JP3263605B2 - Hydrogen storage alloy - Google Patents
Hydrogen storage alloyInfo
- Publication number
- JP3263605B2 JP3263605B2 JP21530696A JP21530696A JP3263605B2 JP 3263605 B2 JP3263605 B2 JP 3263605B2 JP 21530696 A JP21530696 A JP 21530696A JP 21530696 A JP21530696 A JP 21530696A JP 3263605 B2 JP3263605 B2 JP 3263605B2
- Authority
- JP
- Japan
- Prior art keywords
- alloy
- hydrogen storage
- storage alloy
- hydrogen
- quenching
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Battery Electrode And Active Subsutance (AREA)
Description
【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION
【0001】[0001]
【発明の属する技術分野】本発明は、水素を吸蔵及び放
出する水素吸蔵合金に関するものであり、具体的には、
ヒステリシスが小さく、プラトーが低勾配で、水素吸収
/放出の可逆性に優れる水素吸蔵合金に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hydrogen storage alloy for storing and releasing hydrogen.
The present invention relates to a hydrogen storage alloy having a small hysteresis, a low plateau, and excellent reversibility of hydrogen absorption / desorption.
【0002】[0002]
【従来の技術】水素吸蔵合金の水素吸収/放出特性は、
燃料電池やヒートポンプ、蓄熱装置等の種々の装置に利
用されている。水素吸蔵合金の特性は、水素圧力−水素
吸収量等温曲線(P−C−T特性曲線)により評価するこ
とができる。P−C−T特性曲線は、水素固溶領域及び
金属水素化合物領域と、これら領域に挟まれたプラトー
領域で示される。水素吸蔵合金は水素の吸収時と放出時
とではヒステリシスがみられ、またプラトーは平坦では
なく傾斜している。これらの傾向は、殆んどすべての水
素吸蔵合金にみられるものであるが、これら特性が上記
装置の性能に大きく影響を及ぼす。例えば、ヒステリシ
スが大きいと水素圧力差を取りにくくなり、使用温度領
域に制限を受けやすい。また、プラトーの傾斜が大きく
なると、移動する水素量に大きく影響するため、効率が
悪くなる。そこで、ヒステリシスが小さく、且つプラト
ーが平坦、即ちプラトーの傾きが小さく、水素吸収/放
出を高可逆性を以て行なうことのできる水素吸蔵合金の
開発が望まれている。2. Description of the Related Art The hydrogen absorption / release characteristics of a hydrogen storage alloy are as follows.
It is used in various devices such as fuel cells, heat pumps, and heat storage devices. The characteristics of the hydrogen storage alloy can be evaluated by a hydrogen pressure-hydrogen absorption amount isothermal curve (PCT characteristic curve). The PCT characteristic curve is represented by a hydrogen solid solution region and a metal hydride compound region, and a plateau region sandwiched between these regions. The hydrogen storage alloy has a hysteresis between the time of hydrogen absorption and the time of hydrogen release, and the plateau is not flat but inclined. These tendencies are found in almost all hydrogen storage alloys, but these properties greatly affect the performance of the device. For example, if the hysteresis is large, it is difficult to obtain a hydrogen pressure difference, and the operating temperature range is likely to be restricted. In addition, when the inclination of the plateau is large, the amount of moving hydrogen is greatly affected, so that the efficiency is deteriorated. Therefore, it is desired to develop a hydrogen storage alloy having a small hysteresis and a flat plateau, that is, a small inclination of the plateau, and capable of performing hydrogen absorption / desorption with high reversibility.
【0003】水素の吸収/放出を高可逆的に行なうに
は、合金組織の均質性の確保が重要となる。水素吸蔵合
金の作製方法として、水素吸蔵合金の粉末をアーク溶解
炉や高周波誘導炉で溶解する方法がある。この方法で作
製された水素吸蔵合金には、必要に応じて加熱温度10
00〜1400Kにて2〜24時間加熱した後、徐冷を
行なう熱処理が施されるが、得られた水素吸蔵合金の組
織は十分に均質化されていないため、水素の吸収/放出
を高可逆的に行なうことはできなかった。In order to reversibly absorb and release hydrogen, it is important to ensure the homogeneity of the alloy structure. As a method for producing a hydrogen storage alloy, there is a method of melting a powder of a hydrogen storage alloy in an arc melting furnace or a high-frequency induction furnace. The hydrogen storage alloy produced by this method may have a heating temperature of 10 if necessary.
After heating at 00 to 1400 K for 2 to 24 hours, a heat treatment for slow cooling is performed. However, since the structure of the obtained hydrogen storage alloy is not sufficiently homogenized, hydrogen absorption / release is highly reversible. Could not be done.
【0004】また、水素吸蔵合金の作製方法として、溶
湯状の水素吸蔵合金を高速回転するロールに噴射するロ
ール急冷法等の急冷による方法が知られている。しかし
ながら、急冷による合金の作製は、作製プロセスが複雑
であり、また、合金を溶湯の状態から冷却するため、組
織の均質性は向上するが、冷却速度が大きすぎて結晶格
子に歪が生じることがあり、却って可逆性が損われるこ
とがあった。Further, as a method for producing a hydrogen storage alloy, a method of rapid cooling such as a roll quenching method in which a molten hydrogen storage alloy is injected onto a roll rotating at high speed is known. However, the production of alloys by quenching is complicated in the production process.Also, since the alloy is cooled from the molten state, the homogeneity of the structure is improved, but the cooling rate is too high and the crystal lattice is distorted. In some cases, reversibility was impaired.
【0005】[0005]
【発明が解決しようとする課題】本発明の目的は、ヒス
テリシスが小さく、且つプラトーの傾きが小さく、水素
吸収/放出を高可逆的に行なうことのできる水素吸蔵合
金を提供することである。SUMMARY OF THE INVENTION It is an object of the present invention to provide a hydrogen storage alloy which has a small hysteresis, a small plateau gradient, and which can reversibly absorb and release hydrogen.
【0006】[0006]
【課題を解決するための手段】上記課題を解決するため
に、本発明は、組成式A1-xQxB5-yRy(但しAはLa
又はMm(ミッシュメタル)、QはY、BはNi、RはA
l及び/又はMn、x及びyは夫々0.1≦x≦0.3、
0≦y≦1)で表わされる合金のインゴットを、融点よ
りも低い温度、即ち合金が固相の状態を維持する温度
で、所定時間加熱した後、液体冷媒中に浸漬して急冷す
る固相急冷処理を施すことにより、母相中にYが均一に
分散した水素吸蔵合金を作製するものである。固相急冷
処理は、合金の融点の絶対温度の2/3以上で、融点よ
りも低い温度で行なうことが望ましい。また、固相急冷
処理は、99.9999%以上の高純度不活性ガス雰囲
気中で行なうことが望ましい。Means for Solving the Problems In order to solve the above-mentioned problems, the present invention provides a composition represented by the formula A 1-x Q x B 5-y R y (where A is La
Or Mm (Misch metal), Q is Y, B is Ni, R is A
l and / or Mn, x and y are each 0.1 ≦ x ≦ 0.3,
The ingot of the alloy represented by 0 ≦ y ≦ 1) is heated for a predetermined time at a temperature lower than the melting point, that is, at a temperature at which the alloy maintains a solid state, and then immersed in a liquid refrigerant and rapidly cooled. By performing the quenching treatment , Y is evenly distributed in the matrix.
This is for producing a dispersed hydrogen storage alloy. The solid phase quenching treatment is desirably performed at a temperature that is at least 2/3 of the absolute temperature of the melting point of the alloy and lower than the melting point. Further, the solid phase quenching treatment is desirably performed in an atmosphere of a high-purity inert gas of 99.9999% or more.
【0007】[0007]
【作用】水素吸蔵合金のインゴットを、融点よりも低い
温度で加熱して、液体冷媒で急冷することにより、合金
組織の均質性を向上させることができる。従って、ヒス
テリシスが小さく、プラトーの傾きが小さく、高可逆性
を有する水素吸蔵合金を得ることができる。固相急冷処
理を合金の融点よりも低い温度で行なうのは、合金が溶
解しない固相の状態で固相急冷処理を行なうためであ
る。合金の融点以上の温度で加熱すると、合金が溶解
し、急冷の際に結晶格子に歪が生じることがあるからで
ある。固相急冷処理を融点の絶対温度の2/3以上の温
度で行なうのは、これよりも低い温度で実施すると、合
金を十分に均質化することが困難になることがあるから
である。固相急冷処理を99.9999%以上の高純度
不活性ガス雰囲気中で行なうのは、水素吸蔵合金は、酸
化されやすいため、その酸化を防止する必要があるため
である。The ingot of a hydrogen storage alloy is heated at a temperature lower than the melting point and rapidly cooled with a liquid refrigerant, whereby the homogeneity of the alloy structure can be improved. Therefore, a hydrogen storage alloy having small hysteresis, small plateau slope, and high reversibility can be obtained. The reason that the solid phase quenching treatment is performed at a temperature lower than the melting point of the alloy is to perform the solid phase quenching treatment in a solid state where the alloy is not melted. This is because when heated at a temperature equal to or higher than the melting point of the alloy, the alloy is melted, and the crystal lattice may be distorted during rapid cooling. The reason that the solid phase quenching treatment is performed at a temperature equal to or more than 2/3 of the absolute temperature of the melting point is that if the temperature is lower than this, it may be difficult to sufficiently homogenize the alloy. The solid-phase quenching treatment is performed in a high-purity inert gas atmosphere of 99.9999% or more because the hydrogen storage alloy is easily oxidized, and thus it is necessary to prevent the oxidation.
【0008】[0008]
【発明の実施の形態】まず、本発明の水素吸蔵合金を作
製する熱処理装置について例を挙げて説明する。熱処理
装置は、図1、図2に示すように、加熱炉(1)と急冷室
(2)を搬送通路(3)で繋ぎ、搬送通路(3)には通路を気密
に仕切るシャッター(31)を配備している。加熱炉(1)に
は、対向配備された一対のヒータ(11)(11)と、各ヒータ
の後方に設けられた反射板(12)(12)を具えており、ヒー
タ(11)(11)間が炉の有効空間となっている。1組のヒー
タ(11)と反射板(12)は、炉の扉(10)に取り付けられてい
る。扉(10)を閉じると炉の気密が保たれる。DESCRIPTION OF THE PREFERRED EMBODIMENTS First, a heat treatment apparatus for producing a hydrogen storage alloy according to the present invention will be described with reference to examples. The heat treatment equipment consists of a heating furnace (1) and a quenching chamber, as shown in Figs.
(2) is connected by a transport passage (3), and a shutter (31) for airtightly partitioning the passage is provided in the transport passage (3). The heating furnace (1) is provided with a pair of heaters (11) and (11) arranged opposite to each other and reflectors (12) and (12) provided behind each heater. The space between) is the effective space of the furnace. One set of heater (11) and reflector (12) is attached to the furnace door (10). Closing the door (10) keeps the furnace airtight.
【0009】加熱炉(1)には、炉から水素吸蔵合金を気
密搬送通路(3)を通って急冷室(2)に移送する移送手段
(5)が設けられている。移送手段(5)は、前記搬送通路
(3)の延長上にて、加熱炉(1)の側面を気密にスライド可
能に貫通した棒状プッシャー(51)であって、該プッシャ
ーの基端は、加熱炉(1)の外側に配備されたスライド駆
動装置(52)に連繋される。スライド駆動装置(52)は、ラ
ックとピニオンの組合せ、シリンダ装置等の機構であ
り、プッシャー(51)を、その先端が加熱炉(1)から急冷
室(2)へ届くストロークで直線往復運動させることがで
きる。The heating furnace (1) has a transfer means for transferring the hydrogen storage alloy from the furnace to the quenching chamber (2) through an airtight transfer passage (3).
(5) is provided. The transfer means (5) is provided in the transfer passage.
On the extension of (3), a rod-shaped pusher (51) penetrating the side surface of the heating furnace (1) so as to be slidable in an airtight manner, and the base end of the pusher is provided outside the heating furnace (1). Connected to the slide drive device (52). The slide drive device (52) is a mechanism such as a combination of a rack and a pinion, a cylinder device, etc., and causes the pusher (51) to reciprocate linearly with a stroke whose tip reaches the quenching chamber (2) from the heating furnace (1). be able to.
【0010】急冷室(2)は、上記プッシャー(51)によっ
て送り込まれた水素吸蔵合金が載置されるテーブル(2
1)、該テーブル(21)に対してプッシャー(51)とは直交す
る方向の下方位置に配備された液体冷媒を収容する槽(2
2)、急冷室(2)の側壁を気密スライド可能に貫通してテ
ーブル(21)上の水素吸蔵合金を槽(22)に突き落とす突落
とし棒(6)を配備しており、突落とし棒(6)の基端は、急
冷室(2)の外部に配備されたスライド駆動装置(61)に連
繋されている。突落とし棒(6)のスライド駆動装置(61)
は、前記プッシャー(51)のスライド駆動装置(52)と同様
の機構を具えており、テーブル(21)の水素吸蔵合金を槽
(22)に突き落とすことができる。槽(22)に収容する液体
冷媒として、クエンチングオイル、水、液体窒素等を挙
げることができる。急冷室(2)の側面には、扉(20)が設
けられており、扉(20)を閉じると急冷室(2)の気密が保
たれる。The quenching chamber (2) has a table (2) on which the hydrogen storage alloy fed by the pusher (51) is placed.
1), a tank (2) containing a liquid refrigerant disposed at a position below the table (21) in a direction orthogonal to the pusher (51).
2), a drop-off rod (6) that penetrates the side wall of the quenching chamber (2) in a slidable manner and drops the hydrogen storage alloy on the table (21) into the tank (22) is provided. The base end of 6) is connected to a slide drive device (61) provided outside the quenching chamber (2). Slide drive (61) of push-down rod (6)
Has a mechanism similar to that of the slide drive device (52) of the pusher (51), and stores the hydrogen storage alloy of the table (21) in a tank.
(22). Quenching oil, water, liquid nitrogen, and the like can be given as the liquid refrigerant stored in the tank (22). A door (20) is provided on the side of the quenching chamber (2), and when the door (20) is closed, the airtightness of the quenching chamber (2) is maintained.
【0011】次に、上記加熱炉(1)及び急冷室(2)の雰囲
気を不活性ガスに置換する装置について説明する。加熱
炉(1)及び急冷室(2)は、共通の吸引装置(4)が連繋され
る。吸引装置(4)は、メカニカルブースターポンプ(43)
を上流側に、ロータリーポンプ(44)を下流側に具えた管
路(40)を上流側に二股に分岐し、夫々の分岐先端を加熱
炉(1)と急冷室(2)に接続している。管路(40)の分岐部に
は流路切換用のアングル弁(41)が設けられ、アングル弁
(41)と加熱炉(1)及び急冷室(2)との間には第1弁(42)(4
2a)が設けられる。アングル弁(41)とメカニカルブース
ターポンプ(43)との間にピラニー真空計(45)が設けられ
る。Next, an apparatus for replacing the atmosphere in the heating furnace (1) and the quenching chamber (2) with an inert gas will be described. The heating furnace (1) and the quenching chamber (2) are connected to a common suction device (4). The suction device (4) is a mechanical booster pump (43)
To the upstream side, a pipe (40) equipped with a rotary pump (44) on the downstream side is bifurcated to the upstream side, and each branch end is connected to the heating furnace (1) and the quenching chamber (2). I have. An angle valve (41) for switching the flow path is provided at the branch of the pipe (40).
(41) and a first valve (42) (4) between the heating furnace (1) and the quenching chamber (2).
2a) is provided. A Pirani vacuum gauge (45) is provided between the angle valve (41) and the mechanical booster pump (43).
【0012】加熱炉(1)と急冷室(2)は、Arガス等の不
活性ガスを充填したガスボンベ(9)が供給路(91)(91a)を
介して接続される。供給路(91)(91a)にはガスボンベ(9)
側に不活性ガス純化部(7)、加熱炉(1)及び急冷室(2)に
接近して第2弁(92)(92a)が設けられている。A gas cylinder (9) filled with an inert gas such as Ar gas is connected to the heating furnace (1) and the quenching chamber (2) through supply paths (91) and (91a). Gas cylinder (9) in supply path (91) (91a)
A second valve (92) (92a) is provided on the side close to the inert gas purifying section (7), the heating furnace (1) and the quenching chamber (2).
【0013】上記吸引装置(4)のメカニカルブースター
ポンプ(43)、ロータリーポンプ(44)、アングル弁(41)、
第1弁(42)(42a)、ピラニー真空計(45)、加熱炉(1)側の
スライド駆動装置(52)、急冷室(2)側のスライド駆動装
置(61)、搬送通路(3)のシャッター(31)、不活性ガス供
給路(91)は、コントローラ(8)に電気的に接続されて自
動制御される。コントローラ(8)のパネルには、スター
トボタン(81)、加熱炉ガス置換ボタン(82)、急冷室ガス
置換ボタン(83)、加熱炉と急冷室の同時ガス置換ボタン
(84)、置換回数選択ボタン群(85)等の、各種操作ボタン
が配備されている。A mechanical booster pump (43), a rotary pump (44), an angle valve (41),
First valve (42) (42a), Pirani vacuum gauge (45), slide drive device (52) on heating furnace (1) side, slide drive device (61) on quenching chamber (2) side, transfer passage (3) The shutter (31) and the inert gas supply path (91) are electrically connected to the controller (8) and are automatically controlled. On the controller (8) panel, a start button (81), a heating furnace gas replacement button (82), a quench chamber gas replacement button (83), and a simultaneous gas replacement button for the heating furnace and quench chamber
(84), various operation buttons such as a replacement frequency selection button group (85) are provided.
【0014】コントローラ(8)によって、次の動作が自
動的になされる。加熱炉(1)を不活性ガスで置換した
後、水素吸蔵合金を加熱する。加熱炉(1)のガス置換と
同時に、或いはその後、急冷室(2)を不活性ガスで置換
し、搬送通路(3)のシャッター(31)を開き、プッシャー
(51)によって、加熱した水素吸蔵合金を急冷室(2)のテ
ーブル(21)上に突き出す。シャッター(31)を閉じて急冷
室(2)のガス雰囲気を保つ。突落とし棒(6)によって水素
吸蔵合金を槽(22)中に落とし込み急冷する。コントロー
ラ(8)は、加熱炉(1)と急冷室(2)のガス置換に際し、図
3、図4のフローチャートに示すように、吸引装置
(4)、及びガス供給路(91)側の第2弁(92)(92a)を制御す
る。The following operation is automatically performed by the controller (8). After replacing the heating furnace (1) with an inert gas, the hydrogen storage alloy is heated. Simultaneously with or after the replacement of the gas in the heating furnace (1), the quenching chamber (2) is replaced with an inert gas, the shutter (31) of the transfer passage (3) is opened, and the pusher is pressed.
By (51), the heated hydrogen storage alloy is projected onto the table (21) of the quenching chamber (2). Close the shutter (31) to maintain the gas atmosphere in the quench chamber (2). The hydrogen storage alloy is dropped into the tank (22) with the plunging rod (6) and rapidly cooled. As shown in the flow charts of FIGS. 3 and 4, the controller (8) performs a suction device when replacing the gas in the heating furnace (1) and the quenching chamber (2).
(4) and the second valves (92) and (92a) on the gas supply path (91) side are controlled.
【0015】ガス置換する工程をフローチャートに基づ
き説明する。第1弁(42)(42a)、第2弁(92)(92a)は閉じ
ている。先ず、加熱炉(1)のみをガス置換する場合(フロ
ーチャートの左側に示されている)、加熱炉ガス置換ボ
タン(82)を押す。置換回数選択ボタン群(85)によりガス
置換回数を選択する。The gas replacement process will be described with reference to a flowchart. The first valve (42) (42a) and the second valve (92) (92a) are closed. First, when replacing only the heating furnace (1) with gas (shown on the left side of the flowchart), the heating furnace gas replacement button (82) is pressed. The number of times of gas replacement is selected with the number of replacement times selection button group (85).
【0016】スタートボタン(81)を押す。アングル弁(4
1)が開いて、加熱炉(1)側の第1弁(42)とメカニカルブ
ースターポンプ(43)との間を連通させ、急冷室(2)側の
第1弁(42a)とメカニカルブースターポンプ(43)の間を
遮断する。ロータリーポンプ(44)が作動する。第1弁(4
2)が開いて加熱炉(1)とメカニカルブースターポンプ(4
3)との間が連通し、加熱炉(1)内は負圧になる。ピラニ
ー真空計(45)が10Torr以下であることを感知すれば、
メカニカルブースターポンプ(43)が作動する。ピラニー
真空計が1×10-2Torr以下であることを感知すれば、
第1弁(42)が閉じ、メカニカルブースターポンプ(43)が
停止する。Press the start button (81). Angle valve (4
1) is opened to allow communication between the first valve (42) on the heating furnace (1) side and the mechanical booster pump (43), and the first valve (42a) on the quenching chamber (2) side and the mechanical booster pump. Cut off between (43). The rotary pump (44) operates. 1st valve (4
2) Open the heating furnace (1) and mechanical booster pump (4
3) and the inside of the heating furnace (1) becomes negative pressure. If the Pirani gauge (45) senses that it is below 10 Torr,
The mechanical booster pump (43) operates. If the Pirani gauge senses less than 1 × 10 -2 Torr,
The first valve (42) closes, and the mechanical booster pump (43) stops.
【0017】加熱炉(1)側の第2弁(92)が開いて、不活
性ガス供給路(91)が加熱炉(1)に連通し、ドライカラム
(71)を通過した後、Arガスが加熱炉(1)へ流れ込み、
加熱炉(1)内の雰囲気はArガスに置換される。上記動
作が、設定置換回数繰り返されるとロータリーポンプ(4
4)が停止し、ガス置換が終了する。When the second valve (92) on the heating furnace (1) side is opened, the inert gas supply passage (91) communicates with the heating furnace (1), and the dry column
After passing through (71), Ar gas flows into the heating furnace (1),
The atmosphere in the heating furnace (1) is replaced with Ar gas. When the above operation is repeated for the set number of replacements, the rotary pump (4
4) stops, and gas replacement ends.
【0018】急冷室(2)のみをガス置換する場合(フロ
ーチャート図の右側に示されている)は、アングル弁(4
1)が、急冷室(2)側の第1弁(42a)とメカニカルブースタ
ーポンプ(43)との間を連通させ、加熱炉(1)側の第1弁
(42)とメカニカルブースターポンプ(43)との間を遮断す
ることと、ガスボンベ(9)からの供給路(91)及び第2弁
(92a)が相違するだけで、動作は前記加熱炉(1)へのガ
ス置換の場合と同じである。If only the quenching chamber (2) is replaced with gas (shown on the right side of the flow chart), the angle valve (4)
1) connects the first valve (42a) on the quenching chamber (2) side with the mechanical booster pump (43), and the first valve on the heating furnace (1) side.
(42) and the mechanical booster pump (43), and only the difference between the supply path (91) from the gas cylinder (9) and the second valve (92a) is that the operation of the heating furnace (1) is different. ) Is the same as in the case of gas replacement.
【0019】上記熱処理装置によれば、水素吸蔵合金を
高純度の不活性ガス雰囲気下にて、所望温度、所望時間
で熱処理を施すことができる。本発明では、この熱処理
装置を用いて、組成式A1-xQxB5-yRy(但しAはLa
又はMm(ミッシュメタル)、QはY、BはNi、RはA
l及び/又はMn、x及びyは夫々0≦x≦0.3、0
≦y≦1)で表わされる合金のインゴットを、純度99.
9999%以上の不活性ガス雰囲気下、合金の融点の絶
対温度の2/3以上で、融点よりも低い温度で、2〜1
6時間加熱した後、急冷処理を施して、ヒステリシスが
小さく、プラトーの傾きが小さく、水素の吸収/放出を
高可逆的に行なうことのできる水素吸蔵合金を作製し
た。なお、同様の処理を行なうことができる装置であれ
ば、上記熱処理装置に限定されることなく、本発明を実
施できることは勿論である。According to the heat treatment apparatus, the hydrogen storage alloy can be subjected to heat treatment at a desired temperature and for a desired time in a high-purity inert gas atmosphere. In the present invention, the composition formula A 1-x Q x B 5-y R y (where A is La
Or Mm (Misch metal), Q is Y, B is Ni, R is A
l and / or Mn, x and y are respectively 0 ≦ x ≦ 0.3, 0
≦ y ≦ 1).
Under an atmosphere of an inert gas of 9999% or more, at a temperature not less than 2/3 of the absolute temperature of the melting point of the alloy and a temperature lower than the melting point, 2 to 1
After heating for 6 hours, a quenching treatment was performed to produce a hydrogen storage alloy having a small hysteresis, a small plateau gradient, and capable of highly reversibly absorbing / desorbing hydrogen. In addition, as long as the apparatus can perform the same processing, it is needless to say that the present invention can be implemented without being limited to the heat treatment apparatus.
【0020】[0020]
【実施例】実施例1 実施例1は、組成式La0.8Y0.2Ni4.4Al0.6で表わ
される水素吸蔵合金のインゴットに対し、加熱温度を変
えて本発明の固相急冷処理を施し、ヒステリシス及びプ
ラトーの傾きを測定し、比較を行なうものである。原料
粉末をLa:Y:Ni:Al=0.8:0.2:4.4:0.6
(原子比)となるように秤量し、混合した後、プレスを行
ない、アーク溶解炉にて溶解して自然放冷させた合金イ
ンゴット(組成式La0.8Y0.2Ni4.4Al0.6)を複数準
備した。 Example 1 In Example 1, a solid phase quenching treatment of the present invention was performed on an ingot of a hydrogen storage alloy represented by the composition formula La 0.8 Y 0.2 Ni 4.4 Al 0.6 by changing the heating temperature to obtain a hysteresis and The plateau slope is measured and compared. The raw material powder was La: Y: Ni: Al = 0.8: 0.2: 4.4: 0.6.
(Atomic ratio), and after mixing, pressing was performed, and a plurality of alloy ingots (composition formula La 0.8 Y 0.2 Ni 4.4 Al 0.6 ) melted in an arc melting furnace and allowed to cool naturally were prepared. .
【0021】得られた合金インゴットを、上記熱処理装
置にて473K、573K、823K、1073K、1
323K、1423Kの温度で夫々8時間加熱した。熱
処理装置内の雰囲気は、純度99.9999%以上のA
rガスである。加熱後、温度298Kのクエンチングオ
イル中に落とし込み、急冷を行なった。急冷を行なった
合金において、オイルと反応した合金表面をやすりで削
り落とし、供試合金No.1〜No.6とした(表1参照)。The obtained alloy ingot is subjected to 473K, 573K, 823K, 1073K, 1
Heating was performed at 323 K and 1423 K, respectively, for 8 hours. The atmosphere in the heat treatment equipment is A with a purity of 99.9999% or more.
r gas. After heating, the mixture was dropped into a quenching oil at a temperature of 298 K and rapidly cooled. In the alloy that had been quenched, the alloy surface that had reacted with the oil was filed off with a file to form a match gold No. 1 to No. 6 (see Table 1).
【0022】◎◎
【表1】 [Table 1]
【0023】比較を行なうため、準備された合金インゴ
ットについて、熱処理を全く行なわない合金(供試合金N
o.7)と、純度99.9999%以上のArガス雰囲気中
で温度1323Kで8時間加熱した後、室温まで徐冷し
た通常の熱処理による合金(供試合金No.8)と、合金イ
ンゴットを溶解し、純度99.9999%のAr雰囲気
中でロール上に噴射することにより溶湯急冷して得られ
た合金(供試合金No.9)を作製した(表1参照)。In order to make a comparison, the prepared alloy ingot was subjected to an alloy without any heat treatment.
o.7) and an alloy by normal heat treatment after heating at a temperature of 1323 K for 8 hours in an Ar gas atmosphere having a purity of 99.9999% or more (available gold No. 8) and an alloy ingot. The alloy was melted and sprayed on a roll in an Ar atmosphere having a purity of 99.9999% to rapidly cool the molten metal to obtain an alloy (available gold No. 9) (see Table 1).
【0024】作製された供試合金No.1〜No.9を、粒径
約100μmに粉砕し、その5gをステンレス製反応容
器(内容積:10cc)に封入し、活性化処理(真空排気温
度353K、印加水素圧力18atm、活性化時間60
分)を行なった。その後、公知のジーベルツ装置を用い
て、各供試合金の圧力−水素吸収量等温特性(P−C−
T曲線)を403Kの温度で測定した。また、各供試合
金のヒステリシスとプラトーの傾きを測定した。結果を
表1、図5及び図6に示す。The prepared match Nos. 1 to 9 were pulverized to a particle size of about 100 μm, 5 g of which was sealed in a stainless steel reaction vessel (internal volume: 10 cc), and activated (vacuum exhaust temperature). 353K, applied hydrogen pressure 18atm, activation time 60
Min). Thereafter, using a known Siebeltz apparatus, the pressure-hydrogen absorption amount isothermal characteristic (PC-
T curve) was measured at a temperature of 403K. In addition, the hysteresis and plateau slope of each match were measured. The results are shown in Table 1, FIG. 5 and FIG.
【0025】表1、図5及び図6を参照すると、供試合
金No.1〜No.6は、加熱温度が高くなるにつれてヒステ
リシスが小さくなり、プラトーの傾きも小さくなってい
ることが判る。Referring to Table 1, FIG. 5 and FIG. 6, it can be seen that, in the match money Nos. 1 to 6, the hysteresis decreases and the plateau slope decreases as the heating temperature increases.
【0026】供試合金No.1〜No.6を、熱処理を全く行
なわない供試合金No.7と比較すると、No.1は、ヒステ
リシスとプラトーの傾きが共にNo.7とほぼ同じ程度で
あるが、No.2では、プラトーの傾きがNo.1及びNo.7
よりも約20%程度小さくなっていることが判る。ま
た、No.3〜No.6は、No.7よりも、ヒステリシスとプ
ラトーの傾きが共に小さくなっており、No.7より優れ
ていることが判る。Comparing No. 1 to No. 6 with No. 7 which does not perform any heat treatment, No. 1 has almost the same hysteresis and plateau slope as No. 7. However, in No.2, the inclination of the plateau was No.1 and No.7.
It can be seen that it is smaller by about 20%. In addition, No. 3 to No. 6 both have smaller hysteresis and plateau slope than No. 7, indicating that they are superior to No. 7.
【0027】供試合金No.1〜No.6を供試合金No.8と
比較すると、No.1〜No.3は、ヒステリシスとプラトー
の傾きが共に大きく、No.8よりも劣っている。しかし
ながら、No.4は〜No.6は、ヒステリシスとプラトーの
傾きが共に小さく、No.8よりも優れていることが判
る。Comparing the match money No. 1 to No. 6 with the match money No. 8, both No. 1 to No. 3 have larger hysteresis and plateau slope, and are inferior to No. 8. . However, it can be seen that No. 4 to No. 6 have smaller hysteresis and plateau slope, and are superior to No. 8.
【0028】供試合金No.1〜No.6を供試合金No.9と
比較すると、No.1〜No.3は、ヒステリシスとプラトー
の傾きが共に大きく、No.9よりも劣っている。また、N
o.4、No.5は、ヒステリシスはNo.9よりも僅かに劣っ
ているが、プラトーの傾きが40%以上小さくなってお
り、No.9より優れていることが判る。更に、No.6は、
ヒステリシスはNo.9と同程度であるが、プラトーの傾
きは約60%小さくなっており、No.9よりも優れてい
ることがわかる。Comparing the match money No. 1 to No. 6 with the match money No. 9, No. 1 to No. 3 both have a large hysteresis and a plateau slope, and are inferior to No. 9. . Also, N
In Nos. 4 and 5, the hysteresis was slightly inferior to No. 9, but the slope of the plateau was reduced by 40% or more, indicating that the No. 9 was superior to No. 9. In addition, No. 6
Although the hysteresis is almost the same as that of No. 9, the slope of the plateau is reduced by about 60%, which indicates that the plateau is superior to No. 9.
【0029】以上の測定結果及び比較結果より総合的に
評価すると、供試合金No.4〜No.6は、ヒステリシスと
プラトーの傾きを同時に小さくできることが判る。つま
り、水素吸蔵合金を、合金の融点(本実施例の合金は約
1600K)の2/3以上で、融点よりも低い温度で行
なうことによって、ヒステリシスが小さく、プラトーの
傾きが小さく、高可逆性を有する水素吸蔵合金を作製す
ることができる。Comprehensively evaluating from the above measurement results and comparison results, it can be seen that the match money Nos. 4 to 6 can simultaneously reduce the hysteresis and the plateau slope. That is, by performing the hydrogen storage alloy at a temperature that is at least 2/3 of the melting point of the alloy (the alloy of this embodiment is about 1600K) and lower than the melting point, the hysteresis is small, the plateau slope is small, and the high reversibility is obtained. Can be produced.
【0030】上記実施例1で作製された供試合金No.5
と供試合金No.8について、電子線プローブマイクロ分
析(EPMA)によるX線像(1000倍)を図7及び
図8に示す。図8を参照すると、通常の熱処理を施した
供試合金No.8は、Yの分布している相(白く見える部
分)と、Yの分布していない相(黒い帯状の部分)との
境界が明確である。これに対して、本発明の供試合金N
o.5は、Yの凝縮した部分(図中に現れている4つの白
い斑点)がみられるが、母相ではYが比較的均一に分布
しており、図7のような境界の差が明確ではない。本発
明の供試合金No.5は、Yの分布がより均一であるた
め、上述のとおり高可逆性を有しているものと考えられ
る。Match No. 5 prepared in Example 1 above
7 and 8 show X-ray images (1000 times) obtained by electron beam probe microanalysis (EPMA) for No. 8 and Match No. 8. Referring to FIG. 8, a match-treated gold No. 8 which has been subjected to a normal heat treatment has a boundary between a phase in which Y is distributed (a portion that looks white) and a phase in which Y is not distributed (a black band-shaped portion). Is clear. On the other hand, the match money N of the present invention
In the case of o.5, a condensed portion of Y (four white spots appearing in the figure) is observed, but in the parent phase, Y is relatively uniformly distributed, and the difference between the boundaries shown in FIG. Not clear. It is considered that the match money No. 5 of the present invention has high reversibility as described above because the distribution of Y is more uniform.
【0031】以下の実施例にて、本発明の合金の成分
と、置換量の限定理由を説明する。実施例2 上記実施例1で作製された本発明の供試合金No.5と、
通常の熱処理を施した供試合金No.8(共に組成式La
0.8Y0.2Ni4.4Al0.6)のP−C−T特性曲線をジー
ベルツ装置を用いて測定した。また、比較のために、組
成式Ti0.85Zr0.15MnV0.4Ni0.6で示されるTi
系合金に、上記供試合金No.5と同一の固相急冷処理を
施した合金と、供試合金No.8と同一の通常の熱処理を
施した合金を作製して、同様に、P−C−T特性曲線を
ジーベルツ装置にて測定した。結果を図9及び図10に
示す。図9から判るとおり、固相急冷処理を施したNo.
5は、通常の熱処理を施したNo.8に比べて、ヒステリ
シスが小さく、且つプラトーの傾きも小さいことが判
る。また、プラトーの幅(図9参照)で示される有効水
素移動量も大きいことが判る。これに対して、図10に
示すように、Ti系合金に固相急冷処理を施した合金
と、通常熱処理を施した合金とを比べると、固相急冷処
理を施した合金は、ヒステリシスが通常熱処理合金と殆
んど変らず、また、プラトーの傾きについては、通常熱
処理合金よりも大きいことが判る。つまり、固相急冷処
理は、組成式La0.8Y0.2Ni4.4Al0.6で示される水
素吸蔵合金に施すと優れた効果を発揮するが、Ti系合
金に施すと、Ti系合金の水素吸収/放出特性は却って
劣化することが判る。従って、本発明の固相急冷処理
は、La−Ni系の水素吸蔵合金には適しているが、T
i系合金には適していないことが判明した。なお、組成
式A1-xQxB5-yRy(但しAはLa又はMm(ミッシュメ
タル)、QはY、BはNi、RはAl及び/又はMn)で
示される水素吸蔵合金に固相急冷処理を施すと、ヒステ
リシス及びプラトーの傾きを小さくすることができ、水
素吸収/放出を高可逆的に行なえるものと推測される。In the following examples, the components of the alloy of the present invention and the reasons for limiting the replacement amount will be described. Example 2 Match No. 5 of the present invention prepared in Example 1 above,
Match No. 8 with normal heat treatment (both with composition formula La)
0.8 Y 0.2 Ni 4.4 Al 0.6 ) was measured using a Sibeltz apparatus. Also, for comparison, Ti represented by the composition formula Ti 0.85 Zr 0.15 MnV 0.4 Ni 0.6
The same solid-phase quenching treatment as the above-mentioned match No. 5 and the same heat-treated alloy as the match no. The CT characteristic curve was measured with a Siebeltz apparatus. The results are shown in FIGS. As can be seen from FIG. 9, the solid-phase quenched No.
5 shows that the hysteresis is smaller and the plateau slope is smaller than that of No. 8 subjected to the ordinary heat treatment. Also, it can be seen that the effective hydrogen transfer amount indicated by the plateau width (see FIG. 9) is large. On the other hand, as shown in FIG. 10, when an alloy obtained by subjecting a Ti-based alloy to a solid phase quenching treatment and an alloy subjected to a normal heat treatment are compared, the alloy subjected to the solid phase quenching treatment has a normal hysteresis. It turns out that it is almost the same as the heat-treated alloy, and that the inclination of the plateau is larger than that of the normal heat-treated alloy. In other words, the solid-phase quenching treatment exerts an excellent effect when applied to a hydrogen storage alloy represented by the composition formula La 0.8 Y 0.2 Ni 4.4 Al 0.6 , but when applied to a Ti alloy, the hydrogen absorption / desorption of the Ti alloy can be improved. It turns out that the characteristics deteriorate rather. Therefore, the solid-phase quenching treatment of the present invention is suitable for a La—Ni-based hydrogen storage alloy,
It was found that it was not suitable for i-based alloys. A hydrogen storage alloy represented by the composition formula A 1-x Q x B 5-y R y (where A is La or Mm (misch metal), Q is Y, B is Ni, and R is Al and / or Mn) It is presumed that when the solid phase quenching treatment is performed, the hysteresis and the slope of the plateau can be reduced, and the hydrogen absorption / desorption can be performed highly reversibly.
【0032】実施例3 実施例3は、組成式がLa1-xYxNi5-yAlyで示され
る水素吸蔵合金について、Laと置換されるYの量xを
変えたときの有効水素移動量を測定するものである。L
aの一部をYと置換するのは、この置換により水素吸蔵
合金の平衡圧力を上昇させることができるためである。[0032] Example 3 Example 3, the hydrogen storage alloy whose composition formula is represented by La 1-x Y x Ni 5 -y Al y, effective hydrogen when changing the amount x of Y to be substituted for La It measures the amount of movement. L
Part of a is substituted with Y because the substitution can increase the equilibrium pressure of the hydrogen storage alloy.
【0033】Laと置換するYの量xを表2に示すよう
に0〜0.3と変化させ、Niと置換するAlの量yを
0.6とした合金(順に供試合金No.11〜No.14)を準
備し、加熱温度:1323K、加熱時間:8時間、処理雰
囲気:Arガス(純度99.9999%)、急冷媒体:クエ
ンチングオイル、媒体温度:298Kの条件で固相急冷
処理を行ない、ジーベルツ装置を用いて各合金の有効水
素移動量を測定した。結果を表2及び図11に示す。An alloy in which the amount x of Y to replace La was varied from 0 to 0.3 as shown in Table 2 and the amount y of Al to replace Ni was 0.6 (in the order of No. 11 To No. 14), heating temperature: 1323 K, heating time: 8 hours, processing atmosphere: Ar gas (purity 99.9999%), quenching medium: quenching oil, medium temperature: 298 K, solid phase quenching The treatment was performed, and the effective hydrogen transfer amount of each alloy was measured using a Siebeltz apparatus. The results are shown in Table 2 and FIG.
【0034】◎◎
【表2】 [Table 2]
【0035】表2及び図11を参照すると、Yの置換量
が大きくなるにつれて、有効水素移動量は徐々に減少し
ていることが判る。つまり、有効水素移動量の点からみ
れば、Yの置換量は少ないほど望ましい。しかしなが
ら、上述したとおり、Laの一部をYに置換すると、水
素吸蔵合金の平衡圧力を上昇させることができる。従っ
て、Yの置換量は、通常要求される水素吸蔵合金の有効
水素移動量(約0.6重量%)を確保できる範囲内、即
ちxが0.3以下となるように調整することが望まし
い。Referring to Table 2 and FIG. 11, it can be seen that the effective hydrogen transfer amount gradually decreases as the Y substitution amount increases. In other words, from the viewpoint of the effective hydrogen transfer amount, the smaller the substitution amount of Y, the better. However, as described above, when a part of La is replaced with Y, the equilibrium pressure of the hydrogen storage alloy can be increased. Therefore, it is desirable that the substitution amount of Y is adjusted so that the effective hydrogen transfer amount (about 0.6% by weight) of the normally required hydrogen storage alloy can be ensured, that is, x is 0.3 or less. .
【0036】実施例4 実施例4は、組成式がLa1-xYxNi5-yAlyで示され
る水素吸蔵合金について、Niと置換されるAlの量y
を変えたときの有効水素移動量を測定するものである。
Niの一部をAlと置換するのは、この置換により水素
吸蔵合金の耐久性の向上を図ることができるからであ
る。 Example 4 In Example 4, the hydrogen storage alloy represented by the composition formula La 1-x Y x Ni 5-y A y was used to determine the amount y of Al substituted with Ni.
This is to measure the effective hydrogen transfer amount when the value is changed.
The reason why part of Ni is replaced by Al is that the substitution can improve the durability of the hydrogen storage alloy.
【0037】Niと置換するAlの量yを表3に示すよ
うに0〜1.0まで変化させ、Laと置換するYの量x
を0.2とした合金(順に供試合金No.20〜No.25)を
準備し、実施例3と同じ条件で固相急冷処理を行ない、
ジーベルツ装置を用いて各合金の有効水素移動量を測定
した。結果を表3及び図12に示す。The amount y of Al to be replaced with Ni is changed from 0 to 1.0 as shown in Table 3, and the amount x of Y to be replaced with La is x.
Was prepared as an alloy (in the order of No. 20 to No. 25) and subjected to a solid phase quenching treatment under the same conditions as in Example 3.
The effective hydrogen transfer amount of each alloy was measured using a Siebelz apparatus. The results are shown in Table 3 and FIG.
【0038】◎◎
【表3】 [Table 3]
【0039】表3及び図12を参照すると、Alの置換
量が大きくなるにつれて、有効水素移動量は徐々に減少
していることが判る。つまり、有効水素移動量の点から
みれば、Alの置換量は少ないほど望ましい。しかしな
がら、上述したとおり、Niの一部をAlに置換する
と、水素吸蔵合金の耐久性を向上させることができる。
従って、Alの置換量は、通常要求される水素吸蔵合金
の有効水素移動量(約0.6重量%)を確保できる範囲
内、即ちyが1.0以下となるように調整することが望
ましい。なお、Niの一部を、Alに代えてMnと置
換、又はAlとMnで置換しても同様の効果が得られ
る。Referring to Table 3 and FIG. 12, it can be seen that the effective hydrogen transfer amount gradually decreases as the Al substitution amount increases. That is, from the viewpoint of the effective hydrogen transfer amount, the smaller the substitution amount of Al, the better. However, as described above, when part of Ni is replaced with Al, the durability of the hydrogen storage alloy can be improved.
Therefore, it is desirable to adjust the replacement amount of Al so that the effective hydrogen transfer amount (about 0.6% by weight) of the normally required hydrogen storage alloy can be ensured, that is, y is 1.0 or less. . The same effect can be obtained by substituting a part of Ni for Mn instead of Al or for Al and Mn.
【0040】上記実施例1〜4においては、組成式A
1-xQxB5-yRy(但し0≦x≦0.3、0≦y≦1)で表
わされる水素吸蔵合金のAをLaとした例についてのみ
説明したが、AをMm(ミッシュメタル)としても同様の
効果を得ることができる。In Examples 1 to 4, the composition formula A
1-x Q x B 5-y R y (where 0 ≦ x ≦ 0.3, 0 ≦ y ≦ 1) Only the example where A of the hydrogen storage alloy is La has been described, but A is Mm ( The same effect can be obtained as (mish metal).
【0041】上記実施例では、水素吸蔵合金のインゴッ
トをアーク溶解炉によって作製したが、合金インゴット
は、アーク溶解炉に限定されず、高周波誘導炉等の公知
の溶解法を用いて作製することもできる。In the above embodiment, the hydrogen storage alloy ingot was manufactured by the arc melting furnace. However, the alloy ingot is not limited to the arc melting furnace, but may be manufactured by a known melting method such as a high frequency induction furnace. it can.
【0042】[0042]
【発明の効果】本発明の水素吸蔵合金は、合金組織が均
質化されているため、ヒステリシスが小さく、プラトー
の傾きが小さく、また、水素の吸収/放出を高可逆性を
以て行なうことができる。According to the hydrogen storage alloy of the present invention, since the alloy structure is homogenized, the hysteresis is small, the slope of the plateau is small, and the absorption / release of hydrogen can be performed with high reversibility.
【図1】熱処理装置の構成を示す概略図である。FIG. 1 is a schematic diagram showing a configuration of a heat treatment apparatus.
【図2】熱処理装置の加熱炉と急冷室部分を拡大して示
す平面図である。FIG. 2 is an enlarged plan view showing a heating furnace and a quenching chamber portion of the heat treatment apparatus.
【図3】熱処理装置の制御の流れを示すフローチャート
図である。FIG. 3 is a flowchart showing a control flow of the heat treatment apparatus.
【図4】熱処理装置の制御の流れを示すフローチャート
図である。FIG. 4 is a flowchart showing a control flow of the heat treatment apparatus.
【図5】ヒステリシスと処理温度との関係を示すグラフ
である。FIG. 5 is a graph showing a relationship between hysteresis and processing temperature.
【図6】プラトーの傾きと処理温度との関係を示すグラ
フである。FIG. 6 is a graph showing a relationship between a plateau inclination and a processing temperature.
【図7】固相急冷処理を施した供試合金No.5の組織を
EPMAにより示す図面代用写真(×1000)である。FIG. 7 is a drawing substitute photograph (× 1000) showing the structure of match No. 5 subjected to solid phase quenching treatment by EPMA.
【図8】通常熱処理を施した供試合金No.8の組織をE
PMAにより示す図面代用写真(×1000)である。FIG. 8 shows the structure of No. 8 of the match gold which has been subjected to the normal heat treatment.
It is a drawing substitute photograph (x1000) shown by PMA.
【図9】供試合金No.5とNo.8のP−C−T特性曲線で
ある。FIG. 9 is a P-C-T characteristic curve of match money No. 5 and No. 8;
【図10】Ti系合金のP−C−T特性曲線である。FIG. 10 is a PCT characteristic curve of a Ti-based alloy.
【図11】Laの一部をYで置換した置換量と有効水素
移動量との関係を示すグラフである。FIG. 11 is a graph showing the relationship between the amount of La replaced with Y and the amount of effective hydrogen transfer.
【図12】Niの一部をAlで置換した置換量と有効水
素移動量との関係を示すグラフである。FIG. 12 is a graph showing the relationship between the amount of partial replacement of Ni with Al and the effective amount of hydrogen transfer.
(1) 加熱炉 (2) 急冷室 (1) Heating furnace (2) Quench room
フロントページの続き (72)発明者 米津 育郎 大阪府守口市京阪本通2丁目5番5号 三洋電機株式会社内 (72)発明者 西尾 晃治 大阪府守口市京阪本通2丁目5番5号 三洋電機株式会社内 (56)参考文献 特公 昭59−28624(JP,B1) 特公 昭59−28625(JP,B1) 特公 昭59−28626(JP,B1) (58)調査した分野(Int.Cl.7,DB名) C22C 19/00 C22F 1/10 Continuing from the front page (72) Inventor Ikuo Yonezu 2-5-5 Keihanhondori, Moriguchi-shi, Osaka Sanyo Electric Co., Ltd. (72) Inventor Koji Nishio 2-5-5 Keihanhondori, Moriguchi-shi, Osaka Sanyo (56) References JP-B-59-28624 (JP, B1) JP-B-59-28625 (JP, B1) JP-B-59-28626 (JP, B1) (58) Fields surveyed (Int .Cl. 7 , DB name) C22C 19/00 C22F 1/10
Claims (3)
又はMm、QはY、BはNi、RはAl及び/又はM
n、x及びyは夫々0.1≦x≦0.3、0≦y≦1)で
表わされる合金のインゴットを、融点よりも低い温度で
所定時間加熱した後、液体冷媒中に浸漬して急冷する固
相急冷処理により作製され、母相中にYが均一に分散さ
れていることを特徴とする水素吸蔵合金。1. A composition formula A 1-x Q x B 5-y R y (where A is La
Or Mm, Q is Y, B is Ni, R is Al and / or M
n, x and y are respectively 0.1 ≤ x ≤ 0.3, 0 ≤ y ≤ 1) An ingot of the alloy represented by the formula is heated at a temperature lower than the melting point for a predetermined time and then immersed in a liquid refrigerant. Made by solid-phase quenching process in which quenching is performed , and Y is uniformly dispersed in the matrix.
A hydrogen storage alloy, which is characterized in that:
の2/3以上で、融点よりも低い温度で行なうことを特
徴とする請求項1に記載の水素吸蔵合金。2. The hydrogen storage alloy according to claim 1, wherein the solid phase quenching treatment is performed at a temperature that is at least two-thirds of the melting point of the alloy and lower than the melting point.
の高純度不活性ガス雰囲気中で行なうことを特徴とする
請求項1又は請求項2に記載の水素吸蔵合金。3. The hydrogen storage alloy according to claim 1, wherein the solid phase quenching treatment is performed in a high purity inert gas atmosphere of 99.9999% or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21530696A JP3263605B2 (en) | 1996-07-26 | 1996-07-26 | Hydrogen storage alloy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21530696A JP3263605B2 (en) | 1996-07-26 | 1996-07-26 | Hydrogen storage alloy |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH1046275A JPH1046275A (en) | 1998-02-17 |
| JP3263605B2 true JP3263605B2 (en) | 2002-03-04 |
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|---|---|---|---|
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| CN114941058B (en) * | 2022-07-07 | 2023-05-23 | 上海大学 | High-purity Pr5Co19 type La-Y-Ni superlattice alloy and preparation method thereof |
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|---|---|---|---|---|
| JP5928624B1 (en) | 2015-03-04 | 2016-06-01 | 株式会社 大阪合金工業所 | Bronze alloy for musical instrument and percussion instrument using the same |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5928624B1 (en) | 2015-03-04 | 2016-06-01 | 株式会社 大阪合金工業所 | Bronze alloy for musical instrument and percussion instrument using the same |
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| Publication number | Publication date |
|---|---|
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