JPS61278328A - Gas permeable membrane module - Google Patents

Gas permeable membrane module

Info

Publication number
JPS61278328A
JPS61278328A JP12094685A JP12094685A JPS61278328A JP S61278328 A JPS61278328 A JP S61278328A JP 12094685 A JP12094685 A JP 12094685A JP 12094685 A JP12094685 A JP 12094685A JP S61278328 A JPS61278328 A JP S61278328A
Authority
JP
Japan
Prior art keywords
permeable membrane
gas permeable
gas
permeable
breathable
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.)
Pending
Application number
JP12094685A
Other languages
Japanese (ja)
Inventor
Shigeki Hatanaka
茂樹 畠中
Takaki Kobayashi
貴樹 小林
Takanori Sugimoto
高則 杉本
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP12094685A priority Critical patent/JPS61278328A/en
Publication of JPS61278328A publication Critical patent/JPS61278328A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)

Abstract

PURPOSE:To prevent a gas permeable membrane from receiving the tension without expanding in the high temp. and the high pressure in such a state that the decompression is not affected by sticking a stiffened plate, a permeable substance and a permeable sheet in the whole surfaces to make these to one body and making it so as to hold the permeability. CONSTITUTION:When performing the decompression and the suction with a vacuum pump through a fluid discharge port 7 from the outside of a gas permeable membrane 1, the gas is selectively separated through the permeable membrane 1. A permeable sheet 4 is mounted on a permeable substance 3 and stuck in the whole surfaces and the permeable substance 3 is stuck on a stiffened plate in the whole surfaces. These have the permeability after the adhesion in the whole surfaces. The gas permeable membrane 1 and the stiffened plate 2 are sealed and held so that the gas is not introduced through the part other than the gas permeable membrane 1. The permeable sheet 4, the permeable substance 3 and the fluid discharge port 7 are made to a communicated state. The thickness of a spacer 8 of the module can be made thin because the membrane 1 is not expanded.

Description

【発明の詳細な説明】 本発明は、主成分が例えば酸素と窒素とからなる様な混
合気体から一方の成分を富化したガス、例えば酸素富化
ガスを取り出す為の気体透過膜を用いた気体透過膜モジ
ュールに関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention uses a gas permeable membrane for extracting a gas enriched in one component, such as an oxygen-enriched gas, from a mixed gas whose main components are, for example, oxygen and nitrogen. This invention relates to a gas permeable membrane module.

従来の技術 近年の酸素富化ガスは、燃焼用、医療用などに広く利用
されているが、これらの気体を得る方法としては、深冷
分離による酸素分離が一般的であり、他の代表的方法と
しては、固体表面の気体の吸脱着を利用した方法(ゼオ
ライト等)がある一方、簡単に富化ガスを作り出す目的
で、高分子の膜を利用した気体透過膜の開発が盛んに行
なわれている。
Conventional technology In recent years, oxygen-enriched gases have been widely used for combustion, medical purposes, etc., but oxygen separation by cryogenic separation is the most common method for obtaining these gases. While there are methods that utilize adsorption and desorption of gas on solid surfaces (zeolite, etc.), gas permeable membranes using polymeric membranes are being actively developed in order to easily create enriched gas. ing.

選択透過膜を利用した分離の従来の技術としては、例え
ば特開昭57−194006号公報に示される様に選択
性気体透過膜モジュールがある。
As a conventional separation technique using a selectively permeable membrane, there is a selective gas permeable membrane module as disclosed in, for example, Japanese Patent Application Laid-Open No. 194006/1983.

以下図面を参照しながら、上述したような気体分離手段
の一つである、従来の気体透過膜モジュールについて説
明を行う。
A conventional gas permeable membrane module, which is one of the gas separation means described above, will be explained below with reference to the drawings.

第6図は、従来の気体透過膜モジュールの分解斜視図を
示すものである。第6図において、11は混合気体を選
択的に分離する気体透過膜、12は気体透過膜11との
間に空間部が形成されるように、密封保持する補強板、
13は前記空間部内に充填される通気性を有する通気性
物質、14は通気性物質13と気体透過膜11の間に介
在する通気性シート、15は気体透過膜11と補強板1
2を気密に保つ両面粘着テープ、16は前記空間部内の
流体を吐出する流体吐出口である。
FIG. 6 shows an exploded perspective view of a conventional gas permeable membrane module. In FIG. 6, 11 is a gas permeable membrane that selectively separates a mixed gas; 12 is a reinforcing plate that seals and holds the gas permeable membrane 11 so that a space is formed therebetween;
Reference numeral 13 indicates an air-permeable material having air permeability that is filled in the space, 14 indicates an air-permeable sheet interposed between the air-permeable material 13 and the gas-permeable membrane 11, and 15 indicates the gas-permeable membrane 11 and the reinforcing plate 1.
A double-sided adhesive tape 2 is kept airtight, and 16 is a fluid discharge port for discharging the fluid in the space.

第6図は、従来の気体透過膜の縦断面図を示すものであ
る。
FIG. 6 shows a longitudinal cross-sectional view of a conventional gas permeable membrane.

第7図は、従来の気体透過膜の横断面図を示すものであ
る。17は気体透過膜モジュールを積層する場合のスペ
ーサである。
FIG. 7 shows a cross-sectional view of a conventional gas permeable membrane. 17 is a spacer for stacking gas permeable membrane modules.

以上の様に構成された気体透過膜モジュールについて、
以下その動作について説明する。
Regarding the gas permeable membrane module configured as above,
The operation will be explained below.

第6図、第6図において気体透過膜の外部より流体吐出
口16よυ真空ポンプで減圧吸引を行なうと、気体透過
膜モジュールの外部の気体は、気体透過膜11を通って
選択的に分離される。また選択的に分離された気体(酸
素富化空気)は、通気性シート14を通過して通気性物
質13より形成される空間部に侵入し、流体吐出口16
より取り出される。通気性シート14は通気性物質13
0表面が粗面である為、気体透過膜1,1が破損するの
を保護するもので、気体透過膜11が真空ポンプで減圧
された場合に、通気性物質13にくい込まない様に通気
性物質13の上に載せである。
6, when vacuum suction is performed from the outside of the gas permeable membrane through the fluid outlet 16 using the vacuum pump, the gas outside the gas permeable membrane module passes through the gas permeable membrane 11 and is selectively separated. be done. Further, the selectively separated gas (oxygen-enriched air) passes through the breathable sheet 14 and enters the space formed by the breathable material 13, and enters the fluid discharge port 16.
taken out from The breathable sheet 14 is made of a breathable substance 13
Since the surface of 0 is rough, it protects the gas permeable membranes 1, 1 from being damaged, and the gas permeable membrane 11 is made breathable so that it does not get trapped in the gas permeable substance 13 when the pressure is reduced by a vacuum pump. It is placed on top of substance 13.

又補強板12は気体透過膜11との間に空間部が形成さ
れ、気体透過膜11が真空ポンプで減圧された場合に気
体透過膜11を保持しかつ補強するものである。そして
気体透過膜11と補強板12は、前記空間部に通気性物
質13と通気性シート14を充填して両面粘着テープ1
6により密封保持されている。通気性シート14と通気
性物質13と流体吐出口16は連通状態にある。
Further, a space is formed between the reinforcing plate 12 and the gas permeable membrane 11, which holds and reinforces the gas permeable membrane 11 when the gas permeable membrane 11 is depressurized by a vacuum pump. Then, the gas permeable membrane 11 and the reinforcing plate 12 are formed by filling the space with a breathable substance 13 and a breathable sheet 14 to form the double-sided adhesive tape 1.
6 and is kept hermetically sealed. The breathable sheet 14, the breathable material 13, and the fluid outlet 16 are in communication.

発明が解決しようとする問題点 しかしながら、第6図と第7図の様に補強板12の上に
通気性物質13を載せ通気性物質13の上に通気性シー
ト14を載せ、コーナ部を両面粘着テープ15で接着す
る構造においては、高温高湿状態で、真空ポンプより減
圧を受けていない場合は、通気性物質13と通気性シー
ト14の中央部がふくらみ気体透過膜11に張力がかか
り気体透過膜11が破損する。その結果気体透過膜モジ
ュールの寿命が短かくなる。
Problems to be Solved by the Invention However, as shown in FIGS. 6 and 7, a breathable material 13 is placed on the reinforcing plate 12, a breathable sheet 14 is placed on the breathable material 13, and the corner portions are covered on both sides. In a structure in which adhesive tape 15 is used to adhere the adhesive tape 15, when the pressure is not reduced by a vacuum pump under high temperature and high humidity conditions, the central portions of the breathable material 13 and the breathable sheet 14 swell and tension is applied to the gas permeable membrane 11, causing the gas to evaporate. The permeable membrane 11 is damaged. As a result, the life of the gas permeable membrane module is shortened.

又通気性物質13と通気性シート14の中央部がふくら
むと、気体透過膜11が厚み方向に積層された相対する
他の気体透過膜11と接触し、気体透過膜11が破損す
る為、スペーサ17の厚さを気体透過膜が接触しない様
に充分数る必要があり、小型化出来ないという問題点を
有していた。
Furthermore, if the central part of the breathable substance 13 and the breathable sheet 14 swells, the gas permeable membrane 11 will come into contact with the other gas permeable membrane 11 stacked in the thickness direction and the gas permeable membrane 11 will be damaged. 17 must be sufficiently thick so that the gas permeable membranes do not come into contact with each other, and this poses a problem in that miniaturization is not possible.

本発明は、上記問題点に鑑み、気体透過膜の寿命を伸し
、しかも小型のχ体透過膜モジュールを提供するもので
ある。
In view of the above problems, the present invention provides a x-body permeable membrane module that extends the life of a gas permeable membrane and is small in size.

問題点を解決すZ?、tbの手段 この目的を達成する為に本発明の気体透過膜モジュール
は、補強板と通気性物質と通気性シートを熱溶着又は接
着剤により全面接着して7体化し、しかも通気性を有す
る様にした物である。
Z to solve the problem? , tb In order to achieve this object, the gas permeable membrane module of the present invention is made up of seven parts by fully bonding a reinforcing plate, a breathable substance, and a breathable sheet with heat welding or adhesive, and has breathability. It is made in a similar way.

作用 この構成によって、通気性物質と通気性シートが真空ポ
ンプよシ減圧を受けていない状態で、高温高湿時にふく
らまない為、気体透過膜同志が接触せず、しかも気体透
過膜に対し二張力もかからない。
Function: With this configuration, the gas permeable membranes do not come into contact with each other, and the gas permeable membranes do not inflate when the gas permeable membrane is exposed to high temperature and high humidity without being subjected to reduced pressure by a vacuum pump. There is no tension.

その結果、気体透過膜モジュールの寿命を延すことがで
きる。又気体透過膜がふくらまない為、スペーサの厚み
を薄くでき、小型になる。
As a result, the life of the gas permeable membrane module can be extended. Also, since the gas permeable membrane does not swell, the spacer can be made thinner and more compact.

実施例 以下本発明の一実施例について、図面を参照りながら説
明する。
EXAMPLE An example of the present invention will be described below with reference to the drawings.

第1図は、本発明の一実施例における気体透過膜モジュ
ールの分解斜視図、第2図は気体透過膜モジュールの縦
断面図、第3図は気体透過膜モジュールの横断面図、第
4図は従来の気体透過膜モジュールと本発明の一実施例
における気体透過膜モジュールの酸素濃度劣化による寿
命の比較図である。
FIG. 1 is an exploded perspective view of a gas permeable membrane module according to an embodiment of the present invention, FIG. 2 is a longitudinal cross-sectional view of the gas permeable membrane module, FIG. 3 is a cross-sectional view of the gas permeable membrane module, and FIG. 4 is a cross-sectional view of the gas permeable membrane module. 1 is a comparison diagram of the life span due to oxygen concentration deterioration of a conventional gas permeable membrane module and a gas permeable membrane module according to an embodiment of the present invention.

第1図において、1は混合気体を選択的に分離する気体
透過膜、2は気体透過膜1との間に空間部が形成される
ように密封保持する補強板、3は前記空間部内に充填さ
れる通気性を有する通気性物質、4は通気性物質3と気
体透過膜10間に介在する通気性シート、6は補強板2
と通気性物質3と通気性シート4を全面接着する接着剤
、6は気体透過膜1と補強板2を気密に保つ両面粘着テ
ープ、7は前記空間部内の流体を吐出する流体吐出口で
ある。
In FIG. 1, 1 is a gas permeable membrane that selectively separates a mixed gas, 2 is a reinforcing plate that seals and holds a space between the gas permeable membrane 1, and 3 is filled in the space. 4 is a breathable sheet interposed between the breathable substance 3 and the gas permeable membrane 10; 6 is a reinforcing plate 2;
, an adhesive for bonding the entire surface of the breathable substance 3 and the breathable sheet 4; 6 is a double-sided adhesive tape that keeps the gas permeable membrane 1 and the reinforcing plate 2 airtight; and 7 is a fluid outlet for discharging the fluid in the space. .

第3図において、8は気体透過膜モジュールを積層する
場合のスペーサである。
In FIG. 3, 8 is a spacer used when stacking gas permeable membrane modules.

以上の様に構成された気体透過膜モジュールについて、
以下その動作を説明する。
Regarding the gas permeable membrane module configured as above,
The operation will be explained below.

第1図、第2図において気体透過膜1の外部より流体吐
呂ロアより真空ポンプで減圧吸引を行なうと、気体透過
膜モジュールの外部の気体は、気体透過膜1を通って選
択的に分離される。また選択的に分離された気体(酸素
富化空気)は、通気性シート4を通過して通気性物質3
より形成される空間部に侵入し、流体吐出ロアより取り
出される。通気性シート4は通気性物質3の表面が粗面
である為、気体透過膜1が真空ポンプで減圧された場合
に、通気性物質3にくい込まない様に・通気性物質3の
上に載せ全面接着し保護しである。又、補強板2と通気
性物質3と通気性シτト4は接着剤5により全面接着さ
れ、しかも通気性を有する。
In FIGS. 1 and 2, when vacuum suction is performed from the outside of the gas permeable membrane 1 from the fluid nozzle lower using a vacuum pump, the gas outside the gas permeable membrane module passes through the gas permeable membrane 1 and is selectively separated. be done. In addition, the selectively separated gas (oxygen-enriched air) passes through the breathable sheet 4 and passes through the breathable substance 3.
The fluid enters the space formed by the fluid discharge lower and is taken out from the fluid discharge lower. Since the surface of the breathable substance 3 is rough, the breathable sheet 4 is placed on top of the breathable substance 3 to prevent it from getting stuck in the breathable substance 3 when the gas permeable membrane 1 is depressurized by a vacuum pump. Fully adhesive and protected. Further, the reinforcing plate 2, the breathable material 3, and the breathable sheet 4 are fully bonded with an adhesive 5, and are breathable.

補強板2は、気体透過膜1との間に空間部が形成され、
気体透過膜1が真空ポンプで減圧された場合に気体透過
膜1を保持しかつ補強するものである。そして気体透過
膜1と補強板2は、前記空間部に通気性物質3と通気性
シート4を充填し補強板2と通気性物質3と通気性シー
ト4は全面接着し、しかも通気性を有する様にしである
。気体透過膜1と補強板2は気体透過膜1以外から気体
が入らない様に両面粘着テープにより密封保持されてい
る。通気性シート4と通気性物質3と流体吐出ロアは連
通状態にある。
A space is formed between the reinforcing plate 2 and the gas permeable membrane 1,
This is to hold and reinforce the gas permeable membrane 1 when the gas permeable membrane 1 is depressurized by a vacuum pump. Then, the gas permeable membrane 1 and the reinforcing plate 2 fill the space with a breathable substance 3 and a breathable sheet 4, and the reinforcing plate 2, the breathable substance 3, and the breathable sheet 4 are bonded to each other on the entire surface, and have air permeability. It's like that. The gas permeable membrane 1 and the reinforcing plate 2 are sealed and held with double-sided adhesive tape to prevent gas from entering from other than the gas permeable membrane 1. The breathable sheet 4, the breathable substance 3, and the fluid discharge lower are in communication.

第3図において、スペース8は気体透過膜モジュールを
厚み方向に積層した場合に気体透過膜同志が接触しない
様にする働きがある。
In FIG. 3, the space 8 serves to prevent the gas permeable membranes from coming into contact with each other when the gas permeable membrane modules are stacked in the thickness direction.

第4図の様に、第1図〜第3図の様に補強板2と通気性
物質3と通気性レート4を全面接着した場合、本発明者
の実験によると従来の気体透過膜モジュールより、温度
60℃、湿度96%RHの恒温恒湿室内での放置試験で
寿命が約2倍になる。
As shown in Fig. 4, when the reinforcing plate 2, the air permeable material 3, and the air permeable rate 4 are bonded on the entire surface as shown in Figs. The lifespan is approximately doubled in a storage test in a constant temperature and humidity room at a temperature of 60°C and a humidity of 96% RH.

念だし気体透過膜モジュールの寿命は、酸素濃度28%
以下になった場合とする。
As a reminder, the life of the gas permeable membrane module is at an oxygen concentration of 28%.
In the following cases.

以上の様に本実施例によれば、補強板2と通気性物質3
と通気性シート4を全面接着すれば、通気性物質3と通
気性シート4がふくらむ事により、気体透過膜1がふく
らみ気体透過膜同志が接触したり、張力がかかる事がな
くなり、気体透過膜モジュールの寿命が延びる。又気体
透過膜1がふくらまない為に、気体透過膜モジュールの
スペーサ8の厚さを薄くでき小型になる。又初期性能も
従来例と同等の性能が得られる。なお、本実施例では補
強板2と通気性物質3と通気性ンート4を接着剤で接着
したが、補強板2と通気性物質3と通気性シート4の接
着は熱でもよい。
As described above, according to this embodiment, the reinforcing plate 2 and the breathable material 3
If the gas permeable sheet 4 and the gas permeable sheet 4 are completely bonded together, the gas permeable membrane 1 will swell as the gas permeable substance 3 and the gas permeable sheet 4 swell, and the gas permeable membranes will no longer come into contact with each other or be subject to tension. Extends module life. Furthermore, since the gas permeable membrane 1 does not swell, the thickness of the spacer 8 of the gas permeable membrane module can be reduced, resulting in a smaller size. In addition, the initial performance is equivalent to that of the conventional example. In this embodiment, the reinforcing plate 2, the breathable substance 3, and the breathable sheet 4 are bonded together using an adhesive, but the reinforcing plate 2, the breathable substance 3, and the breathable sheet 4 may be bonded together by heat.

発明の効果 以上の様に本発明は、補強板と通気性物質と通気性シー
トを一体化する事により、気体透過膜同志が接触せず気
体透過膜モジュールの寿命が延び、スペーサの厚さを薄
くでき、小型にできると共に従来と同等の初期性能(酸
素富化流量、酸素濃度)が得られる。
Effects of the Invention As described above, the present invention, by integrating the reinforcing plate, the breathable substance, and the breathable sheet, prevents the gas permeable membranes from coming into contact with each other, extending the life of the gas permeable membrane module, and reducing the thickness of the spacer. It can be made thinner and smaller, and the initial performance (oxygen enrichment flow rate, oxygen concentration) equivalent to that of conventional products can be obtained.

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

第1図は本発明の一実施例による気体透過膜モジュール
の分解斜視図、第2図人は同気体透過膜モジュールの縦
断面図、第2図Bは第2図人のa部の拡大図、第3歯は
同気体透過膜モジュールの、横断面図、第4図は本発明
と従来の気体透過膜モジュールの寿命比較図、第5図は
従来の気体透過膜モジュールの分解斜視図、第6図人は
従来の気体透過膜モジュールの縦断面図、第6図Bは第
6図人のa部の拡大図、第7図は従来の気体透過膜モジ
ュールの横断面図である。 1・・・・・・気体透過膜、2・・・・・・補強板、3
・・・・・・通気性物質、4・・・・・・通気性シート
、6・・・・・・接着剤、6・・・・・・両面粘着テー
プ、7・・・・・・流体吐出口。
FIG. 1 is an exploded perspective view of a gas permeable membrane module according to an embodiment of the present invention, FIG. 2 is a vertical sectional view of the same gas permeable membrane module, and FIG. 2B is an enlarged view of part a of FIG. 2. , the third tooth is a cross-sectional view of the same gas permeable membrane module, FIG. 4 is a life comparison diagram of the present invention and a conventional gas permeable membrane module, FIG. 5 is an exploded perspective view of the conventional gas permeable membrane module, and FIG. Figure 6 is a vertical sectional view of a conventional gas permeable membrane module, Figure 6B is an enlarged view of part a of Figure 6, and Figure 7 is a cross sectional view of a conventional gas permeable membrane module. 1... Gas permeable membrane, 2... Reinforcement plate, 3
...Breathable substance, 4 ...Breathable sheet, 6 ... Adhesive, 6 ... Double-sided adhesive tape, 7 ... Fluid Outlet.

Claims (1)

【特許請求の範囲】[Claims] 大気あるいは混合気体を選択的に分離する気体透過膜と
、この気体透過膜との間に空間部が形成されるように密
封保持する補強板と、前記空間部内に充填される通気性
を有する通気性物質と、この通気性物質と前記気体透過
膜の間に介在する通気性シートと、前記空間部内の流体
を吐出する流体吐出口とを有し、前記補強板と前記通気
性物質と前記通気性シートを熱溶着又は接着剤で一体化
することを特徴とする気体透過膜モジュール。
a gas-permeable membrane that selectively separates the atmosphere or a gas mixture; a reinforcing plate that seals and holds a space between the gas-permeable membrane; and a vent that is air-permeable and filled in the space. a gas-permeable material, a gas-permeable sheet interposed between the gas-permeable material and the gas-permeable membrane, and a fluid discharge port for discharging fluid in the space; 1. A gas permeable membrane module characterized by integrating adhesive sheets by heat welding or adhesive.
JP12094685A 1985-06-04 1985-06-04 Gas permeable membrane module Pending JPS61278328A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12094685A JPS61278328A (en) 1985-06-04 1985-06-04 Gas permeable membrane module

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12094685A JPS61278328A (en) 1985-06-04 1985-06-04 Gas permeable membrane module

Publications (1)

Publication Number Publication Date
JPS61278328A true JPS61278328A (en) 1986-12-09

Family

ID=14798882

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12094685A Pending JPS61278328A (en) 1985-06-04 1985-06-04 Gas permeable membrane module

Country Status (1)

Country Link
JP (1) JPS61278328A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6233523A (en) * 1985-08-05 1987-02-13 Teijin Ltd Fluid separating element and fluid separator using said element
US5681373A (en) * 1995-03-13 1997-10-28 Air Products And Chemicals, Inc. Planar solid-state membrane module
US5830261A (en) * 1996-02-26 1998-11-03 Japan Gore-Tex, Inc. Assembly for deaeration of liquids
US5888275A (en) * 1996-02-26 1999-03-30 Japan Gore-Tex, Inc. Assembly for deaeration of liquids
US6171374B1 (en) * 1998-05-29 2001-01-09 Ballard Power Systems Inc. Plate and frame fluid exchanging assembly with unitary plates and seals
US6527832B2 (en) * 2000-06-27 2003-03-04 Nisshin Steel Co., Ltd. Device for recovery of hydrogen

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6233523A (en) * 1985-08-05 1987-02-13 Teijin Ltd Fluid separating element and fluid separator using said element
JPH047252B2 (en) * 1985-08-05 1992-02-10 Teijin Ltd
US5681373A (en) * 1995-03-13 1997-10-28 Air Products And Chemicals, Inc. Planar solid-state membrane module
US5830261A (en) * 1996-02-26 1998-11-03 Japan Gore-Tex, Inc. Assembly for deaeration of liquids
US5888275A (en) * 1996-02-26 1999-03-30 Japan Gore-Tex, Inc. Assembly for deaeration of liquids
US6171374B1 (en) * 1998-05-29 2001-01-09 Ballard Power Systems Inc. Plate and frame fluid exchanging assembly with unitary plates and seals
US6527832B2 (en) * 2000-06-27 2003-03-04 Nisshin Steel Co., Ltd. Device for recovery of hydrogen

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