JPH1199324A - Separation membrane module - Google Patents

Separation membrane module

Info

Publication number
JPH1199324A
JPH1199324A JP26394197A JP26394197A JPH1199324A JP H1199324 A JPH1199324 A JP H1199324A JP 26394197 A JP26394197 A JP 26394197A JP 26394197 A JP26394197 A JP 26394197A JP H1199324 A JPH1199324 A JP H1199324A
Authority
JP
Japan
Prior art keywords
reinforcing plate
metal
separation membrane
membrane module
metal film
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
JP26394197A
Other languages
Japanese (ja)
Other versions
JP3993282B2 (en
Inventor
Yoji Nakano
要治 中野
Toshiro Kobayashi
敏郎 小林
Shigenori Shirogane
重徳 白銀
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP26394197A priority Critical patent/JP3993282B2/en
Publication of JPH1199324A publication Critical patent/JPH1199324A/en
Application granted granted Critical
Publication of JP3993282B2 publication Critical patent/JP3993282B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To provide a separation membrane module which is a gas permeable separation membrane and has high strength and the large permeated quantity and whose manufacturing cost is made lower than before. SOLUTION: This module consists of a metal membrane 1 for selectively permeating specific gas, a reinforcing plate 2 having a lot of holes 13 and supporting the metal plate 1, and a base plate 3 having a gas removal part which can communicate with a gas releasing pipe. The reinforcing plate 2 is covered with one or plural metals selected from the group consisting of Ag, Au, Pt, Ni, and Cu, but it is not joined with them like the conventional one, and the metal film 1 and the reinforcing plate 2 are put together and the outer peripheral parts thereof are seal welded to the base plate 3. Alternatively, without joining, the metal plate 1 is caught in the holes of the reinforcing plate 2 just below it. In this way, even when a joining process or a metal coating film process and the joining process are eliminated, slippage between the metal film 1 and the reinforcing plate 2 can be prevented.

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】本発明は分離膜モジュールに
関し、詳しくは特定ガスの製造装置,回収装置或いは精
製装置等に使用される分離膜モジュールに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a separation membrane module, and more particularly, to a separation membrane module used in an apparatus for producing, recovering or purifying a specific gas.

【0002】[0002]

【従来の技術】ガスを製造、分離、回収又は精製する手
段として、特定ガスを選択的に透過する金属又は合金膜
(以下、「金属膜」と略記する場合もある)を用いる方
法があり、工業的にも半導体製造分野における超高純度
水素製造等に実用化され、また石油化学工業分野でのア
ンモニア製造への適用も進みつつある。金属膜が特定ガ
スのみを透過する現象については、特定ガスを含有する
混合ガスを金属膜の一方の面に接触させると、特定ガス
分子が金属膜に吸収されて原子状態になり、更にイオン
化して金属膜の反対側に拡散し、ここで再結合して再び
特定ガス分子になると説明されている。この現象を利用
して、金属膜の反対側において特定ガスを集めるわけで
ある。金属膜の製造法としては、特定ガス選択透過性
を有する金属又は合金を焼鈍して冷間圧延する、金属
膜の支持体になる多孔質体の表面に、電気メッキ,無電
解メッキ等のメッキ法あるいは電子ビーム加熱による真
空蒸着等の蒸着操作により金属膜を形成させる、等の方
法がある。
2. Description of the Related Art As a means for producing, separating, recovering or purifying a gas, there is a method using a metal or alloy film (hereinafter sometimes abbreviated as "metal film") which selectively transmits a specific gas. Industrially, it has been put to practical use in the production of ultrahigh-purity hydrogen in the semiconductor production field, and its application to the production of ammonia in the petrochemical industry is also advancing. Regarding the phenomenon in which the metal film permeates only the specific gas, when a mixed gas containing the specific gas is brought into contact with one surface of the metal film, the specific gas molecules are absorbed by the metal film, become an atomic state, and further ionized. And diffuses to the opposite side of the metal film, where it recombines and becomes a specific gas molecule again. By utilizing this phenomenon, a specific gas is collected on the opposite side of the metal film. As a method for producing a metal film, a metal or an alloy having a specific gas selective permeability is annealed and cold-rolled, and a surface of a porous body serving as a support of the metal film is plated by electroplating, electroless plating, or the like. Or a method of forming a metal film by a vapor deposition operation such as vacuum deposition by electron beam heating.

【0003】工業的適用においては、以上のような手段
で作成された金属膜(箔)を外側にして目的とする特定
ガスを含有する混合ガス側に配置し、該金属膜の混合ガ
ス接触面とは反対側には、透過してくる特定ガスを集め
る空間(ガス捕捉部)を有し、透過ガスの抜き出し管に
連通するベース部を設けた分離膜モジュールが構成され
る。金属膜の両側での圧力差、即ち混合ガスと透過した
特定ガスとの圧力差が大きいほど、特定ガスの金属膜内
を透過する量が増大するが、金属膜がこの圧力差に耐え
られるように、補強手段が必要となる。そのために、金
属膜とベース部の間には、通常、金属膜を支持し、その
膜強度を補強するために、多孔質体や多孔体からなる補
強材が設けられる。しかし、補強によりガス流路は狭め
られるため、圧損失が大きくなるので、圧力差を大きく
保ち、しかも特定ガスの流路を確保できる補強材が望ま
れ、出願人等は既に、金属繊維不織布と金網を組合せた
補強材と金属箔を接合した構造の分離膜(特願平5−2
03250号明細書)、或いは多数の貫通孔を設けた金
属多孔体(補強板)に金属膜を重ねて接合した平板型又
は管型の分離膜モジュール(特願平8−60883号明
細書)を提案している。
In industrial applications, the metal film (foil) formed by the above-described means is placed on the side of the mixed gas containing the specific gas of interest with the metal film (foil) facing the outside, and the mixed gas contact surface of the metal film is contacted. On the side opposite to this, a separation membrane module having a space (gas trapping portion) for collecting a permeated specific gas and having a base portion communicating with a permeate gas extraction pipe is configured. As the pressure difference between the two sides of the metal film, that is, the pressure difference between the mixed gas and the permeated specific gas is larger, the amount of the specific gas permeating through the metal film increases, but the metal film can withstand this pressure difference. In addition, reinforcing means is required. Therefore, between the metal film and the base portion, a porous body or a reinforcing material made of a porous body is usually provided to support the metal film and reinforce the film strength. However, since the gas flow path is narrowed by the reinforcement, the pressure loss increases, so a reinforcing material that can maintain a large pressure difference and secure the flow path of the specific gas is desired. Separation membrane having a structure in which a reinforcing material combining a wire mesh and a metal foil are joined (Japanese Patent Application No. 5-2 / 1993)
No. 03250) or a plate-type or tube-type separation membrane module (Japanese Patent Application No. 8-60883) in which a metal film is laminated on a porous metal body (reinforcement plate) provided with a large number of through holes and joined. is suggesting.

【0004】[0004]

【発明が解決しようとする課題】前記した特願平8−6
0883号明細書で提案した分離膜モジュールを図4及
び図5により説明する。図4は管型分離膜モジュールの
構造及び製法を説明する図であって、Pd或いはPdを
含有する合金等よりなるガス透過性金属膜(金属膜)1
を、1枚あるいは複数枚(図示の例では2枚)の金属製
で多数の開口部を有する補強板2及び2′に拡散接合す
る〔図4の(a)部分〕。12は拡散接合用の例えばA
g膜等の金属被覆である。前記で得られた金属膜1と補
強板2の接合体5を、多数の孔を有するベース管4〔図
4の(b)部分に示す〕の外周部に巻きつけ、周囲をシ
ール溶接6して分離膜モジュール7′とする〔図4の
(c)部分に示す〕。
Problems to be Solved by the Invention Japanese Patent Application No. 8-6 mentioned above.
The separation membrane module proposed in Japanese Patent No. 0883 will be described with reference to FIGS. FIG. 4 is a view for explaining the structure and manufacturing method of the tubular separation membrane module, and is a gas-permeable metal membrane (metal membrane) 1 made of Pd or an alloy containing Pd or the like.
Is bonded to one or more (two in the illustrated example) metallic reinforcing plates 2 and 2 'having a large number of openings (portion (a) of FIG. 4). 12 is for diffusion bonding, for example, A
It is a metal coating such as a g film. The joined body 5 of the metal film 1 and the reinforcing plate 2 obtained above is wound around the outer peripheral portion of a base tube 4 (shown in FIG. 4B) having a large number of holes, and the periphery is sealed by welding 6. To form a separation membrane module 7 '(shown in FIG. 4C).

【0005】図5は平型分離膜モジュールの構造及び製
法を説明する図であって、ガス透過性金属膜(金属膜)
1を透過したガスの流路となる溝3′を複数本有するベ
ース板3の溝3′側の上面に、図4の(a)の場合と同
様に補強板2′,補強板2及び金属膜1を配置する〔図
5の(a)部分〕。12は拡散接合用の例えばAg膜等
の金属被覆であり、図5の(b)部分に示す部分側面図
のように補強板2の両面と補強板2′の上面に被覆され
ている。金属膜1と補強板2及び2′を接合して接合体
5とし、該接合体5の外周部とベース板3とをシール溶
接6して、分離膜モジュール7′とする。この分離膜モ
ジュール7′にはガス抜き出し管であるノズル8を有す
るヘッダ9を別途溶接により取り付ける〔図5の(c)
部分〕。
FIG. 5 is a view for explaining the structure and manufacturing method of a flat type separation membrane module, wherein a gas-permeable metal membrane (metal membrane) is shown.
As shown in FIG. 4 (a), a reinforcing plate 2 ', a reinforcing plate 2 and a metal are provided on the upper surface of the base plate 3 having a plurality of grooves 3' serving as flow paths for gas permeating through the groove 3 '. The film 1 is arranged (portion (a) of FIG. 5). Reference numeral 12 denotes a metal coating such as an Ag film for diffusion bonding, which is coated on both surfaces of the reinforcing plate 2 and the upper surface of the reinforcing plate 2 'as shown in the partial side view of FIG. The metal membrane 1 and the reinforcing plates 2 and 2 ′ are joined to form a joined body 5, and the outer peripheral portion of the joined body 5 and the base plate 3 are seal-welded 6 to form a separation membrane module 7 ′. A header 9 having a nozzle 8 serving as a gas extraction tube is separately attached to the separation membrane module 7 'by welding (FIG. 5C).
part〕.

【0006】図4及び図5に示すように、従来の分離膜
モジュール7′において金属膜1と補強板2及び2′の
接合は、拡散接合あるいはろう付けによっていた。すな
わち、補強板2及び2′をAg,Au ,Pt,Ni及び
Cuからなる群れから選ばれる1種あるいは複数種の金
属で被覆するか、該金属材をインサートしておいた後に
金属膜1と重ね、真空加圧炉を用いて温度500〜70
0℃、加圧力1〜3kgf/mm2 の条件で実施してい
る(文献:出願人等の出願に係る特開平8−21555
1号公報)。
As shown in FIGS. 4 and 5, in the conventional separation membrane module 7 ', the metal membrane 1 and the reinforcing plates 2 and 2' are joined by diffusion joining or brazing. That is, the reinforcing plates 2 and 2 'are coated with one or more metals selected from the group consisting of Ag, Au, Pt, Ni and Cu, or after the metal material is inserted, the metal film 1 Layer, using a vacuum press furnace at a temperature of 500 to 70
It is carried out under the conditions of 0 ° C. and a pressure of 1 to 3 kgf / mm 2 (Literature: Japanese Unexamined Patent Publication No. Hei.
No. 1).

【0007】従来、上記のように金属膜と補強板を接合
していた理由を図6を参照して説明する。金属膜1を透
過するガス速度Vは数1に示す式(1)で与えられる。
Conventionally, the reason why the metal film and the reinforcing plate are joined as described above will be described with reference to FIG. The gas velocity V permeating the metal film 1 is given by the equation (1) shown in Expression 1.

【数1】 すなわち、透過ガス速度Vは、金属膜1の両側の透過ガ
ス分圧の1/2乗に比例し、差圧が大きいほど透過ガス
速度が大きくなる。目的とするガスの精製装置や製造装
置では、精製量を多くするためには、金属膜1の両側の
差圧が大きいほうが望ましい。
(Equation 1) That is, the permeated gas velocity V is proportional to the half power of the permeated gas partial pressure on both sides of the metal film 1, and the permeated gas velocity increases as the differential pressure increases. In a target gas purifying apparatus or manufacturing apparatus, it is desirable that the differential pressure on both sides of the metal film 1 be large in order to increase the purification amount.

【0008】金属膜1は、開孔13と柱部(開孔と開孔
の間の部分)を有する補強板2(2′)で補強されてお
り、圧力差により撓み10が生じる。この撓み10が大
きいと、精製装置の「ON←→OFF」の繰り返し、即
ち金属膜の「圧力差有り←→圧力差無し」の繰り返しに
より、撓み10の付け根11が疲労し、破損する。補強
板2の開孔ピッチは、撓み10の発生が図6の(a)の
ように均一ならば、充分な寿命を有するように設計して
おり、図6の(b)のように一カ所の開孔13に撓み1
0が集中すると、圧力差の有無により図6の(c)のよ
うに撓み10の方向が逆転し、撓み10の付け根11に
疲労破損が生じてしまう。この撓み10の集中を防止す
るために、また、金属膜1と補強板2のずれを防止する
ために、金属膜1と補強板2を接合をしていたのであ
る。
The metal film 1 is reinforced by a reinforcing plate 2 (2 ') having an opening 13 and a pillar portion (a portion between the openings), and a bending 10 is caused by a pressure difference. If the flexure 10 is large, the base 11 of the flexure 10 is fatigued and broken due to the repetition of the “ON ← → OFF” of the refining device, that is, the repetition of “there is a pressure difference ← → no pressure difference” of the metal film. The opening pitch of the reinforcing plate 2 is designed so as to have a sufficient life if the occurrence of the bending 10 is uniform as shown in FIG. 6A, and one place as shown in FIG. 6B. Deflection 1 in opening 13
When 0 is concentrated, the direction of the flexure 10 is reversed as shown in FIG. 6C depending on the presence or absence of the pressure difference, and the root 11 of the flexure 10 causes fatigue damage. The metal film 1 and the reinforcing plate 2 are joined to prevent the concentration of the flexure 10 and to prevent the metal film 1 and the reinforcing plate 2 from shifting.

【0009】[0009]

【発明が解決しようとする課題】上記した従来技術にお
いては、 1)接合のプロセスが大量生産に向かないため、接合コ
ストが大きいこと、 2)接合のために金属あるいはろう材で補強板を被覆
し、それが接着材の役割を果して金属膜と接合するが、
金属膜のうち補強板と接触し金属あるいはろう材が付着
した部分は、目的とする特定ガスが透過できなくなり、
ガス透過量が減少すること、という問題がある。本発明
は上記1)及び2)の問題を解決し、強度が高くしかも
ガス透過量が大きい分離膜モジュールであって製造コス
トも従来より低いものを課題とするものである。
In the prior art described above, 1) the joining process is not suitable for mass production, so that the joining cost is high. 2) The reinforcing plate is covered with metal or brazing material for joining. And it acts as an adhesive and joins the metal film,
The part of the metal membrane where the metal or brazing material adheres to the reinforcing plate cannot pass the specific gas of interest,
There is a problem that the gas permeation amount is reduced. An object of the present invention is to solve the above problems 1) and 2) and to provide a separation membrane module having a high strength and a large gas permeation amount, and having a lower production cost than the conventional one.

【0010】[0010]

【課題を解決するための手段】上記課題を解決する手段
として本発明は、(1)特定ガスを選択的に透過する金属
膜と、多数の開孔を有し、前記金属膜を支持する補強板
と、ガス抜き出し管に連通できるガス捕捉部を有するベ
ース部からなる分離膜モジュールにおいて、前記補強板
がAg,Au,Pt,Ni及びCuからなる群れから選
ばれる1種又は複数種の金属で被覆されてなり、前記金
属膜と該補強板を重ね合わせたものの外周部が前記ベー
ス部にシール溶接されてなることを特徴とする分離膜モ
ジュール、(2)上記Ag,Au,Pt,Ni及びCuか
らなる群れから選ばれる1種又は複数種の金属の被覆が
前記補強板の表面の一部のみに形成されてなることを特
徴とする前記(1) 記載の分離膜モジュール、(3)特定ガ
スを選択的に透過する金属膜と、多数の開孔を有し、前
記金属膜を支持する補強板と、ガス抜き出し管に連通で
きるガス捕捉部を有するベース部からなる分離膜モジュ
ールにおいて、前記金属膜と該補強板を重ね合わせたも
のの外周部が前記ベース部にシール溶接され、且つ前記
金属膜がその直下の前記補強板の前記開孔に食い込んだ
構造であることを特徴とする分離膜モジュール、及び
(4)前記ベース部が溝を有する板又は多孔管であること
を特徴とする前記(1) ないし(3) のいずれかに記載の分
離膜モジュール、を提供するものである。
As a means for solving the above-mentioned problems, the present invention provides (1) a metal film which selectively permeates a specific gas, and a reinforcing member having a large number of openings and supporting the metal film. In a separation membrane module comprising a plate and a base having a gas trapping part which can communicate with a gas extraction pipe, the reinforcing plate is made of one or more kinds of metals selected from the group consisting of Ag, Au, Pt, Ni and Cu. A separation membrane module, wherein the outer periphery of the metal membrane and the reinforcing plate overlapped with each other is seal-welded to the base, (2) the Ag, Au, Pt, Ni and The separation membrane module according to (1), wherein a coating of one or more kinds of metals selected from the group consisting of Cu is formed on only a part of the surface of the reinforcing plate. Metal that selectively permeates gas In a separation membrane module comprising a membrane, a reinforcing plate having a large number of openings, supporting the metal film, and a base portion having a gas trapping portion capable of communicating with a gas extraction pipe, the metal film and the reinforcing plate are stacked. A separation membrane module, wherein an outer peripheral portion of the combined product is seal-welded to the base portion, and the metal film has a structure in which the metal film cuts into the opening of the reinforcing plate immediately below;
(4) The separation membrane module according to any one of (1) to (3), wherein the base is a plate having a groove or a perforated tube.

【0011】[0011]

【発明の実施の形態】本発明は、補強板にAg,Au,
Pt,Ni及びCuからなる群れから選ばれる1種又は
複数種の金属の被覆(以下単に金属被覆と称する)を行
なうが、図1及び図2の本発明の構造及び製法を示す概
略図にそれぞれ示すように、拡散接合あるいはろう付け
による接合は行わず、そのまま金属膜と重ねてベース部
とシール溶接されていることを第一の特徴とする。な
お、図1及び図2において図4及び図5とそれぞれ共通
する符号部分はおなじ意味を表し、7は本発明の分離膜
モジュールを表す。本発明をこのような構成とする理由
については、後記する本発明の実施例において説明す
る。本発明の構成によって充分に疲労破損を防止できる
とともに、従来例の接合工程をなしにできるので、製造
時間、コスト共に低減できる。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention relates to a method in which Ag, Au,
One or more kinds of metals selected from the group consisting of Pt, Ni and Cu are coated (hereinafter simply referred to as metal coating). FIGS. 1 and 2 are schematic diagrams showing the structure and manufacturing method of the present invention, respectively. As shown in the figure, the first feature is that the bonding by diffusion bonding or brazing is not performed, and the metal film is directly overlapped with the base portion and seal-welded. 1 and 2, the same reference numerals as those in FIGS. 4 and 5 denote the same parts, and 7 denotes a separation membrane module of the present invention. The reason why the present invention is configured as described above will be described in an embodiment of the present invention described later. With the configuration of the present invention, fatigue damage can be sufficiently prevented, and the joining step of the conventional example can be omitted, so that both the manufacturing time and the cost can be reduced.

【0012】本発明において金属膜としては、特定のガ
スを透過する金属膜(箔)であれば特に限定されるとこ
ろはないが、金属の種類として例えばPd又はPd合金
が挙げられる。Pd合金としては、Y及びその他希土類
元素、Ag,Au,Cuなどの11族元素、Pt,Ni
などの10族元素、Rh,Coなどの9族元素、Ru,
Feなどの8族元素、Moなどの6族元素及びVなどの
5族元素からなる群から選ばれる1種以上とPdからな
る合金が好適なものとして挙げられる。金属膜の製法自
体についても特に限定されるところはなく、例えば金属
板を圧延する、基材表面にめっき,溶射,蒸着等の手段
で膜形成した後に該基材を除去する等の手段が挙げられ
る。
In the present invention, the metal film is not particularly limited as long as it is a metal film (foil) permeable to a specific gas, but examples of the metal include Pd or a Pd alloy. Pd alloys include Y and other rare earth elements, Group 11 elements such as Ag, Au and Cu, Pt, Ni
Group 10 elements such as Rh, Co, etc .;
Preferable alloys include one or more selected from the group consisting of Group 8 elements such as Fe, Group 6 elements such as Mo, and Group 5 elements such as V, and Pd. There is no particular limitation on the method of producing the metal film itself, and examples thereof include a method of rolling a metal plate, a method of forming a film on a surface of a substrate by plating, thermal spraying, vapor deposition, and the like, and then removing the substrate. Can be

【0013】本発明において補強板としては、ベース板
とシール溶接可能な部分を有するものを用いる。また、
目的とする特定ガスが透過するように多孔質構造を有す
ることが必要であり(但し外周に非多孔質の枠を有して
いてもよい)、例えば金属(合金を含む)からなり多数
の開孔を有するもの(金属多孔体)等が挙げられる。具
体的にはレーザ法、エッチング法、ドリル法等により孔
あけ加工したもの、網状にしたもの等が挙げられる。補
強板の孔形状、補強板の枚数等は任意に選択できるが、
前記特願平8−60833号で提案した孔の長軸方向が
交互に直交するように重ねた補強板等を利用することは
好ましい実施態様である。
In the present invention, a reinforcing plate having a portion which can be seal-welded to a base plate is used. Also,
It is necessary to have a porous structure so that a specific gas of interest permeates (however, a non-porous frame may be provided on the outer periphery). Those having pores (porous metal body) are exemplified. Specifically, a material formed by drilling by a laser method, an etching method, a drill method, or the like, a material formed into a net shape, and the like can be given. The hole shape of the reinforcing plate, the number of reinforcing plates, etc. can be arbitrarily selected,
It is a preferred embodiment to use a reinforcing plate or the like, which is proposed in Japanese Patent Application No. 8-60833, in which the major axis directions of the holes are alternately perpendicular to each other.

【0014】本発明において補強板表面の金属被覆とし
ては、Ag,Au,Pt,Ni及びCuからなる群れか
ら選ばれる1種又は複数種の金属が挙げられる。被覆の
形成は真空蒸着,イオンプレーティング等の蒸着法、電
気めっき,無電解めっき等のめっき法、溶射法、イオン
注入法等により、特に好ましくは蒸着法により、厚さは
0.1〜5μm程度、好ましくは0.5〜1μm程度と
する。
In the present invention, the metal coating on the surface of the reinforcing plate includes one or more metals selected from the group consisting of Ag, Au, Pt, Ni and Cu. The coating is formed by a vacuum evaporation method, an ion plating method or the like, an electroplating method, an electroless plating method or the like, a thermal spraying method, an ion implantation method or the like, particularly preferably a vapor deposition method, and a thickness of 0.1 to 5 μm. Degree, preferably about 0.5 to 1 μm.

【0015】本発明の第2の特徴は、この金属被覆が従
来のように補強板全面ではなく部分的に被覆したもので
もよいことである。接合は金属膜と補強板のズレを防止
するためのものであり、補強板全面を接合しなくてもズ
レ防止は可能である。そこで補強板の一部にのみ、金属
あるいはろう材の膜を形成すれば、接合部分が金属膜を
覆うことに起因するガス透過面積の低減を防止できる。
これにより充分に疲労破損を防止でき、接合工程なしに
製造できるという前記の効果とともに、特定ガスの透過
量を増大できるという効果も得られる。
A second feature of the present invention is that the metal coating may be partially coated instead of the entire surface of the reinforcing plate as in the prior art. The joining is for preventing the displacement between the metal film and the reinforcing plate, and the displacement can be prevented without joining the entire reinforcing plate. Therefore, if a metal or brazing material film is formed only on a part of the reinforcing plate, it is possible to prevent a reduction in the gas permeation area caused by the joint portion covering the metal film.
Thereby, fatigue damage can be sufficiently prevented, and the effect that the specific gas permeation amount can be increased can be obtained in addition to the above-described effect that the manufacturing can be performed without the joining step.

【0016】補強板の一部にのみ、金属或いはろう材の
膜(金属被覆)を形成する方法は、補強板にマスクを
して金属被覆を真空蒸着法等により形成し、被覆形成後
にマスクを剥がす、全面に金属被覆を形成したのち、
不必要な部分をエッチングする、パターン印刷により
金属被覆を形成する、等のいずれの方法でもよい。
A method of forming a metal or brazing film (metal coating) only on a part of the reinforcing plate is to form a metal coating by a vacuum deposition method using a mask on the reinforcing plate, and to form a mask after forming the coating. Peel off, after forming a metal coating on the entire surface,
Any method such as etching an unnecessary portion or forming a metal coating by pattern printing may be used.

【0017】さらに本発明においては、金属膜と補強板
を重ねた後に、接合の代わりに箔と補強板のズレを防止
する手段として、金属膜を塑性変形させて金属膜を補強
板の孔に食い込ませた構造とすることを、第3の特徴と
する。すなわち、図3(a)に示すように圧力差の有無
による撓みを予め形成しておく。これにより接合なしに
金属膜と補強板のずれを防止し、図3(b)に示すよう
に撓みをごく小さくし、しかも撓みの一カ所集中を防止
できる。この場合、補強板表面の全面又は一部に金属被
覆を設けておいてもよいが、後記する実施例に示すよう
にAg膜等の金属被覆を設けていないものでも充分にず
れを防止できる。このようにAg膜等の金属被覆なしと
したものはさらに製造コストを低減できる。
Further, in the present invention, after the metal film and the reinforcing plate are overlapped, as a means for preventing displacement of the foil and the reinforcing plate instead of joining, the metal film is plastically deformed so that the metal film is inserted into the hole of the reinforcing plate. A third feature is to have a bite structure. That is, as shown in FIG. 3A, the bending due to the presence or absence of the pressure difference is formed in advance. Thereby, the displacement between the metal film and the reinforcing plate can be prevented without joining, the bending can be made very small as shown in FIG. 3 (b), and the bending can be prevented from being concentrated at one place. In this case, a metal coating may be provided on the entire surface or a part of the surface of the reinforcing plate. However, even if a metal coating such as an Ag film is not provided as shown in Examples described later, the displacement can be sufficiently prevented. As described above, the one without the metal coating such as the Ag film can further reduce the manufacturing cost.

【0018】図3の構造とするためには、i)軟ロール使
用法、ii) 高圧法のいずれかによる。i)軟ロール使用法
は、金属膜を補強板の上に重ね、金属膜の側からゴム等
の変形し易い材質のロール或いは板等で押し、金属膜を
塑性変形させる方法である。ii)高圧法は、金属膜の両
側の圧力差により、金属膜を塑性変形させる方法で、こ
れは分離膜モジュールを管型あるいは平型(板型)に製
造した後でも施工可能である。
In order to obtain the structure shown in FIG. 3, any one of i) a method using a soft roll and ii) a high pressure method is used. i) The soft roll method is a method in which a metal film is superimposed on a reinforcing plate and pressed from a side of the metal film with a roll or a plate of easily deformable material such as rubber to deform the metal film plastically. ii) The high-pressure method is a method in which the metal film is plastically deformed by a pressure difference between both sides of the metal film. This method can be applied even after the separation membrane module is manufactured in a tube type or a flat type (plate type).

【0019】本発明においてベース部としては、金属
膜、補強板を透過した特定ガスを捕捉できる捕捉部を有
し、特定ガスを集めることができる構造であれば、その
形状は限定されるところはなく、例えばガス流路となる
溝を形成された板型、あるいは多孔管型等が挙げられ
る。ベース部のガス捕捉部(ガス流路)は特定ガスの抜
き出し管に連通するが、さらにスイープガスの導入管を
設けることもできる。ベース部の材質としては、金属又
は合金が挙げられる。
In the present invention, the shape of the base portion is limited as long as the base portion has a capturing portion capable of capturing a specific gas that has passed through the metal film and the reinforcing plate and can collect the specific gas. For example, a plate type having a groove serving as a gas flow path or a perforated tube type may be used. The gas trapping section (gas flow path) of the base section communicates with a pipe for extracting a specific gas, but a pipe for introducing a sweep gas may be further provided. Examples of the material of the base portion include metals and alloys.

【0020】本発明の分離膜モジュールは以上の金属膜
と金属被覆を形成された補強板を重ねたものの外周部を
ベース板とシール溶接する。このシール溶接の方法とし
てはレーザ溶接、TIG溶接(Tungsten Inert-Gas arc
welding) 等が用いられる。レーザ溶接、TIG溶接を
採用する理由は、微小領域のみを加熱し溶接できるので
入熱が少なく、金属膜へのダメージが小さくできるから
である。
In the separation membrane module of the present invention, the outer peripheral portion of the above-mentioned metal film and the reinforcing plate provided with the metal coating are sealed and welded to the base plate. Laser welding, TIG welding (Tungsten Inert-Gas arc)
welding) is used. The reason for employing laser welding and TIG welding is that only small areas can be heated and welded, so that heat input is small and damage to the metal film can be reduced.

【0021】[0021]

【実施例】【Example】

〔従来例〕従来法により、図5に示す平型分離膜モジュ
ール7′を作製した。ガス透過性金属膜1としては厚さ
20μm、幅70mm、長さ120mmのPd−23%
Ag合金箔、補強板2としてSUS430製の厚さ0.
1mmのもの1枚、補強板2′として同材質で厚さ0.
3mmのもの1枚、の計2枚の補強板を用意した。いず
れも外径は幅70mm、長さ120mm、メッシュ部が
幅60mm、長さ100mmである。図7に示すように
厚さ0.1mmの補強板2のメッシュ部には、幅0.1
6mm、長さ1.0mmの開孔が、0.04mm残し
(柱部)で千鳥状に配置してある。メッシュ部の開孔率
は、開孔の個数が多いので、長方形の開孔面積を図7中
に点線で示す長方形の面積で割った値で近似できる。す
なわち、数2の計算(2)より、
[Conventional Example] A flat separation membrane module 7 'shown in FIG. 5 was manufactured by a conventional method. As the gas permeable metal film 1, Pd-23% having a thickness of 20 μm, a width of 70 mm, and a length of 120 mm
Ag alloy foil, SUS430 as the reinforcing plate 2
One sheet of 1 mm, the same material as the reinforcing plate 2 ′ and a thickness of 0.
A total of two reinforcing plates, one of 3 mm, were prepared. In each case, the outer diameter is 70 mm in width and 120 mm in length, and the mesh portion is 60 mm in width and 100 mm in length. As shown in FIG. 7, the mesh portion of the reinforcing plate 2 having a thickness of 0.1 mm has a width of 0.1 mm.
Openings having a length of 6 mm and a length of 1.0 mm are arranged in a zigzag pattern with 0.04 mm remaining (column portion). Since the number of openings is large, the opening ratio of the mesh portion can be approximated by a value obtained by dividing the rectangular opening area by the area of the rectangle indicated by the dotted line in FIG. That is, from the calculation (2) of Equation 2,

【数2】 0.77である。厚さ0.3mmの補強板2′は幅0.
35mm、長さ1.0mmの長方形の開孔が、厚さ0.
1mmの補強板2と交差する向きに、0.35mm残し
で千鳥状に配置してある。
(Equation 2) 0.77. A 0.3 mm thick reinforcing plate 2 ′ has a width of 0.3 mm.
A rectangular opening having a thickness of 35 mm and a length of 1.0 mm has a thickness of 0.3 mm.
In a direction intersecting with the 1 mm reinforcing plate 2, they are arranged in a zigzag pattern with 0.35 mm remaining.

【0022】まず、厚さ0.1mmの補強板2の両面、
及び厚さ0.3mmの補強板2′の片面に、Agからな
る被覆12を真空蒸着法で形成し、水素透過製金属箔/
厚さ0.1mmの補強板/厚さ0.3mmの補強板の順
に重ね、真空加圧炉を用いて、温度500℃、加圧力2
kgf/mm2 の条件で接合し、接合体5とした。次
に、接合体5をベース板3に重ね、外周部をシール溶接
した。シール溶接6はCO2 レーザ溶接により行った。
ベース板3の溝3′は、片端は閉じており、閉じていな
い他端には水素を排出するノズル8を有するヘッダ9を
溶接により接続した。
First, both sides of the reinforcing plate 2 having a thickness of 0.1 mm,
A coating 12 made of Ag is formed on one side of a reinforcing plate 2 'having a thickness of 0.3 mm by a vacuum evaporation method, and a hydrogen-permeable metal foil /
A reinforcing plate having a thickness of 0.1 mm / a reinforcing plate having a thickness of 0.3 mm are stacked in this order, and using a vacuum pressurizing furnace, at a temperature of 500 ° C. and a pressing force of 2
It joined under the condition of kgf / mm 2 to obtain a joined body 5. Next, the joined body 5 was placed on the base plate 3 and the outer peripheral portion was sealed and welded. Seal welding 6 was performed by CO 2 laser welding.
One end of the groove 3 'of the base plate 3 is closed, and a header 9 having a nozzle 8 for discharging hydrogen is connected to the other end which is not closed by welding.

【0023】以上により試作した水素分離膜モジュール
7′について、水素透過性能評価試験、及び温度・圧力
の昇降繰り返しによる耐久性試験を行った。試験条件
は、水素透過性能評価試験は、試験条件:温度500
℃、水素透過性金属箔の外側水素分圧2kgf/cm2
G、内側の水素分圧0kgf/cm2 G:での水素透過
量測定で評価し、耐久性試験は、試験条件:温度550
℃,外側圧力10kgf/cm2 G←→温度50℃,外
側圧力0kgf/cm2 Gを繰り返した:でのリーク発
生の有無で評価する。評価結果は、水素透過性能が22
Nm3 /hr・m2、耐久性は3000回の繰り返しで
もリークはなかった。
With respect to the hydrogen separation membrane module 7 'produced as described above, an evaluation test of hydrogen permeation performance and a durability test by repeatedly raising and lowering the temperature and pressure were performed. The test conditions were: hydrogen permeation performance evaluation test, test condition: temperature 500
° C, hydrogen partial pressure outside the hydrogen permeable metal foil 2 kgf / cm 2
G, the inner hydrogen partial pressure was 0 kgf / cm 2 G. The durability was evaluated by measuring the amount of permeated hydrogen.
C., an outside pressure of 10 kgf / cm 2 G →→ a temperature of 50 ° C., and an outside pressure of 0 kgf / cm 2 G: The evaluation was made based on whether or not a leak occurred. The evaluation result shows that the hydrogen permeation performance is 22
Nm 3 / hr · m 2 , and durability showed no leakage even after 3,000 repetitions.

【0024】〔比較例〕接合の有効性確認のため、従来
例と同じ部材を用いてAg被覆の形成及び接合を行わ
ず、すなわち水素透過性金属箔1、厚さ0.1mmの補
強板2、及び厚さ0.3mmの補強板2′をベース板3
に重ねただけで、外周部をシール溶接6して、水素分離
膜モジュールとした。得られた水素分離膜モジュールに
ついて、従来例と同様に評価したところ、水素透過性能
は29Nm3 /hr・m2 と増大するが、耐久性は12
00回の繰り返しでリークが発生し、耐久性が問題であ
った。
[Comparative Example] In order to confirm the effectiveness of joining, the same members as in the conventional example were not used to form and join the Ag coating, ie, a hydrogen-permeable metal foil 1 and a reinforcing plate 2 having a thickness of 0.1 mm. And a reinforcing plate 2 'having a thickness of 0.3 mm
The outer peripheral portion was seal-welded 6 to form a hydrogen separation membrane module. When the obtained hydrogen separation membrane module was evaluated in the same manner as in the conventional example, the hydrogen permeation performance was increased to 29 Nm 3 / hr · m 2 , but the durability was 12
Leakage occurred at the repetition of 00 times, and durability was a problem.

【0025】〔実施例1〕従来例と同じ部材を用い、図
1(a)に示すように厚さ0.1mmの補強板2の水素
透過製金属箔1と接する面に従来例と同様にAg膜12
を被覆したが、接合は行わずに、水素透過製金属箔1/
厚さ0.1mmの補強板2/厚さ0.3mmの補強板
2′をベース板3に重ねて、外周部をシール溶接6でシ
ールして、図1(b)に示す水素分離膜モジュール7を
作製した。また、溝3′の閉じていない端部にノズル
(水素抜き出し管)8を有するヘッダを溶接により取り
付けた。得られた水素分離膜モジュール7について、従
来例と同様に評価した。耐久性評価試験前の水素透過性
能は29Nm3 /hr・m2 と比較例と同等に良くなっ
ていた。耐久性評価試験では、3000回の繰り返しで
もリークは生じず、良好な耐久性を示した。また、耐久
性評価試験後には、水素透過性能は22Nm3 /hr・
2 と従来例のレベルに低減していた。
Example 1 Using the same members as in the conventional example, the surface of the reinforcing plate 2 having a thickness of 0.1 mm, which is in contact with the metal foil 1 made of hydrogen permeable, as shown in FIG. Ag film 12
, But without joining, the hydrogen permeable metal foil 1 /
A reinforcing plate 2 having a thickness of 0.1 mm / a reinforcing plate 2 ′ having a thickness of 0.3 mm is placed on the base plate 3, and the outer peripheral portion thereof is sealed with a seal weld 6, and the hydrogen separation membrane module shown in FIG. 7 was produced. Further, a header having a nozzle (hydrogen extraction pipe) 8 was attached to the unclosed end of the groove 3 'by welding. About the obtained hydrogen separation membrane module 7, it evaluated similarly to the conventional example. The hydrogen permeation performance before the durability evaluation test was 29 Nm 3 / hr · m 2, which was as good as the comparative example. In the durability evaluation test, no leak occurred even after 3,000 repetitions, indicating good durability. After the durability evaluation test, the hydrogen permeability was 22 Nm 3 / hr ·
m 2, which is a level of the conventional example.

【0026】実施例1において耐久性評価試験後に水素
透過性能が低下する原因について、水素分離膜を解体し
て調査したところ、水素透過性金属箔1と厚さ0.1m
mの補強板2′がAg膜12により接合されていること
が判った。耐久性評価試験の温度、圧力により、真空加
圧炉での接合と同様の効果が現れたものと推定された。
また、この接合により水素透過面積が減少し、3000
回の圧昇降の後には水素透過性能が従来例のレベルに低
減したと推定された。
In Example 1, the cause of the decrease in the hydrogen permeability after the durability evaluation test was examined by disassembling the hydrogen separation membrane. The hydrogen permeable metal foil 1 and the thickness of 0.1 m were examined.
It was found that the m reinforcing plate 2 ′ was joined by the Ag film 12. It was presumed that the same effect as bonding in a vacuum pressurizing furnace appeared depending on the temperature and pressure in the durability evaluation test.
In addition, the hydrogen permeation area is reduced by this bonding,
It was presumed that the hydrogen permeation performance was reduced to the level of the conventional example after each pressure rise and fall.

【0027】実施例1により、水素膜モジュール製造工
程においては補強板に接合用の金属膜を形成しておきさ
えすれば、耐久性評価、或いは水素精製、水素製造プロ
セス中に接合されることにより、製造工程の接合プロセ
スが省略できることが判った。
According to the first embodiment, in the hydrogen film module manufacturing process, as long as a metal film for bonding is formed on the reinforcing plate, it can be evaluated during durability evaluation or bonded during the hydrogen purification and hydrogen manufacturing process. It has been found that the joining process in the manufacturing process can be omitted.

【0028】〔実施例2〕本実施例では、接合により水
素透過面積が減少することを予防できる構造を検討し
た。まず、従来例と同じ部材を用いて、水素分離膜モジ
ュールを試作した。補強板2への金属被覆12の形成
は、次のようにした。厚さ0.1mmの補強板2に金属
被覆(Ag膜)12を真空蒸着法で被覆するとき、補強
板2の長孔と交差する方向の孔を有するマスク(孔の短
軸の開口幅0.1mm、残幅0.9mm、開口率0.
1)を作製し、マスクを補強板2に重ねて膜を形成し
た。膜はマスクの孔の部分にしか形成されず、補強板2
の表面の10%だけにAg膜が形成された。厚さ0.3
mmの補強板2′についても同様に表面の10%だけに
Ag膜12を形成した。水素透過性金属箔1、厚さ0.
1mmの補強板2及び厚さ0.3mmの補強板2′をベ
ース板に重ねて、接合は行わずにその外周部をベース板
3とシール溶接して、水素分離膜モジュールを製作し
た。
[Embodiment 2] In this embodiment, a structure capable of preventing a reduction in the hydrogen permeable area due to bonding was examined. First, a hydrogen separation membrane module was prototyped using the same members as the conventional example. The metal coating 12 was formed on the reinforcing plate 2 as follows. When the metal coating (Ag film) 12 is coated on the reinforcing plate 2 having a thickness of 0.1 mm by a vacuum deposition method, a mask having a hole in a direction intersecting with the long hole of the reinforcing plate 2 (the opening width of the short axis of the hole is 0). .1 mm, residual width 0.9 mm, aperture ratio 0.
1) was prepared, and a mask was overlaid on the reinforcing plate 2 to form a film. The film is formed only in the holes of the mask, and the reinforcing plate 2
An Ag film was formed on only 10% of the surface of the sample. Thickness 0.3
Similarly, the Ag film 12 was formed on only 10% of the surface of the reinforcing plate 2 'having a thickness of 2 mm. Hydrogen permeable metal foil 1, thickness 0.
A 1 mm reinforcing plate 2 and a 0.3 mm thick reinforcing plate 2 ′ were stacked on a base plate, and the outer peripheral portion thereof was seal-welded to the base plate 3 without joining, thereby producing a hydrogen separation membrane module.

【0029】実施例2で得られた水素分離膜モジュール
について従来例と同様に評価した。耐久性評価試験前の
水素透過性能は29Nm3 /hr・m2 であった。耐久
性評価試験では、3000回の繰り返しでもリークは生
じず、良好な耐久性を示した。耐久性評価後の水素透過
性能は、28Nm3 /hr・m2 と殆ど減少していなか
った。
The hydrogen separation membrane module obtained in Example 2 was evaluated in the same manner as in the conventional example. The hydrogen permeation performance before the durability evaluation test was 29 Nm 3 / hr · m 2 . In the durability evaluation test, no leak occurred even after 3,000 repetitions, indicating good durability. The hydrogen permeability after the durability evaluation was hardly reduced to 28 Nm 3 / hr · m 2 .

【0030】実施例2の結果から、補強板の金属被覆形
成面積を小さくすることにより、その後の実使用におけ
る接合により水素透過性金属箔の水素透過面積が減少す
ることを低減でき、水素透過性能の向上につながった。
なお、実施例2では補強板2及び2′のどちらも、その
表面の10%だけにAg膜を形成したが、両者の被覆割
合を変えること、さらには一方は部分的に被覆し他方は
全面を被覆することも本発明の実施態様として挙げら
れ、いずれも前記の効果を奏することができる。
From the results of Example 2, it can be seen that, by reducing the metal cover forming area of the reinforcing plate, a decrease in the hydrogen permeable area of the hydrogen permeable metal foil due to subsequent joining in actual use can be reduced, and the hydrogen permeable performance can be reduced. Improved.
In the second embodiment, the Ag film was formed on only 10% of the surface of each of the reinforcing plates 2 and 2 '. However, the covering ratio of both was changed, and further, one was partially covered and the other was entirely covered. Is also mentioned as an embodiment of the present invention, and any of the above effects can be obtained.

【0031】〔実施例3〕本実施例も従来例と同じ部材
を用いて水素分離膜を試作したが、厚さ0.1mmの補
強板2及び厚さ0.3mmの補強板2′についてはAg
被覆を形成しなかった。水透過性金属箔1に補強板2を
重ねて、ゴムロールを用いて水素透過性金属箔の側から
加圧力20kgf/mm2 で加圧した。その結果、水素
透過性金属箔1は補強板2の各孔において図3に示すよ
うに塑性変形して補強板厚さと等しく0.1mm撓んで
いた。水素透過性金属箔1/厚さ0.1mmの補強板2
/厚さ0.3mmの補強板2′をベース板3に重ねて、
接合することなく、外周部をシール溶接して、水素分離
膜モジュールを製作した。
[Embodiment 3] In this embodiment, a hydrogen separation membrane was produced by trial using the same members as in the conventional example, but the reinforcing plate 2 having a thickness of 0.1 mm and the reinforcing plate 2 'having a thickness of 0.3 mm were manufactured. Ag
No coating was formed. The reinforcing plate 2 was superimposed on the water-permeable metal foil 1, and a pressure of 20 kgf / mm 2 was applied from the side of the hydrogen-permeable metal foil using a rubber roll. As a result, the hydrogen-permeable metal foil 1 was plastically deformed in each hole of the reinforcing plate 2 as shown in FIG. Hydrogen-permeable metal foil 1 / reinforcement plate 2 with thickness of 0.1 mm
/ Lay a 0.3 mm thick reinforcing plate 2 ′ on the base plate 3,
Without joining, the outer periphery was sealed and welded to produce a hydrogen separation membrane module.

【0032】実施例3で得られた水素分離膜モジュール
について従来例と同様に評価した。水素透過性能は、耐
久性評価試験の前後でともに31Nm3 /hr・m2
非常に良好であった。耐久性評価試験では、3000回
の繰り返しでもリークは生じず、良好な耐久性を示し
た。本実施例において水素透過性能が従来より若干向上
したのは、水素透過性金属箔がゴムロール加圧により、
若干延びて大きくなり、また薄くなった為と考えられ
る。
The hydrogen separation membrane module obtained in Example 3 was evaluated in the same manner as in the conventional example. The hydrogen permeability was very good at 31 Nm 3 / hr · m 2 both before and after the durability evaluation test. In the durability evaluation test, no leak occurred even after 3,000 repetitions, indicating good durability. In the present embodiment, the hydrogen permeation performance was slightly improved from the conventional one because the hydrogen permeable metal foil was pressed by a rubber roll.
It is thought that it became slightly larger and thinner.

【0033】実施例3では、水素透過性金属箔を補強板
の開孔に食い込ませて固定することにより、耐久性が得
られ、かつ接合による水素透過面積減少が防止できるの
で、水素透過性能の向上につながった。また、金属被覆
形成工程及び接合工程をなくせるので製造コストを低減
できた。なお、実施例3のようにAg等の金属被覆を形
成せずに金属膜の塑性変形のみで固定することで充分上
記効果を得られるが、補強板の全面又は一部に金属被覆
を設けておき、さらに金属膜を補強板開孔に食い込ませ
る構造とすれば非常に強固に固定できることはいうまで
もない。
In the third embodiment, since the hydrogen permeable metal foil is fixed by being cut into the opening of the reinforcing plate, durability can be obtained and a reduction in the hydrogen permeable area due to bonding can be prevented. Led to improvement. Further, since the metal coating forming step and the joining step can be eliminated, the manufacturing cost can be reduced. Note that the above effect can be sufficiently obtained by fixing only the plastic deformation of the metal film without forming the metal coating such as Ag as in Example 3, but the metal coating is provided on the entire surface or a part of the reinforcing plate. Needless to say, if the structure is such that the metal film bites into the opening of the reinforcing plate, it can be fixed very firmly.

【0034】以上の実施例1〜3は平型分離膜モジュー
ルについて説明したが、本発明は図2に示す円筒状の多
孔管をベース部とする管型分離膜モジュールについても
同様に、接合なしに、あるいは金属被覆面積を減少して
接合なしに、さらには接合なしに金属膜を補強板に食い
込ませる構造にすることにより、実施例1〜3の場合と
同様に効果を奏した。
Although the first to third embodiments have described the flat type separation membrane module, the present invention similarly applies to the tube type separation membrane module having a cylindrical porous tube shown in FIG. In the same manner as in Examples 1 to 3, a structure in which the metal film is cut into the reinforcing plate without joining, or without joining, by reducing the metal coating area, or without joining, was obtained.

【0035】[0035]

【発明の効果】以上説明のように、本発明の分離膜モジ
ュールは従来より製造工程を減らすことができて製造コ
ストの低減を実現し、しかも充分な耐久性が保証され、
さらにガス透過性能を向上できるという産業上非常に有
利なものである。
As described above, the separation membrane module of the present invention can reduce the number of manufacturing steps compared to the conventional one, realizing a reduction in manufacturing cost, and ensuring sufficient durability.
This is industrially very advantageous in that gas permeation performance can be further improved.

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

【図1】は本発明の一実施例である平型分離膜モジュー
ルの構造、製法を示す概略説明図である。
FIG. 1 is a schematic explanatory view showing the structure and manufacturing method of a flat type separation membrane module according to one embodiment of the present invention.

【図2】は本発明の他の実施例である管型分離膜モジュ
ールの構造、製法を示す概略説明図である。
FIG. 2 is a schematic explanatory view showing the structure and manufacturing method of a tubular separation membrane module according to another embodiment of the present invention.

【図3】は本発明の更に他の実施例である金属膜を補強
板に食い込ませた構造の分離膜モジュールの構造、作用
を説明する概略説明図である。
FIG. 3 is a schematic explanatory view illustrating the structure and operation of a separation membrane module having a structure in which a metal film is cut into a reinforcing plate according to still another embodiment of the present invention.

【図4】は従来の管型分離膜モジュールの一例の概略説
明図である。
FIG. 4 is a schematic explanatory view of an example of a conventional tubular separation membrane module.

【図5】は従来の平型分離膜モジュールの一例の概略説
明図である。
FIG. 5 is a schematic explanatory view of an example of a conventional flat separation membrane module.

【図6】は金属膜の撓みの状態を説明する概略図であ
る。
FIG. 6 is a schematic diagram illustrating a state of bending of a metal film.

【図7】は本発明において補強板のメッシュ部の構造及
び開孔率を説明するための概略図である。
FIG. 7 is a schematic diagram for explaining a structure and a hole ratio of a mesh portion of a reinforcing plate in the present invention.

【符号の説明】[Explanation of symbols]

1 ガス透過性金属膜、 2及び2′ 補強板、
3 ベース板、3′溝、 4 ベー
ス管、 5 接合体、6 シール溶接
7 分離膜モジュール(本発明品)、7′分離膜
モジュール(従来品)、 8 ノズ
ル、9 ヘッダ、 10 撓み、
11 付け根、12 金属被覆、 13
開孔。
1 gas permeable metal membrane, 2 and 2 ′ reinforcing plate,
3 Base plate, 3 'groove, 4 Base tube, 5 Joint, 6 Seal welding
7 Separation membrane module (product of the present invention), 7 'separation membrane module (conventional product), 8 nozzle, 9 header, 10 deflection,
11 base, 12 metal coating, 13
Aperture.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 特定ガスを選択的に透過する金属膜と、
多数の開孔を有し、前記金属膜を支持する補強板と、ガ
ス抜き出し管に連通できるガス捕捉部を有するベース部
からなる分離膜モジュールにおいて、前記補強板がA
g,Au,Pt,Ni及びCuからなる群れから選ばれ
る1種又は複数種の金属で被覆されてなり、前記金属膜
と該補強板を重ね合わせたものの外周部が前記ベース部
にシール溶接されてなることを特徴とする分離膜モジュ
ール。
A metal film that selectively permeates a specific gas;
In a separation membrane module having a large number of openings, a reinforcing plate for supporting the metal membrane, and a base having a gas trapping portion capable of communicating with a gas extraction pipe, the reinforcing plate may have A
g, Au, Pt, Ni and Cu, and is covered with one or more kinds of metals selected from the group consisting of a group consisting of the metal film and the reinforcing plate. A separation membrane module, comprising:
【請求項2】 上記Ag,Au,Pt,Ni及びCuか
らなる群れから選ばれる1種又は複数種の金属の被覆が
前記補強板の表面の一部のみに形成されてなることを特
徴とする請求項1又は請求項2に記載の分離膜モジュー
ル。
2. The method according to claim 1, wherein a coating of one or more metals selected from the group consisting of Ag, Au, Pt, Ni and Cu is formed on only a part of the surface of the reinforcing plate. The separation membrane module according to claim 1 or 2.
【請求項3】 特定ガスを選択的に透過する金属膜と、
多数の開孔を有し、前記金属膜を支持する補強板と、ガ
ス抜き出し管に連通できるガス捕捉部を有するベース部
からなる分離膜モジュールにおいて、前記金属膜と該補
強板を重ね合わせたものの外周部が前記ベース部にシー
ル溶接され、且つ前記金属膜がその直下の前記補強板の
前記開孔に食い込んだ構造であることを特徴とする分離
膜モジュール。
3. A metal film selectively permeating a specific gas,
A separation membrane module having a large number of openings, a reinforcing plate supporting the metal membrane, and a base having a gas trapping portion that can communicate with a gas extraction pipe, wherein the metal membrane and the reinforcing plate are overlapped. A separation membrane module having a structure in which an outer peripheral portion is seal-welded to the base portion, and the metal film bites into the opening of the reinforcing plate immediately below.
【請求項4】 前記ベース部が溝を有する板又は多孔管
であることを特徴とする請求項1ないし請求項3のいず
れかに記載の分離膜モジュール。
4. The separation membrane module according to claim 1, wherein the base portion is a plate having a groove or a perforated tube.
JP26394197A 1997-09-29 1997-09-29 Separation membrane module Expired - Lifetime JP3993282B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26394197A JP3993282B2 (en) 1997-09-29 1997-09-29 Separation membrane module

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26394197A JP3993282B2 (en) 1997-09-29 1997-09-29 Separation membrane module

Publications (2)

Publication Number Publication Date
JPH1199324A true JPH1199324A (en) 1999-04-13
JP3993282B2 JP3993282B2 (en) 2007-10-17

Family

ID=17396394

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26394197A Expired - Lifetime JP3993282B2 (en) 1997-09-29 1997-09-29 Separation membrane module

Country Status (1)

Country Link
JP (1) JP3993282B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008036499A (en) * 2006-08-03 2008-02-21 Noritake Co Ltd Support for oxygen separation membrane and oxygen separation membrane
JP2009507755A (en) * 2005-04-18 2009-02-26 インテリジェント エナジー インコーポレイテッド Hydrogen generator and method of using the same
JP2013126685A (en) * 2011-12-16 2013-06-27 Industrial Technology Research Inst Method of fabricating porous medium and inorganic selective membrane

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009507755A (en) * 2005-04-18 2009-02-26 インテリジェント エナジー インコーポレイテッド Hydrogen generator and method of using the same
JP4762314B2 (en) * 2005-04-18 2011-08-31 インテリジェント エナジー インコーポレイテッド Hydrogen generator and method of using the same
JP2008036499A (en) * 2006-08-03 2008-02-21 Noritake Co Ltd Support for oxygen separation membrane and oxygen separation membrane
US7938940B2 (en) 2006-08-03 2011-05-10 Noritake Co., Limited Support for oxygen separation membrane element and the element using the same
JP2013126685A (en) * 2011-12-16 2013-06-27 Industrial Technology Research Inst Method of fabricating porous medium and inorganic selective membrane

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