JP2003095616A - Hydrogen separating purifier - Google Patents

Hydrogen separating purifier

Info

Publication number
JP2003095616A
JP2003095616A JP2001284344A JP2001284344A JP2003095616A JP 2003095616 A JP2003095616 A JP 2003095616A JP 2001284344 A JP2001284344 A JP 2001284344A JP 2001284344 A JP2001284344 A JP 2001284344A JP 2003095616 A JP2003095616 A JP 2003095616A
Authority
JP
Japan
Prior art keywords
hydrogen
alloy
diaphragm
thickness
hydrogen separation
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.)
Granted
Application number
JP2001284344A
Other languages
Japanese (ja)
Other versions
JP3837481B2 (en
Inventor
Tetsuya Ozaki
哲也 尾崎
Masao Komaki
政雄 古牧
Mutsumi Nishimura
睦 西村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
National Institute for Materials Science
Original Assignee
National Institute for Materials Science
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by National Institute for Materials Science filed Critical National Institute for Materials Science
Priority to JP2001284344A priority Critical patent/JP3837481B2/en
Publication of JP2003095616A publication Critical patent/JP2003095616A/en
Application granted granted Critical
Publication of JP3837481B2 publication Critical patent/JP3837481B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Fuel Cell (AREA)

Abstract

PROBLEM TO BE SOLVED: To realize the reduction of the thickness of a V-Ni alloy and provide a hydrogen separating purifier in which the thinned V-Ni alloy plates are mounted as several shapes of partition walls. SOLUTION: The V-Ni alloy plate is provided with front and rear surfaces covered with an alloy containing Pd or an alloy containing Pd, and the V-Ni alloy plate containing nitrogen of 5-30 atom.% and having a thickness of 0.1 mm-0.001 mm is mounted as a partition film by which hydrogen is purified.

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】この出願の発明は、水素分離
精製装置に関するものである。さらに詳しくは、この出
願の発明は、水素を含む混合ガス中又は不純物を含む未
精製の水素ガス中から水素のみを選択的に分離精製し、
99.99999%以上のいわゆるセブンナイン以上の超高純度
水素を製造することのできる水素分離精製装置に関する
ものである。
TECHNICAL FIELD The invention of this application relates to a hydrogen separation and purification apparatus. More specifically, the invention of this application is such that only hydrogen is selectively separated and purified from a mixed gas containing hydrogen or an unpurified hydrogen gas containing impurities,
The present invention relates to a hydrogen separation and purification device capable of producing ultrahigh-purity hydrogen of 99.99999% or more, so-called Seven Nine or more.

【0002】[0002]

【従来の技術とその課題】たとえば燃料電池自動車など
の重要なエネルギー源とされる超高純度水素を製造する
ための水素分離精製装置として、Pd合金を水素透過膜に
使用したものが開発され、実用化レベルにあるが、その
一方で、合金原料のPdは非常に高価であり、また、300
℃未満の低温での透過特性に難点がある。
2. Description of the Related Art A hydrogen separation / purification device using a Pd alloy for a hydrogen permeable membrane has been developed as a hydrogen separation / purification device for producing ultra-high purity hydrogen, which is an important energy source for fuel cell automobiles, for example. Although it is at the level of practical use, on the other hand, Pd as an alloy raw material is very expensive and
There is a problem in the transmission characteristics at low temperatures below ℃.

【0003】最近、この出願の発明の発明者らにより、
5〜30原子%のNiを含むV-Ni合金が高い水素透過能を有
することが見出され、低価格化が期待されるが、このV-
Ni合金には、加工性に乏しく、薄板化が難しいという問
題がある。すなわち、V-Ni合金は酸化されやすく、酸化
物の融点が低いため、熱間圧延が難しい。また、インゴ
ットを直接冷間圧延すると割れが生じやすいため、1mm
以下の厚さにするには、インゴットを切断した後、研磨
により薄くするしかない。このため、V-Ni合金を水素分
離精製装置に適応するために、膜状、パイプ状などへ加
工するのは効率が非常に悪く、実用化にはほど遠かっ
た。
Recently, by the inventors of the invention of this application,
A V-Ni alloy containing 5 to 30 atomic% Ni was found to have high hydrogen permeability, and it is expected that the price will be reduced.
The Ni alloy has a problem that it has poor workability and it is difficult to make it into a thin plate. That is, the V-Ni alloy is easily oxidized and the melting point of the oxide is low, so that hot rolling is difficult. In addition, if the ingot is directly cold-rolled, cracks are likely to occur, so 1 mm
The only way to achieve the following thickness is to cut the ingot and then polish it to make it thinner. For this reason, it was very inefficient to process the V-Ni alloy into a film shape or a pipe shape in order to apply it to a hydrogen separation / purification device, and it was far from practical use.

【0004】この出願の発明は、以上の通りの事情に鑑
みてなされたものであり、以上のように薄板化が難しい
とされていたV-Ni合金の薄板化を実現し、これを各種形
状の隔壁として装着した水素分離精製装置を提供するこ
とを解決すべき課題としている。
The invention of this application has been made in view of the above-mentioned circumstances. As described above, the V-Ni alloy, which has been considered difficult to be thinned, has been thinned into various shapes. It is an issue to be solved to provide a hydrogen separation and refining device mounted as a partition wall.

【0005】[0005]

【課題を解決するための手段】この出願の発明者らは、
前述の課題を解決するために鋭意検討した結果、高い水
素透過能を有するV-Ni合金にシース圧延を適用すること
により、最も薄くて0.01mmの厚さにまで薄板化すること
ができ、しかもその薄板化は比較的容易であり、また、
薄いものほど大きな水素透過流量が得られ、低温で大量
の水素を効率的に99.99999%以上のいわゆるセブンナイ
ン以上の超高純度まで純化することが可能であるとの知
見を得、また、シース圧延以外にもスパッタリング、真
空蒸着、イオンプレーティングなどにより、厚さ0.001m
mまでの V-Ni合金が作製可能であるとの知見を得、この
出願の発明を完成した。
Means for Solving the Problems The inventors of the present application
As a result of diligent studies to solve the above-mentioned problems, by applying sheath rolling to a V-Ni alloy having high hydrogen permeability, it is possible to make the thinnest plate as thin as 0.01 mm, and Thinning is relatively easy, and
The thinner the hydrogen, the larger the hydrogen permeation flow rate obtained, and the knowledge that it is possible to efficiently purify a large amount of hydrogen at a low temperature to an ultra high purity of 99.99999% or more, so-called Seven Nine, and sheath rolling. Besides, 0.001m thick by sputtering, vacuum deposition, ion plating, etc.
We obtained the finding that V-Ni alloys up to m can be produced, and completed the invention of this application.

【0006】すなわち、この出願の発明は、表裏両面が
Pd又はPdを含む合金で被覆され、5〜30原子%のNiを含
む厚さ0.1 mm〜0.001mmのV-Ni合金が、隔膜として装着
され、この隔膜により水素を純化することを特徴とする
水素分離精製装置(請求項1)を提供する。
That is, the invention of this application has both front and back surfaces.
A V-Ni alloy coated with Pd or an alloy containing Pd and having a thickness of 0.1 mm to 0.001 mm containing 5 to 30 atomic% of Ni is mounted as a diaphragm, and hydrogen is purified by the diaphragm. A hydrogen separation and purification device (claim 1) is provided.

【0007】またこの出願の発明は、V-Ni合金は、厚さ
0.1 mm〜0.01mmのシース圧延された薄板であること(請
求項2)、V-Ni合金は、Mnその他の水素透過能に悪影響
を及ぼさない元素を不可避的不純物元素として、若しく
は最大5原子%まで含有すること(請求項3)、隔膜が、
平板状、蛇腹状、又はパイプ状とされていること(請求
項4)、パイプ状とされた隔膜が、1本配設されている
か、若しくは複数本並設されていること(請求項5)を
それぞれ一態様として提供する。
Further, the invention of this application is such that the V-Ni alloy has a thickness
It is a sheath-rolled thin plate of 0.1 mm to 0.01 mm (claim 2), and the V-Ni alloy contains Mn and other elements that do not adversely affect hydrogen permeability as unavoidable impurity elements or at most 5 atomic%. Up to (claim 3), the diaphragm,
It has a flat plate shape, a bellows shape, or a pipe shape (Claim 4), and one pipe-shaped diaphragm is arranged or a plurality of pipe-shaped diaphragms are arranged in parallel (Claim 5). Are provided as one aspect, respectively.

【0008】以下、図面に沿ってこの出願の発明の水素
分離精製装置についてさらに詳しく説明する。
Hereinafter, the hydrogen separation and purification apparatus of the invention of this application will be described in more detail with reference to the drawings.

【0009】[0009]

【発明の実施の形態】図1<a><b><c>は、各
々、この出願の発明の水素分離精製装置の一実施形態を
概略的に示した断面図である。
BEST MODE FOR CARRYING OUT THE INVENTION FIG. 1 <a><b><c> is a cross-sectional view schematically showing an embodiment of a hydrogen separation and purification apparatus of the invention of this application.

【0010】この出願の発明の水素分離精製装置では、
前述の通り、表裏両面がPd又はPdを含む合金で被覆さ
れ、5〜30原子%のNiを含むV-Ni合金が、シース圧延、
スパッタリング、真空蒸着、イオンプレーティングなど
により厚さ0.1 mm〜0.01mmに作製され、これが隔膜
(1)として装着され、この隔膜(1)により水素を9
9.99999%以上のいわゆるセブンナイン以上の超高純度ま
で純化する。
In the hydrogen separation and purification apparatus of the invention of this application,
As described above, both front and back surfaces are coated with Pd or an alloy containing Pd, and a V-Ni alloy containing 5 to 30 atom% of Ni is sheath rolled,
It is made to have a thickness of 0.1 mm to 0.01 mm by sputtering, vacuum deposition, ion plating, etc. This is attached as a diaphragm (1), and hydrogen is generated by this diaphragm (1).
Purifies to ultra-high purity of 9.99999% or more, so-called Seven Nine.

【0011】シース圧延については、たとえばステンレ
ス管などをさや管として用い、このさや管内にV-Ni合金
のインゴットなどを入れて封入し、さや管ごと熱間圧延
することにより実行可能である。このシース圧延によ
り、これまでは難しいとされていたV-Ni合金の薄板化が
可能となり、隔膜(1)の厚さは、0.1mm以下、最も薄
くて0.01mmまでにすることができる。しかもその薄板化
は比較的容易であり、薄いものほど大きな水素透過流量
が得られ、低温で大量の水素の効率的な純化が可能とな
る。隔膜(1)の厚さが0.1mmを超えると、隔膜(1)
を透過する水素ガスの流量が不十分となり、水素の分離
精製処理速度の低下を招くため、好ましくない。
The sheath rolling can be carried out, for example, by using a stainless steel tube or the like as a sheath tube, inserting a V-Ni alloy ingot in the sheath tube, enclosing the sheath, and hot rolling the sheath tube together. By this sheath rolling, it has become possible to reduce the thickness of the V-Ni alloy, which was considered difficult until now, and the thickness of the diaphragm (1) can be 0.1 mm or less, and the thinnest, up to 0.01 mm. Moreover, the thinning thereof is relatively easy, and the thinner the hydrogen, the larger the hydrogen permeation flow rate can be obtained, and the large amount of hydrogen can be efficiently purified at a low temperature. When the thickness of the diaphragm (1) exceeds 0.1 mm, the diaphragm (1)
The flow rate of the hydrogen gas that permeates through becomes insufficient, which causes a decrease in the hydrogen separation and purification processing rate, which is not preferable.

【0012】スパッタリング、真空蒸着、イオンプレー
ティングなどによりV-Ni合金を作製する場合には、厚さ
0.001mmまでの薄板若しくは薄膜を容易に作製すること
ができる。
When a V-Ni alloy is produced by sputtering, vacuum deposition, ion plating, etc., the thickness
Thin plates or thin films up to 0.001 mm can be easily manufactured.

【0013】以上のV-Ni合金は、その水素透過能に悪影
響を及ぼさない限り、Mnその他の元素を不可避的不純物
元素として、若しくは第3元素、第4元素などとして最
大5原子%まで含有することができる。
The above V-Ni alloy contains up to 5 atomic% of Mn and other elements as unavoidable impurity elements, or third and fourth elements, etc., as long as the hydrogen permeability is not adversely affected. be able to.

【0014】隔膜(1)は、より具体的には、水素分離
精製装置に備えたキャビネット(2)の内部に装着する
ことができるが、その形状には特に制限はない。たとえ
ば、図1<a>に示したような平板状の他、図1<b>
に示したように折り曲げて蛇腹状とすることもできる。
そして、これら平板状、蛇腹状の隔膜(1)は、キャビ
ネット(2)を仕切るように配設することができる。
More specifically, the diaphragm (1) can be mounted inside the cabinet (2) provided in the hydrogen separation and purification apparatus, but its shape is not particularly limited. For example, in addition to the flat plate shape as shown in FIG.
It can be bent into a bellows shape as shown in FIG.
The flat plate-shaped and bellows-shaped diaphragms (1) can be arranged so as to partition the cabinet (2).

【0015】また、隔膜(1)は、図1<c>に示した
ように、パイプ状とすることもできる。薄板化したV-Ni
合金は、加工するのに十分な曲げ強度を有している。パ
イプ状とするときの断面形状は、星形、丸形、楕円形、
四角形、三角形、五角形、六角形、八角形以上の多角形
などの各種の形状が可能である。また、パイプ状とする
場合には、たとえば作製した薄板に電子ビーム溶接、拡
散接合などを適用することができる。このようにしてパ
イプ状とされた隔膜(1)は、キャビネット(2)内に
1本配設しても、また、複数本並設してもよい。パイプ
状の隔膜(1)をキャビネット(2)内に設ける場合に
は、たとえばスウェジロック継手若しくは電子ビーム溶
接などを用いて接合することができる。
Further, the diaphragm (1) may be formed in a pipe shape as shown in FIG. 1 <c>. Thin V-Ni
The alloy has sufficient bending strength to be processed. The cross-sectional shape when made into a pipe shape is star, round, oval,
Various shapes such as a quadrangle, a triangle, a pentagon, a hexagon, and an octagon or more polygon are possible. In the case of a pipe shape, for example, electron beam welding, diffusion bonding, etc. can be applied to the manufactured thin plate. One pipe-shaped diaphragm (1) may be arranged in the cabinet (2) or a plurality thereof may be arranged in parallel. When the pipe-shaped diaphragm (1) is provided in the cabinet (2), it can be joined by using, for example, a swagelok joint or electron beam welding.

【0016】なお、図1<a><b><c>図中に示し
た符号3は、キャビネット(2)へのガス導入部であ
り、符号4は、隔膜(1)による精製後の水素ガス導出
部である。符号5は、残渣ガスのドレインである。
Reference numeral 3 shown in FIG. 1 <a><b><c> is a gas introduction portion to the cabinet (2), and reference numeral 4 is hydrogen after purification by the diaphragm (1). It is a gas outlet. Reference numeral 5 is a drain of residual gas.

【0017】また、この出願の発明の水素分離精製装置
では、V-Ni合金の表裏両面にPd又はPdを含む合金を被覆
するが、これは、V-Ni合金の水素透過性能を劣化させる
表面酸化を防止するとともに、ニ原子分子である水素ガ
スがV-Ni合金に溶け込む際に必要な、原子状水素への解
離反応、すなわち、分離反応を促進させるためである。
Pd又はPdを含む合金のV-Ni合金の表裏両面への被覆法に
ついては、特に制限はなく、真空蒸着法、電気めっき
法、無電解めっき法などが考えられる。中でも無電解め
っき法は、複雑な形状に対しても均一な被覆が可能であ
り、好ましい。なお、被覆するPd又はPdを含む合金の厚
さについても特に制限はなく、隔膜(1)の全体厚さを
考慮し、適宜とすることができる。このPd又はPdを含む
合金の被覆は、隔膜(1)の作製後に行う。
Further, in the hydrogen separation and purification apparatus of the invention of this application, both the front and back surfaces of the V-Ni alloy are coated with Pd or an alloy containing Pd, which is a surface that deteriorates the hydrogen permeation performance of the V-Ni alloy. This is to prevent oxidation and to accelerate the dissociation reaction into atomic hydrogen, that is, the separation reaction, which is necessary when the hydrogen gas, which is a diatomic molecule, dissolves in the V-Ni alloy.
The method for coating Pd or an alloy containing Pd on both front and back surfaces of the V-Ni alloy is not particularly limited, and a vacuum deposition method, an electroplating method, an electroless plating method and the like can be considered. Among them, the electroless plating method is preferable because it can uniformly coat even a complicated shape. The thickness of Pd or the alloy containing Pd to be coated is not particularly limited, and may be set appropriately in consideration of the total thickness of the diaphragm (1). The coating of Pd or an alloy containing Pd is performed after the production of the diaphragm (1).

【0018】以下、この出願の発明の水素分離精製装置
内に装着される薄板化されたV-Ni合金について、実例を
示し、その特性を具体的に示す。
Hereinafter, examples of thinned V-Ni alloys mounted in the hydrogen separation and purification apparatus of the invention of this application will be shown and the characteristics thereof will be specifically shown.

【0019】アルゴン中のアーク溶解法によりV-15原子
%Ni合金を溶製した。このV-15原子%Ni合金に形成された
表面の酸化膜を取り除いた後、これをステンレス管内に
入れ、真空中において電子ビーム溶接によりステンレス
管を封管した。次いで、封管したステンレス管ごと1150
℃において厚さ5mmまで熱間圧延し、シース圧延を実行
した。この後、1200℃において溶体化急冷熱処理を行っ
た。この溶体化急冷熱処理は、Ni原子がVに均一に溶け
込んだ高温状態を急冷し、低温にまで下げる処理であ
り、V-Ni合金の水素透過能及び各種形状への加工性を実
現する。次いで4つに分け、それぞれを0.1mm、0.3mm、
0.4mm、1.1mmの厚さまで室温においてごく一般的なロー
ルを用いて冷間圧延を行った。冷間圧延により薄板表面
はきれいに仕上がる。圧延後の薄板には、いずれも割
れ、ひびなどは一切見られなかった。これまで薄板化が
難しいとされていたV-Ni合金の薄板化が可能となること
が確認された。
V-15 atoms by arc melting method in argon
% Ni alloy was melted. After removing the oxide film on the surface formed on this V-15 atomic% Ni alloy, this was placed in a stainless steel tube, and the stainless steel tube was sealed by electron beam welding in vacuum. Then, 1150 together with the sealed stainless steel pipe
Sheath rolling was performed by hot rolling to a thickness of 5 mm at ℃. Then, solution heat treatment was performed at 1200 ° C. This solution heat treatment for quenching is a treatment for quenching a high temperature state in which Ni atoms are uniformly dissolved in V and lowering it to a low temperature, and realizes hydrogen permeability of the V-Ni alloy and workability into various shapes. Then divide into four, 0.1mm, 0.3mm,
Cold rolling was performed to a thickness of 0.4 mm and 1.1 mm at room temperature using a general roll. By cold rolling, the thin plate surface is finished beautifully. No cracks or cracks were found on any of the thin sheets after rolling. It has been confirmed that it is possible to reduce the thickness of the V-Ni alloy, which has been considered difficult to reduce the thickness.

【0020】作製したそれぞれの薄板から直径約12mmの
円盤状試料を切り出し、その表面をエメリーペーパーや
アルミナ砥粒などを用いた機械研磨及びエッチングを行
う化学研磨により鏡面まで仕上げた後、真空蒸着法によ
り試料の表裏両面にPdを厚さ約0.1μmに被覆した。
A disk-shaped sample having a diameter of about 12 mm was cut out from each of the thin plates prepared, and the surface thereof was mechanically polished using emery paper or alumina abrasive grains and chemically polished for etching to a mirror surface, followed by vacuum deposition. Both sides of the sample were coated with Pd to a thickness of about 0.1 μm.

【0021】このようにして作製した試料を水素透過試
験装置内に装着し、水素透過試験を行った。試験に際
し、試料温度を523Kとし、入り口側に500torrの水素圧
をかけ、出口側を真空引きした。そして、水素透過性
を、実用レベルにあるPd-25Ag合金と比較した。その結
果を示したのが、図2のグラフである。この図2のグラ
フにおいて縦軸を水素流束としているが、水素流束は、
単位面積当たり及び単位時間当たりに流れる水素の体積
を意味する。
The sample thus produced was mounted in a hydrogen permeation test device and a hydrogen permeation test was conducted. During the test, the sample temperature was set to 523 K, hydrogen pressure of 500 torr was applied to the inlet side, and the outlet side was evacuated. Then, the hydrogen permeability was compared with a practical level Pd-25Ag alloy. The result is shown in the graph of FIG. In the graph of FIG. 2, the vertical axis is the hydrogen flux, but the hydrogen flux is
It means the volume of hydrogen flowing per unit area and per unit time.

【0022】図2のグラフから確認されるように、水素
透過流量は、試料の厚さに反比例して増大し、表裏両面
をPdで被覆したV-15Ni合金薄板は、Pd-25Ag合金よりも
より水素透過流量が増大する。
As can be seen from the graph of FIG. 2, the hydrogen permeation flow rate increases in inverse proportion to the thickness of the sample, and the V-15Ni alloy thin plate coated with Pd on both the front and back sides is higher than the Pd-25Ag alloy. The hydrogen permeation flow rate increases.

【0023】さらに、厚さ約0.1mmの、表裏両面をPdで
被覆したV-15Ni合金薄板について曲げ試験を行ったとこ
ろ、十分な曲げ加工性を示し、湾曲部にクラックその他
の欠陥は認められなかった。また、電子ビームを用いて
溶接性も調べたが、溶接部は健全であり、クラックその
他の欠陥は認められなかった。図1<a><b><c>
に例示される各種形状を有する隔膜(1)が実現可能で
あることが確認される。
Further, when a bending test was performed on a V-15Ni alloy thin plate having a thickness of about 0.1 mm and having both front and back surfaces coated with Pd, sufficient bending workability was shown, and cracks and other defects were found in the curved portion. There wasn't. The weldability was also examined using an electron beam, but the welded part was sound and no cracks or other defects were observed. Figure 1 <a><b><c>
It is confirmed that the diaphragm (1) having various shapes exemplified in 1. is feasible.

【0024】もちろん、この出願の発明は、以上の実施
形態によって限定されるものではない。水素分離精製装
置の隔膜を除く構成及び構造、隔膜の形状、作製条件、
及び表裏両面に被覆するPd又はPdを含む合金の厚さのな
どの細部については様々な態様が可能であることはいう
までもない。
Of course, the invention of this application is not limited to the above embodiments. Configuration and structure of the hydrogen separation and purification device excluding the diaphragm, shape of the diaphragm, manufacturing conditions,
It is needless to say that various aspects are possible for details such as the thickness of Pd or an alloy containing Pd coated on both front and back surfaces.

【0025】[0025]

【発明の効果】以上詳しく説明した通り、この出願の発
明によって、薄板化が難しいとされていたV-Ni合金の薄
板化が実現され、これを各種形状の隔壁として装着した
水素分離精製装置が提供され、燃料電池自動車などの重
要なエネルギー源となる99.99999%以上の超高純度水素
を低コストで生産可能となることが期待される。
As described in detail above, according to the invention of this application, thinning of a V-Ni alloy, which has been difficult to be thinned, is realized, and a hydrogen separation / purification device equipped with this as a partition wall of various shapes is provided. It is expected that it will be possible to produce ultra-high purity hydrogen of 99.99999% or more, which will be provided and will be an important energy source for fuel cell vehicles, at low cost.

【図面の簡単な説明】[Brief description of drawings]

【図1】<a><b><c>は、各々、この出願の発明
の水素分離精製装置の一実施形態を概略的に示した断面
図である。
1A to 1C are cross-sectional views schematically showing one embodiment of a hydrogen separation and purification apparatus of the invention of this application.

【図2】水素透過試験装置内に装着した試料の523Kにお
ける厚さの逆数と水素流束との関係を示したグラフであ
る。
FIG. 2 is a graph showing the relationship between the reciprocal of the thickness at 523K and the hydrogen flux of the sample mounted in the hydrogen permeation test apparatus.

【符号の説明】[Explanation of symbols]

1 隔膜 2 キャビネット 3 ガス導入部 4 水素ガス導出部 5 ドレイン 1 diaphragm 2 cabinets 3 gas introduction section 4 Hydrogen gas outlet 5 drain

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 71/02 500 B01D 71/02 500 C22C 27/02 101 C22C 27/02 101Z // H01M 8/06 H01M 8/06 R Fターム(参考) 4D006 GA41 MA02 MA03 MA31 MB04 MC02X NA31 NA50 PA02 PB18 PB66 PC80 4G040 FA02 FB09 FD04 FE01 5H027 AA02 BA16 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) B01D 71/02 500 B01D 71/02 500 C22C 27/02 101 C22C 27/02 101Z // H01M 8/06 H01M 8/06 RF term (reference) 4D006 GA41 MA02 MA03 MA31 MB04 MC02X NA31 NA50 PA02 PB18 PB66 PC80 4G040 FA02 FB09 FD04 FE01 5H027 AA02 BA16

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 表裏両面がPd又はPdを含む合金で被覆さ
れ、5〜30原子%のNiを含む厚さ0.1 mm〜0.001mmのV-Ni
合金が、隔膜として装着され、この隔膜により水素を純
化することを特徴とする水素分離精製装置。
1. V-Ni having a thickness of 0.1 mm to 0.001 mm, which is coated with Pd or an alloy containing Pd on both sides and contains 5 to 30 atom% of Ni.
A hydrogen separating and refining apparatus characterized in that an alloy is mounted as a diaphragm, and hydrogen is purified by the diaphragm.
【請求項2】 V-Ni合金は、厚さ0.1 mm〜0.01mmのシー
ス圧延された薄板である請求項1記載の水素分離精製装
置。
2. The hydrogen separation and purification apparatus according to claim 1, wherein the V-Ni alloy is a sheath-rolled thin plate having a thickness of 0.1 mm to 0.01 mm.
【請求項3】 V-Ni合金は、Mnその他の水素透過能に悪
影響を及ぼさない元素を不可避的不純物元素として、若
しくは最大5原子%まで含有する請求項1又は2記載の水
素分離精製装置。
3. The hydrogen separation and purification apparatus according to claim 1 or 2, wherein the V-Ni alloy contains Mn or other elements that do not adversely affect hydrogen permeability as an unavoidable impurity element or up to 5 atom%.
【請求項4】 隔膜が、平板状、蛇腹状、又はパイプ状
とされている請求項1乃至3いずれかに記載の水素分離
精製装置。
4. The hydrogen separation and purification apparatus according to claim 1, wherein the diaphragm has a flat plate shape, a bellows shape, or a pipe shape.
【請求項5】 パイプ状とされた隔膜が、1本配設され
ているか、若しくは複数本並設されている請求項4記載
の水素分離精製装置。
5. The hydrogen separation and purification apparatus according to claim 4, wherein one pipe-shaped diaphragm is provided, or a plurality of the diaphragms are arranged in parallel.
JP2001284344A 2001-09-19 2001-09-19 Method for thinning V-Ni alloy Expired - Lifetime JP3837481B2 (en)

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JP2008055295A (en) * 2006-08-30 2008-03-13 Ihi Corp Hydrogen separation membrane
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JP2007054788A (en) * 2005-08-26 2007-03-08 Sumitomo Metal Mining Co Ltd Hydrogen-permeable alloy membrane and its manufacturing method
JP2008055295A (en) * 2006-08-30 2008-03-13 Ihi Corp Hydrogen separation membrane
CN110358957A (en) * 2019-07-31 2019-10-22 江苏美特林科特殊合金股份有限公司 A kind of nickel vanadium intermediate alloy and preparation method thereof

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