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TW201938810A - Titanium powder and method for producing same - Google Patents

Titanium powder and method for producing same Download PDF

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Publication number
TW201938810A
TW201938810A TW108107892A TW108107892A TW201938810A TW 201938810 A TW201938810 A TW 201938810A TW 108107892 A TW108107892 A TW 108107892A TW 108107892 A TW108107892 A TW 108107892A TW 201938810 A TW201938810 A TW 201938810A
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Taiwan
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titanium
powder
mgcl
less
pores
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TW108107892A
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Chinese (zh)
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竹中茂久
平嶋謙治
滝千博
齊藤和也
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日商東邦技術服務股份有限公司
日商日立金屬股份有限公司
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Publication of TW201938810A publication Critical patent/TW201938810A/en

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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C1/00Making non-ferrous alloys
    • C22C1/04Making non-ferrous alloys by powder metallurgy
    • C22C1/045Alloys based on refractory metals
    • C22C1/0458Alloys based on titanium, zirconium or hafnium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/02Making metallic powder or suspensions thereof using physical processes
    • B22F9/023Hydrogen absorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/02Making metallic powder or suspensions thereof using physical processes
    • B22F9/04Making metallic powder or suspensions thereof using physical processes starting from solid material, e.g. by crushing, grinding or milling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/02Making metallic powder or suspensions thereof using physical processes
    • B22F9/04Making metallic powder or suspensions thereof using physical processes starting from solid material, e.g. by crushing, grinding or milling
    • B22F2009/048Making metallic powder or suspensions thereof using physical processes starting from solid material, e.g. by crushing, grinding or milling by pulverising a quenched ribbon

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)
  • Powder Metallurgy (AREA)

Abstract

Provided is a titanium powder which is reduced in pores in titanium particles. A titanium powder that is characterized in that the pore area ratio, which is the value obtained by dividing the cross-sectional area of pores in a cross-section of the titanium powder by the area of the cross-section, is 0.3% or less. A method for producing a titanium powder, which is a hydrogenation-dehydrogenation method comprising a hydrogenation step, a pulverization step and a dehydrogenation step to be performed on a titanium starting material, and which is characterized in that the concentration of all MgCl2 contained in the titanium starting material is 1.0 mass% or less, while the internal MgCl2 concentration is 0.1 mass% or less.

Description

鈦系粉及其製造方法Titanium powder and manufacturing method thereof

本發明係關於鈦系粉,詳情係關於藉由氫化去氫法(以下稱作HDH法)來製造之前所未見、嶄新的鈦系粉及其製造方法。The present invention relates to titanium-based powder, and details relate to the production of a new and unprecedented titanium-based powder by a hydrodehydrogenation method (hereinafter referred to as HDH method) and a method for producing the same.

以往,針對鈦系粉中之細孔,在工業上幾乎未受到注目,詳細研究細孔產生機制之文獻等係幾乎沒有的狀態。近年來,隨著使用鈦系粉之燒結體的密度提升要求,或對於由鈦系粉製造之鈦製品的品質要求之高度化,鈦系粉中之細孔減低要求日益提高。In the past, the pores in titanium-based powders have received little attention in the industry, and there are few documents such as literatures that study the pore generation mechanism in detail. In recent years, with the increase in the density of sintered bodies using titanium-based powders or the increase in the quality requirements for titanium products made from titanium-based powders, the requirements for reducing pores in titanium-based powders have increased.

雖針對揭露使鈦系粉之細孔減低的技術之先行技術文獻進行調查,但尚未有所發現。作為關於鈦系粉之製造的先行技術文獻,有專利文獻1及專利文獻2。此外,在本說明書中,將鈦粉及鈦合金粉稱作鈦系粉。Although investigations have been conducted on the prior art literature that discloses techniques for reducing the pores of titanium-based powders, no findings have been found. As prior art documents on the production of titanium-based powder, there are Patent Document 1 and Patent Document 2. In this specification, titanium powder and titanium alloy powder are referred to as titanium-based powder.

『專利文獻』
《專利文獻1》日本專利公開第H5-247503號公報
《專利文獻2》日本專利公開第H7-278601號公報
『Patent Literature』
"Patent Document 1" Japanese Patent Publication No. H5-247503 "Patent Document 2" Japanese Patent Publication No. H7-278601

本發明係以解決上述問題為目的者,亦即在於提供已使鈦系粉中之細孔減低的鈦系粉。The present invention aims to solve the above problems, that is, to provide a titanium-based powder having reduced pores in the titanium-based powder.

為了達成上述之細孔為少之鈦系粉的製造,在本發明詳細分析細孔的構造或產生機轉。其結果,發現藉由調整鈦系粉之原料及製造方法,細孔的產生個數會大幅變化,同時注意到細孔的產生係藉由於鈦系粉中存在(或曾存在)氣體,而殘存截面形狀為略圓形(球形)之細孔的分析結果。In order to achieve the production of the titanium-based powder with few pores as described above, the structure of the pores or the mechanical rotation are analyzed in detail in the present invention. As a result, it was found that by adjusting the raw materials and manufacturing methods of the titanium-based powder, the number of pores generated would be greatly changed. At the same time, it was noted that the generation of the pores was caused by the existence (or existence) of gas in the titanium-based powder. Analysis results of pores with a slightly circular (spherical) cross-sectional shape.

根據本發明之一實施型態,提供一種鈦系粉,其特徵在於:將於鈦系粉之截面中細孔所佔之截面積除以前述鈦系粉之截面之面積的細孔面積比為0.3百分比以下。According to an embodiment of the present invention, a titanium-based powder is provided, characterized in that the ratio of the pore area of the cross-section area occupied by the pores in the cross-section of the titanium-based powder to the area of the cross-section of the aforementioned titanium-based powder is 0.3% or less.

鈦系粉亦可為HDH粉。The titanium-based powder may be an HDH powder.

根據本發明之一實施型態,提供一種鈦系粉之製造方法,係使用鈦系原料之透過包含氫化工序、粉碎工序、去氫工序之氫化去氫法的鈦系粉之製造方法,其特徵在於:前述鈦系原料所含有之總MgCl2 的濃度為1.0 mass%以下,內部MgCl2 濃度為0.1 mass%以下。According to one embodiment of the present invention, there is provided a method for producing a titanium-based powder, which is a method for producing a titanium-based powder through a hydrogenation and dehydrogenation method including a hydrogenation process, a pulverization process, and a dehydrogenation process using a titanium-based raw material. This is because the total MgCl 2 concentration contained in the titanium-based raw material is 1.0 mass% or less, and the internal MgCl 2 concentration is 0.1 mass% or less.

鈦系原料之最大厚度亦可為20 mm以下。The maximum thickness of titanium-based materials can also be 20 mm or less.

在粉碎工序中,氫化鈦系粉末亦可粉碎至D95粒徑為300 μm以下。In the pulverizing step, the titanium hydride-based powder may be pulverized to a D95 particle size of 300 μm or less.

在氫化工序中,亦可在將鈦系原料之溫度調至716℃以上且1050℃以下之範圍內耗費90分鐘以上的時間氫化之。In the hydrogenation step, the titanium-based raw material may be hydrogenated for a period of 90 minutes or more within the range of 716 ° C to 1050 ° C.

鈦系粉中之細孔產生,與氣體有密切的關係。藉由不使氣體捲入鈦系粉中或在鈦系粉內部不使氣體產生,或者藉由將已產生的氣體自鈦系粉內部迅速消除,能夠大幅減低存在細孔之鈦系粉的個數。The generation of pores in titanium-based powders is closely related to the gas. By not entraining the gas in the titanium-based powder or generating gas inside the titanium-based powder, or by rapidly eliminating the generated gas from the inside of the titanium-based powder, the number of pores of the titanium-based powder can be greatly reduced. number.

鈦粉現在幾乎都係將藉由克羅爾法製造之海綿鈦作為原料。並且,就經濟性、資源保護的觀點而言,亦有將廢料(scrap)作為原料活用的情形。Almost all titanium powders use sponge titanium produced by the Kroll method as a raw material. In addition, in terms of economy and resource protection, there are cases where scrap is used as a raw material.

[克羅爾法的說明][Explanation of the Kroll Act]

所謂克羅爾法,係以鎂(Mg)還原將鈦礦石氯化而獲得之四氯化鈦(TiCl4 )以獲得金屬鈦的方法。The so-called Kroll method is a method in which titanium tetrachloride (TiCl 4 ) obtained by chlorinating titanium ore with magnesium (Mg) is reduced to obtain metallic titanium.

在克羅爾法中,由於在還原工序(TiCl4 +2Mg→Ti+2MgCl2 )中生成的MgCl2 會與海綿鈦共存,故使用在分離工序中去除此MgCl2 之後的海綿鈦。然而,若仔細驗看此海綿鈦,即可知殘存有附著於海綿鈦之表面的MgCl2 (表面MgCl2 )與被困進海綿鈦之內部而與外部隔絕的MgCl2 (內部MgCl2 )之2種,並非可完全去除MgCl2In the Kroll method, since MgCl 2 generated in the reduction step (TiCl 4 + 2Mg → Ti + 2MgCl 2 ) coexists with the sponge titanium, sponge titanium after the MgCl 2 is removed in the separation step is used. However, if the sponge titanium is examined carefully, it can be seen that there are 2 remaining MgCl 2 (surface MgCl 2 ) attached to the surface of the sponge titanium and MgCl 2 (internal MgCl 2 ) trapped inside the sponge titanium and isolated from the outside. This method does not completely remove MgCl 2 .

在分離工序未被充分除盡而殘存於海綿鈦之表面的MgCl2 (表面MgCl2 ),可藉由再度在減壓下加熱來去除。另一方面,將在減壓下加熱之後的海綿鈦剖切並驗看內部,可知被困進海綿鈦之內部的MgCl2 (內部MgCl2 )無法以此方法消除。MgCl 2 (surface MgCl 2 ) remaining on the surface of the sponge titanium without being fully removed in the separation step can be removed by heating again under reduced pressure. On the other hand, the sponge titanium after being heated under reduced pressure is cut and the interior is examined. It can be seen that MgCl 2 (internal MgCl 2 ) trapped inside the sponge titanium cannot be eliminated by this method.

[霧化法鈦粉製造方法的說明][Explanation of Manufacturing Method of Titanium Powder by Atomization Method]

鈦粉之製造方法大致上分為霧化法與HDH法。在霧化法,係於使鈦原料熔融之後,在Ar氣中將已液狀化之鈦做成細小液狀之粒的同時,急速冷卻使之固化,藉此製造鈦粉。The manufacturing methods of titanium powder are roughly divided into atomization method and HDH method. In the atomization method, after the titanium raw material is melted, the liquefied titanium is made into fine liquid particles in an Ar gas, and then rapidly cooled to solidify, thereby manufacturing titanium powder.

於本發明人之研究調查中,可得以下結論:在霧化法中,有2個於鈦粉中產生細孔的機制。第1個係存在於鈦原料之內部的MgCl2 (內部MgCl2 )一口氣氣體化並立即急速冷卻,因而已氣體化之MgCl2 被困進已液狀化之鈦粒內部,而於鈦粉中產生細孔的機制。第2個係已液狀化之鈦粒將Ar氣或已氣化之MgCl2 氣體捲入而凝固,因而在鈦粉中產生細孔的機制。職是,得出以下結論:欲達成本發明之目的,以HDH法為合適。In the research and investigation of the present inventors, the following conclusions can be drawn: In the atomization method, there are two mechanisms for generating pores in the titanium powder. The first MgCl 2 (internal MgCl 2 ) existing inside the titanium raw material was gasified at once and rapidly cooled, so the gasified MgCl 2 was trapped inside the liquefied titanium particles, and the titanium powder Mechanism of fine pores. The second is a mechanism in which liquefied titanium particles entrain Ar gas or vaporized MgCl 2 gas to solidify, thereby generating pores in the titanium powder. It is concluded that the HDH method is appropriate for the purpose of cost invention.

[HDH法鈦粉製造方法的說明][Explanation of the manufacturing method of HDH titanium powder]

所謂HDH法,係先將鈦原料氫化形成脆質TiH2 之後,將之粉碎並去氫,藉此獲得鈦粉的方法。亦即係藉由氫化~粉碎~去氫~碎解之工序製造鈦粉(HDH粉)的方法。上述碎解工序係任意,但在鈦粉(HDH粉)之製造中以進行碎解工序為佳。The so-called HDH method is a method in which titanium raw material is first hydrogenated to form brittle TiH 2 , and then pulverized and dehydrogenated to obtain titanium powder. That is, it is a method for producing titanium powder (HDH powder) through the steps of hydrogenation-pulverization-dehydrogenation-disintegration. The above-mentioned disintegration step is arbitrary, but it is preferable to perform the disintegration step in the production of titanium powder (HDH powder).

此時,在氫化之工序中,將鈦原料裝進能夠真空置換的氫化爐,在400℃以上的溫度於氫氣氣體環境中進行氫化處理,自氫氣氣體環境置換成Ar氣氣體環境,藉此獲得氫化鈦之塊狀體。鈦原料因氫化之工序而氫脆化。At this time, in the hydrogenation process, the titanium raw material is charged into a hydrogenation furnace capable of being vacuum-replaced, and hydrogenated in a hydrogen gas environment at a temperature of 400 ° C or higher, thereby replacing the hydrogen gas environment with an Ar gas gas environment, thereby obtaining A block of titanium hydride. The titanium raw material is hydrogen-embrittled by the hydrogenation process.

其次係粉碎之工序。在粉碎之工序,機械粉碎氫化鈦之塊狀體,做成具有機械性破裂面(亦即粉碎面)的氫化鈦粉末。將所獲得之氫化鈦粉末分級及/或篩選以去除氫化鈦之微粉。於氫化鈦之機械性粉碎,可使用球磨機、振動磨機等粉碎裝置,於氫化鈦粉末之粒度調整,亦可使用圓形振動篩、氣流分級機等篩選分級裝置。The second step is the crushing process. In the pulverizing step, the titanium hydride block is mechanically pulverized to make a titanium hydride powder having a mechanically broken surface (that is, a pulverized surface). The obtained titanium hydride powder is classified and / or screened to remove fine powder of titanium hydride. For mechanical pulverization of titanium hydride, a pulverizing device such as a ball mill and a vibrating mill can be used, and the particle size adjustment of the titanium hydride powder can also be performed. A screening device such as a circular vibrating screen and an air classifier can also be used.

在去氫工序,將上述氫化鈦粉末填充於容器,裝進真空加熱型的去氫爐,在例如10-3 Torr(0.13 Pa)以下之真空中加熱至450℃以上之溫度進行去氫,藉此做成去氫鈦粉末。並且,視需求插入Ar氣。In the dehydrogenation step, the above-mentioned titanium hydride powder is filled in a container, put into a vacuum heating type dehydrogenation furnace, and heated to a temperature of 450 ° C or higher in a vacuum of 10 -3 Torr (0.13 Pa) or less for dehydrogenation. This was made into dehydrogenated titanium powder. Also, insert Ar gas as required.

在碎解工序,將在去氫工序已假燒結的去氫鈦之塊狀體之假燒結部分鬆開,恢復成具有粉碎後之粉碎面或碎解面的鈦粉形狀。In the disintegration step, the pseudo-sintered portion of the dehydrogenated titanium bulk that has been pseudo-sintered in the dehydrogenation step is loosened and restored to a titanium powder shape having a crushed surface or a crushed surface.

[在HDH法中之細孔產生機制的說明][Explanation of the pore generation mechanism in the HDH method]

本發明人自細孔的觀點詳細研究調查在HDH法之各製造工序中的條件,查明如何防止細孔的產生。於HDH法,若在各製造工序中無鈦熔融液化一事,則不會捲入氣體環境中之Ar氣造成細孔。在HDH法之熱處理,因係氫化與去氫之2工序,故皆在熔點以下進行即可。惟因一般作為放入鈦材的容器係使用不鏽鋼,若不鏽鋼所包含的鐵與鈦接觸,二者之溫度來到鐵與鈦之共晶溫度以上,則鈦會呈液態而變得不合乎上述目的。因此,本發明人發現:為了防止細孔的產生,必須將鈦控制在鐵與鈦之共晶溫度以下,以防止鈦的液化。亦即,控制上限溫度一事成為本發明之重要的構成要件。From the viewpoint of pores, the present inventors have studied in detail the conditions in each manufacturing process of the HDH method, and found out how to prevent the generation of pores. In the HDH method, if there is no titanium melt liquefaction in each manufacturing process, Ar gas in the gas environment will not cause pores. Since the heat treatment in the HDH method is a two-step process of hydrogenation and dehydrogenation, it may be performed below the melting point. However, because stainless steel is generally used as a container for placing titanium materials, if the iron and titanium contained in the stainless steel are in contact, the temperature of the two is above the eutectic temperature of iron and titanium, the titanium will be in a liquid state and will not meet the above requirements. purpose. Therefore, the present inventors have found that in order to prevent the generation of pores, titanium must be controlled below the eutectic temperature of iron and titanium to prevent the liquefaction of titanium. That is, controlling the upper limit temperature becomes an important constituent element of the present invention.

舉例而言,在專利文獻1及專利文獻2僅記載「於真空氣體環境下升溫至650℃」,對於之後之氫氣體導入後的鈦材之溫度控制並未有所記載。由於將鈦氫化的氫化反應為放熱反應,故最初雖例如於真空爐內在650℃使氫吸收進行,但之後溫度會自發性上升。職是,必須要時常觀察鈦材料放入容器的方式、氫及Ar置入量、置入時間及各部位之溫度,同時為了抑制溫度上升而做冷卻等精細的控制,以使包含局部之任一處皆為共晶溫度以下。For example, Patent Literature 1 and Patent Literature 2 only describe "the temperature is raised to 650 ° C in a vacuum gas environment", and there is no description about the temperature control of the titanium material after the introduction of hydrogen gas. Since the hydrogenation reaction of hydrogenating titanium is an exothermic reaction, although the hydrogen absorption is performed at 650 ° C. in a vacuum furnace at first, the temperature rises spontaneously thereafter. It is necessary to constantly observe the manner in which the titanium material is put into the container, the amount of hydrogen and Ar to be placed, the time and temperature of each part, and at the same time, to control the temperature rise and perform fine control such as cooling, so as to include local tasks. All are below eutectic temperature.

在常壓下之MgCl2 的沸點為1412℃,在此溫度下,被困進鈦原料之內部的MgCl2 (內部MgCl2 )會氣體化。另一方面,鈦的熔點為1668℃,故在1412℃,鈦會以固體狀態存在。經氣體化之內部MgCl2 ,其體積會變得比在固體狀態下大,職是之故,在鈦之內部會形成非常高壓的狀態。由此經氣體化之內部MgCl2 所致之高壓狀態,會使因氫化而變脆的氫化鈦產生龜裂,能自此處將MgCl2 排出至氫化鈦外部。The boiling point of MgCl 2 at normal pressure is 1412 ° C. At this temperature, MgCl 2 (internal MgCl 2 ) trapped inside the titanium raw material will gasify. On the other hand, the melting point of titanium is 1668 ° C, so at 1412 ° C, titanium will exist in a solid state. The volume of the gasified MgCl 2 will be larger than that in the solid state. For this reason, a very high pressure state will be formed inside the titanium. The high-pressure state caused by the gasified internal MgCl 2 will cause cracking of the titanium hydride that is brittle by hydrogenation, and MgCl 2 can be discharged to the outside of the titanium hydride from here.

然而,如前所述,在HDH法中,放入鈦材之容器為不鏽鋼的情形居多,而不會升溫至鐵與鈦之共晶溫度(1085℃)以上。在本發明中,發現遵守受此限制之溫度且將造成細孔的MgCl2 消除之前所未見的控制方法,進而完成本發明。簡言之,將鈦原料之溫度最低調成MgCl2 之熔點(714℃)以上的溫度將MgCl2 做成液相,使MgCl2 之體積相較於在固體狀態下膨脹。此時,鈦由於以固體狀態存在,故內部MgCl2 在液體狀態下的體積會變得比在固體狀態下大,職是之故,在鈦之內部會形成非常高壓的狀態。由此液相之內部MgCl2 所致之高壓狀態,會使因氫化而變脆的氫化鈦產生龜裂。因龜裂而露出至鈦外部的液相之MgCl2 以可藉由緩慢蒸發來氣化的方式為之。此情形中之爐內之溫度及加熱時間(溫度之維持時間)的控制,亦可考量所氫化之鈦原料的厚度或氫化時間而決定。舉例而言,若在鈦脆化之前,因蒸發之MgCl2 而鈦內部的壓力升高,則鈦由於在高溫會軟化而容易變形,故會導致使球狀之細孔形成於鈦內部的結果,此與本發明呈反方向。舉例而言,在本發明中,藉由在716℃以上且1050℃以下之範圍耗費90分鐘以上的時間,存在於鈦原料之內部的MgCl2 可自鈦的龜裂處蒸發,鈦的氫化亦一併實現。理論上,雖可將鈦原料之溫度設定在MgCl2 之熔點(714℃)以上至未達鐵與鈦之共晶溫度(1085℃)的範圍,但可藉由定為上述溫度範圍來進行更加確實的溫度控制。However, as mentioned earlier, in the HDH method, the container in which the titanium material is placed is stainless steel, and the temperature does not rise above the eutectic temperature of iron and titanium (1085 ° C). In the present invention, it has been found that a control method that has not been seen before is to observe the temperature restricted by this limitation and eliminate the pores of MgCl 2 , and then complete the present invention. Briefly, the most low-temperature titaniferous material to a melting point of MgCl 2 (714 deg.] C) temperature above the MgCl 2 liquid phase to make the volume of MgCl 2 as compared to the expansion in the solid state. At this time, because titanium exists in a solid state, the volume of the internal MgCl 2 in the liquid state becomes larger than that in the solid state. For this reason, a very high-pressure state is formed inside the titanium. The high-pressure state caused by the internal MgCl 2 in the liquid phase may cause cracking of the titanium hydride that becomes brittle by hydrogenation. The liquid phase MgCl 2 exposed to the outside of the titanium due to cracking is such that it can be gasified by slow evaporation. In this case, the control of the temperature in the furnace and the heating time (temperature maintaining time) can also be determined by considering the thickness or hydrogenation time of the hydrogenated titanium raw material. For example, if the pressure inside the titanium increases due to the evaporated MgCl 2 before the titanium is embrittled, the titanium will be easily deformed due to softening at high temperature, which will result in the formation of spherical pores inside the titanium. This is in the opposite direction to the present invention. For example, in the present invention, by spending more than 90 minutes in the range of 716 ° C to 1050 ° C, the MgCl 2 existing in the titanium raw material can be evaporated from the crack of titanium, and the hydrogenation of titanium is also Together. Theoretically, although the temperature of the titanium raw material can be set in the range of the melting point (714 ° C) or more of the MgCl 2 to the eutectic temperature (1085 ° C) of iron and titanium, the temperature range can be further improved by setting the temperature range as described above. True temperature control.

此外,在本實施型態相關之HDH法中,以藉由控制溫度使原料之鈦不會熔融的方式為之。然而,於在鈦原料之表面附著有MgCl2 的情況下,就於HDH法之工序中MgCl2 會氣化而言,以為了消除表面之MgCl2 而做成高真空為佳。在本實施型態相關之HDH法中,重要的係在減低隨鈦原料帶入之附著於表面的MgCl2 之量的同時,考量溫度、時間、真空度、Ar置換等、成本而予以最適化。In addition, in the HDH method according to the embodiment, the titanium of the raw material is not melted by controlling the temperature. However, in the case where MgCl 2 is adhered to the surface of the titanium raw material, it is preferable that a high vacuum is used to eliminate MgCl 2 on the surface in order to vaporize MgCl 2 in the HDH process. In the HDH method related to this embodiment, it is important to optimize the temperature, time, vacuum, Ar replacement, and cost while reducing the amount of MgCl 2 attached to the surface brought with the titanium raw material. .

在本實施型態相關之氫化工序,為了使細孔不產生且將存在於鈦內部的MgCl2 (內部MgCl2 )去除,做成體現在本發明發現之上述機制的氫化工序。若耗費充足的時間進行由氫化所致之脆化,則能夠使MgCl2 排出,但在工業上對於生產性及成本並不適合。In the hydrogenation step related to this embodiment mode, in order to prevent pores from being generated and remove MgCl 2 (internal MgCl 2 ) existing in the titanium, a hydrogenation step embodying the above-mentioned mechanism discovered in the present invention is completed. If it takes sufficient time to perform embrittlement by hydrogenation, MgCl 2 can be discharged, but it is not suitable for productivity and cost in industry.

研究調查的結果表明:正因將附著於鈦原料之表面的MgCl2 量控制,將存在於鈦原料之內部的MgCl2 量控制一事對於生產性及成本大有影響。進行了各種實驗,結果表明:必須將鈦原料之總MgCl2 濃度抑於1.0 mass%以下。而且,鈦原料之總MgCl2 濃度以抑於0.05 mass%以下為佳,以抑於0.001 mass%以下為較佳。尤其,可知若將存在於鈦原料之內部的MgCl2 濃度(內部MgCl2 濃度)做成0.5 mass%以下,則在HDH法中,即使將鈦原料之溫度維持在MgCl2 之熔點(714℃)以上且未達鐵與鈦之共晶溫度(1085℃)之範圍的時間為90分鐘,仍可有效率消除造成細孔的MgCl2 。藉由將存在於鈦原料之內部的MgCl2 濃度(內部MgCl2 濃度)做成0.1 mass%以下,效果表現更明確。在本發明,以將被困進鈦原料之內部的MgCl2 濃度(內部MgCl2 濃度)做成0.1 mass%以下為佳,以做成0.001 mass%以下為較佳。Investigation results showed that: because of the amount of MgCl 2 is attached to the surface of the titanium material of the control, the amount of MgCl 2 is present inside the titanium raw materials for the production control and cost concerning large influence. Various experiments have been carried out, and the results show that the total MgCl 2 concentration of the titanium raw material must be suppressed below 1.0 mass%. In addition, the total MgCl 2 concentration of the titanium raw material is preferably less than 0.05 mass%, and more preferably less than 0.001 mass%. In particular, it can be seen that if the MgCl 2 concentration (internal MgCl 2 concentration) existing in the titanium raw material is 0.5 mass% or less, the temperature of the titanium raw material is maintained at the melting point of MgCl 2 (714 ° C) in the HDH method. The above time, which does not reach the eutectic temperature (1085 ° C) range of iron and titanium, is 90 minutes, and can still effectively eliminate the pores of MgCl 2 . By setting the MgCl 2 concentration (internal MgCl 2 concentration) existing in the titanium raw material to 0.1 mass% or less, the effect performance is more clear. In the present invention, the MgCl 2 concentration (internal MgCl 2 concentration) trapped inside the titanium raw material is preferably 0.1 mass% or less, and more preferably 0.001 mass% or less.

〔在原料之細孔抑制方法〕[Method for suppressing pores in raw materials]

此外,在本發明之HDH法,由於鈦不會熔融,故不會產生由Ar氣等之捲入所致之細孔。In addition, in the HDH method of the present invention, since titanium does not melt, pores due to the entrainment of Ar gas or the like are not generated.

作為將鈦原料之總MgCl2 濃度抑於1.0 mass%以下,進一步將被困進鈦原料內部的MgCl2 濃度(內部MgCl2 濃度)抑於0.1 mass%以下的方法,雖耗費成本,但於事前進一步將海綿鈦微細化並再度在真空中進行熱處理的方法亦有效。As a method of reducing the total MgCl 2 concentration of the titanium raw material to less than 1.0 mass%, and further suppressing the MgCl 2 concentration (internal MgCl 2 concentration) trapped inside the titanium raw material to less than 0.1 mass%, although it costs cost, It is also effective to further refine the titanium sponge and heat-treat it in a vacuum again.

並且,鈦原料中,其最大厚度可為20 mm以下,以10 mm以下為較佳。此係因藉由鈦原料之最大厚度為20 mm以下,於氫化時氫會充分擴及原料內部,使鈦脆化並迅速產生龜裂。In addition, the maximum thickness of the titanium raw material may be 20 mm or less, and preferably 10 mm or less. This is because the maximum thickness of the titanium raw material is 20 mm or less. During hydrogenation, hydrogen will sufficiently spread inside the raw material, embrittle the titanium, and rapidly crack.

[總MgCl2 濃度之定義][Definition of total MgCl 2 concentration]

茲說明總MgCl2 之濃度的量測方法。藉由硝酸銀滴定法(JIS H 1615)量測做成對象之鈦原料之氯濃度,由此氯濃度之值換算成MgCl2 濃度,將之定為鈦原料所包含之MgCl2 濃度(總MgCl2 濃度)。The measurement method of the total MgCl 2 concentration is explained below. The chlorine concentration of the target titanium raw material was measured by the silver nitrate titration method (JIS H 1615), and the value of the chlorine concentration was converted into the MgCl 2 concentration, which was determined as the MgCl 2 concentration (total MgCl 2 ) contained in the titanium raw material. concentration).

[內部MgCl2 濃度之定義][Definition of internal MgCl 2 concentration]

茲說明內部MgCl2 之濃度的量測方法。首先,將做成對象之鈦原料在減壓下(50 Pa以下)進行約750℃×1小時的熱處理,藉此使表面MgCl2 逸散。之後,藉由硝酸銀滴定法(JIS H 1615)量測本材料之氯濃度,由此氯濃度之值換算成MgCl2 濃度,將之定為被困進鈦原料之內部而存在的MgCl2 濃度(內部MgCl2 濃度)。The measurement method of the internal MgCl 2 concentration is described below. First, the target titanium raw material was subjected to a heat treatment at a reduced pressure (50 Pa or less) at about 750 ° C. for 1 hour, thereby dissipating the surface MgCl 2 . Thereafter, by silver nitrate titration chlorine concentration (JIS H 1615) of measuring this material, whereby the value of the chlorine concentration in terms of the concentration of MgCl 2, MgCl will be trapped as the raw materials into the titanium concentration exists inside ( Internal MgCl 2 concentration).

[鈦粉之大小的說明][Explanation of the size of titanium powder]

藉由做成具有粉碎面的氫化鈦粉,可進一步提高殘存於氫化鈦之細孔成為起點破裂而被打開的機率,所述氫化鈦粉係透過粉碎工序,將經氫化之氫化鈦粉碎並微細化而成者。愈使氫化鈦粉之粒徑更細,細孔打開的機率即愈高。然而,因工業上有成本及時間之限制,故氫化鈦粉之粒徑為300 μm以下,以150 μm以下為佳即可。於此,在HDH法中製造之經粉碎的氫化鈦粉之粒徑擁有分布,只要全氫化鈦粉之粒徑的95%以上為上述值以下即可。亦即,若將氫化鈦粉末之D95粒徑抑至300 μm以下,以150 μm以下為佳,則有更進一步的效果。D95粒徑的下限側並不特別受限,但若要硬舉出一例,可做成70 μm以上,亦可做成80 μm以上。在本發明中,D95係指在藉由雷射繞射/散射法求得之粒度分布量測中,體積基準的積分分布分別呈95%的粒徑。詳細而言,係依據JIS Z8825:2013來量測。By forming a titanium hydride powder having a pulverized surface, the probability that the pores remaining in the titanium hydride become cracked and opened will be further increased. The titanium hydride powder is pulverized and finely pulverized by passing through the pulverization process. Into a person. The finer the particle size of the titanium hydride powder, the higher the probability of pore opening. However, due to industrial cost and time constraints, the particle size of the titanium hydride powder is preferably 300 μm or less, and preferably 150 μm or less. Here, the particle diameter of the pulverized titanium hydride powder produced in the HDH method has a distribution, as long as 95% or more of the particle diameter of the perhydrogen titanium powder is the above value or less. That is, if the D95 particle diameter of the titanium hydride powder is reduced to 300 μm or less, and preferably 150 μm or less, a further effect is obtained. The lower limit side of the particle size of D95 is not particularly limited, but to give an example, it can be made to be 70 μm or more, or 80 μm or more. In the present invention, D95 means that in the particle size distribution measurement obtained by the laser diffraction / scattering method, the volume-based integral distribution has a particle size of 95%, respectively. Specifically, it is measured in accordance with JIS Z8825: 2013.

並且,在HDH法中製造之經碎解的鈦粉之全鈦粒徑的95%以上只要為150 μm以下即可。In addition, 95% or more of the total titanium particle diameter of the disintegrated titanium powder produced in the HDH method may be 150 μm or less.

〔對於球狀化工序的適用〕[Application to spheroidization process]

在於上已述之HDH法中製造之鈦粉中,MgCl2 的殘留為少。職是,在本發明之HDH法中製造之鈦粉,合適作為「用以使鈦粉之表面熔融(例如電漿熔融),使係為粉碎面或碎解面之帶有稜角的表面球狀化而獲得球狀粉」的原料粉末。在HDH法中製造之經碎解的鈦粉,由於具有「具有凹凸構造」的粉碎面或碎解面,故可藉由其廣大的表面積,促進導入於電漿時的熔融。此外,即使為了球狀化使鈦粉表面熔融,亦不會有Ar等電漿氣體的捲入,可抑制新的細孔。In the titanium powder produced by the HDH method described above, the residue of MgCl 2 is small. The titanium powder produced in the HDH method of the present invention is suitable as "to melt the surface of the titanium powder (for example, plasma melting), and to make the surface of the pulverized or disintegrated surface with an angular surface spherical. Into a spherical powder ". The disintegrated titanium powder produced by the HDH method has a pulverized surface or a disintegrated surface having a "concavo-convex structure". Therefore, its large surface area can promote the melting when it is introduced into the plasma. In addition, even if the surface of the titanium powder is melted for spheroidization, no plasma gas such as Ar is involved, and new pores can be suppressed.

以上發現:為了抑制在HDH法中之細孔產生,可藉由如上所述適當控制溫度、時間、注氫量、材料形狀、MgCl2 帶入量(總體的量與被封入之MgCl2 的量)來達成,使本發明臻至完成。The above findings: In order to suppress the generation of pores in the HDH method, the temperature, time, amount of hydrogen injection, material shape, and the amount of MgCl 2 taken in (the total amount and the amount of MgCl 2 enclosed) can be appropriately controlled as described above ) To achieve the present invention.

在本實施型態中,已就鈦粉予以說明。然而,在於鈦含有50質量%以下之Al或V等元素的鈦合金粉中,亦可以藉由在HDH法控制溫度使原料之鈦合金不會熔融的方式為之,獲得與鈦粉同樣的效果。於鈦所含有之元素以20質量%以下為佳,以15質量%以下為更佳。鈦合金粉亦可包含多種元素。舉例而言,鈦合金粉亦可做成Ti―Al―V合金粉。在此情況下,該Ti―Al―V合金粉可將Al含量做成5.5~7.5質量%,將V含量做成3.5~4.5質量%。In this embodiment, titanium powder has been described. However, in titanium alloy powders in which titanium contains elements such as Al or V in an amount of 50% by mass or less, the titanium alloy of the raw material cannot be melted by controlling the temperature in the HDH method, and the same effect as that of titanium powder can be obtained. . The element contained in titanium is preferably 20% by mass or less, and more preferably 15% by mass or less. The titanium alloy powder may also contain various elements. For example, titanium alloy powder can also be made of Ti-Al-V alloy powder. In this case, the Ti-Al-V alloy powder may have an Al content of 5.5 to 7.5% by mass and a V content of 3.5 to 4.5% by mass.

[截面之細孔面積比的說明][Explanation of pore area ratio of cross section]

藉由本實施型態相關之鈦系粉之製造方法,可實現下述情事:將觀察鈦系粉之任意之截面而出現之內包之細孔(以下,內部細孔)的截面積除以鈦系粉之截面面積的值(截面之細孔面積比)為0.3百分比以下。並且,在本發明中所製造之鈦系粉,以觀察鈦系粉之任意之截面而出現之內部細孔的數量為每單位面積20個/mm2 以下為佳。於此,所謂鈦系粉截面之細孔面積比為0.3百分比以下,意謂將鈦系粉末埋進樹脂並進行研磨之後,對截面以光學顯微鏡在倍率500倍觀察700 μm×500 μm尺寸之任意位置的16個位置時,將藉由影像處理做成亮度90~250之範圍的影像而觀察到之內部細孔之截面積,除以粉之總截面積的值為0.3百分比以下。所謂內部細孔的數量,意謂進行上述觀察時,藉由影像處理做成亮度90~250之範圍的影像而觀察到之內部細孔的數量。此外,在任何觀察時,皆排除因影像處理而長徑為10 μm以下之粉。並且,在影像處理中,排除即使看似內部細孔但由原始影像來看顯為開放的細孔(圖1係影像處理前的照片,圖2係影像處理後的照片)。並且,即使係顯為2個細孔相接的情形,只要係在影像處理中接續之1個內部細孔,則仍計算為1個。在本發明中,上述截面之細孔面積比呈0.3百分比以下,故在本發明相關之製造方法中製造之鈦粉以使用在細孔不得不為少的技術領域(例如航空載具材料等)為合適。另一方面,若截面之細孔面積比超過0.3百分比,則表明在該技術領域使用一事實屬困難。With the manufacturing method of the titanium-based powder according to this embodiment, the following can be achieved: the cross-sectional area of the enclosed pores (hereinafter, the internal pores) appearing when an arbitrary cross section of the titanium-based powder is observed is divided by titanium The value of the cross-sectional area of the powder (cross-sectional area ratio of pores) is 0.3% or less. In addition, in the titanium-based powder produced in the present invention, it is preferable that the number of internal pores appearing when an arbitrary cross section of the titanium-based powder is observed is 20 per unit area / mm 2 or less. Here, the so-called pore area ratio of the cross section of the titanium-based powder is 0.3% or less, which means that after the titanium-based powder is buried in the resin and polished, the cross-section can be observed at an optical microscope at a magnification of 500 μm × 500 μm. In the case of 16 positions, the cross-sectional area of the internal pores observed by making an image in the range of brightness of 90 to 250 by image processing, divided by the total cross-sectional area of the powder is 0.3% or less. The number of internal pores means the number of internal pores observed when the above-mentioned observation is performed by making an image in the range of brightness of 90 to 250 by image processing. In addition, in any observation, powders with a long diameter of 10 μm or less due to image processing were excluded. In addition, in the image processing, even if the internal pores appear to be open from the original image, the pores (Figure 1 is a picture before the image processing, and Figure 2 is a picture after the image processing) are excluded. In addition, even if it is shown that two pores are connected, as long as one internal pore is connected during image processing, it is still counted as one. In the present invention, the pore area ratio of the above-mentioned cross section is 0.3% or less. Therefore, the titanium powder manufactured in the manufacturing method related to the present invention is used in a technical field where the pores have to be small (such as aviation vehicle materials). As appropriate. On the other hand, if the pore area ratio of the cross-section exceeds 0.3%, it indicates that it is difficult to use it in this technical field.

『實施例』『Examples』

[實施例1][Example 1]

使用海綿鈦作為鈦原料。所使用之鈦原料,使用總MgCl2 濃度及內部MgCl2 濃度皆在0.05 mass%以下、直徑為1/2吋以下者。Sponge titanium was used as the titanium raw material. The titanium raw materials used are those whose total MgCl 2 concentration and internal MgCl 2 concentration are both 0.05 mass% or less and the diameter is 1/2 inch or less.

將原料300 kg抽真空成5 Pa以下之後,以加熱器將氣體環境加熱至650℃,保持120分鐘。之後,供給氫並引發儲氫放熱之反應,同時使加熱器之控制或Ar氣插入及冷卻裝置運轉,在以鈦原料呈1000℃以下的方式進行溫度控制的同時,進行氫化120分鐘。此時之溫度範圍為716℃以上且1000℃以下。After 300 kg of the raw material was evacuated to 5 Pa or less, the gas environment was heated to 650 ° C with a heater and held for 120 minutes. After that, hydrogen was supplied and the reaction of hydrogen storage and exotherm was initiated. At the same time, the control of the heater or the Ar gas insertion and cooling device was operated, and the temperature of the titanium raw material was controlled to 1000 ° C or lower, and hydrogenation was performed for 120 minutes. The temperature range at this time is 716 ° C or higher and 1000 ° C or lower.

在氫化時之鈦原料的體密度為1.2 g/cm3The bulk density of the titanium raw material at the time of hydrogenation was 1.2 g / cm 3 .

之後,氫化鈦之塊狀體以粉碎/分級機粉碎而獲得粒徑為10 μm~150 μm的氫化鈦粉末。Thereafter, the titanium hydride bulk was pulverized by a pulverizer / classifier to obtain a titanium hydride powder having a particle diameter of 10 μm to 150 μm.

在真空熱處理爐條件下進行去氫處理之後,去氫鈦之塊狀體進行碎解處理。所獲得之鈦粉的D95粒徑為100 μm。After the dehydrogenation treatment is performed in a vacuum heat treatment furnace, the dehydrogenated titanium bulk is subjected to a disintegration treatment. The D95 particle diameter of the obtained titanium powder was 100 μm.

所獲得之鈦粉的光學顯微鏡照片揭示於圖3。在鈦粉埋進樹脂並研磨樣本之截面後,以光學顯微鏡在倍率500倍觀察700 μm×500 μm尺寸之任意位置的16個位置。分析細孔之數量與面積比的結果,所檢測到的細孔為每單位面積20個/mm2 。並且,細孔面積比為0.11%。An optical microscope photograph of the obtained titanium powder is shown in FIG. 3. After the titanium powder was embedded in the resin and the cross section of the sample was ground, 16 positions at any position of a size of 700 μm × 500 μm were observed with an optical microscope at a magnification of 500 times. As a result of analyzing the ratio of the number of pores to the area, the number of pores detected was 20 per unit area / mm 2 . The pore area ratio was 0.11%.

[實施例2][Example 2]

將「使用總MgCl2 濃度為0.1 mass%以下之海綿鈦原料製造的總MgCl2 濃度0.0002 mass%以下、其最大厚度為7 mm」之屑粉作為鈦原料使用。亦即,該鈦原料之內部MgCl2 濃度亦為0.0002 mass%以下。將原料300 kg抽真空成5 Pa以下之後,以加熱器將氣體環境加熱至650℃,保持120分鐘。之後,供給氫並引發儲氫放熱之反應,同時使加熱器控制或Ar氣插入及冷卻裝置運轉,在以鈦原料呈1000℃以下的方式進行溫度控制的同時,進行氫化120分鐘。此時之溫度範圍為716℃以上且1000℃以下。The chip powder of "a total MgCl 2 concentration of 0.0002 mass% or less and a maximum thickness of 7 mm produced using a sponge titanium raw material having a total MgCl 2 concentration of 0.1 mass% or less" was used as the titanium raw material. That is, the internal MgCl 2 concentration of the titanium raw material is also 0.0002 mass% or less. After 300 kg of the raw material was evacuated to 5 Pa or less, the gas environment was heated to 650 ° C with a heater and held for 120 minutes. After that, hydrogen was supplied and a reaction for exothermic hydrogen storage was initiated. At the same time, the heater control or the Ar gas insertion and cooling device was operated, and the temperature of the titanium raw material was controlled to 1000 ° C. or lower, and hydrogenation was performed for 120 minutes. The temperature range at this time is 716 ° C or higher and 1000 ° C or lower.

氫化時之體密度為1.2 g/cm3 。之後,氫化鈦之塊狀體以粉碎/分級機粉碎而獲得粒徑為10 μm~150 μm之氫化鈦粉末。之後,在真空熱處理爐條件下進行去氫處理之後,去氫鈦之塊狀體進行碎解處理。所獲得之鈦粉的D95粒徑為100 μm。The bulk density upon hydrogenation was 1.2 g / cm 3 . Thereafter, the titanium hydride bulk was pulverized with a pulverizer / classifier to obtain a titanium hydride powder having a particle diameter of 10 μm to 150 μm. After that, after performing dehydrogenation treatment in a vacuum heat treatment furnace condition, the dehydrogenated titanium bulk is subjected to disintegration treatment. The D95 particle diameter of the obtained titanium powder was 100 μm.

將所獲得之鈦粉埋進樹脂並研磨樣本之截面後,以光學顯微鏡在倍率500倍觀察700 μm×500 μm尺寸之任意位置的16個位置之結果,所檢測到的細孔為每單位面積8個/mm2 。並且,細孔面積比為0.02%。After the obtained titanium powder was buried in the resin and the cross section of the sample was ground, the optical microscope was used to observe 16 positions at any position of a size of 700 μm × 500 μm at a magnification of 500 times. The pores detected were per unit area. 8 pieces / mm 2 . The pore area ratio was 0.02%.

此外,在上述實施例2中,以係為鈦原料中之雜質的鐵濃度為200質量ppm以下,以及超過200質量ppm且500質量ppm以下這2種,來製造鈦粉。在任何情形中,所檢測到的細孔皆為每單位面積8~10個/mm2 。在任何情形中,細孔面積比皆為0.02%。職是,認為係為雜質之鐵量的多寡,換言之即鈦純度,與細孔的動作並無相關。Furthermore, in Example 2 described above, titanium powder was produced by using two kinds of iron concentrations of impurities in the titanium raw material as 200 mass ppm or less and more than 200 mass ppm and 500 mass ppm or less. In any case, the pores detected were 8 to 10 per unit area / mm 2 . In any case, the pore area ratio was 0.02%. It is considered that it is the amount of iron in impurities, in other words, the purity of titanium, and it has nothing to do with the action of pores.

[實施例3][Example 3]

使用總MgCl2 濃度為0.1 mass%以下之海綿鈦原料與60%Al―40%V之合金而製造之90%Ti―6%Al―4%V(質量%)屑粉作為原料使用。作為原料使用之鈦合金屑粉的總MgCl2 濃度為0.0002 mass%以下,其最大厚度為7 mm。亦即,該鈦合金屑粉之內部MgCl2 濃度亦為0.0002 mass%以下。將原料300 kg抽真空成5 Pa以下之後,以加熱器將氣體環境加熱至650℃,保持120分鐘。之後,供給氫並引發儲氫放熱之反應,同時使加熱器控制或Ar氣插入及冷卻裝置運轉,在以鈦合金屑粉呈1000℃以下的方式進行溫度控制的同時,進行氫化120分鐘。此時之溫度範圍為716℃以上且1000℃以下。90% Ti-6% Al-4% V (mass%) crumb powder manufactured using a sponge titanium raw material with a total MgCl 2 concentration of 0.1 mass% or less and 60% Al-40% V alloy is used as the raw material. The titanium alloy chip powder used as a raw material has a total MgCl 2 concentration of 0.0002 mass% or less, and a maximum thickness of 7 mm. That is, the internal MgCl 2 concentration of the titanium alloy chip powder is also 0.0002 mass% or less. After 300 kg of the raw material was evacuated to 5 Pa or less, the gas environment was heated to 650 ° C with a heater and held for 120 minutes. After that, hydrogen is supplied and a reaction for exothermic hydrogen storage is initiated. At the same time, the heater control or the Ar gas insertion and cooling device is operated, and the hydrogenation is performed for 120 minutes while controlling the temperature of the titanium alloy chip powder to 1000 ° C or lower. The temperature range at this time is 716 ° C or higher and 1000 ° C or lower.

氫化時之體密度為1.2 g/cm3 。之後,氫化鈦之塊狀體以粉碎/分級機粉碎而獲得10 μm~150 μm之粉末。之後,在真空熱處理爐條件下進行去氫處理,去氫鈦之塊狀體進行碎解處理。所獲得之鈦粉的D95粒徑為100 μm。The bulk density upon hydrogenation was 1.2 g / cm 3 . Thereafter, the bulk of the titanium hydride was pulverized by a pulverizer / classifier to obtain a powder of 10 μm to 150 μm. After that, a dehydrogenation treatment is performed under a vacuum heat treatment furnace condition, and the dehydrogenated titanium bulk is subjected to a disintegration treatment. The D95 particle diameter of the obtained titanium powder was 100 μm.

將所獲得之鈦合金粉埋進樹脂並研磨樣本之截面後,以光學顯微鏡在倍率500倍觀察700 μm×500 μm尺寸之任意位置的16個位置之結果,所檢測到的細孔為每單位面積9個/mm2 。並且,細孔面積比為0.03%。After the obtained titanium alloy powder was buried in the resin and the cross section of the sample was ground, the optical microscope was used to observe 16 positions at any position of a size of 700 μm × 500 μm at a magnification of 500 times. The pores detected were per unit. Area 9 pcs / mm 2 . The pore area ratio was 0.03%.

將在上述獲得之鈦合金粉利用高頻熱感應電漿裝置以Ar氣作為電漿氣體熔化表面以進行球狀化。此外,球狀化之條件如同表1。所獲得之鈦合金粉之光學顯微鏡照片揭示於圖4。鈦合金粉埋進樹脂,對樣本之截面以光學顯微鏡將倍率定為500倍觀察700 μm×500 μm尺寸之任意位置之16個位置。分析細孔之數量與面積比的結果,所檢測到的細孔為每單位面積3個/mm2 。並且,細孔面積比為0.01%。在HDH法中製造之經碎解的鈦合金粉,可確認到對球狀粉的原料粉末而言實屬有用。The titanium alloy powder obtained above was spheroidized by melting the surface with Ar gas as the plasma gas using a high-frequency thermal induction plasma device. The conditions for spheroidization are as shown in Table 1. An optical microscope photograph of the obtained titanium alloy powder is disclosed in FIG. 4. Titanium alloy powder was embedded in the resin, and the magnification of the cross section of the sample was set to 500 times with an optical microscope to observe 16 positions at any position of a size of 700 μm × 500 μm. As a result of analyzing the ratio of the number of pores to the area, the number of pores detected was 3 per unit area / mm 2 . The pore area ratio was 0.01%. It is confirmed that the disintegrated titanium alloy powder produced by the HDH method is useful for the raw material powder of the spherical powder.

『表1』
"Table 1"

[實施例4][Example 4]

使用總MgCl2 濃度為0.1 mass%以下之海綿鈦原料與70%Al―40%V之合金而製造之89%Ti―7%Al―4%V(質量%)屑粉作為原料使用。作為原料使用之鈦合金屑粉的總MgCl2 濃度為0.0002 mass%以下,其最大厚度為2 mm。亦即,該鈦合金屑粉之內部MgCl2 濃度亦為0.0002 mass%以下。將原料300 kg抽真空成5 Pa以下之後,以加熱器將氣體環境加熱至650℃,保持120分鐘。之後,供給氫並引發儲氫放熱之反應,同時使加熱器控制或Ar氣插入及冷卻裝置運轉,在以鈦合金屑粉呈1000℃以下的方式進行溫度控制的同時,進行氫化120分鐘。此時之溫度範圍為716℃以上且1000℃以下。89% Ti-7% Al-4% V (mass%) crumb powder made from an alloy of sponge titanium raw material with a total MgCl 2 concentration of 0.1 mass% or less and 70% Al-40% V is used as the raw material. The titanium alloy chip powder used as a raw material has a total MgCl 2 concentration of 0.0002 mass% or less and a maximum thickness of 2 mm. That is, the internal MgCl 2 concentration of the titanium alloy chip powder is also 0.0002 mass% or less. After 300 kg of the raw material was evacuated to 5 Pa or less, the gas environment was heated to 650 ° C with a heater and held for 120 minutes. After that, hydrogen is supplied and a reaction for exothermic hydrogen storage is initiated. At the same time, the heater control or the Ar gas insertion and cooling device is operated, and the hydrogenation is performed for 120 minutes while controlling the temperature of the titanium alloy chip powder to 1000 ° C or lower. The temperature range at this time is 716 ° C or higher and 1000 ° C or lower.

氫化時之體密度為1.2 g/cm3 。之後,氫化鈦之塊狀體以粉碎/分級機粉碎而獲得10 μm~150 μm之粉末。之後,在真空熱處理爐條件下進行去氫處理,去氫鈦之塊狀體進行碎解處理。所獲得之鈦粉的D95粒徑為100 μm。The bulk density upon hydrogenation was 1.2 g / cm 3 . Thereafter, the bulk of the titanium hydride was pulverized by a pulverizer / classifier to obtain a powder of 10 μm to 150 μm. After that, a dehydrogenation treatment is performed under a vacuum heat treatment furnace condition, and the dehydrogenated titanium bulk is subjected to a disintegration treatment. The D95 particle diameter of the obtained titanium powder was 100 μm.

將所獲得之鈦合金粉埋進樹脂並研磨樣本之截面後,以光學顯微鏡在倍率500倍觀察700 μm×500 μm尺寸之任意位置的16個位置之結果,所檢測到的細孔為每單位面積為9個/mm2 。並且,細孔面積比為0.03%。After the obtained titanium alloy powder was buried in the resin and the cross section of the sample was ground, the optical microscope was used to observe 16 positions at any position of a size of 700 μm × 500 μm at a magnification of 500 times. The pores detected were per unit. The area is 9 pieces / mm 2 . The pore area ratio was 0.03%.

與使用實施例2之鈦屑粉之結果比較,實施例3及實施例4之使用Ti―Al―V合金、屑粉之結果係同等。職是,本實施型態相關之鈦粉之製造方法,可認為亦合適於鈦合金粉之製造。Compared with the results of using the titanium shavings powder of Example 2, the results of using Ti—Al—V alloy and shavings powder of Examples 3 and 4 are equivalent. It is considered that the manufacturing method of the titanium powder related to this embodiment mode is also considered to be suitable for the manufacturing of titanium alloy powder.

[比較例1][Comparative Example 1]

使用內部MgCl2 濃度為0.2 mass%之海綿鈦作為鈦原料,其他以與實施例1同樣的條件製造鈦粉。此外,該海綿鈦之總MgCl2 濃度為0.3 mass%。將所獲得之鈦粉末埋進樹脂並研磨樣本之截面後,以光學顯微鏡將倍率定為500倍觀察700 μm×500 μm尺寸之任意位置的16個位置。分析細孔之數量與面積比的結果,所檢測到的細孔為每單位面積85個/mm2 。並且,細孔面積比為0.7%。Titanium sponge having an internal MgCl 2 concentration of 0.2 mass% was used as a titanium raw material, and titanium powder was produced under the same conditions as in Example 1. In addition, the total MgCl 2 concentration of the sponge titanium was 0.3 mass%. After the obtained titanium powder was buried in the resin and the cross section of the sample was ground, the magnification was set to 500 times with an optical microscope to observe 16 positions at any position of a size of 700 μm × 500 μm. As a result of analyzing the number of pores and the area ratio, the number of pores detected was 85 per unit area / mm 2 . The pore area ratio was 0.7%.

[比較例2][Comparative Example 2]

購入與實施例1同粒徑之在氣體霧化法中製造之鈦粉末,埋進樹脂並研磨樣本之截面後,以光學顯微鏡將倍率定為500倍觀察700 μm×500 μm尺寸之任意位置的16個位置。分析細孔之數量與面積比的結果,所檢測到的細孔為每單位面積130個/mm2 。並且,細孔面積比為1.0%(圖5)。The titanium powder manufactured in the gas atomization method with the same particle diameter as in Example 1 was purchased, and the cross section of the sample was buried in the resin, and then the magnification was set to 500 times with an optical microscope. 16 positions. As a result of analyzing the number of pores and the area ratio, the number of pores detected was 130 per unit area / mm 2 . The pore area ratio was 1.0% (Fig. 5).

無。no.

〈圖1〉係用以表示影像處理之方法的圖,尤其係繪示內包之細孔的圖。<Fig. 1> is a diagram showing a method of image processing, especially a diagram showing pores in an inner package.

〈圖2〉係用以表示影像處理之方法的圖,尤其係繪示呈開放之細孔的圖。 <Fig. 2> is a diagram showing a method of image processing, especially a diagram showing open fine holes.

〈圖3〉係實施例1相關之鈦粉的光學顯微鏡照片。 <Fig. 3> is an optical microscope photograph of the titanium powder according to Example 1.

〈圖4〉係實施例3相關之鈦粉的光學顯微鏡照片。 <Fig. 4> is an optical microscope photograph of the titanium powder according to Example 3.

〈圖5〉係在比較例2相關之鈦粉的光學顯微鏡照片中進行影像處理時的照片。 <Fig. 5> is a photograph when image processing is performed on an optical microscope photograph of the titanium powder according to Comparative Example 2.

Claims (7)

一種鈦系粉,其中將於前述鈦系粉之截面中細孔所佔之截面積除以前述鈦系粉之截面之面積的細孔面積比為0.3百分比以下。A titanium-based powder in which a pore area ratio of a cross-sectional area occupied by pores in a cross-section of the titanium-based powder divided by an area of a cross-section of the titanium-based powder is 0.3% or less. 如請求項1所述之鈦系粉,其中前述鈦系粉為HDH粉。The titanium-based powder according to claim 1, wherein the titanium-based powder is HDH powder. 一種鈦系粉之製造方法,其係對於鈦系原料使用包含氫化工序、粉碎工序、去氫工序之氫化去氫法的鈦系粉之製造方法,前述鈦系原料所含有之總MgCl2 的濃度為1.0 mass%以下,內部MgCl2 濃度為0.1 mass%以下。A method for producing a titanium-based powder, which is a method for producing a titanium-based powder by using a hydrogen-dehydrogenation method including a hydrogenation step, a pulverization step, and a dehydrogenation step, and a concentration of the total MgCl 2 contained in the titanium-based raw material. It is 1.0 mass% or less, and the internal MgCl 2 concentration is 0.1 mass% or less. 如請求項3所述之鈦系粉之製造方法,其中前述鈦系原料之最大厚度為20 mm以下。The method for manufacturing a titanium-based powder according to claim 3, wherein a maximum thickness of the aforementioned titanium-based raw material is 20 mm or less. 如請求項3所述之鈦系粉之製造方法,其中在前述粉碎工序中,氫化鈦系粉末粉碎至D95粒徑為300 μm以下。The method for producing a titanium-based powder according to claim 3, wherein in the aforementioned pulverizing step, the titanium hydride-based powder is pulverized to a D95 particle size of 300 μm or less. 如請求項4所述之鈦系粉之製造方法,其中在前述粉碎工序中,氫化鈦系粉末粉碎至D95粒徑為300 μm以下。The method for producing a titanium-based powder according to claim 4, wherein in the aforementioned pulverizing step, the titanium hydride-based powder is pulverized to a D95 particle size of 300 μm or less. 如請求項3至請求項6之任一項所述之鈦系粉之製造方法,其中在前述氫化工序中,在將前述鈦系原料之溫度調至716℃以上且1050℃以下之範圍內耗費90分鐘以上的時間使之氫化。The method for producing a titanium-based powder according to any one of claim 3 to claim 6, wherein in the aforementioned hydrogenation step, it costs to adjust the temperature of the aforementioned titanium-based raw material to a range of 716 ° C to 1050 ° C. It was hydrogenated for more than 90 minutes.
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