JP2007237074A - Hydrogen permeable separation membrane exhibiting excellent hydrogen permeable separation capability - Google Patents

Hydrogen permeable separation membrane exhibiting excellent hydrogen permeable separation capability Download PDF

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JP2007237074A
JP2007237074A JP2006062922A JP2006062922A JP2007237074A JP 2007237074 A JP2007237074 A JP 2007237074A JP 2006062922 A JP2006062922 A JP 2006062922A JP 2006062922 A JP2006062922 A JP 2006062922A JP 2007237074 A JP2007237074 A JP 2007237074A
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hydrogen permeable
alloy
hydrogen
permeable separation
solid solution
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JP4953278B2 (en
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Koichi Kita
晃一 喜多
Kiyoshi Aoki
清 青木
Kazuhiro Ishikawa
和宏 石川
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Mitsubishi Materials Corp
Kitami Institute of Technology NUC
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Kitami Institute of Technology NUC
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Priority to AU2007225886A priority patent/AU2007225886B2/en
Priority to CN2007800078803A priority patent/CN101394918B/en
Priority to US12/281,663 priority patent/US8105424B2/en
Priority to EP07738042A priority patent/EP1992401B1/en
Priority to PCT/JP2007/054552 priority patent/WO2007105594A1/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a hydrogen permeable separation membrane exhibiting excellent hydrogen permeable separation capability. <P>SOLUTION: The hydrogen permeable separation membrane is made of a high strength Ni-Ti-Nb alloy with a composition containing Nb: 10-47% by atom, Ti: 20-52% by atom, and balance Ni and inevitable impurities (containing Ni: 20-48% by atom), made to be a refining heat treated material of a cast foil material of the composition with a thickness of 0.07 mm or thinner by a roll quenching method, and having an alloy structure consisting of a basis metal containing Ni-Ti (Nb) intermetallic compound, which is formed by forming a solid solution of Nb by replacing a portion of Ti in a Ni-Ti intermetallic compound, and fine particles of a Nb-based solid solution alloy formed by forming solid solution of Nb with Ni and Ti. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

この発明は、高い機械的強度を有するNi−Ti−Nb合金で構成され、したがって、厚さ:0.07mm(70μm)以下の薄膜化を可能とし、この結果実用に際して、薄膜化による水素透過分離性能の著しい向上を可能とした水素透過分離薄膜に関するものである。   The present invention is composed of a Ni—Ti—Nb alloy having a high mechanical strength, and thus enables a thin film with a thickness of 0.07 mm (70 μm) or less. The present invention relates to a hydrogen permeation separation thin film that can significantly improve performance.

近年、例えば水素燃料電池や水素ガスタービンなどのエネルギーシステムの燃料ガスとして高純度水素ガスが注目されており、この高純度水素ガスが、水を電気分解して得られた混合ガスや液化天然ガス(LNG)を水蒸気改質して得られた混合ガスなどの水素含有原料ガスから、例えば図3に概略説明図で示される通り、外周部を例えばNi製などの枠体で補強され、かつ材質的に水素だけが透過できる機能を有する厚さ:0.1〜3mmの水素透過分離膜で左右両側室に仕切られ、左側室には水素含有原料ガス導入管と排ガス取出管が、右側室には高純度水素ガス取出管が取り付けられた、例えばステンレス鋼製などの反応室を中央部に設けた構造の水素高純度精製装置を用い、前記反応室を200〜300℃に加熱し、前記導入管より水素含有原料ガスを導入し、前記水素透過分離膜を通して分離精製された高純度水素ガスが存在する右側室の内圧を0.1MPaに保持し、一方前記水素含有原料ガスの存在する左側室の内圧を0.2〜0.5MPaに保持した条件で前記水素透過分離膜を通して高純度水素ガスを分離精製することにより生産されることが知られている。
また、上記の水素透過分離膜が、水素の選択的移動を前記水素透過分離膜を通して行なう、例えば炭化水素の水蒸気改質プロセスや、ベンゼン⇔シクロヘキサン反応などの水添/脱水素プロセスなどの化学反応プロセスに広く用いられていることもよく知られるところである。
In recent years, high-purity hydrogen gas has attracted attention as a fuel gas for energy systems such as hydrogen fuel cells and hydrogen gas turbines, and this high-purity hydrogen gas is a mixed gas or liquefied natural gas obtained by electrolyzing water. As shown in the schematic explanatory view of FIG. 3, for example, the outer peripheral portion is reinforced with a frame body made of Ni, for example, as shown in the schematic explanatory diagram of FIG. Thickness capable of only hydrogen permeation: 0.1 to 3 mm hydrogen permeable separation membrane partitioned into left and right side chambers, hydrogen-containing source gas introduction pipe and exhaust gas extraction pipe in left side chamber, right side chamber Is a high-purity hydrogen purifier having a structure in which a reaction chamber made of high-purity hydrogen gas is attached, for example, made of stainless steel, in the center, and the reaction chamber is heated to 200 to 300 ° C. Than tube The internal pressure of the right side chamber where the high-purity hydrogen gas separated through the hydrogen permeation separation membrane is introduced is kept at 0.1 MPa, while the internal pressure of the left side chamber where the hydrogen-containing source gas exists is introduced. It is known that it is produced by separating and refining high-purity hydrogen gas through the hydrogen permeable separation membrane under the condition that is maintained at 0.2 to 0.5 MPa.
Further, the hydrogen permeable separation membrane performs a selective hydrogen transfer through the hydrogen permeable separation membrane, for example, a chemical reaction such as a hydrocarbon steam reforming process or a hydrogenation / dehydrogenation process such as a benzene-cyclohexane reaction. It is well known that it is widely used in processes.

さらに、上記の水素透過分離膜が、
(a) Ni:25〜45原子%、 Ti:26〜50原子%、
を含有し、残りがNbと不可避不純物(ただし、Nb:11〜48原子%含有)からなる成分組成、
(b)鋳造インゴットから放電加工により切り出された厚さ:0.1〜3mmの鋳造薄板材にして、図2に走査型電子顕微鏡による組織写真(倍率:2500倍)で示される通り、Niを固溶したNbTi相とNbを固溶したNiTi相との共晶組織を素地とし、この素地に初晶NbTi相が分散分布した合金組織、
以上(a)の成分組成および(b)の合金組織を有するNi−Ti−Nb合金で構成されることも知られている。
特開2005−232491号公報
Furthermore, the hydrogen permeable separation membrane is
(A) Ni: 25-45 atomic%, Ti: 26-50 atomic%,
And the remainder is composed of Nb and inevitable impurities (however, Nb: 11 to 48 atom%),
(B) Thickness cut out from the casting ingot by electric discharge machining: 0.1 to 3 mm of cast thin plate material, and as shown in the structural photograph (magnification: 2500 times) by a scanning electron microscope in FIG. An eutectic structure of a solid solution NbTi phase and a NiTi phase solid solution of Nb is used as a base material, and an alloy structure in which primary crystal NbTi phases are dispersed and distributed on the base material,
It is also known that it is composed of a Ni—Ti—Nb alloy having the component composition (a) and the alloy structure (b).
JP 2005-232491 A

一方、上記の水素高純度精製装置を含め各種の化学反応装置の高性能化に対する要求はきわめて強く、これに伴ない、前記装置の構造部材として用いられている水素透過分離膜にはより一段と高い水素透過分離性能を具備することが求められ、また、一般に前記水素透過分離膜の場合、これの膜厚を薄くすればするほど水素透過分離性能が向上するようになることも知られていることから、前記水素透過分離膜を構成するNi−Ti−Nb合金の高強度化に関する開発が盛んに行なわれているが、上記の従来水素透過分離膜においては、これを構成するNi−Ti−Nb合金の具備する機械的強度が十分でないために、0.1mm以下の厚さに薄膜化することができず、このため満足な水素透過分離性能の向上が図れないのが現状である。   On the other hand, the demand for high performance of various chemical reaction apparatuses including the above-described hydrogen high-purity purification apparatus is extremely strong, and accordingly, the hydrogen permeation separation membrane used as a structural member of the apparatus is much higher. It is required to have hydrogen permeation separation performance, and generally, in the case of the hydrogen permeation separation membrane, it is known that the hydrogen permeation separation performance is improved as the film thickness is reduced. From the above, the development relating to the strengthening of the Ni—Ti—Nb alloy constituting the hydrogen permeable separation membrane has been actively carried out. However, in the conventional hydrogen permeable separation membrane, the Ni—Ti—Nb constituting this has been developed. Since the mechanical strength of the alloy is not sufficient, it cannot be thinned to a thickness of 0.1 mm or less, so that satisfactory hydrogen permeation separation performance cannot be improved at present.

そこで、本発明者等は、上述のような観点から、上記の各種化学反応装置の高性能化を図るべく、特にこれの構造部材である水素透過分離膜の薄膜化を可能ならしめる目的で、前記水素透過分離膜を構成するNi−Ti−Nb合金の高強度化に着目し、研究を行った結果、前記水素透過分離膜を、原子%(以下、%は原子%を示す)で、
Nb:10〜47%、 Ti:20〜52%、
を含有し、残りがNiと不可避不純物(ただし、Ni:20〜48%含有)からなる成分組成に特定した上で、これの合金溶湯を、ロール急冷法により厚さ:0.07mm以下の鋳造箔材とし、この鋳造箔材に、酸化を防止する目的で不活性ガス雰囲気中、または真空雰囲気中で、温度:300〜1100℃に所定時間加熱保持の条件で調質熱処理を施すと、この結果の調質熱処理材は、図1に走査型電子顕微鏡による組織写真(倍率:2500倍)で示される通り、Ni−Ti金属間化合物におけるTiの一部をNbが置換する状態で固溶含有したNi−Ti(Nb)金属間化合物からなる素地(図1に黒色で示されている)に、NbにNiおよびTiが固溶してなるNb基固溶合金の微細粒(図1に白色で示されている)が分散分布した合金組織をもつようになり、この合金組織のNi−Ti−Nb合金は、きわめて高い機械的強度を有し、したがって水素透過分離膜としての実用に際しては、膜厚を0.07mm以下にすることが可能となり、一段とすぐれた水素透過分離性能を長期に亘って発揮するようになる、という研究結果を得たのである。
In view of the above, the present inventors have made it possible to reduce the thickness of the hydrogen permeable separation membrane, which is a structural member, in order to improve the performance of the various chemical reaction devices described above. As a result of conducting research while focusing on increasing the strength of the Ni-Ti-Nb alloy constituting the hydrogen permeable separation membrane, the hydrogen permeable separation membrane is expressed in atomic% (hereinafter,% indicates atomic%).
Nb: 10 to 47%, Ti: 20 to 52%,
The remaining alloy is specified as a component composition consisting of Ni and inevitable impurities (Ni: 20 to 48%), and the molten alloy is cast into a thickness of 0.07 mm or less by a roll quenching method. When a tempering heat treatment is applied to the cast foil material in an inert gas atmosphere or a vacuum atmosphere for the purpose of preventing oxidation under a condition of heating and holding at a temperature of 300 to 1100 ° C. for a predetermined time, The resulting tempered heat treatment material contains solid solution in a state where Nb replaces a part of Ti in the Ni-Ti intermetallic compound as shown in the structural photograph (magnification: 2500 times) by a scanning electron microscope in FIG. The fine particles of the Nb-based solid solution alloy in which Ni and Ti are dissolved in Nb (shown in black in FIG. 1) on the substrate made of the Ni—Ti (Nb) intermetallic compound (shown in black in FIG. 1) Distributed) The Ni-Ti-Nb alloy with this alloy structure has an extremely high mechanical strength. Therefore, in practical use as a hydrogen permeable separation membrane, the film thickness should be 0.07 mm or less. As a result, research results have been obtained that hydrogen permeation and separation performance will be improved over a long period of time.

この発明は、上記の研究結果に基づいてなされたものであって、
(a) Nb:10〜47%、 Ti:20〜52%、
を含有し、残りがNiと不可避不純物(ただし、Ni:20〜48%含有)からなる成分組成、
(b)ロール急冷法による厚さ:0.07mm以下の鋳造箔材の調質熱処理材にして、Ni−Ti金属間化合物におけるTiの一部をNbが置換する状態で固溶含有したNi−Ti(Nb)金属間化合物からなる素地に、NbにNiおよびTiが固溶してなるNb基固溶合金の微細粒が分散分布した合金組織、
以上(a)の成分組成および(b)の合金組織を有する高強度Ni−Ti−Nb合金で構成してなる、すぐれた水素透過分離性能を発揮する水素透過分離薄膜に特徴を有するものである。
This invention was made based on the above research results,
(A) Nb: 10 to 47%, Ti: 20 to 52%,
Component composition consisting of Ni and inevitable impurities (however, Ni: 20-48% content),
(B) Thickness by roll quenching method: Ni--containing a solid solution in a state where a part of Ti in a Ni-Ti intermetallic compound is substituted by Nb as a tempered heat treatment material of a cast foil material of 0.07 mm or less An alloy structure in which fine particles of an Nb-based solid solution alloy in which Ni and Ti are solid-dissolved in Nb are dispersed and distributed on a substrate made of a Ti (Nb) intermetallic compound,
It is characterized by a hydrogen permeation separation thin film that exhibits excellent hydrogen permeation separation performance and is composed of a high-strength Ni—Ti—Nb alloy having the component composition (a) and the alloy structure (b). .

つぎに、この発明の水素透過分離薄膜において、これを構成するNi−Ti−Nb合金の組成を上記の通りに限定した理由を説明する。
(a)Nb
Nb成分には、上記の通りNi−Ti金属間化合物におけるTiの一部を置換した形で含有して、素地を構成するNi−Ti(Nb)金属間化合物を形成し、もって、前記素地の水素透過分離性能を向上させるほか、NiおよびTiを固溶含有したNb基固溶合金を形成して、前記素地中に微細粒として分散分布し、すぐれた水素透過分離性能を発揮する作用があるが、その含有量が10%未満では薄膜の厚さを0.07mm以下に薄肉化しても所望のすぐれた水素透過分離性能を発揮させることができず、一方その含有量が47%を越えると、前記の合金組織を安定して確保することができなくなることから、その含有量を10〜47%と定めた。
Next, the reason why the composition of the Ni—Ti—Nb alloy constituting the hydrogen permeation separation thin film of the present invention is limited as described above will be described.
(A) Nb
As described above, the Nb component contains a part of Ti in the Ni—Ti intermetallic compound in a substituted form to form a Ni—Ti (Nb) intermetallic compound constituting the substrate, In addition to improving hydrogen permeation separation performance, an Nb-based solid solution alloy containing Ni and Ti as a solid solution is formed and dispersed and distributed as fine particles in the substrate, thereby exhibiting excellent hydrogen permeation separation performance. However, if the content is less than 10%, the desired excellent hydrogen permeation separation performance cannot be exhibited even if the thickness of the thin film is reduced to 0.07 mm or less, while if the content exceeds 47%. Since the alloy structure cannot be secured stably, the content is determined to be 10 to 47%.

(b)TiおよびNi
TiおよびNi成分には、素地を構成するNi−Ti(Nb)金属間化合物を形成して、薄膜の機械的強度を向上させ、もって、0.07mm以下の厚さでの実用化を可能とするほか、前記素地に微細粒として分散分布するNb基固溶合金に固溶して、これの機械的強度を高める作用があるが、TiおよびNiのいずれかの含有量が、Ti:20%未満、Ni:20%未満になると、薄膜に所望の機械的強度を確保することができず、この0.07mm以下の厚さでの実用化が困難となり、一方TiおよびNiのいずれかの含有量でも、Ti:52%、Ni:48%を越えると、水素透過分離性能の低下が避けられなくなることから、その含有量を、それぞれTi:20〜52%、Ni:20〜48%と定めた。
(B) Ti and Ni
For the Ti and Ni components, a Ni—Ti (Nb) intermetallic compound constituting the substrate is formed to improve the mechanical strength of the thin film, thereby enabling practical use with a thickness of 0.07 mm or less. In addition, it has the effect of increasing the mechanical strength of the Nb-based solid solution alloy dispersed and distributed as fine grains in the substrate, but the content of either Ti or Ni is Ti: 20% If Ni is less than 20%, the desired mechanical strength cannot be ensured for the thin film, making practical use at a thickness of 0.07 mm or less difficult, while containing either Ti or Ni Even if the amount exceeds Ti: 52% and Ni: 48%, the decrease in hydrogen permeation separation performance is unavoidable. Therefore, the contents are defined as Ti: 20-52% and Ni: 20-48%, respectively. It was.

この発明の水素透過分離薄膜は、高い機械的強度を有する素地のNi−Ti(Nb)金属間化合物によって、0.07mm以下の厚さへの薄肉化が可能となり、この薄肉化による水素透過分離性能の向上と、前記素地に微細粒として均一に分散分布するNb基固溶合金が、すぐれた水素透過分離性能を発揮することと相俟って、これを各種の化学反応装置に用いた場合、すぐれた水素透過分離性能を長期に亘って発揮するようになるのである。   The hydrogen permeation separation thin film of the present invention can be thinned to a thickness of 0.07 mm or less by the Ni—Ti (Nb) intermetallic compound of the base having high mechanical strength, and hydrogen permeation separation by this thinning is possible. When the Nb-based solid solution alloy that is uniformly distributed as fine particles on the substrate exhibits excellent hydrogen permeation separation performance, it is used in various chemical reactors. Thus, excellent hydrogen permeation separation performance is exhibited over a long period of time.

つぎに、この発明の水素透過分離薄膜を実施例により具体的に説明する。   Next, the hydrogen permeation separation thin film of the present invention will be specifically described with reference to examples.

原料として、純度:99.9%の高純度Nbショット材、同99.9%の高純度Niショット材、および同99.5%の高純度Tiスポンジ材を用い、これら原料をそれぞれ表1に示される割合に配合し、高純度Ar雰囲気中でアーク溶解して、鋳塊とし、この鋳塊を20mm角に切断した状態で、底部に長さ:20mm×幅:0.3mmの寸法をもったスリットが形成された黒鉛ルツボに装入し、0.06MPaの減圧アルゴン雰囲気中で高周波誘導加熱炉で再溶解し、この溶湯を前記スリットから20m/secのロール速度で回転する水冷銅ロールの表面に0.05MPaの噴射圧で吹き付けて、いずれも長さ:20m×幅:20mmの平面寸法を有するが、厚さはそれぞれ表1に示される平均厚さ(任意5ヶ所の平均値)をもったNi−Ti−Nb合金の鋳造箔材を形成し、つぎに、これを真空炉に装入し、10−2Pa以下の真空中、それぞれ300〜1100℃の範囲内の所定の温度に5時間保持後炉冷の条件で調質熱処理を施し、調質熱処理後、幅:20mm×長さ:60mmの平面寸法に切り出すことにより本発明水素透過分離薄膜(以下、本発明水素透過薄膜という)1〜24をそれぞれ製造した。 Purity: 99.9% high purity Nb shot material, 99.9% high purity Ni shot material, and 99.5% high purity Ti sponge material were used. Blended at the indicated ratio, arc melted in a high purity Ar atmosphere to form an ingot, and this ingot is cut into 20 mm squares, and the bottom has a length: 20 mm x width: 0.3 mm. Of a water-cooled copper roll that is charged into a graphite crucible having a slit formed therein and re-melted in a high-frequency induction heating furnace in a reduced pressure argon atmosphere of 0.06 MPa, and the molten metal is rotated at a roll speed of 20 m / sec from the slit. Each surface was sprayed with an injection pressure of 0.05 MPa, and each had a planar dimension of length: 20 m × width: 20 mm, but the thicknesses were the average thicknesses shown in Table 1 (average values at five arbitrary locations). Ni -A cast foil material of Ti-Nb alloy is formed, and then this is charged into a vacuum furnace and kept at a predetermined temperature within a range of 300 to 1100 ° C for 5 hours in a vacuum of 10 -2 Pa or less. Heat treatment is performed under conditions of post furnace cooling, and after the heat treatment, the hydrogen permeation separation thin film of the present invention (hereinafter referred to as the present hydrogen permeation thin film) 1 to 2 is cut out into a plane dimension of width: 20 mm × length: 60 mm. 24 were produced respectively.

また、比較の目的で、同じく原料として、純度:99.9%の高純度Nbショット材、同99.9%の高純度Niショット材、および同99.5%の高純度Tiスポンジ材を用い、これら原料をそれぞれ表2に示される割合に配合し、高純度Ar雰囲気中でアーク溶解し、鋳造して、直径:80mm×厚さ:10mmの寸法をもったNi−Ti−Nb合金鋳塊とし、この鋳塊から、放電加工にて、いずれも幅:20mm×長さ:60mmの平面寸法を有するが、厚さをそれぞれ表2に示される平均厚さ(任意5ヶ所の平均値)とした薄板材に切出すことにより、鋳物切出し薄板材からなる従来水素透過分離膜(以下、従来水素透過膜という)1〜10をそれぞれ製造した。   For the purpose of comparison, as a raw material, a high purity Nb shot material having a purity of 99.9%, a high purity Ni shot material having a purity of 99.9%, and a high purity Ti sponge material having a purity of 99.5% are used. Each of these raw materials was blended in the proportions shown in Table 2, arc-melted in a high-purity Ar atmosphere, cast, and Ni—Ti—Nb alloy ingot having a diameter of 80 mm × thickness of 10 mm. From this ingot, both have a plane dimension of width: 20 mm × length: 60 mm by electric discharge machining, and the thicknesses are the average thicknesses shown in Table 2 (average values at five arbitrary locations). The conventional hydrogen permeation separation membranes (hereinafter referred to as conventional hydrogen permeation membranes) 1 to 10 each made of a cast cut thin plate material were produced by cutting the thin plate material.

この結果得られた本発明水素透過薄膜1〜24および従来水素透過膜1〜10について、その成分組成をエネルギー分散型蛍光X線分析装置を用いて測定したところ、いずれも表1,2に示される配合組成と実質的に同じ分析値を示し、また、その組織を走査型電子顕微鏡およびX線回折装置を用いて観察したところ、前記本発明水素透過薄膜1〜24では、図1に本発明水素透過薄膜19の合金組織を示す通り、いずれもNi−Ti金属間化合物におけるTiの一部をNbが置換する状態で固溶含有したNi−Ti(Nb)金属間化合物からなる素地に、NbにNiおよびTiが固溶してなるNb基固溶合金の微細粒が分散分布した合金組織を示し、一方、上記従来水素透過膜1〜10では、図2に従来水素透過膜8の合金組織を示す通り、いずれもNiを固溶したNbTi相とNbを固溶したNiTi相との共晶組織を素地とし、この素地に初晶NbTi相が分散分布した合金組織、を示した。   The resulting hydrogen permeable thin films 1 to 24 of the present invention and the conventional hydrogen permeable membranes 1 to 10 were measured for their component compositions using an energy dispersive X-ray fluorescence spectrometer. The analysis value was substantially the same as the composition of the composition, and the structure was observed using a scanning electron microscope and an X-ray diffractometer. As a result, the present invention hydrogen permeable thin films 1 to 24 show the present invention in FIG. As shown in the alloy structure of the hydrogen permeable thin film 19, all of the Ni—Ti intermetallic compound containing Ni—Ti (Nb) intermetallic compound containing Ni—Ti (Nb) intermetallic compound in a state where a part of Ti is substituted by Nb FIG. 2 shows an alloy structure in which fine particles of an Nb-based solid solution alloy in which Ni and Ti are solid-dissolved are dispersed and distributed. On the other hand, in the conventional hydrogen permeable films 1 to 10, the alloy structure of the conventional hydrogen permeable film 8 is shown in FIG. As shown Both the eutectic structure of the NiTi phase solid solution of NbTi phase and Nb was dissolved the Ni and the matrix, the primary crystal NbTi phase showed alloy structure, dispersed distributed in this matrix.

ついで、上記の本発明水素透過薄膜1〜24および従来水素透過膜1〜10のそれぞれの両面に、スパッタリング法により厚さ:0.1μmのPd薄膜を蒸着形成し(この場合電気メッキ法により形成しても良い)、かつそれぞれ横外寸:20mm×縦外寸:60mm×枠幅:5mm×枠厚:0.5mmの寸法をもった2枚の銅製補強枠体で両側から挟み、前記各種の透過膜を前記補強枠体に固定した状態で、図3に示される構造の水素高純度精製装置と同じ構造の水素透過評価装置の反応室内に設置し、前記反応室内を300℃に加熱し、反応室の左側室に、水素ガスを導入して、まず、反応室の左側室および右側室の内圧を0.1MPaとし、ついで、前記右側室の内圧を0.1MPaに保持しながら、前記左側室の内圧を0.1MPa当たり5分の速度で、本発明水素透過薄膜1〜7および従来水素透過膜1,2については0.7MPaまで、本発明水素透過薄膜8〜24および従来水素透過膜3〜9については0.5MPaまで、そして従来水素透過膜10については0.3MPaまで、それぞれ昇圧し、この条件で1時間保持した時点で、透過した水素ガスの流量(表1,2に初期透過水素流量で示す)をガスフローメーターで測定し、さらにこの条件、すなわち、右側室の内圧を0.1MPa、左側室の内圧をそれぞれ0.7MPa、0.5MPa、および0.3MPaに昇圧し、この条件で1時間保持した時点から、同条件で20時間続行した時点で、同じく透過した水素ガスの流量(表1,2に後期透過水素流量で示す)を測定し、これらの測定結果を表1,2に示した。   Next, a Pd thin film having a thickness of 0.1 μm is deposited on both surfaces of the hydrogen permeable thin films 1 to 24 of the present invention and the conventional hydrogen permeable films 1 to 10 by sputtering (in this case, formed by electroplating). Each of which is sandwiched from two sides by two copper reinforcing frames having dimensions of 20 mm × vertical outer dimensions: 60 mm × frame width: 5 mm × frame thickness: 0.5 mm. In a state where the permeable membrane is fixed to the reinforcing frame, it is installed in a reaction chamber of a hydrogen permeation evaluation apparatus having the same structure as the hydrogen high-purity purification apparatus having the structure shown in FIG. 3, and the reaction chamber is heated to 300 ° C. Then, hydrogen gas was introduced into the left chamber of the reaction chamber, first, the internal pressure of the left chamber and the right chamber of the reaction chamber was set to 0.1 MPa, and then the internal pressure of the right chamber was maintained at 0.1 MPa, The internal pressure of the left chamber was 0.1 MPa At a rate of 5 minutes, the hydrogen permeable thin films 1 to 7 of the present invention and the conventional hydrogen permeable films 1 and 2 are up to 0.7 MPa, and the hydrogen permeable thin films of the present invention 8 to 24 and the conventional hydrogen permeable thin films 3 to 9 are 0.5 MPa. Up to 0.3 MPa for the conventional hydrogen permeable membrane 10, and when maintained for 1 hour under these conditions, the permeated hydrogen gas flow rate (shown in Tables 1 and 2 as the initial permeated hydrogen flow rate) is gas. Measured with a flow meter and further increased under these conditions, that is, the internal pressure of the right side chamber was increased to 0.1 MPa, and the internal pressure of the left side chamber was increased to 0.7 MPa, 0.5 MPa, and 0.3 MPa, respectively, and held for 1 hour. From the time point, when it continued for 20 hours under the same conditions, the flow rate of the permeated hydrogen gas (shown as the late permeate hydrogen flow rate in Tables 1 and 2) was measured, and the measurement results are shown in Tables 1 and 2 .

Figure 2007237074
Figure 2007237074

Figure 2007237074
Figure 2007237074

表1,2に示される通り、本発明水素透過薄膜1〜24は、いずれも高い機械的強度が素地のNi−Ti(Nb)金属間化合物によって確保され、0.07mm以下の厚さへの薄肉化が可能となるので、前記素地に微細粒として分散分布するNb基固溶合金が、すぐれた水素透過分離性能を発揮することと相俟って、すぐれた水素透過分離性能を長期に亘って発揮し、
すぐれた耐久性(使用寿命)を示すのに対して、従来水素透過膜1〜10は、いずれも機械的強度の面から膜厚を0.1mm以下にすることができず、このため水素透過分離性能の低いものとなることが明らかである。
As shown in Tables 1 and 2, each of the hydrogen permeable thin films 1 to 24 of the present invention has a high mechanical strength ensured by the base Ni—Ti (Nb) intermetallic compound, and has a thickness of 0.07 mm or less. The Nb-based solid solution alloy that is dispersed and distributed as fine particles on the substrate exhibits excellent hydrogen permeation separation performance together with excellent hydrogen permeation separation performance over a long period of time. To demonstrate
In contrast to excellent durability (service life), the conventional hydrogen permeable membranes 1 to 10 cannot be made to have a film thickness of 0.1 mm or less from the viewpoint of mechanical strength. It is clear that the separation performance is low.

上述のように、この発明の水素透過分離薄膜は、高い機械的強度を有するNi−Ti−Nb合金で構成され、厚さ:0.07mm以下への薄膜化を可能とするものであり、実用に際して、すぐれた水素透過分離性能を長期に亘って発揮するものであるから、水素透過分離膜が構造部材として用いられている各種の化学反応装置の高性能化の要求に満足に対応できるものである。   As described above, the hydrogen permeation separation thin film of the present invention is composed of a Ni—Ti—Nb alloy having high mechanical strength, and can be thinned to a thickness of 0.07 mm or less. At this time, since the excellent hydrogen permeation separation performance is demonstrated over a long period of time, the hydrogen permeation separation membrane can satisfactorily meet the demand for high performance of various chemical reactors used as structural members. is there.

本発明水素透過薄膜19を構成するNi−Ti−Nb合金の走査型電子顕微鏡による組織写真(倍率:2500倍)である。It is a structure | tissue photograph (magnification: 2500 times) of the Ni-Ti-Nb alloy which comprises this invention hydrogen permeable thin film 19 by the scanning electron microscope. 従来水素透過膜8を構成するNi−Ti−Nb合金の走査型電子顕微鏡による組織写真(倍率:2500倍)である。It is the structure | tissue photograph (magnification: 2500 times) of the Ni-Ti-Nb alloy which comprises the conventional hydrogen permeable film 8 by the scanning electron microscope. 水素高純度精製装置を例示する概略説明図である。It is a schematic explanatory drawing which illustrates a hydrogen high purity refiner.

Claims (1)

(a) Nb:10〜47原子%、 Ti:20〜52原子%、
を含有し、残りがNiと不可避不純物(ただし、Ni:20〜48原子%含有)からなる成分組成、
(b)ロール急冷法による厚さ:0.07mm以下の鋳造箔材の調質熱処理材にして、Ni−Ti金属間化合物におけるTiの一部をNbが置換する状態で固溶含有したNi−Ti(Nb)金属間化合物からなる素地に、NbにNiおよびTiが固溶してなるNb基固溶合金の微細粒が分散分布した合金組織、
以上(a)の成分組成および(b)の合金組織を有する高強度Ni−Ti−Nb合金で構成したことを特徴とするすぐれた水素透過分離性能を発揮する水素透過分離薄膜。
(A) Nb: 10 to 47 atomic%, Ti: 20 to 52 atomic%,
And the remainder is composed of Ni and inevitable impurities (however, Ni: 20 to 48 atomic%),
(B) Thickness by roll quenching method: Ni--containing a solid solution in a state where a part of Ti in a Ni-Ti intermetallic compound is substituted by Nb as a tempered heat treatment material of a cast foil material of 0.07 mm or less An alloy structure in which fine particles of an Nb-based solid solution alloy in which Ni and Ti are solid-dissolved in Nb are dispersed and distributed on a substrate made of a Ti (Nb) intermetallic compound,
A hydrogen permeation separation thin film exhibiting excellent hydrogen permeation separation performance, characterized by comprising a high-strength Ni—Ti—Nb alloy having the component composition (a) and the alloy structure (b).
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1813344A1 (en) * 2004-11-15 2007-08-01 Nippon Mining & Metals Co., Ltd. Hydrogen separation membrane, sputtering target for forming of hydrogen separation membrane, and process for producing the same
JP2013086038A (en) * 2011-10-19 2013-05-13 Jx Nippon Oil & Energy Corp Alloy film for hydrogen permeation

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8636826B2 (en) * 2009-11-03 2014-01-28 Societe Bic Hydrogen membrane separator
CN112957912B (en) * 2021-01-29 2022-09-06 中国工程物理研究院材料研究所 Multilayer selective hydrogen permeation composite membrane and preparation and application thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000159503A (en) * 1998-11-20 2000-06-13 Mitsubishi Heavy Ind Ltd Hydrogen separating film of niobium alloy
JP2004042017A (en) * 2002-05-20 2004-02-12 Fukuda Metal Foil & Powder Co Ltd Hydrogen separation membrane and production method therefor
JP2005232491A (en) * 2004-02-17 2005-09-02 Ulvac Japan Ltd Dual-phase alloy for hydrogen separation and purification and its manufacturing method, and metal film for hydrogen separation and purification and its manufacturing method
JP2006118035A (en) * 2004-09-22 2006-05-11 Kitami Institute Of Technology Crystalline dual-phase hydrogen permeable alloy and crystalline dual-phase hydrogen permeable alloy film
JP2006265638A (en) * 2005-03-24 2006-10-05 Kitami Institute Of Technology Compound phase hydrogen permeation alloy and hydrogen permeation alloy membrane

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1185363C (en) * 2001-10-25 2005-01-19 北京华瑞能科技发展有限责任公司 Metal ceramic film
AU2003289507A1 (en) * 2003-02-24 2004-09-09 Fukuda Metal Foil And Powder Co., Ltd. Hydrogen separation membrane and process for producing the same

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000159503A (en) * 1998-11-20 2000-06-13 Mitsubishi Heavy Ind Ltd Hydrogen separating film of niobium alloy
JP2004042017A (en) * 2002-05-20 2004-02-12 Fukuda Metal Foil & Powder Co Ltd Hydrogen separation membrane and production method therefor
JP2005232491A (en) * 2004-02-17 2005-09-02 Ulvac Japan Ltd Dual-phase alloy for hydrogen separation and purification and its manufacturing method, and metal film for hydrogen separation and purification and its manufacturing method
JP2006118035A (en) * 2004-09-22 2006-05-11 Kitami Institute Of Technology Crystalline dual-phase hydrogen permeable alloy and crystalline dual-phase hydrogen permeable alloy film
JP2006265638A (en) * 2005-03-24 2006-10-05 Kitami Institute Of Technology Compound phase hydrogen permeation alloy and hydrogen permeation alloy membrane

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1813344A1 (en) * 2004-11-15 2007-08-01 Nippon Mining & Metals Co., Ltd. Hydrogen separation membrane, sputtering target for forming of hydrogen separation membrane, and process for producing the same
EP1813344B1 (en) * 2004-11-15 2014-08-13 JX Nippon Mining & Metals Corporation Hydrogen separation membrane, sputtering target for forming of hydrogen separation membrane, and process for producing the same
JP2013086038A (en) * 2011-10-19 2013-05-13 Jx Nippon Oil & Energy Corp Alloy film for hydrogen permeation

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