improves the cleanliness of the molten metal. A purification method is described.
 一般的に、CCIMなどの高周波誘導炉を用いて非金属介在物を含んだ金属を溶解する場合には、非金属介在物はTiなどの金属と比較して電気伝導度が低いため、溶融金属の外側(水冷銅るつぼ側)に集まる傾向があることが知られている。そのため、特許文献4の手法を用いればTi-Al系合金からAlなどの非金属介在物を局在化させて物理的に除去できる可能性がある。 Generally, when a metal containing non-metallic inclusions is melted using a high-frequency induction furnace such as CCIM, the non-metallic inclusions have a lower electrical conductivity than metals such as Ti. It is known that there is a tendency to gather outside (water-cooled copper crucible side). Therefore, if the method of Patent Document 4 is used, non-metallic inclusions such as Al 2 O 3 may be localized and physically removed from the Ti—Al-based alloy.
 さらに、特許文献5には、炉内に収容された収容物に対してるつぼ本体が上下方向に相対移動可能とされた水冷銅るつぼを備えた誘導溶解炉が開示されている。この特許文献5には、金属原料の溶解と水冷銅るつぼの引き下げとを繰り返し行って、長尺な活性金属鋳塊を製造することも記載されている。この特許文献5も、水冷銅るつぼを備えた高周波誘導炉を使用しているという点で特許文献4と同様であり、原理的には、金属鋳塊の外側に非金属介在物が集まる傾向があるため、特許文献4同様Ti-Al系合金からAlなどの非金属介在物を物理的に除去できる可能性がある。 Furthermore, Patent Document 5 discloses an induction melting furnace provided with a water-cooled copper crucible in which a crucible main body is movable in the vertical direction relative to the contents accommodated in the furnace. This Patent Document 5 also describes that a long active metal ingot is produced by repeatedly dissolving a metal raw material and lowering a water-cooled copper crucible. This Patent Document 5 is also similar to Patent Document 4 in that a high-frequency induction furnace equipped with a water-cooled copper crucible is used. In principle, non-metallic inclusions tend to gather outside the metal ingot. Therefore, there is a possibility that non-metallic inclusions such as Al 2 O 3 can be physically removed from the Ti—Al based alloy as in Patent Document 4.
国際公開第2016/035824号International Publication No. 2016/035824 日本国特開昭53-86603号公報Japanese Unexamined Patent Publication No. 53-86603 日本国特開2013-49084号公報Japanese Unexamined Patent Publication No. 2013-49084 日本国特開平11-246919号公報Japanese Laid-Open Patent Publication No. 11-246919 日本国特開2006-122920号公報Japanese Unexamined Patent Publication No. 2006-122920
 特許文献2の方法であれば、特許文献1で問題となるTi-Al系合金中に残留しているAlやCaO-CaF系フラックスを、機械的に除去可能な鋳塊表面に排出することも可能であるが、特許文献2の方法は、鋳塊の鋳肌を平滑にする目的でCaF等のフラックスを投入しており、脱酸や介在物除去の効果は期待できない。 With the method of Patent Document 2, Al 2 O 3 and CaO—CaF 2 flux remaining in the Ti—Al based alloy, which is a problem in Patent Document 1, can be mechanically removed on the ingot surface. Although it can be discharged, the method of Patent Document 2 uses a flux such as CaF 2 for the purpose of smoothing the cast surface of the ingot, and cannot be expected to have an effect of deoxidation or inclusion removal.
 また、特許文献3の連続鋳造方法のように、プラズマアークを熱源とし、無底の水冷銅鋳型に高酸素TiとAlとCaO-CaFフラックスをそれぞれ連続的に投入して溶解しつつ下方に引抜いた場合、フラックスは、固体のまま、あるいは溶解後ただちに水冷銅鋳型とTi-Al系合金の溶湯との間に移行して凝固するため、フラックスにAlが溶解されてAlの活量が十分に低下する前に凝固が行われてしまうことになり、Alの活量低下による脱酸促進効果および介在物の除去効果はほとんど期待できないと考えられる。 Further, as in the continuous casting method of Patent Document 3, a plasma arc is used as a heat source, and high oxygen Ti, Al, and CaO—CaF 2 fluxes are continuously added to a bottomless water-cooled copper mold and melted downward. If withdrawn, the flux remains solid, or to coagulate migrate between the molten metal dissolves immediately after a water-cooled copper mold and Ti-Al alloy, it is dissolved Al 2 O 3 in the flux Al 2 O Solidification is performed before the activity of 3 is sufficiently reduced, and it is considered that the deoxidation promoting effect and inclusion removal effect due to the decrease in the activity of Al 2 O 3 can hardly be expected.
 特許文献4の溶融金属の精製方法は、非金属介在物を含んだ金属をコールドクルーシブル型浮揚溶解装置(CCIM)を用いて単純に溶解するのみとなっており、Al等の非金属介在物がフラックス中に移行するに適した条件とはなっていない。そのため、フラックスへの非金属介在物の移行が起こったとしても、量的に十分な移行が行われる可能性は低く、非金属介在物が溶融金属中に残留してしまう可能性が高い(後述する第2実施形態にかかる実施例の比較例1、比較例2では非金属介在物が残留する結果が実際に得られている)。 The method for refining molten metal disclosed in Patent Document 4 simply dissolves a metal containing non-metallic inclusions using a cold-crucible levitation and dissolution apparatus (CCIM), and a non-metal such as Al 2 O 3. It is not a suitable condition for inclusions to migrate into the flux. Therefore, even if the transition of non-metallic inclusions to the flux occurs, the possibility that a sufficient amount of transition is performed is low, and there is a high possibility that the non-metallic inclusions remain in the molten metal (described later). In the comparative example 1 and the comparative example 2 of the example according to the second embodiment, the result that the nonmetallic inclusion remains is actually obtained).
 加えて、Al等の非金属介在物の移行が十分に行われたとしても、溶融金属中に残留しているフラックスをどのように処理するかについての記載が特許文献4には無い。つまり、溶融金属中に残留しているフラックスを何らかの方法で溶融金属から除去できなければ、特許文献4の技術を用いても清浄度の高いTi-Al系合金を得ることはできない。 In addition, even if the migration of nonmetallic inclusions such as Al 2 O 3 is sufficiently performed, Patent Document 4 does not describe how to treat the flux remaining in the molten metal. . In other words, if the flux remaining in the molten metal cannot be removed from the molten metal by any method, a Ti—Al alloy with high cleanliness cannot be obtained even using the technique of Patent Document 4.
 また、特許文献5の活性金属鋳塊の製造方法も、原理的には特許文献4と同様に、金属鋳塊の外側に非金属介在物を集めることができるものであるが、非金属介在物がフラックス中に移行するに適した条件とはなっていないため、実際にTi-Al系合金中のAlなどの非金属介在物を除去できない可能性がある(後述する第2実施形態にかかる実施例の比較例3では非金属介在物が残留する結果が実際に得られている)。 In addition, the method for producing an active metal ingot of Patent Document 5 can in principle collect non-metallic inclusions on the outside of the metal ingot, as in Patent Document 4, but non-metallic inclusions. Since it is not a condition suitable for transferring to the flux, there is a possibility that non-metallic inclusions such as Al 2 O 3 in the Ti—Al alloy cannot be actually removed (second embodiment described later). In Comparative Example 3 of the example, a result in which nonmetallic inclusions remain is actually obtained).
 さらに、特許文献5では、フラックスを添加した溶解を想定しておらず、脱酸や介在物除去に関しての記載も無い。従って、特許文献5に規定される引き下げ速度で引き下げを行った場合は、問題なく脱酸や介在物除去が行われるかどうかも不明である。例えば、特許文献5では、引き下げ時の速度を毎分30mm以下としているが、このような速い引き下げ速度の場合、フラックス層が破断して、溶湯が漏れ出るなどしてしまい、脱酸が確実に行われない可能性もある。 Furthermore, Patent Document 5 does not assume dissolution with addition of flux, and there is no description regarding deoxidation and inclusion removal. Therefore, it is unclear whether deoxidation or inclusion removal can be performed without any problems when the pulling-down is performed at the pulling-down rate specified in Patent Document 5. For example, in Patent Document 5, the speed at the time of lowering is set to 30 mm or less per minute. However, in such a fast lowering speed, the flux layer breaks and the molten metal leaks out, so that deoxidation is ensured. It may not be done.
 本発明は、上述の問題に鑑みてなされたものであり、酸素を高濃度で含むような低品位のチタン材料から、高品位且つ低酸素のTi-Al系合金を、歩留まり良く、効率的に製造することができるTi-Al系合金の製造方法を提供することを目的とする。 The present invention has been made in view of the above-mentioned problems. From a low-grade titanium material containing a high concentration of oxygen, a high-grade and low-oxygen Ti—Al alloy is efficiently produced with a high yield. It is an object of the present invention to provide a method for producing a Ti—Al based alloy that can be produced.
 上記課題を解決するため、本発明のTi-Al系合金の製造方法は以下の技術的手段を講じている。
 即ち、本発明のTi-Al系合金の製造方法は、チタン材料およびアルミニウム材料よりなる、酸素を合計で0.1質量%以上且つAlを40質量%以上含有するTi-Al系合金に対して、酸化カルシウムにフッ化カルシウムを35~95質量%配合したCaO-CaF系のフラックスを、Ti-Al系合金に対して3~20質量%となるように添加した溶解原料を、1.33Pa以上の雰囲気で水冷銅容器を用いた溶解法により溶解し保持することで1次鋳塊を溶製する1次鋳塊製造工程と、前記1次鋳塊を1.33Pa以上の雰囲気で無底の水冷銅鋳型を用いた溶解法により溶解しつつ連続的に下方に引抜き2次鋳塊を得る2次鋳塊製造工程と、前記2次鋳塊の表面付着フラックス層を機械的に除去するフラックス層除去工程と、を有することを特徴とする(以下、この実施形態を第1実施形態ということがある)。
In order to solve the above problems, the manufacturing method of the Ti—Al based alloy of the present invention takes the following technical means.
That is, the method for producing a Ti—Al based alloy of the present invention is based on a Ti—Al based alloy comprising a titanium material and an aluminum material and containing a total of 0.1 mass% or more of oxygen and 40 mass% or more of Al. A dissolved raw material obtained by adding a CaO—CaF 2 -based flux in which 35 to 95% by mass of calcium fluoride is mixed with calcium oxide to 3 to 20% by mass with respect to the Ti—Al-based alloy is added to 1.33 Pa. A primary ingot manufacturing process in which the primary ingot is melted by melting and holding by a melting method using a water-cooled copper container in the above atmosphere, and the primary ingot is bottomless in an atmosphere of 1.33 Pa or more A secondary ingot manufacturing step for continuously drawing a secondary ingot while being melted by a melting method using a water-cooled copper mold, and a flux for mechanically removing the surface adhering flux layer of the secondary ingot A layer removal step, Characterized by (hereinafter sometimes referred to this embodiment the first embodiment).
 また、本発明の別のTi-Al系合金の製造方法は、チタン材料およびアルミニウム材料よりなる、酸素を合計で0.1質量%以上且つAlを40質量%以上含有するTi-Al系合金に対して、酸化カルシウムにフッ化カルシウムを35~95質量%配合したCaO-CaF系のフラックスを、Ti-Al系合金に対して3~20質量%となるように配合した溶解原料を、鋳造終了時の最終目標鋳塊重量に対して分割後の溶解原料の重量が最大で全体の4/5以下となるようにn分割する原料分割工程と、前記原料分割工程で分割された溶解原料の第1分割体を、無底の水冷銅鋳型に装入して1.33Pa以上の不活性ガス雰囲気下で溶解させ且つ前記水冷銅鋳型の底部を毎分15mm以下の速度で下方に引き下げる操作を行い、その後、前記原料分割工程で分割された溶解原料の第2分割体を、前記水冷銅鋳型に装入して1.33Pa以上の不活性ガス雰囲気下で溶解させ且つ前記水冷銅鋳型を毎分15mm以下の速度で下方に引き下げる操作を行い、以降、第n分割体まで前記操作を繰り返すことで鋳塊を得る分割体ベース鋳塊製造工程と、前記分割体ベース鋳塊製造工程で形成させた鋳塊の表面に付着するフラックス層を機械的に除去するフラックス層除去工程と、を有することを特徴とする(以下、この実施形態を第2実施形態ということがある)。 Further, another Ti—Al based alloy production method of the present invention is a Ti—Al based alloy comprising a titanium material and an aluminum material and containing a total of 0.1 mass% or more of oxygen and 40 mass% or more of Al. On the other hand, a melting raw material in which CaO—CaF 2 flux containing 35 to 95% by mass of calcium fluoride and calcium oxide is mixed to 3 to 20% by mass with respect to the Ti—Al alloy is cast. The raw material dividing step of dividing n so that the weight of the molten raw material after the division becomes a maximum of 4/5 or less with respect to the final target ingot weight at the end, and the molten raw material divided in the raw material dividing step The first divided body is charged into a bottomless water-cooled copper mold, dissolved in an inert gas atmosphere of 1.33 Pa or higher, and the bottom of the water-cooled copper mold is pulled down at a rate of 15 mm or less per minute. Done, then The melted raw material second divided body divided in the raw material dividing step is charged into the water-cooled copper mold and dissolved in an inert gas atmosphere of 1.33 Pa or more, and the water-cooled copper mold is 15 mm or less per minute. The operation of pulling down at a speed is performed, and thereafter, the above-described operation is repeated up to the n-th divided body to obtain an ingot, and the ingot formed in the divided body-based ingot manufacturing process. And a flux layer removing step of mechanically removing the flux layer adhering to the surface (hereinafter, this embodiment may be referred to as a second embodiment).
 なお、好ましくは、前記フラックス層除去工程後の鋳塊にチタン材料を添加して1.33Pa位上の雰囲気で水冷銅容器を用いた溶解法によって溶解すること(以下、チタン材料添加・溶解工程ということがある)により、Al含有量が40質量%未満のTi-Al系合金を得るとよい。 Preferably, a titanium material is added to the ingot after the flux layer removing step and dissolved by a melting method using a water-cooled copper container in an atmosphere of about 1.33 Pa (hereinafter referred to as titanium material adding / dissolving step). Therefore, it is preferable to obtain a Ti—Al alloy having an Al content of less than 40% by mass.
 なお、好ましくは、前記1次鋳塊製造工程における水冷銅容器を用いた溶解法は、アーク溶解法、プラズマアーク溶解法、または誘導溶解法のいずれかであるとよい。
 なお、好ましくは、前記2次鋳塊製造工程および前記分割体ベース鋳塊製造工程における無底の水冷銅鋳型を用いた溶解法は、プラズマアークまたは誘導加熱を熱源とするとよい。
Preferably, the melting method using the water-cooled copper container in the primary ingot manufacturing process is any one of an arc melting method, a plasma arc melting method, and an induction melting method.
Preferably, the melting method using a bottomless water-cooled copper mold in the secondary ingot manufacturing step and the divided body base ingot manufacturing step may use plasma arc or induction heating as a heat source.
 本発明のTi-Al系合金の製造方法によれば、酸素を高濃度で含むような低品位のチタン材料から、高品位且つ低酸素のTi-Al系合金を、歩留まり良く、効率的に製造することができる。 According to the method for producing a Ti—Al based alloy of the present invention, a high quality and low oxygen Ti—Al based alloy is efficiently produced from a low quality titanium material containing a high concentration of oxygen with a high yield. can do.
本発明の第1実施形態にかかるTi-Al系合金の製造方法を工程ごとに分けて示した図である。FIG. 3 is a diagram showing a Ti—Al-based alloy manufacturing method according to the first embodiment of the present invention divided into processes. 本発明の第2実施形態にかかるTi-Al系合金の製造方法を工程ごとに分けて模式的に示した図である。FIG. 5 is a diagram schematically showing a Ti—Al-based alloy manufacturing method according to a second embodiment of the present invention, divided into processes. 本発明の製造方法で得られる2次鋳塊の断面のSEM像を示す図である。It is a figure which shows the SEM image of the cross section of the secondary ingot obtained by the manufacturing method of this invention.
 以下、本発明に係るTi-Al系合金の製造方法の実施形態を、図面に基づき詳しく説明する。 Hereinafter, embodiments of a method for producing a Ti—Al alloy according to the present invention will be described in detail with reference to the drawings.
 まず、第1実施形態について説明する。図1に示すように、本実施形態のTi-Al系合金の製造方法は、1次鋳塊製造工程~フラックス層除去工程の3つの工程を経て、好適には1次鋳塊製造工程~フラックス層除去工程の後にさらにチタン材料添加・溶解工程を行って、酸素を0.1質量%以上含むTi-Al系合金の合金材料Wから酸素の含有量が0.1質量%未満とされた高品位なTi-Al系合金Zを製造するものとなっている。 First, the first embodiment will be described. As shown in FIG. 1, the Ti—Al-based alloy manufacturing method of the present embodiment has three steps of a primary ingot manufacturing process to a flux layer removing process, preferably a primary ingot manufacturing process to a flux. After the layer removal step, a titanium material addition / dissolution step is further performed to increase the oxygen content to less than 0.1% by mass from the Ti-Al alloy material W containing 0.1% by mass or more of oxygen. A high-quality Ti—Al-based alloy Z is manufactured.
 具体的には、このTi-Al系合金Zの製造方法に用いられる合金材料Wはチタン材料にアルミニウム材料を混ぜ合わせたものであり、溶解中にアルミニウム材料に含まれるアルミの作用で脱酸を行うものとなっている。また、本発明の製造方法では合金材料WにさらにCaO-CaFのフラックスαを添加して、脱酸を促進させている。このような本発明の製造方法によれば、酸素が0.1質量%以上含まれた合金材料Wから、最終的には酸素が0.1質量%未満の高品位なTi-Al系合金Zを得ることができる。 Specifically, the alloy material W used in the manufacturing method of the Ti—Al-based alloy Z is a mixture of a titanium material and an aluminum material, and during the melting, deoxidation is caused by the action of aluminum contained in the aluminum material. It is to do. Further, in the manufacturing method of the present invention, CaO—CaF 2 flux α is further added to the alloy material W to promote deoxidation. According to such a production method of the present invention, from an alloy material W containing 0.1% by mass or more of oxygen, finally, a high-grade Ti—Al based alloy Z having less than 0.1% by mass of oxygen. Can be obtained.
 以降では、本発明の製造方法に設けられる1次鋳塊製造工程~チタン材料添加・溶解工程の各工程についてそれぞれ説明する。 Hereinafter, each step of the primary ingot manufacturing process to the titanium material addition / dissolution process provided in the manufacturing method of the present invention will be described.
 1次鋳塊製造工程は、チタン材料にアルミニウム材料を加えて、Ti-Al系合金の合金材料Wに対して脱酸を行い、脱酸された合金材料を1次鋳塊Xとして溶製する工程である。 In the primary ingot manufacturing process, an aluminum material is added to the titanium material, the Ti-Al alloy alloy material W is deoxidized, and the deoxidized alloy material is melted as the primary ingot X. It is a process.
 上述した合金材料Wは、酸素(O)を合計で0.1質量%以上、且つ、アルミ(Al)を40質量%以上含有している。つまり、合金材料Wを構成するチタン材料は、低品位で酸素を多く含むスポンジチタン、スクラップ原料、ルチル鉱石などの酸化チタン(TiO)などを含むものである。このように合金材料Wに低品位なチタン材料を用いる理由は、これらチタン材料が廉価であり調達し易いからである。 The alloy material W described above contains oxygen (O) in a total amount of 0.1% by mass or more and aluminum (Al) in an amount of 40% by mass or more. That is, the titanium material constituting the alloy material W includes titanium oxide (TiO 2 ) such as low-quality and high-oxygen sponge titanium, scrap raw material, and rutile ore. The reason why low-grade titanium materials are used for the alloy material W is that these titanium materials are inexpensive and easy to procure.
 また、上述した合金材料Wは、酸素の合計含有量を0.1質量%以上とされている。例えば、合金材料W中の酸素の合計含有量が0.1質量%未満の場合には、酸素の含有量は僅かであり脱酸自体が必要ないからである。なお、本発明では、酸素の含有量の上限は規定しないが、合金材料Wに実際に含有される酸素の合計含有量の上限は、25質量%程度であると考えられる。 In addition, the alloy material W described above has a total oxygen content of 0.1% by mass or more. For example, when the total content of oxygen in the alloy material W is less than 0.1% by mass, the content of oxygen is small and deoxidation itself is not necessary. In the present invention, the upper limit of the oxygen content is not specified, but the upper limit of the total content of oxygen actually contained in the alloy material W is considered to be about 25% by mass.
 また、1次鋳塊製造工程で脱酸される合金材料Wについて、Alを40質量%以上含有するTi-Al系合金を用いるのは、以下のような理由に基づいている。 The reason why the Ti—Al-based alloy containing 40% by mass or more of Al is used for the alloy material W to be deoxidized in the primary ingot manufacturing process is as follows.
  例えば、公知のTi-Al-Oの3元系状態図(国際公開2016/035824の図5などを参照)によれば、Ti-Al系合金中に固溶する最大酸素量は、Ti-Al系合金Z中のAl含有量を大きくするほど、固溶酸素濃度が低くなる傾向を有している。つまり、低品位なチタン材料を用いて作製したTi-Al系合金の合金材料Wであっても、Alの含有量を40質量%以上まで高めれば、脱酸を行った際に合金材料中の酸素を下げることができるのではないかと考え、本発明者らは本発明を完成させるに至ったのである。 For example, according to a known ternary phase diagram of Ti—Al—O (see FIG. 5 of International Publication No. 2016/035824), the maximum amount of oxygen dissolved in a Ti—Al alloy is Ti—Al As the Al content in the alloy Z increases, the solid solution oxygen concentration tends to decrease. In other words, even in the case of the Ti-Al alloy material W produced using a low-grade titanium material, if the Al content is increased to 40% by mass or more, the alloy material W in the alloy material when deoxidation is performed. The present inventors have completed the present invention, thinking that oxygen can be lowered.
 上述したフラックスαは、合金材料Wに添加されることで合金材料W中のAlの活量を低下させ、脱酸反応を促進させる機能を有している。つまり、このフラックスαは、Ti-Al系合金の脱酸生成物であるAlを溶解させることで、脱酸反応における生成種であるAlの活量を低下させ、脱酸反応を促進させる効果を備えている。 The flux α described above has a function of reducing the activity of Al 2 O 3 in the alloy material W by being added to the alloy material W and promoting the deoxidation reaction. That is, the flux α dissolves Al 2 O 3 which is a deoxidation product of the Ti—Al alloy, thereby reducing the activity of Al 2 O 3 which is a generated species in the deoxidation reaction, and deoxidizing the flux α. Has the effect of promoting the reaction.
 なお、このフラックスαへのAlの溶解は、フラックスαが溶融した状態で初めて生じるものである。そのため、フラックスαの融点が高くなりすぎると、フラックスαが溶融しなくなりAlの溶解が生じなくなる。つまり、CaO-CaFのフラックスαでは、CaFの含有量を増加させるなどして、フラックスαの融点を低下させる必要がある。そこで、本実施形態の脱酸では、フラックスαの融点が1800K以下となるように、フラックスα中のCaFの含有量を35質量%以上としている。また、製品として得られるTi-Al系合金ZがCaF中のふっ素で汚染されることがないように、フラックスα中のCaFの含有量を95質量%以下としている。 The dissolution of Al 2 O 3 in the flux α occurs only when the flux α is melted. Therefore, if the melting point of the flux α becomes too high, the flux α does not melt and Al 2 O 3 does not dissolve. That is, in the CaO—CaF 2 flux α, it is necessary to decrease the melting point of the flux α by increasing the CaF 2 content. Therefore, in the deoxidation of the present embodiment, the content of CaF 2 in the flux α is set to 35% by mass or more so that the melting point of the flux α is 1800K or less. Further, Ti-Al alloy Z obtained as a product so as not to be contaminated with fluorine in CaF 2, the content of CaF 2 in the flux α is set to 95 wt% or less.
 また、上述したCaO-CaF系のフラックスαの合金材料Wに対する添加量は、Ti-Al系合金Zに対して3質量%~20質量%となっている。Ti-Al系合金Zに対する添加量が3質量%より少なければ、Al活量の低下があまり生じず、脱酸促進効果がほとんど得られない。Ti-Al系合金Zに対する添加量がの20質量%より多くなれば、添加したフラックスαが製造されたTi-Al系合金Z中に残留してしまうリスクが高くなってしまう。 The amount of the CaO—CaF 2 -based flux α added to the alloy material W is 3% by mass to 20% by mass with respect to the Ti—Al-based alloy Z. If the amount added to the Ti—Al-based alloy Z is less than 3% by mass, the Al 2 O 3 activity is not significantly reduced, and the deoxidation promoting effect is hardly obtained. If the amount added to the Ti—Al-based alloy Z is more than 20% by mass, the risk that the added flux α remains in the manufactured Ti—Al-based alloy Z increases.
 また、1次鋳塊製造工程で行われる脱酸は、Alの含有量を高めることで低酸素化を実現するものであるため、脱酸を行う雰囲気は必ずしも高真空でなくとも良い。つまり、高真空雰囲気ではないような雰囲気、具体的には1.33Pa以上の雰囲気に容器内が調製された水冷銅容器を用いた溶解であっても、脱酸を十分に行うことが可能である。 Moreover, since the deoxidation performed in the primary ingot manufacturing process realizes a reduction in oxygen by increasing the Al content, the atmosphere in which the deoxidation is performed does not necessarily have to be a high vacuum. That is, it is possible to sufficiently perform deoxidation even when dissolution is performed using a water-cooled copper container prepared in an atmosphere that is not a high vacuum atmosphere, specifically, an atmosphere of 1.33 Pa or higher. is there.
 また、1.33Pa以上の雰囲気で脱酸を行えば、高真空雰囲気での脱酸のようにAlやTiの揮発ロスが生じることが無くなる。つまり、1次鋳塊製造工程では、AlやTiの揮発ロスを少なくしつつ(実質的にTi含有量を低下させることなく)、目標の組成の低酸素Ti-Al系合金(高品位Ti-Al系合金)を容易に製造することができる。
 具体的には、1次鋳塊製造工程の1次鋳塊Xの溶製は、水冷銅容器1の内部を1.33Pa以上の雰囲気、より好ましくは1.33Pa~5.33×10Pa(≒5気圧)の雰囲気に調製して行われる。
Further, if deoxidation is performed in an atmosphere of 1.33 Pa or higher, the loss of volatilization of Al or Ti as in the case of deoxidation in a high vacuum atmosphere is eliminated. In other words, in the primary ingot manufacturing process, a low-oxygen Ti—Al alloy (high-grade Ti—) having a target composition is obtained while reducing the volatilization loss of Al and Ti (without substantially reducing the Ti content). Al-based alloy) can be easily manufactured.
Specifically, in the melting of the primary ingot X in the primary ingot manufacturing process, the inside of the water-cooled copper container 1 is in an atmosphere of 1.33 Pa or more, more preferably 1.33 Pa to 5.33 × 10 5 Pa. It is carried out by adjusting to an atmosphere of (≈5 atm).
 なお、1次鋳塊製造工程において1次鋳塊Xを溶製するに際しては、フラックスαを添加後、容器1内で攪拌を十分に行って脱酸反応を促進させるのが好ましい。 In addition, when melting the primary ingot X in the primary ingot manufacturing process, it is preferable to promote the deoxidation reaction by sufficiently stirring in the container 1 after adding the flux α.
 例えば、このような攪拌としては、攪拌子を用いた攪拌なども考えられるが、本実施形態のように容器1(鋳型)内で鋳塊が凝固した後、天地を反転して鋳塊をひっくり返し、再溶解させるといった操作を複数回に亘って行っても良い。この鋳塊(1次鋳塊F)の天地返しによる攪拌操作は、より好ましくは2回~5回に亘って行うことができる。このように鋳塊を天地反転させつつ複数回に亘って鋳造すれば、添加したフラックスαを合金材料に確実に混ぜ合わせて脱酸反応を促進させることができ、脱酸が十分に行われた1次鋳塊Xを溶製することができる。 For example, as such agitation, agitation using a stirrer may be considered, but after the ingot is solidified in the container 1 (mold) as in the present embodiment, the top and bottom are inverted to pull the ingot. The operation of repeating and re-dissolving may be performed a plurality of times. The stirring operation by turning the ingot (primary ingot F) upside down can be performed more preferably 2 to 5 times. In this way, if the ingot is cast several times while reversing the top and bottom, the added flux α can be reliably mixed with the alloy material to promote the deoxidation reaction, and the deoxidation is sufficiently performed. The primary ingot X can be melted.
 つまり、1次鋳塊製造工程のように水冷銅容器1を用いた溶解法においては、水冷銅容器1の容器壁に近い部分の合金材料は抜熱の影響で溶解されない。そのため、1回の溶解では未溶解(未反応)部分が存在してしまい、未溶解部分では脱酸を促進するための反応(脱酸生成物のAlとCaO-CaFフラックスαとの反応)が十分に進行しない可能性がある。そこで、本実施形態の製造方法では、1次鋳塊Xの天地を反転させて再び溶解を行う操作を複数回に亘って繰り返している。このようにすれば1回目の溶解で未溶解であった部分が天地反転後の再溶解で溶解し、フラックスαとの間に反応が進行する。このような操作を複数回行えば、容器1(鋳型)内の溶湯が余すことなくフラックスαと反応するため、水冷銅容器1を用いていても脱酸が十分に行われた1次鋳塊Xを溶製することができるのである。 That is, in the melting method using the water-cooled copper container 1 as in the primary ingot manufacturing process, the alloy material in the portion near the container wall of the water-cooled copper container 1 is not melted due to the effect of heat removal. Therefore, there is an undissolved (unreacted) portion in one dissolution, and a reaction for promoting deoxidation (deoxidation products Al 2 O 3 and CaO—CaF 2 flux α) in the undissolved portion. Reaction) may not proceed sufficiently. Therefore, in the manufacturing method of the present embodiment, the operation of inverting the top of the primary ingot X and melting again is repeated a plurality of times. If it does in this way, the part which was not melt | dissolved by 1st melt | dissolution will melt | dissolve by the redissolving after top-and-bottom reversal, and reaction will advance between flux (alpha). If such an operation is performed a plurality of times, the molten metal in the container 1 (mold) reacts with the flux α without leaving any excess, so that the primary ingot is sufficiently deoxidized even if the water-cooled copper container 1 is used. X can be melted.
 上述した1次鋳塊製造工程を行った1次鋳塊X中には、脱酸反応により生成したAlが、フラックスαとして含まれている。2次鋳塊製造工程では、1次鋳塊製造工程で生成したAlを後述するフラックス層除去工程で機械的に除去しやすいように、フラックスαを鋳塊(2次鋳塊Y)の一部分(本実施形態では外周側)に偏って集めている。このようにフラックスが偏って集められた鋳塊が2次鋳塊Yである。 In the primary ingot X subjected to the above-described primary ingot manufacturing process, Al 2 O 3 generated by the deoxidation reaction is included as the flux α. In the secondary ingot manufacturing process, the flux α is ingot (secondary ingot Y) so that Al 2 O 3 generated in the primary ingot manufacturing process is easily removed mechanically in the flux layer removing process described later. Are gathered biased to a part (in this embodiment, the outer peripheral side). The ingot in which the fluxes are biased in this way is the secondary ingot Y.
 具体的には、2次鋳塊製造工程は、1次鋳塊Xを1.33Pa以上の雰囲気で無底の水冷銅鋳型2を用いた溶解法により溶解しつつ連続的に下方に引抜き2次鋳塊Yを得るものとなっている。この水冷銅鋳型2を用いた溶解法には、プラズマアークまたは誘導加熱を熱源として溶解を行う方法を用いることができるが、好ましくはプラズマアークを熱源として溶解を行う方法を用いるのが良い。水冷銅鋳型2の内部に供給された溶湯の表面では、Alが溶解したフラックスαが浮遊しており、熱源にプラズマアークを用いれば表面に吹き付けられたアークによってフラックスαが鋳型2の内周面近傍に偏って集まり、偏って集まった状態で凝固が行われる。その結果、2次鋳塊製造工程で溶製される2次鋳塊Yでは、下方に引き抜かれる2次鋳塊Yの外周側にフラックスαが偏って存在するようになる。このように外周側にフラックスαが偏って存在する2次鋳塊Yであれば、2次鋳塊Yの外周表面に形成された表面付着フラックス層βをフラックス層除去工程のショットブラストや研削などの機械的手段3で削り取れば、フラックスごとAlを除去することが可能となる。 Specifically, in the secondary ingot manufacturing process, the primary ingot X is continuously drawn out downward while being melted by a melting method using a bottomless water-cooled copper mold 2 in an atmosphere of 1.33 Pa or higher. The ingot Y is obtained. As the melting method using the water-cooled copper mold 2, a method of melting using a plasma arc or induction heating as a heat source can be used, but a method of melting using a plasma arc as a heat source is preferably used. On the surface of the molten metal supplied to the inside of the water-cooled copper mold 2, a flux α in which Al 2 O 3 is dissolved floats. If a plasma arc is used as a heat source, the flux α is generated by the arc sprayed on the surface. Coagulation is performed in a state of being concentrated in the vicinity of the inner peripheral surface and being concentrated in the vicinity. As a result, in the secondary ingot Y that is melted in the secondary ingot manufacturing process, the flux α is biased to exist on the outer peripheral side of the secondary ingot Y that is drawn downward. In this way, if the secondary ingot Y is present with the flux α being biased on the outer peripheral side, the surface adhering flux layer β formed on the outer peripheral surface of the secondary ingot Y is shot blasted or ground in the flux layer removing process. If the mechanical means 3 is used, the Al 2 O 3 together with the flux can be removed.
 フラックス層除去工程は、2次鋳塊製造工程で2次鋳塊の外周表面に形成された表面付着フラックス層βを、ショットブラストや研削などの機械的手段3で削り取るものである。このフラックス層除去工程を行うことで、2次鋳塊Yの酸素濃度を全体として下げることができる。 The flux layer removing step is a step of scraping off the surface-adhered flux layer β formed on the outer peripheral surface of the secondary ingot in the secondary ingot manufacturing step by mechanical means 3 such as shot blasting or grinding. By performing this flux layer removal step, the oxygen concentration of the secondary ingot Y can be lowered as a whole.
 上述した1次鋳塊製造工程からフラックス層除去工程を経て得られるTi-Al系合金Zは、2次鋳塊製造工程で2次鋳塊Yの外周表面に偏ったフラックスαやAlなどの表面付着フラックス層βが、フラックス層除去工程のショットブラストや研削などの機械的手段3で除去されているため、Ti-Al系合金Z中に含まれる酸素含有量が大きく低下し、合金材料Wに当初含まれていた酸素を確実に脱酸して低減することが可能となる。つまり、本実施形態のTi-Al系合金Zの製造方法であれば、酸素を高濃度で含む低品位のチタンから、高品位すなわち低酸素のTi-Al系合金Zを、歩留まり良く、効率的に製造することができる。 Ti-Al alloy Z obtained through the flux layer removing step from the primary ingot manufacturing process described above, the flux biased to the outer periphery surface of the secondary ingot Y in the secondary ingot manufacturing process α, Al 2 O 3, or the The surface-attached flux layer β is removed by mechanical means 3 such as shot blasting or grinding in the flux layer removing process, so that the oxygen content contained in the Ti—Al-based alloy Z is greatly reduced. Oxygen initially contained in the material W can be reliably deoxidized and reduced. That is, according to the manufacturing method of the Ti—Al-based alloy Z of the present embodiment, the high-quality, that is, the low-oxygen Ti—Al-based alloy Z is efficiently obtained from low-grade titanium containing a high concentration of oxygen with high yield. Can be manufactured.
 なお、本実施形態のTi-Al系合金Zの製造方法は、合金材料W中のAl含有量を40質量%以上にすることで、Ti-Al系合金Z中に含まれる酸素含有量を合計で0.1質量%未満とするものであるため、製造されるTi-Al系合金Zは必然的にAl含有量が40質量%以上になる。しかし、得られたTi-Al系合金Zを利用する場合には、Al含有量を40質量%未満まで下げたいという要望も存在する。 Note that, in the manufacturing method of the Ti—Al based alloy Z of the present embodiment, the oxygen content contained in the Ti—Al based alloy Z is totaled by setting the Al content in the alloy material W to 40 mass% or more. Therefore, the Ti-Al alloy Z to be manufactured necessarily has an Al content of 40% by mass or more. However, when the obtained Ti—Al-based alloy Z is used, there is a desire to reduce the Al content to less than 40% by mass.
 このような場合は、上述した1次鋳塊製造工程~フラックス層除去工程に加えて、以降に示すチタン材料添加・溶解工程を行うとよい。 In such a case, in addition to the primary ingot manufacturing process to the flux layer removing process described above, the titanium material addition / dissolution process described below may be performed.
 すなわち、チタン材料添加・溶解工程は、2次鋳塊Yにチタン材料Vを添加して1.33Pa以上の雰囲気で水冷銅鋳型4(水冷銅容器)を用いた溶解法によって溶解することにより、Al含有量が40質量%未満のTi-Al系合金Z2を得るものとなっている。なお、図例の溶解法は水冷銅容器を用いたものであるが、このチタン材料添加・溶解工程に用いられる溶解法は水冷銅式誘導溶解(CCIM)以外の溶解法、例えば真空アーク溶解法(VAR)や真空誘導溶解(VIM)などを用いても良い。 That is, the titanium material addition / dissolution step is performed by adding the titanium material V to the secondary ingot Y and dissolving it by a melting method using a water-cooled copper mold 4 (water-cooled copper container) in an atmosphere of 1.33 Pa or more. A Ti—Al based alloy Z2 having an Al content of less than 40% by mass is obtained. The melting method shown in the figure uses a water-cooled copper container, but the melting method used in this titanium material addition / dissolution step is a melting method other than water-cooled copper induction melting (CCIM), such as a vacuum arc melting method. (VAR) or vacuum induction melting (VIM) may be used.
 具体的には、チタン材料添加・溶解工程で2次鋳塊Yに添加されるチタン材料Vは、このチタン材料添加・溶解工程後にAl含有量が40質量%未満のTi-Al系合金Z2を得る場合には、Al含有量が40質量%未満のチタン材料Vとされるのが良い。例えば、アルミを不純物に含まない純TiのようなAl含有量が40質量%未満のチタン材料Vを添加すれば、2次鋳塊Yに含まれるAl含有量が希釈により小さくなるため、Al含有量が40質量%未満となるようなTi-Al系合金Z2を得ることができる。 Specifically, the titanium material V added to the secondary ingot Y in the titanium material addition / melting step is a Ti-Al alloy Z2 having an Al content of less than 40% by mass after the titanium material addition / melting step. In the case of obtaining the titanium material V, the Al content is preferably less than 40% by mass. For example, if a titanium material V having an Al content of less than 40% by mass, such as pure Ti that does not contain aluminum as an impurity, is added, the Al content contained in the secondary ingot Y is reduced by dilution. A Ti—Al-based alloy Z2 whose amount is less than 40% by mass can be obtained.
 なお、チタン材料添加・溶解工程で添加されるチタン材料Vは、製造しようとするTi-Al系合金Z2の要求品質によって変化するため、チタン材料Vにおけるアルミ以外の成分(Sn、V、Mnのようなアルミ以外の金属)の濃度は規定することはできない。
 しかし、上述した1次鋳塊製造工程~フラックス層除去工程に加えてチタン材料添加・溶解工程を行えば、酸素やアルミ以外の組成についても要求品質に合致したTi-Al系合金Z2を得ることができ、本発明の製造方法の利便性をさらに高めることが可能となる。
Since the titanium material V added in the titanium material addition / dissolution process varies depending on the required quality of the Ti—Al alloy Z2 to be manufactured, components other than aluminum in the titanium material V (Sn, V, Mn The concentration of such metals other than aluminum cannot be specified.
However, if the titanium material addition / dissolution process is performed in addition to the primary ingot manufacturing process to the flux layer removal process described above, a Ti-Al alloy Z2 that meets the required quality can be obtained for the composition other than oxygen and aluminum. Thus, the convenience of the production method of the present invention can be further enhanced.
 次に、第2実施形態について説明する。
 図2に示すように、本実施形態のTi-Al系合金101の製造方法は、原料分割工程~フラックス層除去工程の3つの工程を経て、好適には原料分割工程~フラックス層除去工程の後にさらにチタン材料添加・溶解工程を行って、酸素を0.1質量%以上含むTi-Al系合金101の合金材料から酸素の含有量が0.1質量%未満とされた高品位なTi-Al系合金101を製造するものとなっている。
Next, a second embodiment will be described.
As shown in FIG. 2, the manufacturing method of the Ti—Al-based alloy 101 according to the present embodiment has three steps of a raw material dividing step to a flux layer removing step, preferably after the raw material dividing step to the flux layer removing step. Further, a titanium material addition / dissolution step is performed to obtain a high-grade Ti—Al in which the oxygen content is less than 0.1% by mass from the alloy material of the Ti—Al alloy 101 containing 0.1% by mass or more of oxygen. The system alloy 101 is manufactured.
 具体的には、このTi-Al系合金101の製造方法に用いられる合金材料はチタン材料にアルミニウム材料を混ぜ合わせたものである。このようにしてアルミが配合された溶解原料102を分割体ベース鋳塊製造工程で溶解させると、アルミが合金材料中の酸素と反応して脱酸が行われる。また、本発明の製造方法では、原料分割工程において合金材料に脱酸を促進させる目的でCaO-CaF系のフラックス103を添加している。このようなフラックス103を原料分割工程で添加すると分割体ベース鋳塊製造工程での脱酸がさらに促進されて、酸素が0.1質量%以上含まれた合金材料から最終的には酸素が0.1質量%未満の高品位なTi-Al系合金101を得ることができる。 Specifically, the alloy material used in the manufacturing method of the Ti—Al alloy 101 is a mixture of a titanium material and an aluminum material. When the melting raw material 102 mixed with aluminum is melted in the divided body base ingot manufacturing process in this way, the aluminum reacts with oxygen in the alloy material to perform deoxidation. In the production method of the present invention, CaO—CaF 2 -based flux 103 is added to the alloy material for the purpose of promoting deoxidation in the raw material dividing step. When such a flux 103 is added in the raw material dividing step, deoxidation in the divided base ingot manufacturing step is further promoted, and oxygen is finally reduced from an alloy material containing 0.1% by mass or more of oxygen. It is possible to obtain a high-grade Ti—Al-based alloy 101 of less than 1 mass%.
 また、原料分割工程ではフラックス103が添加された溶解原料102が複数個に分割されて分割体が形成される。そして、分割体ベース鋳塊製造工程では、溶解原料102の分割体の溶解操作に続いて引き下げ操作がすべての分割体に対して行われ、フラックス103にAl等の非金属介在物を移行させると共に、非金属介在物が移行したフラックス103を鋳塊の外周面に偏在化(局在化)させることができるようになっている。このようにして偏在化した非金属介在物及びフラックス103をフラックス層除去工程で機械的に除去するか、好ましくはチタン材料添加・溶解工程で成分調整をさらに行うことで、本発明のTi-Al系合金101が製造される。 In the raw material dividing step, the melted raw material 102 to which the flux 103 is added is divided into a plurality of pieces to form divided bodies. In the divided body base ingot manufacturing process, the lowering operation is performed on all the divided bodies following the melting operation of the divided body of the melting raw material 102, and non-metallic inclusions such as Al 2 O 3 are added to the flux 103. In addition to the transition, the flux 103 to which the non-metallic inclusions are transferred can be unevenly distributed (localized) on the outer peripheral surface of the ingot. The non-metallic inclusions and the flux 103 that are unevenly distributed in this way are mechanically removed in the flux layer removing step, or preferably the component adjustment is further performed in the titanium material adding / dissolving step, so that the Ti—Al of the present invention A system alloy 101 is manufactured.
 以降では、本発明の製造方法に設けられる原料分割工程~チタン材料添加・溶解工程の各工程についてそれぞれ説明する。 Hereinafter, each step of the raw material dividing step to the titanium material addition / dissolution step provided in the production method of the present invention will be described.
 原料分割工程は、Ti-Al系合金101の合金材料にフラックス103を加えて溶解原料102を作製し、作製した溶解原料102をn個に分割して、溶解原料102の第1分割体141~第n分割体を形成するものとなっている。この溶解原料102の分割操作が、本発明の製造方法の特徴となっている。 In the raw material dividing step, the flux 103 is added to the alloy material of the Ti—Al-based alloy 101 to produce the molten raw material 102, the produced molten raw material 102 is divided into n pieces, and the first divided body 141˜ The n-th divided body is formed. This dividing operation of the melting raw material 102 is a feature of the manufacturing method of the present invention.
 具体的には、溶解原料102に用いられるTi-Al系合金101の合金材料は、チタン材料およびアルミニウム材料よりなるものであり、酸素を合計で0.1質量%以上、且つAlを40質量%以上含有している。また、合金材料に配合されるフラックス103は、酸化カルシウムにフッ化カルシウムを35~95質量%配合したCaO-CaF系のフラックス103となっている。そして、上述した合金材料にフラックス103を3~20質量%となるように配合したものが、本実施形態の溶解原料102となっている。 Specifically, the alloy material of the Ti—Al based alloy 101 used for the melting raw material 102 is made of a titanium material and an aluminum material, and the total amount of oxygen is 0.1 mass% or more and Al is 40 mass%. Contains above. Further, the flux 103 blended in the alloy material is a CaO—CaF 2 -based flux 103 in which 35 to 95 mass% of calcium fluoride is blended with calcium oxide. The alloy material described above is blended with the flux 103 in an amount of 3 to 20% by mass to form the melting raw material 102 of this embodiment.
 なお、上述した合金材料を構成するチタン材料は、低品位で酸素を多く含むスポンジチタン、スクラップ原料、ルチル鉱石などの酸化チタン(TiO)などを含むものである。このように合金材料に低品位なチタン材料を用いる理由は、これらチタン材料が廉価であり調達し易いからである。 Incidentally, the titanium material constituting the above-mentioned alloy material is one containing a sponge titanium containing much oxygen in low-grade scrap material, titanium oxide such as rutile ore (TiO 2). The reason why low-grade titanium materials are used in this way is that these titanium materials are inexpensive and easy to procure.
 また、上述した合金材料は、酸素の合計含有量を0.1質量%以上とされている。例えば、合金材料中の酸素の合計含有量が0.1質量%未満の場合には、酸素の含有量は僅かであり脱酸自体が必要ないからである。なお、本発明では、酸素の含有量の上限は規定しないが、合金材料に実際に含有される酸素の合計含有量の上限は、25質量%程度であると考えられる。 Further, the above-described alloy material has a total oxygen content of 0.1% by mass or more. For example, when the total content of oxygen in the alloy material is less than 0.1% by mass, the content of oxygen is small and deoxidation itself is not necessary. In the present invention, the upper limit of the oxygen content is not specified, but the upper limit of the total content of oxygen actually contained in the alloy material is considered to be about 25% by mass.
 また、原料分割工程の溶解原料102に用いられる合金材料に、Alを40質量%以上含有するTi-Al系合金101を用いるのは、以下のような理由に基づいている。
 例えば、公知のTi-Al-Oの3元系状態図(国際公開2016/035824の図5などを参照)によれば、Ti-Al系合金101中に固溶する最大酸素量は、Ti-Al系合金101中のAl含有量を大きくするほど、固溶酸素濃度が低くなる傾向を有している。つまり、低品位なチタン材料を用いて作製したTi-Al系合金101を含む溶解原料102であっても、Alの含有量を40質量%以上まで高めれば、分割体ベース鋳塊製造工程で脱酸を行った際に合金材料中の酸素を下げることができるのではないかと考え、本発明者らは本発明を完成させるに至ったのである。
The reason why the Ti—Al alloy 101 containing 40% by mass or more of Al is used as the alloy material used for the melting raw material 102 in the raw material dividing step is based on the following reason.
For example, according to a known ternary phase diagram of Ti—Al—O (see FIG. 5 of International Publication 2016/035824), the maximum amount of oxygen dissolved in the Ti—Al alloy 101 is Ti— As the Al content in the Al-based alloy 101 is increased, the dissolved oxygen concentration tends to decrease. In other words, even the melting raw material 102 containing the Ti—Al alloy 101 produced using a low-grade titanium material can be removed in the divided base ingot manufacturing process if the Al content is increased to 40% by mass or more. The inventors have thought that oxygen in the alloy material can be lowered when acid is performed, and the present inventors have completed the present invention.
 上述したフラックス103は、溶解原料102に添加されることで溶解原料102中のAlの活量を低下させ、後述する分割体ベース鋳塊製造工程で脱酸反応を促進させる機能を有している。つまり、このフラックス103は、Ti-Al系合金101の脱酸生成物であるAlを溶解させることで、脱酸反応における生成種であるAlの活量を低下させ、脱酸反応を促進させる効果を備えている。 The flux 103 described above has the function of reducing the activity of Al 2 O 3 in the melting raw material 102 by being added to the melting raw material 102 and promoting the deoxidation reaction in the divided body ingot manufacturing process described later. is doing. That is, the flux 103 dissolves Al 2 O 3 which is a deoxidation product of the Ti—Al-based alloy 101, thereby reducing the activity of Al 2 O 3 which is a generated species in the deoxidation reaction. Has the effect of promoting acid reaction.
 なお、このフラックス103へのAlの溶解は、フラックス3が溶融した状態で初めて生じるものである。そのため、フラックス103の融点が高くなりすぎると、フラックス103が溶融しなくなりAlの溶解が生じなくなる。つまり、CaO-CaF系のフラックス103の場合であれば、融点が低いCaFの含有量を増加させるなどして、フラックス103自体の融点を低下させる必要がある。具体的には、本実施形態の脱酸では、フラックス103の融点が1800K以下となるように、フラックス103中のCaFの含有量は35質量%以上とされている。また、フラックス層除去工程またはチタン材料添加・溶解工程後に製品として得られるTi-Al系合金101がCaF中のふっ素で汚染されることがないように、フラックス103中のCaFの含有量は95質量%以下とされている。 The dissolution of Al 2 O 3 in the flux 103 occurs only when the flux 3 is melted. Therefore, if the melting point of the flux 103 becomes too high, the flux 103 does not melt and Al 2 O 3 does not dissolve. That is, in the case of the CaO—CaF 2 based flux 103, it is necessary to decrease the melting point of the flux 103 itself by increasing the content of CaF 2 having a low melting point. Specifically, in the deoxidation of the present embodiment, the content of CaF 2 in the flux 103 is set to 35% by mass or more so that the melting point of the flux 103 is 1800K or less. Moreover, so as not to Ti-Al alloy 101 obtained as a product after the flux layer removing step or titanium material adding and dissolving process is contaminated with fluorine in CaF 2, the content of CaF 2 in the flux 103 It is 95 mass% or less.
 また、上述した溶解原料102に対するCaO-CaF系のフラックス103の添加量は、製品であるTi-Al系合金101に対して3質量%~20質量%となっている。Ti-Al系合金101に対する添加量が3質量%より少なければ、Al活量の低下があまり生じず、脱酸促進効果がほとんど得られない。Ti-Al系合金101に対する添加量が20質量%より多くなれば、添加したフラックス103が製造されたTi-Al系合金101中に残留してしまうリスクが高くなってしまう。 The addition amount of the CaO—CaF 2 -based flux 103 to the melting raw material 102 is 3% by mass to 20% by mass with respect to the Ti—Al-based alloy 101 as a product. If the addition amount relative to Ti-Al alloy 101 is less than 3 wt%, Al 2 O 3 does not occur reduction in the activity of so much, no deoxidation promoting effect is hardly obtained. If the amount added to the Ti—Al based alloy 101 is more than 20 mass%, the risk that the added flux 103 remains in the manufactured Ti—Al based alloy 101 increases.
 このようにして原料分割工程では、合金材料にフラックス103を配合して溶解原料102がまず調製される。 In this way, in the raw material dividing step, the melting raw material 102 is first prepared by blending the flux 103 with the alloy material.
 ところで、上述した原料分割工程でTi-Al系合金101の合金材料にフラックス103が配合された溶解原料102を水冷銅るつぼ105に装入して溶解させる(るつぼ内凝固法を行う)だけでは、Al等の非金属介在物を十分に除去することはできない。非金属介在物を十分に除去するためには、以降に示すような分割体ベース鋳塊製造工程の操作を行うことが必要となる。 By the way, the melting raw material 102 in which the flux 103 is mixed with the alloy material of the Ti—Al alloy 101 in the above-described raw material dividing step is charged into the water-cooled copper crucible 105 and melted (the solidification method in the crucible is performed). Non-metallic inclusions such as Al 2 O 3 cannot be sufficiently removed. In order to sufficiently remove the non-metallic inclusions, it is necessary to perform an operation of a divided body base ingot manufacturing process as described below.
 具体的には、上述した溶解原料102が調製されたら、次に調製された溶解原料102をn個に分割して、第1分割体141~第n分割体を形成する。この溶解原料102の分割数である「n」は2以上の整数となっており、原料分割工程においては溶解原料102が複数個の分割体に分割される。 Specifically, when the above-described dissolving raw material 102 is prepared, the prepared dissolving raw material 102 is divided into n pieces to form the first divided body 141 to the n-th divided body. “N”, which is the number of divisions of the melting raw material 102, is an integer of 2 or more, and the melting raw material 102 is divided into a plurality of divided bodies in the raw material dividing step.
 また、原料分割工程において溶解原料102を分割する場合には、鋳造終了時の最終目標鋳塊重量に対して各分割体(第1分割体141~第n分割体)の重量が最大で全体の4/5以下となるように調整後の溶解原料2をn分割する。例えば、図2に示す如く、最終目標鋳塊重量が100tonの場合において、溶解原料2を3分割する場合であれば、第1分割体141~第3分割体143のいずれもが80ton以下となるように分割する必要がある。工業的には、分割体は等分割(この場合は33.3ton)することが好ましいが、本発明は、分割体を等分割することに限定はされない。 Further, when the melting raw material 102 is divided in the raw material dividing step, the weight of each divided body (the first divided body 141 to the nth divided body) is the maximum with respect to the final target ingot weight at the end of casting. The melted raw material 2 after adjustment is divided into n so as to be 4/5 or less. For example, as shown in FIG. 2, when the final target ingot weight is 100 ton and the melting raw material 2 is divided into three, all of the first divided body 141 to the third divided body 143 are 80 ton or less. Need to be divided like so. Industrially, the divided body is preferably equally divided (in this case, 33.3 ton), but the present invention is not limited to equally dividing the divided body.
 このような分割を行えば、原料分割工程において得られる第1分割体141~第n分割体がいずれも鋳造終了時の最終目標鋳塊重量の4/5を超えないものとなり、鋳造時における水冷銅るつぼ105の底部107からの抜熱を抑制可能となって、脱酸反応を十分に促進可能となる。 If such a division is performed, none of the first divided body 141 to the n-th divided body obtained in the raw material dividing step will exceed 4/5 of the final target ingot weight at the end of casting. Heat removal from the bottom 107 of the copper crucible 105 can be suppressed, and the deoxidation reaction can be sufficiently promoted.
 より詳しく説明すれば、上述したように溶解原料102を分割した後の個々の分割体の原料重量は、最終鋳塊重量に対して、最大でも全体の4/5以下となるように分割する。つまり、最低、2回の溶解操作と2回の引き下げ操作(分割体の装入/溶解→引き下げ→分割体の装入/溶解→引き下げ)が必要である。なぜならば、1回の溶解操作のみでは、底部107の水冷銅るつぼ105に近い部分は強冷却されており、投入されたフラックス103が十分に溶融しないうちに凝固が進行するため、Al等の非金属介在物とフラックス103とが反応しにくい。この点、2回目以降の溶解操作については底部107からの抜熱が抑制されるため、2回目以降の溶解の際にフラックス103と非金属介在物とが十分に反応し合って脱酸が促進する。 More specifically, as described above, the raw material weight of each divided body after dividing the molten raw material 102 is divided so as to be 4/5 or less of the whole at the maximum with respect to the final ingot weight. That is, at least two melting operations and two lowering operations (partition body charging / dissolution → lowering → partition body charging / dissolution → lowering) are required. This is because the portion close to the water-cooled copper crucible 105 at the bottom 107 is strongly cooled by only one melting operation, and solidification proceeds before the charged flux 103 is sufficiently melted. Therefore, Al 2 O 3 It is difficult for non-metallic inclusions such as these to react with the flux 103. In this regard, since the heat removal from the bottom 107 is suppressed in the second and subsequent melting operations, the flux 103 and the non-metallic inclusions sufficiently react with each other during the second and subsequent melting, thereby promoting deoxidation. To do.
 なお、個々の分割体の重量を、最終目標重量に対して、全体の4/5超の重量にすると、2回目以降の溶解操作を行ったとしても、メタルとフラックス103の分離効率が下がる可能性がある。例えば、第1分割体141の重量が最終目標重量の4/5超となる場合には、2回目以降の溶解で残りの1/Vより少ない量を溶解させても、非金属介在物とフラックス103との反応が起こりにくくなる。そのため、分割体の重量は最大でも全体の4/5以下に分割することが望ましく、好ましくは全体の2/3以下、より好ましくは全体のI/2以下とされるのが望ましい。 In addition, if the weight of each divided body is more than 4/5 of the final target weight, the separation efficiency between the metal and the flux 103 can be lowered even if the second and subsequent melting operations are performed. There is sex. For example, when the weight of the first divided body 141 exceeds 4/5 of the final target weight, the non-metallic inclusions and the flux can be dissolved even if the amount less than the remaining 1 / V is dissolved in the second and subsequent dissolutions. Reaction with 103 is less likely to occur. For this reason, it is desirable to divide the divided body into a maximum of 4/5 or less, preferably 2/3 or less of the whole, more preferably I / 2 or less of the whole.
 なお、図1に示される本実施形態では、原料分割工程で溶解原料102を3分割して脱酸させる例を挙げて、本発明を説明しているが、分割数は、5分割であっても11分割であっても何ら問題はない。 In the present embodiment shown in FIG. 1, the present invention has been described by giving an example in which the dissolved raw material 102 is divided into three parts and deoxidized in the raw material dividing step, but the number of divisions is five. Even if it is 11 divisions, there is no problem.
 分割体ベース鋳塊製造工程は、原料分割工程で分割された溶解原料102の第1分割体141を、水冷銅るつぼ105(底引き水冷銅るつぼ105)に装入して1.33Pa以上の不活性ガス雰囲気下で溶解させ且つ水冷銅るつぼ105を毎分15mm以下の速度で下方に引き下げる操作を行い、その後、原料分割工程で分割された溶解原料102の第2分割体142を、底引き水冷銅るつぼ105に装入して1.33Pa以上の不活性ガス雰囲気下で溶解させ且つ水冷銅るつぼ105を毎分15mm以下の速度で下方に引き下げる操作を行い、以降、第n分割体まで同様な操作を繰り返すことで鋳塊を形成するものとなっている。 In the divided body base ingot manufacturing process, the first divided body 141 of the melted raw material 102 divided in the raw material dividing process is charged into a water-cooled copper crucible 105 (bottomed water-cooled copper crucible 105) to be inactive at 1.33 Pa or more. An operation of melting under a gas atmosphere and pulling down the water-cooled copper crucible 105 at a speed of 15 mm or less per minute is performed, and then the second divided body 142 of the melted raw material 102 divided in the raw material dividing step is bottomed out. 105 is dissolved in an inert gas atmosphere of 1.33 Pa or higher, and the water-cooled copper crucible 105 is lowered downward at a speed of 15 mm or less per minute, and thereafter the same operation is performed up to the n-th divided body. The ingot is formed by repeating.
 言い換えれば、分割体ベース鋳塊製造工程は、溶解原料102の分割体を水冷銅るつぼ105に装入して1.33Pa以上の不活性ガス雰囲気下で溶解させる溶解操作と、この溶解操作に続いて水冷銅るつぼ105を毎分15mm以下の速度で下方に引き下げるという引き下げ操作とを、1回ずつ連続して行う操作を「基本操作」とするものである。そして、この基本操作を、第1分割体141、第2分割体142、・・・、第n分割体のそれぞれについて、順番に1回ずつ行うものとなっている。
 なお、1.33Pa以上の不活性ガス雰囲気下とする理由は、高真空雰囲気での溶解のようにAlやTiの揮発ロスが生じることが無くなるからである。より好ましくは、1.33Pa~5.33×10Pa(≒5気圧)の不活性ガス雰囲気下で溶解させる。
In other words, the divided body base ingot manufacturing process includes a melting operation in which a divided body of the melting raw material 102 is charged into a water-cooled copper crucible 105 and melted in an inert gas atmosphere of 1.33 Pa or more, and this melting operation is followed. Then, the operation of continuously lowering the water-cooled copper crucible 105 downward at a speed of 15 mm / min or less is performed as “basic operation”. And this basic operation is performed once in order about each of the 1st division body 141, the 2nd division body 142, ..., and the nth division body.
The reason why the inert gas atmosphere is 1.33 Pa or more is that no volatilization loss of Al or Ti occurs as in the case of melting in a high vacuum atmosphere. More preferably, it is dissolved in an inert gas atmosphere of 1.33 Pa to 5.33 × 10 5 Pa (≈5 atm).
 なお、本実施形態の場合であれば、溶解原料102は3分割されるため、第1分割体141の溶解操作→第1分割体141の引き下げ操作→第2分割体142の溶解操作→第2分割体142の引き下げ操作→第3分割体143の溶解操作→第3分割体143の引き下げ操作という順番で溶解原料102を処理することで分割体ベース鋳塊製造工程が進行する。 In the case of the present embodiment, since the melting raw material 102 is divided into three, the melting operation of the first divided body 141 → the lowering operation of the first divided body 141 → the melting operation of the second divided body 142 → the second The divided body base ingot manufacturing process proceeds by processing the melting raw material 102 in the order of the lowering operation of the divided body 142, the melting operation of the third divided body 143, and the lowering operation of the third divided body 143.
 次に、分割体ベース鋳塊製造工程において溶解原料102の各分割体に対して行われる溶解操作及び引き下げ操作について、詳しく説明する。 Next, the melting operation and the lowering operation performed on each divided body of the melting raw material 102 in the divided body base ingot manufacturing process will be described in detail.
 分割体ベース鋳塊製造工程は、溶解原料102の各分割体を1.33Pa以上の不活性ガス雰囲気に容器内が調製された水冷銅るつぼ105(水冷銅鋳型)内に装入して、水冷銅るつぼ105内で溶解原料102の各分割体をプラズマアークまたは誘導加熱を熱源として溶解を行うことにより、鋳塊を鋳造するものとなっている。なお、水冷銅るつぼ105を用いて溶解原料102の分割体を溶解させる際には、好ましくは誘導加熱を熱源として溶解を行うのが良い。一般的に、誘導加熱により酸化物などの非金属介在物を含んだ金属を溶解した場合、非金属介在物と金属の電気伝導率の違いにより、非金属介在物は、溶融金属の外側に集まることが知られている。つまり、水冷銅るつぼ105の内部に供給された溶湯中のAlが溶解したフラックス103は、誘導加熱により鋳型内周面近傍に偏って集まり、偏って集まった状態で凝固が行われる。その結果、分割体ベース鋳塊製造工程で溶製される鋳塊には、下方に引き抜かれる鋳塊の外周側にフラックス103が偏って存在する表面付着フラックス層108が形成されるようになる。このように外周側に表面付着フラックス層108が存在する鋳塊であれば、表面付着フラックス層108をフラックス層除去工程のショットブラストや研削などの機械的手段で削り取ることが可能となり、フラックス103ごとAl等の非金属介在物を除去することが可能となるからである。
 また、分割体ベース鋳塊製造工程において溶解原料102の分割体の溶解操作に続いて行われる引き下げ操作は、上述した溶解操作でフラックス103を溶解させることにより鋳塊の表面に形成される表面付着フラックス層108を、鋳型と鋳塊との間に偏在させるものである。具体的には、上述した水冷銅るつぼ105は、上方と下方との双方に向かって開口した筒形状のるつぼ本体106と、るつぼ本体106の底側に配備された底部107とを組み合わせた構造となっている。この水冷銅るつぼ105の底部107はるつぼ本体106に対して上下方向に移動可能に取り付けられており、るつぼ本体106に対して底部107を下降させれば、底部107の上側に載置された鋳塊も下降させることが可能となる。分割体ベース鋳塊製造工程では、このような引き下げ操作を行うことで、表面付着フラックス層108を、鋳塊の外周側、言い換えれば鋳型と鋳塊との間に偏在させている。
In the divided body base ingot manufacturing process, each divided body of the melting raw material 102 is charged into a water-cooled copper crucible 105 (water-cooled copper mold) prepared in an inert gas atmosphere of 1.33 Pa or more, and water-cooled. The ingot is cast by melting each divided body of the melting raw material 102 in the copper crucible 105 using a plasma arc or induction heating as a heat source. In addition, when the divided body of the melting raw material 102 is melted using the water-cooled copper crucible 105, the melting is preferably performed using induction heating as a heat source. Generally, when metals containing non-metallic inclusions such as oxides are melted by induction heating, the non-metallic inclusions gather outside the molten metal due to the difference in electrical conductivity between the non-metallic inclusions and the metal. It is known. That is, the flux 103 in which the Al 2 O 3 in the molten metal supplied into the water-cooled copper crucible 105 is concentrated in the vicinity of the inner peripheral surface of the mold due to induction heating, and solidification is performed in the state of being concentrated. As a result, the surface-attached flux layer 108 in which the flux 103 is biased and present on the outer peripheral side of the ingot drawn downward is formed in the ingot melted in the divided body base ingot manufacturing process. In the case of an ingot in which the surface-attached flux layer 108 exists on the outer peripheral side in this way, the surface-attached flux layer 108 can be scraped off by mechanical means such as shot blasting or grinding in the flux layer removing process. This is because non-metallic inclusions such as Al 2 O 3 can be removed.
Further, the pulling-down operation performed following the melting operation of the divided body of the melting raw material 102 in the divided body base ingot manufacturing process is the surface adhesion formed on the surface of the ingot by melting the flux 103 by the above-described melting operation. The flux layer 108 is unevenly distributed between the mold and the ingot. Specifically, the above-described water-cooled copper crucible 105 has a structure in which a cylindrical crucible body 106 that opens both upward and downward and a bottom portion 107 that is disposed on the bottom side of the crucible body 106 are combined. It has become. The bottom 107 of the water-cooled copper crucible 105 is attached to the crucible main body 106 so as to be movable in the vertical direction. When the bottom 107 is lowered with respect to the crucible main body 106, the cast placed on the upper side of the bottom 107 is performed. The lump can also be lowered. In the divided body base ingot manufacturing process, by performing such a pulling-down operation, the surface adhering flux layer 108 is unevenly distributed between the outer periphery side of the ingot, in other words, between the mold and the ingot.
 また、本実施形態の引き下げ操作では、鋳塊の引き下げ速度、言い換えれば水冷銅るつぼ105の底部107の下降速度を、15mm/分以下、好ましくは10mm/分以下としている。鋳塊の引き下げ速度が15mm/分を超えると、上述した分割体ベース鋳塊製造工程で鋳塊の外周表面に形成された表面付着フラックス層108が破断されてしまい、表面付着フラックス層108を鋳型と鋳塊との間に十分に偏在させることが困難になるからである。 In the lowering operation of this embodiment, the ingot lowering speed, in other words, the lowering speed of the bottom 107 of the water-cooled copper crucible 105 is set to 15 mm / min or less, preferably 10 mm / min or less. If the ingot lowering speed exceeds 15 mm / min, the surface-adhered flux layer 108 formed on the outer peripheral surface of the ingot in the above-described divided body base ingot manufacturing process is broken, and the surface-adhered flux layer 108 is used as a mold. This is because it is difficult to make it unevenly distributed between the steel and the ingot.
 上述した溶解操作と引き下げ操作とを続けて1回ずつ行うものが、ある分割体に対する「基本操作」となる。この「基本操作」は、第1分割体141、第2分割体142、・・・、第n分割体のそれぞれに対して1回ずつ行われる。 The one that performs the above-described dissolving operation and pulling-down operation once at a time is the “basic operation” for a certain divided body. This “basic operation” is performed once for each of the first divided body 141, the second divided body 142,.
 例えば、図例の分割体ベース鋳塊製造工程の場合であれば、溶解原料102が3分割されており、第1分割体141、第2分割体142、第3分割体143が存在するため、第1分割体141の溶解操作→第1分割体141の引き下げ操作→第2分割体142の溶解操作→第2分割体142の引き下げ操作→第3分割体143の溶解操作→第3分割体143の引き下げ操作が行われ、最終的には上下方向に長尺な円筒状の鋳塊が分割体ベース鋳塊製造工程で溶製(鋳造)されることになる。 For example, in the case of the divided body base ingot manufacturing process of the illustrated example, the melting raw material 102 is divided into three, and the first divided body 141, the second divided body 142, and the third divided body 143 exist, Melting operation of first divided body 141 → Lowering operation of first divided body 141 → Melting operation of second divided body 142 → Lowering operation of second divided body 142 → Melting operation of third divided body 143 → Third divided body 143 In the end, a cylindrical ingot that is long in the vertical direction is melted (cast) in the divided base ingot manufacturing process.
 上述した分割体ベース鋳塊製造工程で鋳造された鋳塊の外周面にはフラックス103が偏った状態で凝固した表面付着フラックス層108が形成されており、この表面付着フラックス層108にはAl等の非金属介在物も高濃度で含まれている。それゆえ、鋳塊の外周面に形成された表面付着フラックス層108をフラックス層除去工程のショットブラストや研削などの機械的手段で削り取れば、フラックス103ごとAl3等の非金属介在物を除去することが可能となり、鋳塊に含まれる酸素濃度を全体として下げることができる。 The outer peripheral surface of the ingot was cast with the above-mentioned divided body based ingot manufacturing process and surface deposition flux layer 108 solidified in a state where the flux 103 is biased is formed on the surface adhering flux layer 108 Al 2 Non-metallic inclusions such as O 3 are also contained at a high concentration. Therefore, if the surface adhering flux layer 108 formed on the outer peripheral surface of the ingot is scraped by mechanical means such as shot blasting or grinding in the flux layer removing step, the non-metallic inclusions such as Al 2 O 3 together with the flux 103 The oxygen concentration contained in the ingot can be lowered as a whole.
 上述した原料分割工程からフラックス層除去工程を経て得られるTi-Al系合金101は、分割体ベース鋳塊製造工程で鋳塊の外周面に形成されていた表面付着フラックス層108が、フラックス層除去工程のショットブラストや研削などの機械的手段で除去されているため、Ti-Al系合金101中に含まれる酸素含有量が大きく低下し、合金材料に当初含まれていた酸素が確実に脱酸されて低減されたものとなっている。つまり、本実施形態のTi-Al系合金101の製造方法であれば、酸素を高濃度で含む低品位のチタンから、高品位すなわち低酸素のTi-Al系合金101を、歩留まり良く、効率的に製造することができる。 The Ti—Al-based alloy 101 obtained from the raw material dividing step through the flux layer removing step has the surface-attached flux layer 108 formed on the outer peripheral surface of the ingot in the divided body base ingot manufacturing step. Since it is removed by mechanical means such as shot blasting and grinding in the process, the oxygen content contained in the Ti-Al alloy 101 is greatly reduced, and the oxygen originally contained in the alloy material is reliably deoxidized. Has been reduced. That is, according to the manufacturing method of the Ti—Al based alloy 101 of the present embodiment, the high quality, that is, the low oxygen Ti—Al based alloy 101 is efficiently produced from the low quality titanium containing a high concentration of oxygen with a high yield. Can be manufactured.
 なお、本実施形態のTi-Al系合金101の製造方法は、合金材料中のAl含有量を40質量%以上にすることで、Ti-Al系合金101中に含まれる酸素含有量を合計で0.1質量%未満とするものであるため、製造されるTi-Al系合金101は必然的にAl含有量が40質量%以上になる。しかし、得られたTi-Al系合金101を利用する場合には、Al含有量を40質量%未満まで下げたいという要望も存在する。 Note that, in the manufacturing method of the Ti—Al based alloy 101 of the present embodiment, the oxygen content contained in the Ti—Al based alloy 101 is totaled by setting the Al content in the alloy material to 40% by mass or more. Since the Ti content is less than 0.1% by mass, the produced Ti—Al-based alloy 101 inevitably has an Al content of 40% by mass or more. However, when the obtained Ti—Al-based alloy 101 is used, there is a desire to reduce the Al content to less than 40% by mass.
 このような場合は、上述した原料分割工程~フラックス層除去工程に加えて、以降に示すチタン材料添加・溶解工程を行うとよい。 In such a case, in addition to the above-described raw material dividing step to flux layer removing step, the titanium material addition / dissolution step described below may be performed.
 すなわち、チタン材料添加・溶解工程は、鋳塊にチタン材料を添加して1.33Pa以上の雰囲気で水冷銅鋳型(水冷銅容器109)を用いた溶解法によって溶解することにより、Al含有量が40質量%未満のTi-Al系合金101を得るものとなっている。なお、図2に例示する溶解法は水冷銅容器を用いたものであるが、このチタン材料添加・溶解工程に用いられる溶解法は水冷銅式誘導溶解(CCIM)以外の溶解法、例えば真空アーク溶解法(VAR)や真空誘導溶解(VIM)などを用いて行っても良い。
 具体的には、チタン材料添加・溶解工程で鋳塊に添加されるチタン材料は、このチタン材料添加・溶解工程後にAl含有量が40質量%未満のTi-Al系合金101を得る場合には、Al含有量が40質量%未満のチタン材料とされるのが良い。例えば、アルミを不純物に含まない純TiのようなAl含有量が40質量%未満のチタン材料を添加すれば、鋳塊に含まれるAl含有量が希釈により小さくなるため、Al含有量が40質量%未満となるようなTi-Al系合金101を得ることができる。
That is, in the titanium material addition / dissolution step, the titanium content is added to the ingot and melted by a melting method using a water-cooled copper mold (water-cooled copper container 109) in an atmosphere of 1.33 Pa or higher, so that the Al content is increased. A Ti—Al alloy 101 of less than 40% by mass is obtained. The melting method illustrated in FIG. 2 uses a water-cooled copper container, but the melting method used in this titanium material addition / dissolution step is a melting method other than water-cooled copper induction melting (CCIM), such as a vacuum arc. A melting method (VAR) or vacuum induction melting (VIM) may be used.
Specifically, the titanium material added to the ingot in the titanium material addition / melting step is to obtain a Ti—Al alloy 101 having an Al content of less than 40 mass% after the titanium material addition / melting step. The titanium content is preferably less than 40% by mass. For example, if a titanium material with an Al content of less than 40% by mass, such as pure Ti that does not contain aluminum as an impurity, is added, the Al content contained in the ingot is reduced by dilution, so the Al content is 40% by mass. A Ti—Al alloy 101 that is less than 1% can be obtained.
 なお、チタン材料添加・溶解工程で添加されるチタン材料は、製造しようとするTi-Al系合金101の要求品質によって変化するため、チタン材料におけるアルミ以外の成分(Sn、V、Mnのようなアルミ以外の金属)の濃度は規定することはできず、任意に変更可能となっている。 The titanium material added in the titanium material addition / dissolution step varies depending on the required quality of the Ti—Al alloy 101 to be manufactured. Therefore, components other than aluminum (such as Sn, V, Mn, etc.) in the titanium material. The concentration of the metal other than aluminum cannot be specified and can be arbitrarily changed.
 また、本実施形態の製造方法においては、最終鋳塊高さH(最終目標鋳塊高さ)と、鋳塊直径Dとの比(H/D)は、特に限定はしないが、生産性の観点から1以上とするのが好ましい。 In the manufacturing method of the present embodiment, the ratio (H / D) between the final ingot height H (final target ingot height) and the ingot diameter D is not particularly limited. From the viewpoint, it is preferably 1 or more.
 上述した原料分割工程~フラックス層除去工程に加えてチタン材料添加・溶解工程を行えば、酸素やアルミ以外の組成についても要求品質に合致したTi-Al系合金101を得ることができ、本発明の製造方法の利便性をさらに高めることが可能となる。 If the titanium material addition / dissolution step is performed in addition to the above-described raw material splitting step to flux layer removal step, the Ti—Al alloy 101 that matches the required quality can be obtained for the composition other than oxygen and aluminum. The convenience of the manufacturing method can be further enhanced.
 次に、比較例及び実施例を用いて、本発明のTi-Al系合金の製造方法が有する作用効果について詳しく説明する。 Next, the effects of the method for producing a Ti—Al alloy of the present invention will be described in detail using comparative examples and examples.
(第1実施形態にかかる実施例)
 実施例及び比較例は、チタン材料にアルミ材料を混ぜ合わせて調整された合金材料Wに対して、CaO-CaFのフラックスαを添加して、合金材料W中に含まれるO(酸素)を脱酸したものである。
(Example according to the first embodiment)
In Examples and Comparative Examples, CaO—CaF 2 flux α is added to an alloy material W prepared by mixing an aluminum material with a titanium material, and O (oxygen) contained in the alloy material W is added. Deoxidized.
 なお、実施例1はAlを40質量%、Oを0.8質量%含む合金材料Wについて、1次鋳塊製造工程~チタン材料添加・溶解工程の処理を行ったものであり、実施例2は実施例1よりもAlの含有量が50質量%と大きく、Oを0.8質量%含む合金材料Wについて、1次鋳塊製造工程~チタン材料添加・溶解工程の処理を行ったものである。 In Example 1, the alloy material W containing 40% by mass of Al and 0.8% by mass of O was processed from the primary ingot manufacturing process to the titanium material adding / dissolving process. Is an alloy material W containing 50% by mass of Al and 0.8% by mass of O as compared with Example 1 and subjected to the treatment from the primary ingot manufacturing process to the titanium material addition / dissolution process. is there.
 また、比較例1及び比較例2は、本発明の製造方法を構成する4つの工程のうち、1次鋳塊製造工程の後、2次鋳塊製造工程及びフラックス層除去工程を行わずに、直接チタン材料添加・溶解工程を行ったものである。なお、比較例1は1次鋳塊製造工程後に発生が確認された介在物を除去せずにそのまま残したものであり、比較例2は介在物を極力除去したものである。 Moreover, the comparative example 1 and the comparative example 2 do not perform a secondary ingot manufacturing process and a flux layer removal process after a primary ingot manufacturing process among four processes which comprise the manufacturing method of this invention, The titanium material is directly added and dissolved. In Comparative Example 1, the inclusions that were confirmed to be generated after the primary ingot manufacturing step were left without being removed, and Comparative Example 2 was obtained by removing inclusions as much as possible.
 また、1次鋳塊製造工程は、スクラップTi、酸化チタン(TiO)、純Al、CaO-CaFを原料に、プラズマアーク溶解法により、中間素材(Ti-40,50質量%Al-0.8質量%O)を溶製する工程、2次鋳塊製造工程は、1次鋳塊製造工程で溶製した鋳塊を、プラズマアーク引抜溶解法により再溶解する工程、フラックス層除去工程は、2次鋳塊製造工程後の鋳塊表面に付着した(Al3含有)フラックス層を機械的に除去する工程、チタン材料添加・溶解工程は、1次鋳塊製造工程(比較例1、比較例2)または、1次鋳塊製造工程+2次鋳塊製造工程+フラックス層除去工程(実施例1、実施例2)で製造したTi-Al鋳塊に純Ti(O:0.05質量%含有)を添加して、プラズマアーク溶解法にて、Ti-30質量%Al鋳塊を溶製する工程である。 Further, the primary ingot manufacturing process, scrap Ti, titanium oxide (TiO 2), pure Al, the CaO-CaF 2 as a raw material by a plasma arc melting method, intermediate material (Ti-40, 50 wt% Al-0 .8 mass% O), the secondary ingot manufacturing step, the ingot manufactured in the primary ingot manufacturing step is remelted by the plasma arc drawing melting method, and the flux layer removing step is The step of mechanically removing the flux layer (containing Al 2 O 3 ) adhering to the ingot surface after the secondary ingot manufacturing step and the titanium material addition / dissolution step are the primary ingot manufacturing step (Comparative Example 1). Comparative Example 2) or Ti—Al ingot produced in the primary ingot production process + secondary ingot production process + flux layer removal process (Examples 1 and 2), pure Ti (O: 0. In a plasma arc melting method, A step of melting the -30 wt% Al ingot.
「比較例1」
 スクラップチタン及びルチル鉱石に含まれる酸化チタン(TiO)などのチタン材料に、純Alのアルミ材料を配合し、Ti中にAlが40質量%、Oが0.8質量%含まれたTi-Al系合金の合金材料を調整した。さらに、この合金材料に、CaO-CaFのフラックスを、Ti-Al系合金の総重量に対して5%の添加量となるように添加した。このようにしてフラックスが添加された合金材料を、100kWプラズマアーク炉で鋳造し、脱酸を行いつつ一次鋳塊を溶製した。
 なお、上述したCaO-CaFのフラックスは、CaOとCaFとの比率が重量比でCaO:CaF=2:8とされたものである。また、一次鋳塊の溶製に用いたプラズマアーク炉は、プラズマガスとしてArを用いたものであり、プラズマガスを圧力1.20×10Paで炉内に供給して、溶解を行ったものである。
"Comparative Example 1"
A titanium material such as titanium oxide (TiO 2 ) contained in scrap titanium and rutile ore is mixed with pure Al aluminum material, and Ti—40% by mass of Al and 0.8% by mass of O in Ti— An alloy material of an Al alloy was prepared. Further, a CaO—CaF 2 flux was added to this alloy material so that the addition amount was 5% with respect to the total weight of the Ti—Al alloy. Thus, the alloy material to which the flux was added was cast in a 100 kW plasma arc furnace, and the primary ingot was melted while performing deoxidation.
Note that the flux of CaO-CaF 2 described above, CaO ratio of CaO and CaF 2 are in a weight ratio: in which is an 8: CaF 2 = 2. Further, the plasma arc furnace used for melting the primary ingot was one using Ar as the plasma gas, and the plasma gas was supplied into the furnace at a pressure of 1.20 × 10 5 Pa to perform melting. Is.
 また、この比較例1では、1次鋳塊製造工程の後、直接チタン材料添加・溶解工程を行って、Ti-Al系合金を溶製している。つまり、比較例1では、無底の水冷銅鋳型を用いた溶解法により1次鋳塊を溶解しつつ連続的に下方に引抜く2次鋳塊製造工程は行っていないため、1次鋳塊内部にAlやフラックスが巻き込まれて残留しており、フラックス層除去工程を実施していない。 In Comparative Example 1, a Ti-Al alloy is melted by directly adding and melting a titanium material after the primary ingot manufacturing process. That is, in Comparative Example 1, the primary ingot is not subjected to the secondary ingot manufacturing process in which the primary ingot is continuously drawn while being melted by a melting method using a bottomless water-cooled copper mold. internal and remains from entrapment as Al 2 O 3 or flux, not performed the flux layer removing step.
 1次鋳塊製造工程後の鋳塊の切断を行い、切断面をSEMにて観察し、鋳塊の内部組織を観察した。SEMによる断面観察の結果、比較例1の鋳塊の内部には、フラックスやAl3等の酸化物系介在物が存在する部位が確認されると共に、フラックスやAl等の介在物が存在しない部位も確認された。介在物の確認がされた部分と、介在物の確認されなかった部分との双方に対して、不活性ガス溶融法により酸素濃度を計測したところ、表1に示すように、介在物が確認された位置では酸素濃度が1.82質量%、介在物が確認されなかった位置では酸素濃度が0.24質量%となっていた。このことからSEM観察で確認された介在物は、フラックスやAl等の介在物であることがわかる。 The ingot after the primary ingot manufacturing process was cut, the cut surface was observed with an SEM, and the internal structure of the ingot was observed. Result of section observation by SEM, in the interior of the ingot in Comparative Example 1, with portions oxide inclusions such as flux, Al 2 O 3, or the there is confirmed, interposed such flux, Al 2 O 3, or the Sites where no objects exist were also confirmed. When the oxygen concentration was measured by the inert gas melting method for both the portion where the inclusion was confirmed and the portion where the inclusion was not confirmed, the inclusion was confirmed as shown in Table 1. At the position where the oxygen concentration was 1.82% by mass, and at the position where no inclusion was confirmed, the oxygen concentration was 0.24% by mass. From this, it can be seen that the inclusions confirmed by SEM observation are inclusions such as flux and Al 2 O 3 .
 また、1次鋳塊製造工程後の鋳塊に対して、さらに酸素が0.05質量%含まれたチタン材料(純Ti)を添加し、Alの含有量が30質量%となるように溶製すると、酸素濃度が0.79質量%のTi-Al系合金が得られた。このチタン材料添加・溶解工程後のTi-Al系合金の断面観察をSEMで行うと、1次鋳塊製造工程後には観察されていた酸化物系介在物が確認されなかった。 In addition, a titanium material (pure Ti) containing 0.05% by mass of oxygen is added to the ingot after the primary ingot manufacturing process, so that the Al content becomes 30% by mass. As a result, a Ti—Al alloy having an oxygen concentration of 0.79% by mass was obtained. When the cross-sectional observation of the Ti—Al based alloy after the titanium material addition / melting step was performed by SEM, the oxide inclusions observed after the primary ingot manufacturing step were not confirmed.
 このことから、比較例1に示すように、フラックス層除去工程後に酸化物系介在物が残った合金材料に対して、チタン材料添加・溶解工程で純Ti(Oが0.05質量%含まれたチタン材料)を加えると、Al等の酸化物が分解されて溶湯中に再溶解し、酸素濃度がかえって上昇してしまうことがわかる。 From this, as shown in Comparative Example 1, pure Ti (0.05% by mass of O is contained in the titanium material addition / dissolution step with respect to the alloy material in which oxide inclusions remain after the flux layer removal step. When the titanium material is added, oxides such as Al 2 O 3 are decomposed and redissolved in the molten metal, and the oxygen concentration is increased.
「比較例2」
 上述した比較例1に対し、比較例2は、1次鋳塊製造工程後に確認された酸化物系介在物を含むTi-Al合金領域を機械的に除去したものとなっている。つまり、介在物の除去によりTi-Al系合金中から酸素が除去されているため、Alの含有量が30質量%となるように溶製した場合には、比較例2の酸素含有量は比較例1よりも酸素含有量が小さい0.21質量%となる。しかし、この酸化物系介在物の除去の際には、鋳塊に含まれる介在物だけでなくメタル(Ti-Al系合金)も失われることになる。そのため、合金材料のうち、どの程度の割合がTi-Al系合金となったかを示す「中間素材使用量」、言い換えれば「歩留」は、比較例1の半分程度である50%となっている。
"Comparative Example 2"
In contrast to Comparative Example 1 described above, Comparative Example 2 is obtained by mechanically removing the Ti—Al alloy region containing oxide inclusions that was confirmed after the primary ingot manufacturing process. That is, since oxygen is removed from the Ti—Al based alloy by removing inclusions, the oxygen content of Comparative Example 2 is comparative when the Al content is 30% by mass. The oxygen content is 0.21% by mass, which is smaller than in Example 1. However, when removing the oxide inclusions, not only the inclusions contained in the ingot but also the metal (Ti—Al alloy) is lost. Therefore, the “intermediate material use amount” indicating how much of the alloy material has become a Ti—Al alloy, in other words, “yield” is 50%, which is about half of Comparative Example 1. Yes.
「実施例1」
 上述した比較例1及び比較例2に対し、実施例1は、比較例1及び比較例2と同じ原料を配合して合金材料Wを調整し、さらにこの合金材料WにCaO-CaFのフラックスα(CaO:CaF=2:8重量比)を添加して1次鋳塊Xを溶製したものである。この1次鋳塊Xを溶製する際の処理条件も、100kWプラズマアーク炉を用い、圧力は1.20×10Paで溶解を行うものであり、比較例と同じである。
"Example 1"
In contrast to Comparative Example 1 and Comparative Example 2 described above, Example 1 is prepared by mixing the same raw materials as Comparative Example 1 and Comparative Example 2 to adjust the alloy material W, and further adding CaO—CaF 2 flux to the alloy material W. The primary ingot X is melted by adding α (CaO: CaF 2 = 2: 8 weight ratio). The processing conditions for melting the primary ingot X are also the same as in the comparative example, using a 100 kW plasma arc furnace and melting at a pressure of 1.20 × 10 5 Pa.
 実施例1が比較例と異なっているのは、比較例ではなかった天地反転と再溶解を3回に亘って繰り返し行っている点である。 Example 1 differs from the comparative example in that the upside down and remelting, which was not the comparative example, is repeated three times.
 つまり、比較例1及び比較例2と同様に、1次鋳塊製造工程の後に、介在物が確認される部位と、介在物が確認されない部位との双方に対して、それぞれの部位の(トータルでの)酸素濃度を不活性ガス融解法にて分析すると、介在物が未確認の部位については酸素濃度が0.19質量%、介在物が確認された部位(介在物が残留している部位)については酸素濃度が1.90質量%となった。これは、1次鋳塊製造工程で天地反転と再溶解を繰り返し3回実施したことにより、AlとCaO-CaF系のフラックスαの反応がより進行し、脱酸反応が促進されたためであると推測される。 That is, as in Comparative Example 1 and Comparative Example 2, after the primary ingot manufacturing process, each of the parts (total) for both the part where the inclusion is confirmed and the part where the inclusion is not confirmed. When the oxygen concentration is analyzed by an inert gas melting method, the oxygen concentration is 0.19% by mass for the site where the inclusion is not confirmed, and the site where the inclusion is confirmed (the site where the inclusion remains) The oxygen concentration was 1.90% by mass. This is because the top and bottom reversal and remelting were repeated three times in the primary ingot manufacturing process, and the reaction of Al 2 O 3 and CaO—CaF 2 flux α progressed further, and the deoxidation reaction was promoted. This is presumed to be due to this.
 このようにして1次鋳塊製造工程で溶製された1次鋳塊Xに対して、プラズマアークを熱源とする溶解法にて鋳塊を下方に引き抜きつつ、2次鋳塊Yを溶製した。
 図3に示すように、この2次鋳塊Yの表面には、Alを含有したCaO-CaF系のフラックスαが排出されて付着していた。一方、2次鋳塊Yの内部には、殆ど酸化物系介在物は存在しておらず、内部に不均一に存在していた介在物の大部分は、鋳塊表面に排出されていることが分かった。
For the primary ingot X melted in the primary ingot manufacturing step in this way, the secondary ingot Y is melted while being drawn downward by a melting method using a plasma arc as a heat source. did.
As shown in FIG. 3, CaO—CaF 2 -based flux α containing Al 2 O 3 was discharged and adhered to the surface of the secondary ingot Y. On the other hand, there are almost no oxide inclusions inside the secondary ingot Y, and most of the inclusions that were unevenly present inside are discharged to the ingot surface. I understood.
 この2次鋳塊Yに対して、フラックス層除去工程でショットブラスト(機械的手段3)を行って、2次鋳塊Yの表面のフラックス層βを除去した。フラックス層βが除去された鋳塊に、チタン材料添加・溶解工程としてさらに純Ti(酸素濃度0.05質量%)を添加して、Ti-30質量%Al合金Z2を溶製し酸素濃度を分析した。 The secondary ingot Y was subjected to shot blasting (mechanical means 3) in the flux layer removing step to remove the flux layer β on the surface of the secondary ingot Y. To the ingot from which the flux layer β has been removed, pure Ti (oxygen concentration 0.05 mass%) is further added as a titanium material addition / dissolution step, and Ti-30 mass% Al alloy Z2 is melted to reduce the oxygen concentration. analyzed.
 分析の結果、チタン材料添加・溶解工程を行った後のTi-Al系合金Z2中には酸素が0.16質量%含まれていることがわかった。合金の内部組織には、酸化物系介在物が殆ど存在していなかったことから、比較例1のようにフラックスの再溶解による酸素濃度の上昇が起きていないことがわかる。また、フラックス層除去工程でフラックスのみを効率的に除去しているため、比較例2のように歩留低下を招くことも無い。それゆえ、実施例1のような手順で脱酸を行えば、低品位なチタン原料を用いても、Al含有量が40質量%未満となるような高品位で低酸素なTi-Al系合金Z2を製造することが可能であると判断される。 As a result of analysis, it was found that 0.16% by mass of oxygen was contained in the Ti—Al-based alloy Z2 after the titanium material addition / dissolution step. Since almost no oxide inclusions were present in the internal structure of the alloy, it can be understood that the oxygen concentration did not increase due to remelting of the flux as in Comparative Example 1. Further, since only the flux is efficiently removed in the flux layer removing step, the yield is not reduced as in Comparative Example 2. Therefore, if deoxidation is performed according to the procedure as in Example 1, even if a low-grade titanium raw material is used, a high-grade, low-oxygen Ti—Al-based alloy that results in an Al content of less than 40% by mass. It is determined that Z2 can be manufactured.
「実施例2」
 なお、上述した実施例1で得られたような知見は、実施例1よりもAl含有量が50質量%と高い実施例2の合金材料Wに対しても得ることができる。
"Example 2"
In addition, the knowledge as obtained in Example 1 described above can also be obtained for the alloy material W of Example 2 in which the Al content is 50 mass% higher than in Example 1.
 つまり、表1に示すように、合金材料Wの組成がTi-50質量%Al-0.8質量%Oとされた場合でも、Ti-30質量%Al合金を溶製すれば、酸素濃度が0.07質量%のTi-Al系合金Z2を製造することが可能である。 That is, as shown in Table 1, even when the composition of the alloy material W is Ti-50 mass% Al-0.8 mass% O, if the Ti-30 mass% Al alloy is melted, the oxygen concentration is reduced. It is possible to produce a 0.07 mass% Ti—Al-based alloy Z2.
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
(第2実施形態にかかる実施例)
 実施例及び比較例は、チタン材料にアルミ材料を混ぜ合わせて調整された合金材料に対して、CaO-CaFのフラックス103を添加して、合金材料中に含まれるO(酸素)を脱酸したものである。
(Example according to the second embodiment)
In Examples and Comparative Examples, CaO—CaF 2 flux 103 is added to an alloy material prepared by mixing an aluminum material with a titanium material to deoxidize O (oxygen) contained in the alloy material. It is a thing.
 なお、実施例1はAlを40質量%、Oを0.8質量%含む合金材料について、原料分割工程~チタン材料添加・溶解工程の処理を行ったものである。また、実施例2はAlを60質量%、Oを0.8質量%含む合金材料について、原料分割工程~チタン材料添加・溶解工程の処理を行ったものである。実施例3はAlを45質量%、Oを0.8質量%含む合金材料について、原料分割工程~チタン材料添加・溶解工程の処理を行ったものである。実施例4はAlを52質量%、Oを0.8質量%含む合金材料について、原料分割工程~チタン材料添加・溶解工程の処理を行ったものである。 In Example 1, the alloy material containing 40% by mass of Al and 0.8% by mass of O was processed from the raw material dividing step to the titanium material adding / dissolving step. In Example 2, the alloy material containing 60% by mass of Al and 0.8% by mass of O was processed from the raw material dividing step to the titanium material adding / dissolving step. In Example 3, the alloy material containing 45% by mass of Al and 0.8% by mass of O was subjected to the raw material dividing step to the titanium material adding / dissolving step. In Example 4, the alloy material containing 52% by mass of Al and 0.8% by mass of O is subjected to the raw material dividing step to the titanium material adding / dissolving step.
 なお、実施例1~4の溶解原料2の分割数は「11」であり、第1分割体141~第11分割体(図示せず)のそれぞれに対して、1回の溶解操作と1回の引き下げ操作とで構成された「基本操作」を行っている。 The number of divisions of the melting raw material 2 in Examples 1 to 4 is “11”, and one melting operation and one time are performed for each of the first divided body 141 to the eleventh divided body (not shown). The "basic operation" consists of a pull-down operation.
 また、比較例1は、実施例1と同じ組成の合金材料を用いたものであるが、原料分割工程の際に溶解原料102の分割を行わず、分割体ベース鋳塊製造工程で溶解操作だけを行って鋳塊を得たものとなっている。比較例1では、得られた鋳塊に対して、さらにチタン材料添加・溶解工程を行って、Ti-30Alの鋳塊を得たものとなっている。 Further, Comparative Example 1 uses an alloy material having the same composition as Example 1, but the melting raw material 102 is not divided during the raw material dividing step, and only the melting operation is performed in the divided body base ingot manufacturing step. The ingot is obtained by performing. In Comparative Example 1, the obtained ingot was further subjected to a titanium material addition / dissolution step to obtain a Ti-30Al ingot.
 さらに、比較例2は、比較例1と同じ処理を行って鋳塊を得たものであり、得られた鋳塊の特定部位のみを用いてチタン材料添加・溶解工程を行ったものである。 Furthermore, Comparative Example 2 was obtained by performing the same process as Comparative Example 1 to obtain an ingot, and the titanium material addition / dissolution step was performed using only a specific part of the obtained ingot.
 さらに、比較例3は、実施例1と同様に、Alを40質量%、Oを0.8質量%含む合金材料について、原料分割工程~チタン材料添加・溶解工程の処理を行ったものである。比較例3が実施例1と異なるのは溶解原料102にフラックス103を配合していない点である。 Further, in Comparative Example 3, as in Example 1, the alloy material containing 40% by mass of Al and 0.8% by mass of O was processed from the raw material dividing step to the titanium material adding / dissolving step. . Comparative Example 3 is different from Example 1 in that the flux 103 is not blended with the melting raw material 102.
 具体的には、上述した原料分割工程~チタン材料添加・溶解工程は、以下のような条件で実施した。 Specifically, the above-described raw material dividing step to titanium material addition / dissolution step were performed under the following conditions.
 まず、原料分割工程は、スクラップTi、酸化チタン(TiO)、純Alを合金材料とし、比較例1、比較例2、実施例1についてはCaO-CaF系のフラックス103をTi-Al系合金101の重量に対して10%配合して、比較例3についてはフラックス103を配合せずに、溶解原料102を作製した。これらの比較例及び実施例に用いるフラックス103は、CaO:CaF=2:8重量比となるようにCaOとCaFとを含むフラックス103(CaO-CaF系のフラックス103)である。 First, in the raw material dividing step, scrap Ti, titanium oxide (TiO 2 ), and pure Al are used as alloy materials. For Comparative Example 1, Comparative Example 2, and Example 1, a CaO—CaF 2 flux 103 is used as a Ti—Al system. 10% of the weight of the alloy 101 was blended, and in Comparative Example 3, the melting raw material 102 was produced without blending the flux 103. The flux 103 used in these comparative examples and examples is a flux 103 (CaO—CaF 2 -based flux 103) containing CaO and CaF 2 so that the CaO: CaF 2 = 2: 8 weight ratio.
 また、分割体ベース鋳塊製造工程は、底がない(無底の)水冷銅るつぼ105(内径80mm)中に原料分割工程で調製した溶解原料102を装入し、不活性ガスであるアルゴンを用いたAr雰囲気下で、圧力が6.6×10Paとされた条件下で誘導溶解装置を用いて溶解した。なお、実施例1~4及び比較例3の分割体ベース鋳塊製造工程では、原料分割工程で溶解原料102を11分割して第1分割体141~第11分割体(図示せず)を予め形成しておき、溶解操作と引き下げ操作とをそれぞれの分割体に対して1回ずつ行い、溶解原料102を溶解させて脱酸を進行させた。また、比較例1及び比較例2については、上述したように分割体ベース鋳塊製造工程自体を実施していない。 Further, in the split body base ingot manufacturing process, the melted raw material 102 prepared in the raw material splitting process is charged into a water-cooled copper crucible 105 (inner diameter 80 mm) having no bottom, and argon as an inert gas is introduced. It melt | dissolved using the induction dissolving apparatus on the conditions made into the pressure of 6.6 * 10 < 4 > Pa under Ar atmosphere used. In the divided body base ingot manufacturing process of Examples 1 to 4 and Comparative Example 3, the melting raw material 102 is divided into 11 parts in the raw material dividing process, and the first divided body 141 to the 11th divided body (not shown) are preliminarily formed. After the formation, the dissolution operation and the pull-down operation were performed once for each of the divided bodies, and the dissolution raw material 102 was dissolved to proceed with deoxidation. Moreover, about the comparative example 1 and the comparative example 2, as above-mentioned, the division body base ingot manufacturing process itself is not implemented.
 このようにして分割体ベース鋳塊製造工程で鋳造された鋳塊については、溶製後の鋳塊内部をSEMにて観察した。 For the ingot cast in the divided body base ingot manufacturing process in this way, the inside of the ingot after melting was observed with an SEM.
 また、フラックス層除去工程では、分割体ベース鋳塊製造工程で鋳造された鋳塊について、鋳塊の表面に対して機械的手段としてショットブラストを行い、鋳塊の表面に付着した表面付着フラックス層108を除去した。フラックス層除去工程で表面付着フラックス層108が除去された鋳塊については、鋳塊中に含まれる酸素濃度を不活性ガス融解法にて分析した。 In addition, in the flux layer removing step, the surface-attached flux layer adhered to the surface of the ingot by performing shot blasting as a mechanical means on the surface of the ingot with respect to the ingot cast in the divided body base ingot manufacturing step 108 was removed. About the ingot from which the surface adhesion flux layer 108 was removed in the flux layer removing step, the oxygen concentration contained in the ingot was analyzed by an inert gas melting method.
 さらに、チタン材料添加・溶解工程では、フラックス層除去工程で表面付着フラックス層108が除去された鋳塊について、プラズマアーク溶解炉を用いて、酸素濃度が0.05質量%の純Tiを添加し、Ti-30質量%Al合金を溶製した。チタン材料添加・溶解工程で溶製されたTi-30質量%Al合金の鋳塊についても、フラックス層除去工程後の鋳塊と同様に酸素濃度を不活性ガス融解法にて分析した。 Further, in the titanium material addition / melting step, pure Ti having an oxygen concentration of 0.05 mass% is added to the ingot from which the surface adhering flux layer 108 has been removed in the flux layer removing step using a plasma arc melting furnace. Ti-30 mass% Al alloy was melted. As for the ingot of the Ti-30 mass% Al alloy produced in the titanium material addition / dissolution step, the oxygen concentration was analyzed by an inert gas melting method in the same manner as the ingot after the flux layer removal step.
 実施例及び比較例の分析結果を表2に示す。 Table 2 shows the analysis results of Examples and Comparative Examples.
Figure JPOXMLDOC01-appb-T000002
Figure JPOXMLDOC01-appb-T000002
「比較例1」
 比較例1は、上述したように原料分割工程で溶解原料102の分割を行わず、分割体ベース鋳塊製造工程では分割されていない溶解原料102に対して引き下げ操作を伴わない溶解操作のみを行って、鋳塊を得たものである。
"Comparative Example 1"
In Comparative Example 1, as described above, the melting raw material 102 is not divided in the raw material dividing step, and only the melting operation without the pulling-down operation is performed on the molten raw material 102 that is not divided in the divided body base ingot manufacturing process. Thus, an ingot is obtained.
 比較例1で得られた鋳塊を、分割体ベース鋳塊製造工程後に取り出して目視すると、鋳塊の表面には表面付着フラックス層108が形成されていた。また、比較例1においては、合金組織の内部に巻込まれているフラックス103も目視で確認できた。 When the ingot obtained in Comparative Example 1 was taken out after the divided body base ingot manufacturing process and visually observed, a surface adhesion flux layer 108 was formed on the surface of the ingot. Moreover, in the comparative example 1, the flux 103 currently wound inside the alloy structure was also confirmed visually.
 また、「比較例1」の鋳塊については、鋳塊内部に対するSEM観察も行っている。SEMによって観察したところ、鋳塊内部に、Al3やフラックス103が存在しない部位と、フラックス103が存在する部位とが、混在していることが確認された。 Moreover, about the ingot of "Comparative example 1," the SEM observation with respect to the inside of an ingot is also performed. Was observed by SEM, the inner ingot, a portion as Al 2 O 3 and flux 103 does not exist, and the site where the flux 103 is present, it was confirmed that a mixture.
 さらに、得られた鋳塊について酸素濃度を不活性ガス融解法にて分析した結果、介在物が存在していない部位には酸素が0.50質量%、介在物が存在している部位には酸素が1.16質量%検出された。 Further, as a result of analyzing the oxygen concentration of the obtained ingot by an inert gas melting method, oxygen was 0.50% by mass in a site where no inclusion was present, and in a site where an inclusion was present 1.16% by mass of oxygen was detected.
 さらに、上述した鋳塊をチタン材料添加・溶解工程でプラズマアーク溶解炉を用いて溶解し、上記鋳塊に純Ti(酸素濃度0.05質量%)を添加してTi-30質量%Al合金を溶製して、得られたTi-30質量%Al合金の鋳塊の酸素濃度を不活性ガス融解法で分析した。分析の結果、酸素が0.79質量%検出された。さらにまた、Ti-30質量%Al合金の鋳塊の内部をSEMにて観察すると、Al等の酸化物介在物の存在は確認されなかった。 Further, the ingot described above is melted using a plasma arc melting furnace in the titanium material addition / melting step, and pure Ti (oxygen concentration 0.05 mass%) is added to the ingot to obtain a Ti-30 mass% Al alloy. The oxygen concentration of the resulting Ti-30 mass% Al alloy ingot was analyzed by an inert gas melting method. As a result of the analysis, 0.79% by mass of oxygen was detected. Furthermore, when the inside of an ingot of Ti-30 mass% Al alloy was observed with an SEM, the presence of oxide inclusions such as Al 2 O 3 was not confirmed.
 上述した目視検査及びSEM観察の結果から、比較例1では、得られた鋳塊にフラックス103及び酸化物系介在物(非金属系介在物)が残り、このフラックス103及び酸化物系介在物が鋳塊内部にまで残っていると判断され、Ti-Al系合金101中の酸素を十分に低減できていないことがわかる。 From the results of the visual inspection and SEM observation described above, in Comparative Example 1, the flux 103 and oxide inclusions (non-metallic inclusions) remain in the obtained ingot, and the flux 103 and oxide inclusions are present. It is judged that the inside of the ingot remains, and it can be seen that oxygen in the Ti—Al alloy 101 cannot be sufficiently reduced.
 また、比較例のTi-Al系合金101中の酸素濃度を計測すると、介在物の有無にかかわらず0.1質量%を大きく上回る酸素が検出されており、酸素濃度からもTi-Al系合金101中から酸素を十分に低減できていないことがわかった。 Further, when the oxygen concentration in the Ti—Al based alloy 101 of the comparative example was measured, oxygen greatly exceeding 0.1 mass% was detected regardless of the presence or absence of inclusions, and the Ti—Al based alloy was also detected from the oxygen concentration. It turned out that oxygen was not fully reduced out of 101.
 さらに、一度溶製した鋳塊をチタン材料添加・溶解工程で再溶解させると、介在物が存在していない部分では酸素濃度が0.50質量%から0.79質量%に上昇した。これは、チタン材料添加・溶解工程で鋳塊に純Ti110を添加して成分調整を行うと、鋳塊中に残されていた酸化物系介在物が純Tiにより分解してTi-Al中に再溶解し、酸素濃度が上昇してしまったものと考えられる。 Furthermore, when the ingot once melted was redissolved in the titanium material addition / dissolution step, the oxygen concentration increased from 0.50% by mass to 0.79% by mass in the portion where no inclusion was present. This is because, when pure Ti110 is added to the ingot in the titanium material addition / melting step and the components are adjusted, the oxide inclusions remaining in the ingot are decomposed by pure Ti and become Ti-Al. It is considered that the oxygen concentration has increased due to re-dissolution.
「比較例2」
 比較例2は、比較例1と同様の溶解原料102、溶解方法にて鋳塊を溶製したものである。そのため、溶製した鋳塊の介在物が存在していない部位の酸素濃度は0.51質量%であり、介在物が存在している部位は1.12質量%となっている。この比較例2の鋳塊のうち、介在物が存在していない部位を選んで、プラズマアーク溶解炉を用いて溶解し、純Ti110(酸素濃度0.05質量%)を添加してTi-30質量%Al合金の鋳塊を溶製した。溶製した鋳塊について酸素濃度を分析した結果、酸素濃度は0.42質量%と比較例1よりも低下した結果となった。
"Comparative Example 2"
In Comparative Example 2, the ingot is melted by the same melting raw material 102 and melting method as in Comparative Example 1. Therefore, the oxygen concentration of the site where the melted ingot inclusions are not present is 0.51% by mass, and the site where the inclusions are present is 1.12% by mass. Of the ingot of Comparative Example 2, a portion where no inclusions were present was selected and melted using a plasma arc melting furnace, and pure Ti110 (oxygen concentration 0.05 mass%) was added to obtain Ti-30. An ingot of mass% Al alloy was melted. As a result of analyzing the oxygen concentration of the molten ingot, the oxygen concentration was 0.42% by mass, which was lower than that of Comparative Example 1.
 このことから、比較例1と異なり、Al等の介在物がほとんど確認されなかった部位を使用してチタン材料添加・溶解工程を行うと、鋳塊に含まれていたAl等の酸化物系介在物の分解に伴う酸素濃度上昇は抑えられることがわかる。しかし、介在物が存在する部位は再溶解の原料としては使用できないため、表1の「歩留」の評価は比較例1が○であるのに対し、×の評価結果となっている。このことから、比較例2では、鋳塊に含まれる酸素濃度は低下できるものの、歩留が悪いという結果となり、総合的な評価は×となっている。 Therefore, unlike the Comparative Example 1, when a titanium material adding and dissolving step using site inclusions of Al 2 O 3 or the like was not almost observed, Al 2 O 3 contained in the ingot It can be seen that an increase in oxygen concentration due to the decomposition of oxide inclusions such as is suppressed. However, since the site where inclusions are present cannot be used as a raw material for redissolution, the evaluation of “yield” in Table 1 is an evaluation result of “x” while Comparative Example 1 is “good”. From this, in Comparative Example 2, although the oxygen concentration contained in the ingot can be reduced, the yield is poor, and the overall evaluation is x.
「比較例3」
 比較例1及び比較例2と同様に、Ti-40質量%Al-0.8質量%Oとなるように、溶解原料102を調製し、鋳塊(2800g)を溶製した。なお、比較例3の溶解原料102は、比較例1及び比較例2と異なり、原料分割工程で合金材料にフラックス103を配合せずに溶解原料102を作製したものであり、また溶解原料102を11個に分割したものとなっている。具体的には、最初に水冷銅るつぼ105に装入する第1分割体141は原料重量が800g(フラックス103は除く)であり、それ以降に追加装入する第2分割体142~第11分割体151は原料重量がいずれも200gとされている。この第1分割体141の原料(800g)を、純Ti製のスターティングブロック(水冷銅るつぼ105の底部107)上に装入し、Ar雰囲気下で、圧力が6.6×10Paのるつぼ内で溶解した。第1分割体141が溶解した後、るつぼの底部107を毎分2mmの速度で5分間(10mm)引き下げて引き下げ操作を実施した。その後、追加装入原料フィーダーに予め装入していた第2以降の分割体の追加原料(200g)を水冷銅るつぼ105内に装入して溶解し、溶解後にるつぼの底部107を引き下げる操作を、第2分割体142~第11分割体151の全てに対して行って、鋳塊を溶製した。
“Comparative Example 3”
In the same manner as in Comparative Example 1 and Comparative Example 2, the melting raw material 102 was prepared so as to be Ti-40 mass% Al-0.8 mass% O, and an ingot (2800 g) was melted. Unlike the comparative example 1 and the comparative example 2, the melting raw material 102 of the comparative example 3 was prepared by dissolving the raw material 102 without adding the flux 103 to the alloy material in the raw material dividing step. It is divided into 11 pieces. Specifically, the first divided body 141 initially charged in the water-cooled copper crucible 105 has a raw material weight of 800 g (excluding the flux 103), and thereafter the second divided body 142 to the eleventh divided portion to be additionally charged. The body 151 has a raw material weight of 200 g. The raw material (800 g) of the first divided body 141 was charged on a starting block made of pure Ti (the bottom 107 of the water-cooled copper crucible 105), and the pressure was 6.6 × 10 4 Pa in an Ar atmosphere. Dissolved in the crucible. After the 1st division body 141 melt | dissolved, the bottom part 107 of the crucible was pulled down for 5 minutes (10 mm) at the speed | rate of 2 mm / min, and the pulling-down operation was implemented. Thereafter, an additional raw material (200 g) of the second and subsequent divided bodies charged in advance in the additional charged raw material feeder is charged into the water-cooled copper crucible 105 and melted, and the bottom 107 of the crucible is lowered after melting. The ingots were melted by performing the process on all of the second divided body 142 to the eleventh divided body 151.
 溶製後の比較例3の鋳塊内部をSEMにて観察した結果、比較例1や比較例2と同様に、非金属介在物のAlが殆ど存在していない部位と存在している部位とが内部組織にあることが分かった。また、鋳塊の酸素濃度を不活性ガス融解法にて分析した結果、非金属介在物が殆ど存在していない部位の酸素濃度は0.75質量%となり、非金属介在物が存在している部位の酸素濃度は0.94質量%となった。このことから、フラックス103を用いずに溶解及び脱酸を行った場合には、Ti-Al中の非金属介在物であるAlは鋳塊表面に殆ど移行せず、鋳塊内に留まってしまっているため、原料分割工程で溶解原料102の分割を行っていても、酸素濃度は殆ど低減できていないことがわかる。 Result of observation of the ingot inside of Comparative Example 3 by SEM after melting, in the same manner as in Comparative Example 1 and Comparative Example 2, the existence and the site of Al 2 O 3 of nonmetallic inclusions does not almost exist It was found that the internal part is in the internal tissue. In addition, as a result of analyzing the oxygen concentration of the ingot by the inert gas melting method, the oxygen concentration in the portion where almost no non-metallic inclusions are present is 0.75% by mass, and non-metallic inclusions are present. The oxygen concentration at the site was 0.94% by mass. Therefore, when dissolution and deoxidation are performed without using the flux 103, Al 2 O 3 which is a non-metallic inclusion in Ti—Al hardly migrates to the ingot surface, and does not enter the ingot. Since it has remained, it can be seen that even when the dissolved raw material 102 is divided in the raw material dividing step, the oxygen concentration is hardly reduced.
 また、上述した比較例3の鋳塊に対して、プラズマアーク溶解炉を用いて、純Ti110(酸素濃度0.05質量%)を添加しTi-30質量%Al合金を溶製してTi-30質量%Al合金の鋳塊を鋳造し、Ti-30質量%Al合金の鋳塊の酸素濃度を分析すると0.60質量%という結果が得られた。このことから、比較例1と同様に、酸化物系介在物が鋳塊内部にまで残っている鋳塊に対して純Tiを添加して成分調整を行っても、鋳塊中に残されていた酸化物系介在物が純Tiにより分解してTi-Al中の酸素濃度が上昇するため、Ti-Al系合金101中の酸素を十分に低減できないと判断される。 In addition, pure Ti110 (oxygen concentration 0.05 mass%) was added to the ingot of Comparative Example 3 described above using a plasma arc melting furnace, and a Ti-30 mass% Al alloy was melted to produce Ti— A 30% by mass Al alloy ingot was cast and the oxygen concentration of the Ti-30% by mass Al alloy ingot was analyzed. As a result, a result of 0.60% by mass was obtained. From this, as in Comparative Example 1, even if the oxide inclusions remain in the ingot and the pure Ti is added to adjust the components, the oxide inclusions remain in the ingot. Since the oxide inclusions are decomposed by pure Ti and the oxygen concentration in Ti—Al increases, it is determined that the oxygen in the Ti—Al alloy 101 cannot be sufficiently reduced.
「実施例1」
 実施例1は、比較例3と同様に溶解原料102を11個に分割し鋳塊を溶製したものである。実施例1が比較例3と異なるのは、フラックス103をTi-Al系合金101の重量に対して10質量%配合していることである。
"Example 1"
In Example 1, as in Comparative Example 3, the melting raw material 102 was divided into 11 pieces and the ingot was melted. The difference between Example 1 and Comparative Example 3 is that 10% by mass of the flux 103 is blended with respect to the weight of the Ti—Al alloy 101.
 溶解操作終了後に取り出した鋳塊表面を目視で確認すると、添加したフラックス103が溶解/凝固して形成されたと思われる層(表面付着フラックス層108)が鋳塊の表面に付着していた。同様な鋳塊内部をSEMにて観察すると、鋳塊内部には殆どAl等の非金属介在物(酸化物系介在物)は存在していないことが分かった。これは、鋳塊表面に形成されたフラックス層にAl等の非金属介在物が移行したことによるものと推測された。 When the surface of the ingot taken out after completion of the melting operation was visually confirmed, a layer (surface adhesion flux layer 108) that seems to have been formed by melting / solidifying the added flux 103 was adhered to the surface of the ingot. Observation under the same ingot inside a SEM, most of Al 2 O 3 or the like non-metallic inclusions inside the ingot (oxide inclusions) was found not to exist. This was presumed to be due to the transfer of non-metallic inclusions such as Al 2 O 3 to the flux layer formed on the ingot surface.
 また、この鋳塊表面のフラックス層(表面付着フラックス層108)は、ショットブラストにより、容易に除去することができた。ショットブラストにより表面付着フラックス層108が除去された鋳塊の酸素濃度を不活性ガス融解法にて分析した結果、Alが存在していない部位の酸素濃度は0.30質量%であり、わずかにAl等の酸化物系介在物が確認された部位でも酸素濃度は0.40質量%と非常に少なかった。このことから、原料分割工程でフラックス103を配合すると共に溶解原料102を分割し、分割体ベース鋳塊製造工程で分割体ごとに溶解操作と引き下げ操作とを繰り返し行った実施例1では、鋳塊中の酸素濃度を大きく低減できることがわかる。 Further, the flux layer on the surface of the ingot (surface-adhered flux layer 108) could be easily removed by shot blasting. As a result of analyzing the oxygen concentration of the ingot from which the surface adhering flux layer 108 has been removed by shot blasting using an inert gas melting method, the oxygen concentration in the portion where Al 2 O 3 does not exist is 0.30% by mass. Even at a site where oxide inclusions such as Al 2 O 3 were slightly observed, the oxygen concentration was as very low as 0.40% by mass. Therefore, in Example 1 in which the flux 103 was blended in the raw material dividing step and the melting raw material 102 was divided, and the melting operation and the lowering operation were repeated for each divided body in the divided body base ingot manufacturing step. It can be seen that the oxygen concentration inside can be greatly reduced.
 また、上述した実施例1の鋳塊についてプラズマアーク溶解炉を用いて溶解しつつ、純Ti110(酸素濃度0.05質量%)を添加してTi-30質量%Al合金の鋳塊を溶製すると、Ti-30質量%Al合金の鋳塊の酸素濃度は0.25質量%にまで低下した。 Further, while melting the ingot of Example 1 described above using a plasma arc melting furnace, pure Ti110 (oxygen concentration 0.05 mass%) was added to melt an ingot of Ti-30 mass% Al alloy. Then, the oxygen concentration in the ingot of the Ti-30 mass% Al alloy was reduced to 0.25 mass%.
 このことから、実施例1のチタン材料添加・溶解工程では、比較例1~比較例3とは異なり、鋳塊中に酸化物系介在物がほとんど存在していなかったため、再溶解しても酸素濃度が上昇しておらず、また歩留低下も無いことがわかった。それゆえ、本発明の製造方法を用いれば、低品位な原料を用いて、Al含有量40質量%未満の低酸素なTi-Al系合金101を、歩留まり良く、効率的に製造することが可能であると判断される。 Therefore, unlike the comparative examples 1 to 3, in the titanium material addition / dissolution step of Example 1, almost no oxide inclusions were present in the ingot. It was found that the concentration did not increase and there was no yield reduction. Therefore, by using the production method of the present invention, it is possible to efficiently produce a low-oxygen Ti—Al-based alloy 101 having an Al content of less than 40% by mass with good yield using low-grade raw materials. It is judged that.
「実施例2」
 実施例2は、比較例3と同様に溶解原料102を11個に分割し鋳塊を溶製したものである。実施例2が比較例3と異なるのは、フラックス103をTi-Al系合金101の重量に対して10質量%配合していることである。
"Example 2"
In Example 2, as in Comparative Example 3, the melting raw material 102 was divided into 11 pieces and the ingot was melted. The difference between Example 2 and Comparative Example 3 is that 10% by mass of the flux 103 is blended with respect to the weight of the Ti—Al-based alloy 101.
 溶解操作終了後に取り出した鋳塊表面を目視で確認すると、添加したフラックス103が溶解/凝固して形成されたと思われる層(表面付着フラックス層108)が鋳塊の表面に付着していた。同様な鋳塊内部をSEMにて観察すると、鋳塊内部には殆どAl等の非金属介在物(酸化物系介在物)は存在していないことが分かった。これは、鋳塊表面に形成されたフラックス層にAl等の非金属介在物が移行したことによるものと推測された。 When the surface of the ingot taken out after completion of the melting operation was visually confirmed, a layer (surface adhesion flux layer 108) that seems to have been formed by melting / solidifying the added flux 103 was adhered to the surface of the ingot. Observation under the same ingot inside a SEM, most of Al 2 O 3 or the like non-metallic inclusions inside the ingot (oxide inclusions) was found not to exist. This was presumed to be due to the transfer of non-metallic inclusions such as Al 2 O 3 to the flux layer formed on the ingot surface.
 また、この鋳塊表面のフラックス層(表面付着フラックス層108)は、ショットブラストにより、容易に除去することができた。ショットブラストにより表面付着フラックス層108が除去された鋳塊の酸素濃度を不活性ガス融解法にて分析した結果、Alが存在していない部位の酸素濃度は0.045質量%であり、わずかにAl3等の酸化物系介在物が確認された部位でも酸素濃度は0.065質量%と非常に少なかった。このことから、原料分割工程でフラックス103を配合すると共に溶解原料102を分割し、分割体ベース鋳塊製造工程で分割体ごとに溶解操作と引き下げ操作とを繰り返し行った実施例2では、鋳塊中の酸素濃度を大きく低減できることがわかる。 Further, the flux layer on the surface of the ingot (surface-adhered flux layer 108) could be easily removed by shot blasting. As a result of analyzing the oxygen concentration of the ingot from which the surface adhering flux layer 108 has been removed by shot blasting using an inert gas melting method, the oxygen concentration of the portion where Al 2 O 3 does not exist is 0.045% by mass. Even at a site where oxide inclusions such as Al 2 O 3 were slightly observed, the oxygen concentration was as very low as 0.065% by mass. Therefore, in Example 2 in which the flux 103 was blended in the raw material dividing step and the melting raw material 102 was divided, and the melting operation and the lowering operation were repeated for each divided body in the divided body base ingot manufacturing step. It can be seen that the oxygen concentration inside can be greatly reduced.
 また、上述した実施例2の鋳塊についてプラズマアーク溶解炉を用いて溶解しつつ、純Ti10(酸素濃度0.05質量%)を添加してTi-30質量%Al合金の鋳塊を溶製すると、Ti-30質量%Al号金の鋳塊の酸素濃度は0.057質量%にまで低下した。 In addition, while melting the ingot of Example 2 described above using a plasma arc melting furnace, pure Ti10 (oxygen concentration 0.05 mass%) was added to melt an ingot of Ti-30 mass% Al alloy. Then, the oxygen concentration of the ingot of Ti-30 mass% Al No. gold was reduced to 0.057 mass%.
 このことから、実施例2のチタン材料添加・溶解工程では、比較例1~比較例3とは異なり、鋳塊中に酸化物系介在物がほとんど存在していなかったため、再溶解しても酸素濃度が上昇しておらず、また歩留低下も無いことがわかった。それゆえ、本発明の製造方法を用いれば、低品位な原料を用いて、Al含有量60質量%未満の低酸素なTi-Al系合金101を、歩留まり良く、効率的に製造することが可能であると判断される。 Therefore, unlike the comparative examples 1 to 3, the oxide material inclusions in the ingot were hardly present in the titanium material addition / dissolution step of Example 2, so that even when remelted, oxygen It was found that the concentration did not increase and there was no yield reduction. Therefore, by using the production method of the present invention, it is possible to efficiently produce a low-oxygen Ti—Al-based alloy 101 having an Al content of less than 60 mass% with a high yield using low-grade raw materials. It is judged that.
「実施例3」
 実施例3は、比較例3と同様に溶解原料102を11個に分割し鋳塊を溶製したものである。実施例3が比較例3と異なるのは、フラックス103をTi-Al系合金101の重量に対して10質量%配合していることである。
"Example 3"
In Example 3, as in Comparative Example 3, the melting raw material 102 was divided into 11 pieces and the ingot was melted. Example 3 is different from Comparative Example 3 in that the flux 103 is blended by 10 mass% with respect to the weight of the Ti—Al alloy 101.
 溶解操作終了後に取り出した鋳塊表面を目視で確認すると、添加したフラックス103が溶解/凝固して形成されたと思われる層(表面付着フラックス層108)が鋳塊の表面に付着していた。同様な鋳塊内部をSEMにて観察すると、鋳塊内部には殆どAl等の非金属介在物(酸化物系介在物)は存在していないことが分かった。これは、鋳塊表面に形成されたフラックス層にAl等の非金属介在物が移行したことによるものと推測された。 When the surface of the ingot taken out after completion of the melting operation was visually confirmed, a layer (surface adhesion flux layer 108) that seems to have been formed by melting / solidifying the added flux 103 was adhered to the surface of the ingot. When the same ingot was observed with an SEM, it was found that almost no non-metallic inclusions (oxide inclusions) such as Al 2 O 3 were present in the ingot. This was presumed to be due to the transfer of non-metallic inclusions such as Al 2 O 3 to the flux layer formed on the ingot surface.
 また、この鋳塊表面のフラックス層(表面付着フラックス層108)は、ショットブラストにより、容易に除去することができた。ショットブラストにより表面付着フラックス層108が除去された鋳塊の酸素濃度を不活性ガス融解法にて分析した結果、Alが存在していない部位の酸素濃度は0.16質量%であり、わずかにAl等の酸化物系介在物が確認された部位でも酸素濃度は0.20質量%と非常に少なかった。このことから、原料分割工程でフラックス103を配合すると共に溶解原料102を分割し、分割体ベース鋳塊製造工程で分割体ごとに溶解操作と引き下げ操作とを繰り返し行った実施例3では、鋳塊中の酸素濃度を大きく低減できることがわかる。 Further, the flux layer on the surface of the ingot (surface-adhered flux layer 108) could be easily removed by shot blasting. As a result of analyzing the oxygen concentration of the ingot from which the surface-adhered flux layer 108 was removed by shot blasting using an inert gas melting method, the oxygen concentration in the portion where Al 2 O 3 does not exist is 0.16% by mass. Even at a site where oxide inclusions such as Al 2 O 3 were slightly observed, the oxygen concentration was as low as 0.20% by mass. Therefore, in Example 3 in which the flux 103 was blended in the raw material dividing step and the melting raw material 102 was divided, and the melting operation and the lowering operation were repeatedly performed for each divided body in the divided body base ingot manufacturing step. It can be seen that the oxygen concentration inside can be greatly reduced.
 また、上述した実施例3の鋳塊についてプラズマアーク溶解炉を用いて溶解しつつ、純Ti110(酸素濃度0.05質量%)を添加してTi-30質量%Al合金の鋳塊を溶製すると、Ti-30質量%Al合金の鋳塊の酸素濃度は0.15質量%にまで低下した。
 このことから、実施例3のチタン材料添加・溶解工程では、比較例1~比較例3とは異なり、鋳塊中に酸化物系介在物がほとんど存在していなかったため、再溶解しても酸素濃度が上昇しておらず、また歩留低下も無いことがわかった。それゆえ、本発明の製造方法を用いれば、低品位な原料を用いて、Al含有量45質量%未満の低酸素なTi-Al系合金101を、歩留まり良く、効率的に製造することが可能であると判断される。
Further, while melting the ingot of Example 3 described above using a plasma arc melting furnace, pure Ti110 (oxygen concentration 0.05 mass%) was added to melt an ingot of Ti-30 mass% Al alloy. Then, the oxygen concentration in the ingot of the Ti-30 mass% Al alloy was reduced to 0.15 mass%.
From this, in the titanium material addition / dissolution step of Example 3, unlike Comparative Examples 1 to 3, there were almost no oxide inclusions in the ingot. It was found that the concentration did not increase and there was no yield reduction. Therefore, by using the production method of the present invention, it is possible to efficiently produce a low-oxygen Ti—Al alloy 101 having an Al content of less than 45 mass% with a high yield using low-grade raw materials. It is judged that.
「実施例4」
 実施例4は、比較例3と同様に溶解原料102を11個に分割し鋳塊を溶製したものである。実施例4が比較例3と異なるのは、フラックス103をTi-Al系合金101の重量に対して10質量%配合していることである。
Example 4
In Example 4, as in Comparative Example 3, the melting raw material 102 was divided into 11 pieces and the ingot was melted. The difference between Example 4 and Comparative Example 3 is that 10% by mass of the flux 103 is blended with respect to the weight of the Ti—Al-based alloy 101.
 溶解操作終了後に取り出した鋳塊表面を目視で確認すると、添加したフラックス103が溶解/凝固して形成されたと思われる層(表面付着フラックス層108)が鋳塊の表面に付着していた。同様な鋳塊内部をSEMにて観察すると、鋳塊内部には殆どAl等の非金属介在物(酸化物系介在物)は存在していないことが分かった。これは、鋳塊表面に形成されたフラックス層にAl等の非金属介在物が移行したことによるものと推測された。 When the surface of the ingot taken out after completion of the melting operation was visually confirmed, a layer (surface adhesion flux layer 108) that seems to have been formed by melting / solidifying the added flux 103 was adhered to the surface of the ingot. When the same ingot was observed with an SEM, it was found that almost no non-metallic inclusions (oxide inclusions) such as Al 2 O 3 were present in the ingot. This non-metallic inclusions of Al 2 O 3 or the like is presumed to be due to the transition to the flux layer formed on the ingot surface.
 また、この鋳塊表面のフラックス層(表面付着フラックス層108)は、ショットブラストにより、容易に除去することができた。ショットブラストにより表面付着フラックス層108が除去された鋳塊の酸素濃度を不活性ガス融解法にて分析した結果、Alが存在していない部位の酸素濃度は0.042質量%であり、わずかにAl等の酸化物系介在物が確認された部位でも酸素濃度は0.060質量%と非常に少なかった。このことから、原料分割工程でフラックス103を配合すると共に溶解原料102を分割し、分割体ベース鋳塊製造工程で分割体ごとに溶解操作と引き下げ操作とを繰り返し行った実施例4では、鋳塊中の酸素濃度を大きく低減できることがわかる。 Further, the flux layer on the surface of the ingot (surface-adhered flux layer 108) could be easily removed by shot blasting. As a result of analyzing the oxygen concentration of the ingot from which the surface adhering flux layer 108 has been removed by shot blasting using an inert gas melting method, the oxygen concentration in the portion where Al 2 O 3 does not exist is 0.042% by mass. Even at a site where oxide inclusions such as Al 2 O 3 were slightly confirmed, the oxygen concentration was as very low as 0.060% by mass. From this, in Example 4 where the flux 103 was blended in the raw material dividing step and the melting raw material 102 was divided, and the melting operation and the lowering operation were repeated for each divided body in the divided body base ingot manufacturing step, the ingot It can be seen that the oxygen concentration inside can be greatly reduced.
 また、上述した実施例4の鋳塊についてプラズマアーク溶解炉を用いて溶解しつつ、純Ti110(酸素濃度0.05質量%)を添加してTi-30質量%Al合金の鋳塊を溶製すると、Ti-30質量%Al合金の鋳塊の酸素濃度は0.055質量%にまで低下した。
 このことから、実施例4のチタン材料添加・溶解工程では、比較例1~比較例3とは異なり、鋳塊中に酸化物系介在物がほとんど存在していなかったため、再溶解しても酸素濃度が上昇しておらず、また歩留低下も無いことがわかった。それゆえ、本発明の製造方法を用いれば、低品位な原料を用いて、Al含有量52質量%未満の低酸素なTi-Al系合金101を、歩留まり良く、効率的に製造することが可能であると判断される。
In addition, while melting the ingot of Example 4 described above using a plasma arc melting furnace, pure Ti110 (oxygen concentration 0.05 mass%) was added to melt an ingot of Ti-30 mass% Al alloy. Then, the oxygen concentration of the ingot of the Ti-30 mass% Al alloy was reduced to 0.055 mass%.
From this, in the titanium material addition / dissolution step of Example 4, unlike Comparative Examples 1 to 3, there were almost no oxide inclusions in the ingot. It was found that the concentration did not increase and there was no yield reduction. Therefore, by using the production method of the present invention, it is possible to efficiently produce a low-oxygen Ti—Al alloy 101 having an Al content of less than 52 mass% with a high yield using low-grade raw materials. It is judged that.
 なお、今回開示された実施形態はすべての点で例示であって制限的なものではないと考えられるべきである。特に、今回開示された実施形態において、明示的に開示されていない事項、例えば、運転条件や操業条件、各種パラメータ、構成物の寸法、重量、体積などは、当業者が通常実施する範囲を逸脱するものではなく、通常の当業者であれば、容易に想定することが可能な値を採用している。 In addition, it should be thought that embodiment disclosed this time is an illustration and restrictive at no points. In particular, in the embodiment disclosed this time, matters that are not explicitly disclosed, for example, operating conditions and operating conditions, various parameters, dimensions, weights, volumes, and the like of a component deviate from a range that a person skilled in the art normally performs. Instead, values that can be easily assumed by those skilled in the art are employed.
 本出願は、2017年2月23日出願の日本特許出願(特願2017-032273)、2017年4月13日出願の日本特許出願(特願2017-079928)、2017年10月11日出願の日本特許出願(特願2017-197905)に基づくものであり、その内容はここに参照として取り込まれる。 The present application includes a Japanese patent application filed on February 23, 2017 (Japanese Patent Application No. 2017-032273), a Japanese patent application filed on April 13, 2017 (Japanese Patent Application No. 2017-079928), and an application filed on October 11, 2017. This is based on a Japanese patent application (Japanese Patent Application No. 2017-197905), the contents of which are incorporated herein by reference.
 本発明によれば、酸素を高濃度で含むような低品位のチタン材料から、高品位且つ低酸素のTi-Al系合金を歩留まりよく、効率的に製造することができ、航空機や自動車向け素材の製造に特に有用である。 According to the present invention, a high-grade and low-oxygen Ti—Al alloy can be efficiently produced from a low-grade titanium material containing oxygen at a high concentration with a high yield, and it is a material for aircraft and automobiles. It is particularly useful in the production of
1 水冷銅容器
2 水冷銅鋳型(2次鋳塊製造工程)
3 機械的手段
4 水冷銅鋳型(チタン材料添加・溶解工程)
V チタン材料
W 合金材料
X 1次鋳塊
Y 2次鋳塊
Z Ti-Al系合金(O含有量が0.1質量%未満となるもの)
Z2 Ti-Al系合金(O含有量が0.1質量%未満であって、Al含有量が40質量%未満となるもの)
α フラックス
β フラックス層
101 Ti-Al系合金
102 溶解原料
103 フラックス
141 第1分割体
142 第2分割体
143 第3分割体
105 水冷銅るつぼ
106 るつぼ本体
107 底部
108 表面付着フラックス層
109 水冷銅容器
110 純Ti
1 Water-cooled copper container 2 Water-cooled copper mold (secondary ingot manufacturing process)
3 Mechanical means 4 Water-cooled copper mold (titanium material addition / dissolution process)
V Titanium material W Alloy material X Primary ingot Y Secondary ingot Z Ti—Al alloy (O content is less than 0.1% by mass)
Z2 Ti-Al alloy (O content is less than 0.1% by mass and Al content is less than 40% by mass)
α flux β flux layer 101 Ti—Al alloy 102 melting raw material 103 flux 141 first divided body 142 second divided body 143 third divided body 105 water-cooled copper crucible 106 crucible body 107 bottom 108 surface adhesion flux layer 109 water-cooled copper container 110 Pure Ti

Claims (5)

  1.  チタン材料およびアルミニウム材料よりなる、酸素を合計で0.1質量%以上且つAlを40質量%以上含有するTi-Al系合金に対して、酸化カルシウムにフッ化カルシウムを35~95質量%配合したCaO-CaF系のフラックスを、Ti-Al系合金に対して3~20質量%となるように添加した溶解原料を、1.33Pa以上の雰囲気で水冷銅容器を用いた溶解法により溶解し保持することで1次鋳塊を溶製する1次鋳塊製造工程と、
     前記1次鋳塊を1.33Pa以上の雰囲気で無底の水冷銅鋳型を用いた溶解法により溶解しつつ連続的に下方に引抜き2次鋳塊を得る2次鋳塊製造工程と、
     前記2次鋳塊の表面付着フラックス層を機械的に除去するフラックス層除去工程と、
     を有することを特徴とするTi-Al系合金の製造方法。
    Calcium oxide is mixed with 35 to 95% by mass of calcium fluoride with respect to a Ti—Al alloy composed of titanium material and aluminum material and containing 0.1% by mass or more of oxygen and 40% by mass or more of Al. A melting material obtained by adding CaO—CaF 2 flux to 3-20 mass% with respect to the Ti—Al alloy is melted by a melting method using a water-cooled copper container in an atmosphere of 1.33 Pa or more. A primary ingot manufacturing process for melting the primary ingot by holding;
    A secondary ingot manufacturing step of continuously drawing the primary ingot by a melting method using a bottom-free water-cooled copper mold in an atmosphere of 1.33 Pa or more to obtain a secondary ingot;
    A flux layer removing step of mechanically removing the surface adhering flux layer of the secondary ingot;
    A method for producing a Ti—Al-based alloy, comprising:
  2.  チタン材料およびアルミニウム材料よりなる、酸素を合計で0.1質量%以上且つAlを40質量%以上含有するTi-Al系合金に対して、酸化カルシウムにフッ化カルシウムを35~95質量%配合したCaO-CaF系のフラックスを、Ti-Al系合金に対して3~20質量%となるように配合した溶解原料を、鋳造終了時の最終目標鋳塊重量に対して分割後の溶解原料の重量が最大で全体の4/5以下となるようにn分割する原料分割工程と、
     前記原料分割工程で分割された溶解原料の第1分割体を、無底の水冷銅鋳型に装入して1.33Pa以上の不活性ガス雰囲気下で溶解させ且つ前記水冷銅鋳型の底部を毎分15mm以下の速度で下方に引き下げる操作を行い、その後、前記原料分割工程で分割された溶解原料の第2分割体を、前記水冷銅鋳型に装入して1.33Pa以上の不活性ガス雰囲気下で溶解させ且つ前記水冷銅鋳型を毎分15mm以下の速度で下方に引き下げる操作を行い、以降、第n分割体まで前記操作を繰り返すことで鋳塊を得る分割体ベース鋳塊製造工程と、
     前記分割体ベース鋳塊製造工程で形成させた鋳塊の表面に付着するフラックス層を機械的に除去するフラックス層除去工程と、
    を有することを特徴とするTi-Al系合金の製造方法。
    Calcium oxide is mixed with 35 to 95% by mass of calcium fluoride with respect to a Ti—Al alloy composed of titanium material and aluminum material and containing 0.1% by mass or more of oxygen and 40% by mass or more of Al. A melting raw material in which a CaO—CaF 2 type flux is blended in an amount of 3 to 20% by mass with respect to the Ti—Al type alloy, A raw material dividing step of dividing n so that the weight is at most 4/5 of the total,
    The first divided body of the molten raw material divided in the raw material dividing step is charged into a bottomless water-cooled copper mold and melted in an inert gas atmosphere of 1.33 Pa or more, and the bottom of the water-cooled copper mold is removed every time. An operation of pulling downward at a speed of 15 mm or less is performed, and then the second divided body of the melted raw material divided in the raw material dividing step is charged into the water-cooled copper mold and an inert gas atmosphere of 1.33 Pa or higher The lower body is melted below and the water-cooled copper mold is pulled downward at a speed of 15 mm or less per minute, and thereafter the divided body base ingot manufacturing step for obtaining an ingot by repeating the above operation up to the nth divided body,
    A flux layer removing step for mechanically removing the flux layer adhering to the surface of the ingot formed in the divided body base ingot manufacturing step;
    A method for producing a Ti—Al-based alloy, comprising:
  3.  前記フラックス層除去工程後の鋳塊にチタン材料を添加して1.33Pa以上の雰囲気で水冷銅容器を用いた溶解法によって溶解することにより、Al含有量が40質量%未満のTi-Al系合金を得ることを特徴とする請求項1または2に記載のTi-Al系合金の製造方法。 By adding a titanium material to the ingot after the flux layer removing step and dissolving it by a melting method using a water-cooled copper container in an atmosphere of 1.33 Pa or more, a Ti-Al system having an Al content of less than 40% by mass 3. The method for producing a Ti—Al based alloy according to claim 1, wherein an alloy is obtained.
  4.  前記1次鋳塊製造工程における水冷銅容器を用いた溶解法は、アーク溶解法、プラズマアーク溶解法、または誘導溶解法のいずれかであることを特徴とする請求項1に記載のTi-Al系合金の製造方法。 The Ti-Al of claim 1, wherein the melting method using the water-cooled copper container in the primary ingot manufacturing process is any one of an arc melting method, a plasma arc melting method, and an induction melting method. Of the production of the aluminum alloy.
  5.  前記2次鋳塊製造工程および前記分割体ベース鋳塊製造工程における無底の水冷銅鋳型を用いた溶解法は、プラズマアークまたは誘導加熱を熱源とすることを特徴とする請求項1または2に記載のTi-Al系合金の製造方法。 3. The melting method using a bottomless water-cooled copper mold in the secondary ingot manufacturing step and the divided body base ingot manufacturing step uses plasma arc or induction heating as a heat source. The manufacturing method of the Ti-Al type alloy as described.
PCT/JP2018/006823 2017-02-23 2018-02-23 Method for producing ti-al alloy WO2018155658A1 (en)

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JP2017032273A JP6794598B2 (en) 2017-02-23 2017-02-23 Manufacturing method of Ti—Al alloy
JP2017-079928 2017-04-13
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JP2017197905A JP6756078B2 (en) 2017-04-13 2017-10-11 Manufacturing method of Ti—Al alloy
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110629180A (en) * 2019-10-16 2019-12-31 河北冠靶科技有限公司 Production device and method for large-size oxygen-free copper ingot applied to target material
CN113684456A (en) * 2021-08-25 2021-11-23 湖南稀土金属材料研究院有限责任公司 La-Ti alloy target and preparation method thereof
CN115369258A (en) * 2022-08-04 2022-11-22 江苏鑫瑞崚新材料科技有限公司 Low-silver low-sulfur ultrahigh-purity copper purification vacuum melting process

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5386603A (en) 1977-10-11 1978-07-31 Daido Steel Co Ltd Production of active metal ingot by plasma arc melting
JPH11246919A (en) 1998-03-03 1999-09-14 Natl Res Inst For Metals Method for refining molten metal
JP2006122920A (en) 2004-10-26 2006-05-18 Kobe Steel Ltd Method for producing long-length ingot of active high melting point metal-containing alloy
JP2013049084A (en) 2011-08-31 2013-03-14 Kobe Steel Ltd Method and device for continuously casting slab comprising titanium or titanium alloy
WO2016035824A1 (en) 2014-09-04 2016-03-10 株式会社神戸製鋼所 METHOD FOR DEOXIDIZING Ti-Al ALLOY
JP2017032273A (en) 2015-07-31 2017-02-09 ダイキン工業株式会社 Air conditioner
JP2017079928A (en) 2015-10-26 2017-05-18 ホシザキ株式会社 Cold/warm storage device
JP2017197905A (en) 2016-04-25 2017-11-02 シバタ工業株式会社 Construction method of reinforcement structure for erosion control dam, and reinforcement structure of erosion control dam

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5386603A (en) 1977-10-11 1978-07-31 Daido Steel Co Ltd Production of active metal ingot by plasma arc melting
JPH11246919A (en) 1998-03-03 1999-09-14 Natl Res Inst For Metals Method for refining molten metal
JP2006122920A (en) 2004-10-26 2006-05-18 Kobe Steel Ltd Method for producing long-length ingot of active high melting point metal-containing alloy
JP2013049084A (en) 2011-08-31 2013-03-14 Kobe Steel Ltd Method and device for continuously casting slab comprising titanium or titanium alloy
WO2016035824A1 (en) 2014-09-04 2016-03-10 株式会社神戸製鋼所 METHOD FOR DEOXIDIZING Ti-Al ALLOY
JP2017032273A (en) 2015-07-31 2017-02-09 ダイキン工業株式会社 Air conditioner
JP2017079928A (en) 2015-10-26 2017-05-18 ホシザキ株式会社 Cold/warm storage device
JP2017197905A (en) 2016-04-25 2017-11-02 シバタ工業株式会社 Construction method of reinforcement structure for erosion control dam, and reinforcement structure of erosion control dam

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP3586998A4 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110629180A (en) * 2019-10-16 2019-12-31 河北冠靶科技有限公司 Production device and method for large-size oxygen-free copper ingot applied to target material
CN113684456A (en) * 2021-08-25 2021-11-23 湖南稀土金属材料研究院有限责任公司 La-Ti alloy target and preparation method thereof
CN115369258A (en) * 2022-08-04 2022-11-22 江苏鑫瑞崚新材料科技有限公司 Low-silver low-sulfur ultrahigh-purity copper purification vacuum melting process

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