JPH07103407B2 - Continuous production method of rapidly solidified metal powder - Google Patents
Continuous production method of rapidly solidified metal powderInfo
- Publication number
- JPH07103407B2 JPH07103407B2 JP25574890A JP25574890A JPH07103407B2 JP H07103407 B2 JPH07103407 B2 JP H07103407B2 JP 25574890 A JP25574890 A JP 25574890A JP 25574890 A JP25574890 A JP 25574890A JP H07103407 B2 JPH07103407 B2 JP H07103407B2
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- JP
- Japan
- Prior art keywords
- cooling liquid
- metal powder
- peripheral surface
- liquid layer
- cylindrical body
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、金属溶湯を旋回移動する冷却液層中に噴射し
て金属粉末を製造する方法に関し、金属溶湯の粉末化か
ら脱液、乾燥まで連続的に処理することができる方法に
関するものである。Description: TECHNICAL FIELD The present invention relates to a method for producing a metal powder by injecting a molten metal into a swirling moving cooling liquid layer. Up to a method that can be continuously processed.
(従来の技術) 急冷凝固金属粉末は、結晶粒が微細で合金元素も過飽和
に含有させることができるので、例えばアルミニウムや
その合金の急冷凝固金属粉末によって形成された押出材
は、溶製材では具備することのない優れた材質特性を有
し、機械部品等の素材として注目されている。(Prior Art) Since the rapidly solidified metal powder has fine crystal grains and can contain alloy elements in a supersaturated state, for example, an extruded material formed by rapidly solidified metal powder of aluminum or its alloy is not included in the ingot material. It has excellent material characteristics that do not occur, and is attracting attention as a material for machine parts and the like.
前記急冷凝固金属粉末の好適な製造方法として、回転ド
ラム法がある。この方法は、第3図に示すように、回転
する冷却ドラム61の内周面に冷却液層62を遠心力の作用
で形成し、該冷却液層62に溶融金属を噴射し、微細に分
断して急冷凝固粉末を得る方法である。同図において、
63は加熱用の高周波コイル64が装着された噴射ルツボで
あり、その下部側壁には噴射ノズル65が開設されてい
る。前記ルツボ63内の溶融金属66は、該ルツボ63に不活
性ガス67を加圧注入することによって前記ノズル65から
噴出される。A rotating drum method is a suitable method for producing the rapidly solidified metal powder. According to this method, as shown in FIG. 3, a cooling liquid layer 62 is formed on the inner peripheral surface of a rotating cooling drum 61 by the action of centrifugal force, and molten metal is injected into the cooling liquid layer 62 to finely divide the cooling liquid layer 62. Is a method of obtaining a rapidly solidified powder. In the figure,
Reference numeral 63 is an injection crucible to which a high-frequency coil 64 for heating is attached, and an injection nozzle 65 is opened on the lower side wall thereof. Molten metal 66 in the crucible 63 is ejected from the nozzle 65 by injecting an inert gas 67 into the crucible 63 under pressure.
そして、冷却ドラム61内の金属粉末は、一定量溜まる
と、冷却ドラム61の回転を止め、冷却液と共に回収さ
れ、脱水後、乾燥される。Then, when a certain amount of the metal powder in the cooling drum 61 is accumulated, the rotation of the cooling drum 61 is stopped, the metal powder is collected together with the cooling liquid, dehydrated and then dried.
(発明が解決しようとする課題) しかしながら、回転ドラム法では、いわゆるバッチ式乾
燥となり、生産性が劣るうえ、粉末回収時に溶湯の噴射
も止めなければならないため、ノズルに孔詰りが生じ易
いという問題がある。また、金属溶湯の粉末化から乾燥
までの時間が長くなり、すなわち粉末が冷却液に接触し
ている時間が長く、粉末中の水素・酸素等のガス含有量
が増大し、粉末の押出時や押出材の熱処理時にガス欠陥
が生じ易くなるという問題がある。(Problems to be Solved by the Invention) However, in the rotary drum method, so-called batch type drying is performed, which is inferior in productivity, and since the injection of the molten metal must be stopped at the time of powder recovery, there is a problem that the nozzle is likely to be clogged. There is. In addition, the time from pulverization to drying of the molten metal is long, that is, the time the powder is in contact with the cooling liquid is long, the gas content of hydrogen, oxygen, etc. in the powder is increased, and There is a problem that gas defects are likely to occur during heat treatment of the extruded material.
本発明はかかる問題に鑑みなされたもので、金属粉末の
連続生産が可能で、また粉末化から乾燥まで速やかに処
理することができる急冷凝固金属粉末の連続製造方法を
提供することを目的とする。The present invention has been made in view of the above problems, and an object of the present invention is to provide a continuous production method of rapidly solidified metal powder capable of continuous production of metal powder and capable of being rapidly processed from pulverization to drying. .
(課題を解決するための手段) 上記問題を解決するためになされた本発明の製造方法
は、筒体21の内周面に沿って冷却液を噴出供給して筒体
内周面に沿って旋回しながら流下する冷却液層31を形成
し、該冷却液層31の内周面側より金属溶湯を噴射し、冷
却液層31によって分断し冷却凝固させて金属粉末を得、
筒体21より冷却液と共に流下した金属粉末を連続的に脱
液した後、続いて連続的に乾燥することを発明の構成と
するものである。(Means for Solving the Problem) The manufacturing method of the present invention made to solve the above-mentioned problem is such that the cooling liquid is jetted and supplied along the inner peripheral surface of the cylindrical body 21 and swirled along the inner peripheral surface of the cylindrical body. While forming the cooling liquid layer 31 flowing down, injecting a molten metal from the inner peripheral surface side of the cooling liquid layer 31, to obtain a metal powder by cooling and solidifying by cutting by the cooling liquid layer 31,
The configuration of the present invention is that the metal powder that has flowed down from the cylindrical body 21 together with the cooling liquid is continuously drained and then continuously dried.
(作 用) 筒体21の内周面に沿って噴出供給された冷却液は、筒体
内周面に沿って旋回しながら流下し、旋回時の遠心力の
作用でほぼ一定内径の冷却液層31を形成する。この冷却
液層31の内周面より金属溶湯を噴射供給すると、溶湯は
旋回流により分断されると共に急冷凝固され、粉末とな
る。(Operation) The cooling liquid jetted and supplied along the inner peripheral surface of the cylindrical body 21 flows down while swirling along the inner peripheral surface of the cylindrical body, and the centrifugal force at the time of swirling causes the cooling liquid layer having a substantially constant inner diameter. Forming 31. When the molten metal is injected and supplied from the inner peripheral surface of the cooling liquid layer 31, the molten metal is divided by the swirling flow and rapidly cooled and solidified into powder.
この際、冷却液層31は常に新たに供給される冷却液によ
って形成されるために一定の温度が容易に維持される。
このため、温度制御のために液面より冷却液を排出、供
給する必要がなく、液面には乱れは生じず、安定した状
態が維持される。それ故、冷却液層31に噴射された金属
溶湯は常に一定状態の下で冷却液層31中に注入、分断さ
れ、一定温度の下で冷却凝固されるため、金属粉末の品
質が安定する。At this time, since the cooling liquid layer 31 is always formed by the newly supplied cooling liquid, a constant temperature is easily maintained.
Therefore, it is not necessary to discharge and supply the cooling liquid from the liquid surface for temperature control, and the liquid surface is not disturbed and a stable state is maintained. Therefore, the molten metal injected into the cooling liquid layer 31 is constantly injected into the cooling liquid layer 31 under a constant state, is divided, and is cooled and solidified at a constant temperature, so that the quality of the metal powder is stabilized.
冷却液層31中の金属粉末は冷却液と共に旋回しながら流
下し、筒体21の下端より排出されるので、金属粉末の連
続生産が可能となる。The metal powder in the cooling liquid layer 31 flows down while swirling together with the cooling liquid and is discharged from the lower end of the cylindrical body 21, so that continuous production of the metal powder is possible.
更に、冷却液と共に排出された金属粉末は、連続的に脱
液され、続いて乾燥されるので、粉化から乾燥まで冷却
液と接触している期間が短かく、ガス成分の吸収が少な
い。Furthermore, since the metal powder discharged together with the cooling liquid is continuously deliquored and subsequently dried, the period of contact with the cooling liquid from pulverization to drying is short, and the absorption of gas components is small.
(実施例) 第1図は本発明を実施するための装置の全体構成を示し
ており、連続注湯装置1から送出された金属溶湯は、粉
化装置2、連続脱液機3および連続乾燥装置4を経て製
品金属粉末とされる。(Example) FIG. 1 shows the overall configuration of an apparatus for carrying out the present invention. The molten metal sent from the continuous pouring apparatus 1 is a powdering apparatus 2, a continuous dewatering machine 3, and a continuous drying apparatus. The product metal powder is passed through the device 4.
前記連続注湯装置1は、耐火性断熱材で形成された本体
容器6を備え、該容器6には蓋体7により密閉自在とさ
れた金属溶湯供給口8が開設され、不活性ガス等の圧媒
供給管9、容器内溶湯の排出管10が設けられており、底
部には誘導加熱用コイル11を有する凹部12が設けられて
いる。該コイル11によって、容器6内の金属溶湯13は温
度制御が行われ、圧媒供給管9より注入されるアルゴン
ガス等の不活性ガスにより排出管10を介して粉化装置2
へ圧送される。排出管10は、断熱層の形成やインダクシ
ョンヒータ等の適宜の保温手段により保温される。The continuous pouring device 1 includes a main body container 6 formed of a refractory heat insulating material, and the container 6 is provided with a metal melt supply port 8 which can be sealed by a lid 7 so that an inert gas or the like A pressure medium supply pipe 9 and a discharge pipe 10 for the molten metal in the container are provided, and a recess 12 having an induction heating coil 11 is provided at the bottom. The temperature of the molten metal 13 in the container 6 is controlled by the coil 11, and the powdering device 2 is evacuated by the inert gas such as argon gas injected from the pressure medium supply pipe 9 through the discharge pipe 10.
Pumped to. The discharge pipe 10 is kept warm by the formation of a heat insulating layer and an appropriate heat keeping means such as an induction heater.
前記粉化装置2は、旋回する冷却液層を形成するための
筒体21と、冷却液層に金属溶湯を噴射供給するための噴
射ルツボ22と、前記筒体21に冷却液を供給するためのポ
ンプ26等の手段とを備えている。The pulverization device 2 is provided with a cylinder 21 for forming a swirling cooling liquid layer, an injection crucible 22 for injecting and supplying molten metal into the cooling liquid layer, and for supplying the cooling liquid to the cylinder 21. The pump 26 and other means.
前記筒体21は、第2図に示すように、円筒状であり、そ
の上端には中心部に適宜大きさの開口23を有する蓋体24
が被着形成されており、上端部外周側には筒体内周面に
沿って接線方向から冷却液を噴出供給するための冷却液
噴出孔25が設けられており、ポンプ26の吐出口に配管接
続されている。筒体21の中間部内周面には冷却液層の層
厚調整用リング27がボルト28によって着脱、交換自在に
取り付けられている。筒体21の下端には液切り用の円筒
状網体29が連設されており、その下端には漏斗体30が取
り付けられている。As shown in FIG. 2, the tubular body 21 has a cylindrical shape, and a lid body 24 having an opening 23 of an appropriate size in the center portion at the upper end thereof.
Is formed on the outer peripheral side of the upper end portion thereof, and a cooling liquid ejection hole 25 for ejecting and supplying the cooling liquid from the tangential direction along the outer peripheral surface of the cylinder is provided, and a pipe is provided at the discharge port of the pump 26. It is connected. A ring thickness adjusting ring 27 for the cooling liquid layer is detachably attached and replaceable by a bolt 28 on the inner peripheral surface of the middle portion of the cylindrical body 21. A cylindrical net body 29 for draining liquid is continuously provided at the lower end of the tubular body 21, and a funnel body 30 is attached to the lower end thereof.
冷却液噴出孔25から筒体21内周面に沿って噴出された冷
却液は、筒体21内周面に沿って旋回しながら流下すると
共に旋回流の遠心力の作用で一定内径の冷却液層31を形
成する。層厚調整用リング27を乗り越えて流下した冷却
液は、遠心力の作用で網体29より排出されると共に漏斗
体30に流入する。網体29より排出された冷却液は、網体
29の外周に設けられたカバー32の底部よりタンク33に回
収される。タンク33内の冷却液はポンプ26によって筒体
21に循環供給される。尚、タンク33には、図示省略の補
給用の冷却液供給管が設けられ、またタンク内や循環経
路の途中に冷却器を適宜介在させてもよい。冷却液とし
ては、一般的に水が使用される。The cooling liquid ejected from the cooling liquid ejection hole 25 along the inner peripheral surface of the cylindrical body 21 flows down while swirling along the inner peripheral surface of the cylindrical body 21, and at the same time, the cooling liquid having a constant inner diameter by the action of the centrifugal force of the swirling flow. Form layer 31. The cooling liquid which has flowed over the layer thickness adjusting ring 27 and flows down is discharged from the net body 29 and flows into the funnel body 30 by the action of centrifugal force. The cooling liquid discharged from the net 29 is
It is collected in the tank 33 from the bottom of the cover 32 provided on the outer periphery of 29. The coolant in the tank 33 is cylindrical by the pump 26.
Circulated to 21. The tank 33 may be provided with a replenishing cooling liquid supply pipe (not shown), and a cooler may be appropriately interposed in the tank or in the circulation path. Water is generally used as the cooling liquid.
前記蓋体24の上方には金属溶湯供給手段としての噴射ル
ツボ22が設けられており、その外周には加熱用コイル36
が巻回形成され、その底部にはノズル孔37が開設されて
いる。噴射ルツボ22には前記連続注湯装置1から金属溶
湯が圧送される。An injection crucible 22 as a molten metal supply means is provided above the lid 24, and a heating coil 36 is provided on the outer periphery thereof.
Is wound and formed with a nozzle hole 37 at the bottom thereof. The molten metal is pressure-fed from the continuous pouring device 1 to the injection crucible 22.
前記連続脱液機3は、上方に拡経した回転ドラム41を備
え、該ドラム41の中間部周壁は多数の細孔を有するスク
リーンプレートで形成され、内周面には脱水後の粉末を
上方へ送り出すための凸状リブ42が多数形成されてい
る。回転ドラム41の外周面側には冷却液回収カバー43が
設けられており、脱液された冷却液は、その底部よりタ
ンク33に回収される。また、回転ドラム41の上部には金
属粉末回収カバー44が設けられ、排出シュート45が付設
されている。The continuous liquid eliminator 3 includes a rotating drum 41 which is expanded upward, and an intermediate peripheral wall of the drum 41 is formed of a screen plate having a large number of pores. A large number of convex ribs 42 for sending out to the are formed. A cooling liquid recovery cover 43 is provided on the outer peripheral surface side of the rotary drum 41, and the drained cooling liquid is recovered in the tank 33 from the bottom thereof. Further, a metal powder recovery cover 44 is provided above the rotary drum 41, and a discharge chute 45 is attached.
前記連続乾燥装置4は、多数の細孔を有する流動48を有
する乾燥容器47と、該容器47の上部より湿潤原料を供給
するためのロータリーフィーダーを有する供給装置49
と、容器47の下部より熱風を供給するための熱風発生装
置50と、容器47上部より排出した排風より微粉を捕収す
るためのサイクロン51とを備えており、容器47の上部お
よび下部側壁には排出管52が付設されている。The continuous drying device 4 includes a drying container 47 having a flow 48 having a large number of pores, and a supply device 49 having a rotary feeder for supplying a wet raw material from the upper part of the container 47.
And a hot air generator 50 for supplying hot air from the lower part of the container 47, and a cyclone 51 for collecting fine powder from the exhaust air discharged from the upper part of the container 47, and the upper and lower side walls of the container 47. A discharge pipe 52 is attached to the.
本発明を実施するには、先ずポンプ26を作動させて、筒
体21の内周面に高速旋回しながら流下する冷却液層31を
形成する。In order to carry out the present invention, first, the pump 26 is operated to form a cooling liquid layer 31 that flows down while swirling at high speed on the inner peripheral surface of the cylindrical body 21.
次に、筒体21の上部に設けられた噴射ルツボ22に連続注
湯装置1より金属溶湯を圧送し、ルツボ22内の金属溶湯
38をノズル孔37より冷却液層31内面に噴射し、分断、急
冷凝固させて粉末化する。Next, the molten metal in the crucible 22 is pressure-fed from the continuous pouring device 1 to the injection crucible 22 provided in the upper part of the cylinder 21.
38 is sprayed from the nozzle hole 37 to the inner surface of the cooling liquid layer 31, divided, rapidly cooled and solidified to be powdered.
金属粉末は冷却液層31を形成した冷却液と共に液体21の
下端開口より排出される。冷却液の大部分は、漏斗体30
に流下するまでに、冷却液自体のもつ遠心力の作用で網
体29によって分離排出される。漏斗体30に流下した金属
粉末と冷却液は、引き続いて連続脱液機3に供給され、
遠心力の作用で脱液される。この際、前記網体29によっ
て、処理物は一次脱液されているので、脱液効率が良好
である。The metal powder is discharged from the lower end opening of the liquid 21 together with the cooling liquid forming the cooling liquid layer 31. Most of the coolant is a funnel body 30
By the action of the centrifugal force of the cooling liquid itself, it is separated and discharged by the mesh 29 before it flows down to the. The metal powder and the cooling liquid flowing down to the funnel body 30 are continuously supplied to the continuous liquid remover 3,
It is drained by the action of centrifugal force. At this time, since the treated material is primarily deliquored by the net 29, the deliquoring efficiency is good.
連続脱液機3の排出シュート45より排出された湿潤金属
粉末は引き続いて連続乾燥装置4の供給装置49へ投入さ
れ、ロータリーフィーダーによって乾燥容器47に送り込
まれる。容器47内では流動床48上に下から吹き上げられ
る熱風によって流動層53が形成されており、湿潤金属粉
末は、流動層53中で熱風と激しく混合され、熱交換さ
れ、速やかに乾燥されて、通常オーバーフローにより排
出管52を介して外部に取り出される。The wet metal powder discharged from the discharge chute 45 of the continuous dewatering device 3 is subsequently put into the supply device 49 of the continuous drying device 4 and sent into the drying container 47 by the rotary feeder. The fluidized bed 53 is formed by hot air blown from below on the fluidized bed 48 in the container 47, the wet metal powder is vigorously mixed with hot air in the fluidized bed 53, heat exchanged, and quickly dried, Usually, it is taken out to the outside through the discharge pipe 52 by overflow.
尚、本発明を実施するに際して、連続注湯装置、連続脱
液機、連続乾燥装置は既述のものに限らず、市場に供給
されている適宜のものを使用することができる。In carrying out the present invention, the continuous pouring device, the continuous dewatering device, and the continuous drying device are not limited to those described above, and any appropriate device supplied to the market can be used.
(発明の効果) 以上説明した通り、本発明の急冷凝固金属粉末の連続製
造方法は、筒体の内周面に沿って冷却液を噴出供給し
て、筒体内周面に沿って旋回しながら流下する冷却液層
を形成するので、金属溶湯が注入される冷却液層の内周
面が安定し、冷却液層の温度も容易に均一に保持され
る。そして、該冷却液層中に金属溶湯を噴射供給するの
で、品質一定の急冷凝固粉末が連続的に生産され、生産
性が高く、噴射ノズルに孔詰りも生じない。また、冷却
液と共に流下された金属粉末は、連続的に脱液、乾燥さ
れるため、冷却液と接触する時間が短縮され、ガス含有
量を低減させることができ、押出等の加工時に生じるガ
ス欠陥の防止に寄与することができる。(Effects of the Invention) As described above, the method for continuously producing rapidly solidified metal powder according to the present invention is such that the cooling liquid is jetted and supplied along the inner peripheral surface of the cylindrical body while swirling along the peripheral surface of the cylindrical body. Since the flowing cooling liquid layer is formed, the inner peripheral surface of the cooling liquid layer into which the molten metal is poured is stabilized, and the temperature of the cooling liquid layer is easily and uniformly maintained. Further, since the molten metal is injected and supplied into the cooling liquid layer, the rapidly solidified powder having a constant quality is continuously produced, the productivity is high, and the injection nozzle is not clogged. Further, since the metal powder flowed down together with the cooling liquid is continuously removed and dried, the time for contact with the cooling liquid can be shortened, the gas content can be reduced, and the gas generated during processing such as extrusion can be reduced. It can contribute to the prevention of defects.
第1図は本発明を実施するための金属粉末製造設備の全
体構成図、第2図は金属粉末を連続生産するための筒体
の断面図、第3図は従来の金属粉末製造装置の要部断面
図である。 21……筒体、31……冷却液層。FIG. 1 is an overall configuration diagram of a metal powder production facility for carrying out the present invention, FIG. 2 is a cross-sectional view of a cylinder for continuously producing metal powder, and FIG. 3 is a view of a conventional metal powder production apparatus. FIG. 21 …… Cylinder, 31 …… Coolant layer.
Claims (1)
供給して筒体内周面に沿って旋回しながら流下する冷却
液層(31)を形成し、該冷却液層(31)の内周面側より
金属溶湯を噴射し、冷却液層(31)によって分断し冷却
凝固させて金属粉末を得、筒体(21)より冷却液と共に
流下した金属粉末を連続的に脱液した後、続いて連続的
に乾燥することを特徴とする急冷凝固金属粉末の連続製
造方法。1. A cooling liquid layer (31) is formed by jetting and supplying a cooling liquid along the inner peripheral surface of a cylindrical body (21) while swirling along the peripheral surface of the cylindrical body, and forming the cooling liquid layer. The metal melt is injected from the inner peripheral surface side of (31), divided by the cooling liquid layer (31) and cooled and solidified to obtain a metal powder, and the metal powder flowing down together with the cooling liquid from the cylindrical body (21) is continuously supplied. A method for continuously producing rapidly solidified metal powder, which comprises continuously drying after deliquoring.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25574890A JPH07103407B2 (en) | 1990-09-25 | 1990-09-25 | Continuous production method of rapidly solidified metal powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25574890A JPH07103407B2 (en) | 1990-09-25 | 1990-09-25 | Continuous production method of rapidly solidified metal powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04136108A JPH04136108A (en) | 1992-05-11 |
| JPH07103407B2 true JPH07103407B2 (en) | 1995-11-08 |
Family
ID=17283086
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP25574890A Expired - Lifetime JPH07103407B2 (en) | 1990-09-25 | 1990-09-25 | Continuous production method of rapidly solidified metal powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07103407B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115837468B (en) * | 2023-02-23 | 2023-05-05 | 天津市生态环境科学研究院(天津市环境规划院、天津市低碳发展研究中心) | Production equipment for rapidly solidifying metal powder |
-
1990
- 1990-09-25 JP JP25574890A patent/JPH07103407B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04136108A (en) | 1992-05-11 |
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