JPH06246125A - Gas separation membrane module - Google Patents

Gas separation membrane module

Info

Publication number
JPH06246125A
JPH06246125A JP3158693A JP3158693A JPH06246125A JP H06246125 A JPH06246125 A JP H06246125A JP 3158693 A JP3158693 A JP 3158693A JP 3158693 A JP3158693 A JP 3158693A JP H06246125 A JPH06246125 A JP H06246125A
Authority
JP
Japan
Prior art keywords
gas
gas separation
exhaust pipe
raw material
air supply
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
JP3158693A
Other languages
Japanese (ja)
Inventor
Masanori Kimura
雅典 木村
Tasuke Sawada
太助 沢田
Shigeki Hatanaka
茂樹 畠中
Takaki Kobayashi
貴樹 小林
Masaya Sugafuji
雅哉 菅藤
Katsuhide Kaneharu
克秀 金治
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 JP3158693A priority Critical patent/JPH06246125A/en
Publication of JPH06246125A publication Critical patent/JPH06246125A/en
Pending legal-status Critical Current

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To provide a spiral gas separation membrane module utilizing a flat gas separation membrane and enhanced in concentration efficiency. CONSTITUTION:A raw gas passage material and a flat gas separation composite membrane obtained by folding back flat gas separation composite membranes 2 with a permeated gas passage material in between are put on each other, and the assembly is wound on a gas supply and discharge pipe 4 to constitute a gas separation membrane module 2. The final end of the winding is positioned at the folded part of the composite membrane, the initial end of the gas separation membrane module 2 is stuck to the pipe 4 so that the raw gas passage 1 communicates with the supply pipe 5 of the pipe 4 and the permeated gas passage 3 with the discharge pipe 6 of the pipe 4, and both ends in the winding direction are sealed so that the raw gas passage and the permeated gas passage are airtightly separated.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は平膜の気体分離複合膜を
巻回してなるスパイラル型気体分離膜モジュールに関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a spiral type gas separation membrane module formed by winding a flat gas separation composite membrane.

【0002】[0002]

【従来の技術】一般に平膜を巻回してなるスパイラル型
の分離膜モジュールは、透過流体流路を形成する透過流
体流路材を平膜分離膜で挟んで、穴を有する中空管の穴
に透過流体流路が連通するように中空管に平膜分離膜を
接着し、原料流体流路を形成する原料流体流路材と共に
中空管の周りに巻回して構成される。また平膜分離膜
(透過流体流路材を挟んだ)の巻回方向(中空管に対し
て垂直方向)の両側端面は封止してあり、原料流体流路
は解放されている。
2. Description of the Related Art Generally, a spiral type separation membrane module formed by winding a flat membrane is a hole of a hollow tube having a hole in which a permeation fluid channel material forming a permeation fluid channel is sandwiched between flat membrane separation membranes. A flat membrane separation membrane is adhered to the hollow tube so that the permeate fluid flow path communicates with the hollow tube, and is wound around the hollow tube together with the raw material fluid flow path material forming the raw material fluid flow path. Further, both end faces of the flat membrane separation membrane (with the permeating fluid channel material sandwiched) in the winding direction (the direction perpendicular to the hollow tube) are sealed, and the raw material fluid channel is open.

【0003】従来例の分離膜モジュールの流体の分離、
濃縮について原料流体を空気とし窒素を分離、濃縮する
場合について説明する。図6は従来のスパイラル型気体
分離膜モジュールの例である。原料気体供給流路材22
で構成された原料気体供給流路に原料空気を矢印(実
線)の方向に供給すると、原料空気は酸素を優先的に透
過する気体分離複合膜21の表面上を流れていく。その
時酸素は優先的に気体分離複合膜21を透過し透過気体
流路材23で構成された透過気体流路を中空管24の方
向(矢印:破線)に流れていく。そのため気体分離膜上
を通過し、膜モジュールから出て来た空気は窒素が濃縮
されることとなる。
Separation of fluid in a conventional separation membrane module,
Concentration A case of separating and concentrating nitrogen by using a raw material fluid as air will be described. FIG. 6 shows an example of a conventional spiral type gas separation membrane module. Raw material gas supply flow path member 22
When the raw material air is supplied in the direction of the arrow (solid line) to the raw material gas supply passage constituted by, the raw material air flows on the surface of the gas separation composite membrane 21 that preferentially permeates oxygen. At that time, oxygen preferentially permeates the gas separation composite membrane 21 and flows through the permeable gas channel constituted by the permeable gas channel member 23 in the direction of the hollow tube 24 (arrow: broken line). Therefore, the air that has passed through the gas separation membrane and exited from the membrane module is concentrated in nitrogen.

【0004】[0004]

【発明が解決しようとする課題】気体分離膜による気体
の分離、濃縮は原料気体が気体分離複合膜表面に接しな
がら流れていく過程で、気体分離複合膜を透過し易い気
体が次々と透過していき気体分離複合膜表面の気体が濃
縮されることとなり、気体分離複合膜が長くなれば長く
なるほど気体分離膜表面の気体は濃縮されることとな
る。
Gas separation and concentration by a gas separation membrane is a process in which a raw material gas flows while being in contact with the surface of a gas separation composite membrane. The gas on the surface of the gas separation composite membrane is concentrated, and the longer the gas separation composite membrane is, the more the gas on the surface of the gas separation membrane is concentrated.

【0005】しかしながら上記の従来の構成では、原料
空気が気体分離複合膜の表面を流れる距離が短いため、
窒素濃度の高い空気を得ることが出来ないという問題点
を有していた。
However, in the above-mentioned conventional configuration, since the raw material air has a short distance to flow on the surface of the gas separation composite membrane,
There was a problem that air with a high nitrogen concentration could not be obtained.

【0006】本発明は上記従来の問題点を解決するもの
で、濃縮効率の良い気体分離膜モジュールを提供するこ
とを目的とする。
The present invention solves the above-mentioned conventional problems, and an object of the present invention is to provide a gas separation membrane module having a high concentration efficiency.

【0007】[0007]

【課題を解決するための手段】この目的を達成するため
に本発明の気体分離膜モジュールは、原料気体流路材
と、透過気体流路材を挟んで折り返した平膜状の気体分
離複合膜とを重ねて一単位とし、原料空気を供給する給
気管と透過気体を排気する排気管とが一体となった給排
気管の回りにスパイラル状に巻回した気体分離膜モジュ
ールで、巻終わりの一端が気体分離複合膜の折り返し部
となるようにし、巻始めの一端は原料気体流路と給排気
管の給気管が連通し、かつ、透過気体流路と給排気管の
排気管が連通するように給排気管に気体分離複合膜を接
着し、巻回方向の両側端部は原料気体流路と透過気体流
路を気密に隔てるように封止した構造、あるいは、原料
気体流路材と、平膜状の第1の気体分離複合膜と、透過
気体流路材と、平膜状の第2の気体分離複合膜とを、上
記の順に重ねて一単位とし、原料空気を供給する給気管
と透過気体を排気する排気管とが一体となった給排気管
の回りにスパイラル状に巻回した気体分離膜モジュール
で、巻始めの一端は原料気体流路と給排気管の給気管が
連通し、かつ、透過気体流路と給排気管の排気管が連通
するように給排気管に第1及び第2の気体分離複合膜を
接着し、巻終わりの一端は透過気体流路を閉じるように
第1及び第2の気体分離複合膜を接着し、巻回方向の両
側端部は原料気体流路と透過気体流路を気密に隔てるよ
うに封止した構造をしている。
In order to achieve this object, a gas separation membrane module of the present invention is a gas separation composite membrane in the form of a flat film folded with a raw material gas flow path member and a permeation gas flow path material sandwiched therebetween. The gas separation membrane module spirally wound around the air supply / exhaust pipe in which the air supply pipe for supplying the raw material air and the exhaust pipe for exhausting the permeated gas are integrated into one unit. One end serves as a folded portion of the gas separation composite membrane, and one end of the winding start communicates with the raw material gas passage and the supply pipe of the supply / exhaust pipe, and the permeate gas passage communicates with the exhaust pipe of the supply / exhaust pipe. As described above, a gas separation composite membrane is adhered to the air supply / exhaust pipe, and both ends in the winding direction are sealed so as to hermetically separate the raw gas flow passage and the permeation gas flow passage, or a raw gas flow passage material and A flat membrane-like first gas separation composite membrane, a permeating gas channel material, and a flat membrane The second gas separation composite membrane of No. 1 is stacked in the above order to form one unit, and is spirally formed around the air supply / exhaust pipe in which the air supply pipe for supplying the raw material air and the exhaust pipe for exhausting the permeated gas are integrated. In the wound gas separation membrane module, the supply / exhaust pipe is connected at one end of the winding so that the raw material gas flow passage and the supply / exhaust pipe are connected, and the permeated gas flow passage and the supply / exhaust pipe are connected. The first and second gas separation composite membranes are bonded to each other, and the first and second gas separation composite membranes are bonded to one end of the winding end so as to close the permeation gas flow path, and both end portions in the winding direction are It has a structure in which the raw material gas passage and the permeation gas passage are hermetically sealed.

【0008】[0008]

【作用】この構成によって、給気管から供給された原料
気体は原料気体流路を巻回された方向に流れていくた
め、気体分離複合膜の長さを長くすることにより、原料
気体流路を長くすることが出来る。原料気体は気体分離
複合膜表面に接しながら流れていくため、気体分離複合
膜を透過し易い気体は次々と透過していくこととなり、
気体分離複合膜が長くなれば長くなるほど気体分離膜表
面の気体は濃縮されることとなる。
With this configuration, since the raw material gas supplied from the air supply pipe flows in the direction in which the raw material gas flow passage is wound, the length of the gas separation composite membrane is increased so that the raw material gas flow passage is It can be lengthened. Since the raw material gas flows while being in contact with the surface of the gas separation composite membrane, the gas that easily permeates the gas separation composite membrane will pass one after another,
The longer the gas separation composite membrane, the more concentrated the gas on the surface of the gas separation membrane.

【0009】[0009]

【実施例】【Example】

(実施例1)以下本発明の一実施例について、図面を参
照しながら説明する。図1は本実施例の気体分離膜モジ
ュールの展開横断面図、図2は本実施例の使用例であ
る。
(Embodiment 1) An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a developed cross-sectional view of the gas separation membrane module of this embodiment, and FIG. 2 is a usage example of this embodiment.

【0010】図1において、1は原料気体流路材で、1
5メッシュのポリエチレン成形ネットである。2は気体
分離複合膜で、多孔質支持体上にポリ4メチルペンテン
1の気体分離膜を積層し更にその上にポリジメチルシロ
キサンを積層した非対称構造で、分離膜側が原料気体流
路材1と相対し、15メッシュのポリエチレン成形ネッ
トで構成された透過気体流路材3を挟んで折り返すよう
に配されており、巻始めの膜端は給排気管4に気密に接
着されている。4は給排気管で給気管5と排気管6が、
長さ方向に平行に配されている。
In FIG. 1, reference numeral 1 is a raw material gas channel material,
It is a 5 mesh polyethylene molding net. Reference numeral 2 is a gas separation composite membrane, which has an asymmetric structure in which a gas separation membrane of poly (4-methylpentene 1) is laminated on a porous support, and polydimethylsiloxane is further laminated thereon, and the separation membrane side is the raw material gas flow path material 1 They are arranged so as to face each other and fold back with the permeable gas flow path member 3 made of a 15-mesh polyethylene molding net sandwiched therebetween, and the film end at the beginning of winding is air-tightly bonded to the air supply / exhaust pipe 4. 4 is an air supply / exhaust pipe, and the air supply pipe 5 and the exhaust pipe 6 are
They are arranged parallel to the length direction.

【0011】以上の原料気体流路材1から透過気体流路
材3の材料を給排気管4の回りにスパイラル状に巻回し
た後、巻回方向の両側端部他を図2のように封止材7に
よって原料気体流路と、透過気体流路を気密に隔てるよ
うに接着封止する。以上のように構成された気体分離膜
モジュールを圧力容器8内に収納し、給気管5から59
2Pa(5kgf/cm2G)に加圧された空気4.2×
10-43/s(25l/min)を供給し、流量調節
弁9から得られる窒素濃縮空気流量を8.3×10-5
3/s(5l/min)に調節したところ窒素濃度は9
7.7%であった。
After winding the material of the permeated gas flow channel material 3 from the raw material gas flow channel material 1 in a spiral shape around the supply / exhaust pipe 4 as shown in FIG. The raw material gas flow path and the permeation gas flow path are bonded and sealed by the sealing material 7 so as to be airtightly separated. The gas separation membrane module configured as described above is housed in the pressure vessel 8, and the air supply pipes 5 to 59 are installed.
Air pressurized to 2 Pa (5 kgf / cm 2 G) 4.2 ×
10 −4 m 3 / s (25 l / min) is supplied, and the nitrogen enriched air flow rate obtained from the flow rate control valve 9 is 8.3 × 10 −5 m 2.
When adjusted to 3 / s (5 l / min), the nitrogen concentration was 9
It was 7.7%.

【0012】以上のように本実施例によれば、原料気体
流路材と、透過気体流路材を挟んで折り返した平膜状の
気体分離複合膜とを重ねて一単位とし、原料空気を供給
する給気管と透過気体を排気する排気管とが一体となっ
た給排気管の回りにスパイラル状に巻回した気体分離膜
モジュールで、巻終わりの一端が気体分離複合膜の折り
返し部となるようにし、巻始めの一端は原料気体流路と
給排気管の給気管が連通し、かつ、透過気体流路と給排
気管の排気管が連通するように給排気管に気体分離複合
膜を接着し、巻回方向の両側端部は原料気体流路と透過
気体流路を気密に隔てるように封止する事により、原料
空気が気体分離膜表面上を流れる距離を長くすることが
出来、濃縮効率の高い気体分離膜モジュールが得られ
る。
As described above, according to the present embodiment, the raw material gas flow channel material and the flat membrane-like gas separation composite membrane folded back with the permeated gas flow channel material sandwiched are made into one unit, and the raw material air is supplied. A gas separation membrane module in which a supply air supply pipe and an exhaust pipe for exhausting permeated gas are integrally wound around a supply and exhaust pipe in a spiral shape, and one end of the winding end serves as a folded portion of the gas separation composite membrane. Thus, at one end of the winding start, the gas separation composite membrane is attached to the supply / exhaust pipe so that the raw material gas flow passage and the air supply pipe of the supply / exhaust pipe communicate with each other, and the permeation gas flow passage and the exhaust pipe of the supply / exhaust pipe communicate with each other. By bonding and sealing both ends of the winding direction so that the raw material gas passage and the permeating gas passage are airtightly separated, it is possible to increase the distance that the raw material air flows on the surface of the gas separation membrane. A gas separation membrane module with high concentration efficiency can be obtained.

【0013】尚、本実施例では、原料気体流路と、透過
気体流路材を挟んだ平膜状の気体分離複合膜とを重ねて
一単位とし、この一組のみを給排気管の回りにスパイラ
ル状に巻回した構成としたが、図3に示すように複数組
を巻回した構成としても良い。
In this embodiment, the raw material gas passage and the flat membrane-like gas separation composite membrane sandwiching the permeation gas passage material are overlapped to form one unit, and only this set is connected around the supply / exhaust pipe. Although the spirally wound structure is used, a plurality of sets may be wound as shown in FIG.

【0014】(実施例2)以下本発明の第2の実施例に
ついて、図面を参照しながら説明する。図4は本実施例
の気体分離膜モジュールの展開横断面図である。
(Second Embodiment) A second embodiment of the present invention will be described below with reference to the drawings. FIG. 4 is a developed cross-sectional view of the gas separation membrane module of this embodiment.

【0015】図4において、1は原料気体流路材、3は
透過気体流路材、4は給気管5と排気管6が長さ方向に
平行に配された給排気管で、以上は実施例1と同様な構
成である。2−1及び2−2は気体分離複合膜で、これ
も実施例1の気体分離複合膜2と同様な構成であり、分
離膜側が原料気体流路材1と相対するように配されてお
り、巻始めの一端は給排気管4に気密に接着されてい
る。以上の原料気体流路材1から透過気体流路材3の材
料を給排気管5の回りにスパイラル状に巻回した後、巻
終わりの一端で気体分離複合膜2−1及び2−2を膜封
止材2−3で気密に接着し、巻回方向の両側端部他を図
2のように封止材7によって原料気体流路と、透過気体
流路を気密に隔てるように接着封止する。
In FIG. 4, 1 is a raw material gas flow path member, 3 is a permeation gas flow path member, 4 is an air supply / exhaust pipe in which an air supply pipe 5 and an exhaust pipe 6 are arranged in parallel in the longitudinal direction. The configuration is the same as in Example 1. 2-1 and 2-2 are gas separation composite membranes, which also have the same structure as the gas separation composite membrane 2 of Example 1, and are arranged so that the separation membrane side faces the raw material gas flow path member 1. The one end of the winding start is airtightly bonded to the air supply / exhaust pipe 4. After spirally winding the material of the permeating gas flow channel material 3 from the raw material gas flow channel material 1 above, the gas separation composite membranes 2-1 and 2-2 are formed at one end of the winding end. The film sealing material 2-3 is airtightly adhered, and both ends in the winding direction are adhesively sealed by the sealing material 7 so as to airtightly separate the raw material gas passage and the permeation gas passage as shown in FIG. Stop.

【0016】以上のように構成された気体分離膜モジュ
ールを圧力容器8内に収納し、給気管5から592Pa
(5kgf/cm2G)に加圧された空気4.2×10-4
3/s(25l/min)を供給し、流量調節弁9か
ら得られる窒素濃縮空気流量を8.3×10-53/s
(5l/min)に調節したところ窒素濃度は97.5
%であった。
The gas separation membrane module configured as described above is housed in the pressure vessel 8 and is connected to the air supply pipe 5 at 592 Pa.
Air pressurized to (5 kgf / cm 2 G) 4.2 × 10 -4
m 3 / s (25 l / min) is supplied, and the nitrogen-concentrated air flow rate obtained from the flow rate control valve 9 is 8.3 × 10 −5 m 3 / s.
When adjusted to (5 l / min), the nitrogen concentration is 97.5.
%Met.

【0017】以上のように本実施例によれば、原料気体
流路材と、平膜状の第1の気体分離複合膜と、透過気体
流路材と、平膜状の第2の気体分離複合膜とを、上記の
順に重ねて一単位とし、原料空気を供給する給気管と透
過気体を排気する排気管とが一体となった給排気管の回
りにスパイラル状に巻回した気体分離膜モジュールで、
巻始めの一端は原料気体流路と給排気管の給気管が連通
し、かつ、透過気体流路と給排気管の排気管が連通する
ように給排気管に第1及び第2の気体分離複合膜を接着
し、巻終わりの一端は透過気体流路を閉じるように第1
及び第2の気体分離複合膜を接着し、巻回方向の両側端
部は原料気体流路と透過気体流路を気密に隔てるように
封止する事により、原料空気が気体分離膜表面上を流れ
る距離を長くすることが出来、濃縮効率の高い気体分離
膜モジュールが得られる。
As described above, according to this embodiment, the raw material gas flow channel material, the flat membrane-like first gas separation composite membrane, the permeation gas flow channel material, and the flat membrane-like second gas separation material. A gas separation membrane spirally wound around a supply / exhaust pipe in which a composite membrane and the above-mentioned are stacked in the above order to form a unit, and a supply pipe for supplying raw material air and an exhaust pipe for exhausting permeated gas are integrated. In a module,
The first and second gas separations to the supply / exhaust pipe so that the raw material gas flow passage and the supply / exhaust pipe of the supply / exhaust pipe communicate with each other at one end of the winding start, and the permeation gas flow passage and the exhaust pipe of the supply / exhaust pipe communicate with each other. Adhere the composite membrane and put the first end so that the end of the winding closes the permeate gas channel.
And the second gas separation composite membrane are adhered to each other, and the both ends in the winding direction are sealed so that the raw material gas passage and the permeation gas passage are airtightly separated from each other, so that the raw material air flows over the surface of the gas separation membrane. A flow distance can be lengthened and a gas separation membrane module with high concentration efficiency can be obtained.

【0018】尚、本実施例の気体分離複合膜2−1及び
2−2は同一の気体分離膜構成としたが、これは異なっ
た気体分離膜を用いた気体分離複合膜の組み合わせでも
よく、例えば、第1の気体分離複合膜に本実施例のよう
な高分離性の気体分離膜を用い、第2の気体分離複合膜
にポリジフェニルアセチレン等の高透過性の気体分離膜
を用いることによって、更に濃縮効率を高めることが出
来る。
Although the gas separation composite membranes 2-1 and 2-2 of this embodiment have the same gas separation membrane structure, this may be a combination of gas separation composite membranes using different gas separation membranes, For example, by using a gas separation membrane having a high separation property as in this embodiment as the first gas separation composite membrane and using a gas separation membrane having a high permeability such as polydiphenylacetylene as the second gas separation composite membrane. Moreover, the concentration efficiency can be further enhanced.

【0019】また、本実施例では、原料気体流路材と、
平膜状の第1の気体分離複合膜と、透過気体流路材と、
平膜状の第2の気体分離複合膜とを重ねて一単位とし、
この一組のみを給排気管の回りにスパイラル状に巻回し
た構成としたが、複数組を巻回した構成としても良い。
Further, in the present embodiment, a raw material gas flow path material,
A flat membrane-like first gas separation composite membrane, and a permeating gas channel material,
A flat membrane-like second gas separation composite membrane is overlaid to form one unit,
Although only one set is wound around the supply and exhaust pipe in a spiral shape, a plurality of sets may be wound.

【0020】(実施例3)以下本発明の第3の実施例に
ついて図面を参照しながら説明する。図5(a)は本実
施例の気体分離膜モジュールの横断面図、(b)はその
縦断面図である。
(Embodiment 3) A third embodiment of the present invention will be described below with reference to the drawings. FIG. 5A is a horizontal sectional view of the gas separation membrane module of this embodiment, and FIG. 5B is a vertical sectional view thereof.

【0021】給排気管4を図5のように長さ方向に対し
て垂直に仕切板を設けた構造とし、実施例1と同様にス
パイラルモジュールを製作して圧力容器に収納し給気管
5から592Pa(5kgf/cm2G)に加圧された空
気4.2×10-43/s(25l/min)を供給
し、流量調節弁9から得られる窒素濃縮 空気流量を
8.3×10-53/s(5l/min)に調節したと
ころ 窒素濃度は97.0%であった。
As shown in FIG. 5, the air supply / exhaust pipe 4 has a structure in which a partition plate is provided perpendicularly to the lengthwise direction, and a spiral module is manufactured in the same manner as in the first embodiment and is housed in a pressure vessel to be connected to the air supply pipe 5. The nitrogen enriched air flow rate obtained from the flow rate control valve 9 is 8.3 × by supplying pressurized air 4.2 × 10 −4 m 3 / s (25 l / min) to 592 Pa (5 kgf / cm 2 G). When adjusted to 10 -5 m 3 / s (5 l / min), the nitrogen concentration was 97.0%.

【0022】以上のように本実施例によれば、原料気体
流路材と、透過気体流路材を挟んで折り返した平膜状の
気体分離複合膜とを重ねて一単位とし、長さ方向に対し
て垂直に仕切板を設置した給排気管の回りにスパイラル
状に巻回した気体分離膜モジュールで、巻終わりの一端
が気体分離複合膜の折り返し部となるようにし、巻始め
の一端は原料気体流路と給排気管の給気管が連通し、か
つ、透過気体流路と給排気管の排気管が連通するように
給排気管に気体分離複合膜を接着し、巻回方向の両側端
部は原料気体流路と透過気体流路を気密に隔てるように
封止する事により、原料空気が気体分離膜表面上を流れ
る距離を長くすることが出来、濃縮効率の高い気体分離
膜モジュールが得られる。
As described above, according to this embodiment, the raw material gas flow path member and the flat membrane-like gas separation composite membrane folded back with the permeation gas flow path material sandwiched therebetween are made into one unit, and the length direction is set. A gas separation membrane module spirally wound around an air supply / exhaust pipe in which a partition plate is installed perpendicularly to the end of one end of the gas separation composite membrane, and one end of the start of winding The gas separation composite membrane is adhered to the supply / exhaust pipe so that the raw material gas flow passage and the supply / exhaust pipe are connected to each other, and the permeation gas flow passage and the exhaust pipe of the supply / exhaust pipe are connected to each other. By sealing the ends so that the raw material gas passage and the permeating gas passage are airtightly separated, the distance that the raw material air flows on the surface of the gas separation membrane can be lengthened, and the gas separation membrane module with high concentration efficiency can be obtained. Is obtained.

【0023】[0023]

【発明の効果】以上のように本発明によれば、原料気体
流路材と、透過気体流路材を挟んで折り返した平膜状の
気体分離複合膜とを重ねて一単位とし、原料空気を供給
する給気管と透過気体を排気する排気管とが一体となっ
た給排気管の回りにスパイラル状に巻回した気体分離膜
モジュールで、巻終わりの一端が気体分離複合膜の折り
返し部となるようにし、巻始めの一端は原料気体流路と
給排気管の給気管が連通し、かつ、透過気体流路と給排
気管の排気管が連通するように給排気管に気体分離複合
膜を接着し、巻回方向の両側端部は原料気体流路と透過
気体流路を気密に隔てるように封止する事により、ある
いは、原料気体流路材と、平膜状の第1の気体分離複合
膜と、透過気体流路材と、平膜状の第2の気体分離複合
膜とを、上記の順に重ねて一単位とし、原料空気を供給
する給気管と透過気体を排気する排気管とが一体となっ
た給排気管の回りにスパイラル状に巻回した気体分離膜
モジュールで、巻始めの一端は原料気体流路と給排気管
の給気管が連通し、かつ、透過気体流路と給排気管の排
気管が連通するように給排気管に第1及び第2の気体分
離複合膜を接着し、巻終わりの一端は透過気体流路を閉
じるように第1及び第2の気体分離複合膜を接着し、巻
回方向の両側端部は原料気体流路と透過気体流路を気密
に隔てるように封止する事により、原料空気が気体分離
膜表面上を流れる距離を長くすることが出来、濃縮効率
の高い気体分離膜モジュールが得られる。
As described above, according to the present invention, the raw material gas flow channel member and the flat membrane-shaped gas separation composite membrane folded back with the permeated gas flow channel member sandwiched therebetween are made into one unit, Is a gas separation membrane module spirally wound around an air supply / exhaust pipe in which an air supply pipe for supplying air and an exhaust pipe for exhausting permeated gas are integrated, and one end of the winding end is a folded portion of the gas separation composite membrane. The gas separation composite membrane is connected to the air supply / exhaust pipe so that the raw material gas flow passage and the air supply / exhaust pipe air supply pipe communicate with each other, and the permeate gas flow passage communicates with the air supply / exhaust pipe exhaust pipe at one end of the winding start. By sealing the raw material gas flow passage and the permeating gas flow passage so as to hermetically separate the raw material gas flow passage and the permeating gas flow passage from each other, or the raw material gas flow passage material and the flat film-like first gas. The separation composite membrane, the permeating gas channel material, and the flat membrane-shaped second gas separation composite membrane are arranged in the above-mentioned order. It is a gas separation membrane module that is spirally wound around an air supply / exhaust pipe in which an air supply pipe for supplying raw material air and an exhaust pipe for exhausting permeated gas are integrated into one unit. The first and second gas separation composite membranes are adhered to the air supply / exhaust pipe so that the raw material gas flow passage and the air supply pipe of the air supply / exhaust pipe communicate with each other, and the permeation gas flow passage communicates with the exhaust pipe of the air supply / exhaust pipe. , The first and second gas separation composite membranes are adhered so that one end of the winding end closes the permeable gas flow passage, and both ends in the winding direction airtightly separate the raw material gas flow passage and the permeable gas flow passage. By sealing the gas separation membrane with the above, the distance that the raw material air flows on the surface of the gas separation membrane can be lengthened, and a gas separation membrane module with high concentration efficiency can be obtained.

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

【図1】本発明の第1の実施例における気体分離膜モジ
ュールの展開横断面図
FIG. 1 is a developed transverse sectional view of a gas separation membrane module according to a first embodiment of the present invention.

【図2】本発明の第1または第2の実施例における気体
分離膜モジュールの組立完成品説明図
FIG. 2 is an explanatory diagram of a completed assembly product of the gas separation membrane module according to the first or second embodiment of the present invention.

【図3】本発明の第1の実施例における気体分離膜モジ
ュールの変形例を示す展開横断面図
FIG. 3 is a developed transverse cross-sectional view showing a modified example of the gas separation membrane module according to the first embodiment of the present invention.

【図4】本発明の第2の実施例における気体分離膜モジ
ュールの展開横断面図
FIG. 4 is a developed transverse sectional view of a gas separation membrane module according to a second embodiment of the present invention.

【図5】(a)本発明の第3の実施例における気体分離
膜モジュールの展開横断面図 (b)同展開縦断面図
FIG. 5 (a) is a developed horizontal sectional view of a gas separation membrane module according to a third embodiment of the present invention.

【図6】従来のスパイラル型分離膜モジュールの構成図FIG. 6 is a block diagram of a conventional spiral separation membrane module.

【符号の説明】[Explanation of symbols]

1 原料空気流路材 2 気体分離複合膜 2−1 第1の気体分離複合膜 2−2 第2の気体分離複合膜 2−3 膜封止材 3 透過気体流路材 4 給排気管 5 給気管 6 排気管 7 封止材 8 圧力容器 1 Raw Material Air Channel Material 2 Gas Separation Composite Membrane 2-1 First Gas Separation Composite Membrane 2-2 Second Gas Separation Composite Membrane 2-3 Membrane Encapsulation Material 3 Permeation Gas Channel Material 4 Supply / Exhaust Pipe 5 Supply Trachea 6 Exhaust pipe 7 Sealant 8 Pressure vessel

フロントページの続き (72)発明者 小林 貴樹 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 菅藤 雅哉 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 金治 克秀 大阪府門真市大字門真1006番地 松下電器 産業株式会社内Front page continued (72) Inventor Takaki Kobayashi 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Inventor Masaya Sudo, 1006 Kadoma, Kadoma City Osaka Prefecture Katsuhide Kinji 1006 Kadoma, Kadoma-shi, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 原料気体流路材と、透過気体流路材を挟
んで折り返した平膜状の気体分離複合膜とを重ねて一単
位とし、原料空気を供給する給気管と透過気体を排気す
る排気管とが一体となった給排気管の回りにスパイラル
状に巻回した気体分離膜モジュールで、巻終わりの一端
が気体分離複合膜の折り返し部となるようにし、巻始め
の一端は原料気体流路と給排気管の給気管が連通し、か
つ、透過気体流路と給排気管の排気管が連通するように
給排気管に気体分離複合膜を接着し、巻回方向の両側端
部は原料気体流路と透過気体流路を気密に隔てるように
封止したことを特徴とする気体分離膜モジュール。
1. A feed gas pipe for supplying raw material air and a permeated gas are exhausted by stacking a raw material gas flow path member and a flat membrane-like gas separation composite membrane folded back with a permeated gas flow path material sandwiched therebetween. A gas separation membrane module spirally wound around a supply / exhaust pipe that is integrated with an exhaust pipe, so that one end of the winding end is a folded portion of the gas separation composite membrane and one end of the winding end is a raw material. Adhere the gas separation composite membrane to the air supply / exhaust pipe so that the gas flow passage and the air supply pipe of the air supply / exhaust pipe communicate with each other, and the permeate gas flow passage and the exhaust pipe of the air supply / exhaust pipe communicate with each other. The part is a gas separation membrane module characterized in that a raw material gas passage and a permeating gas passage are hermetically separated from each other.
【請求項2】 原料気体流路材と、平膜状の第1の気体
分離複合膜と、透過気体流路材と、平膜状の第2の気体
分離複合膜とを、上記の順に重ねて一単位とし、原料空
気を供給する給気管と透過気体を排気する排気管とが一
体となった給排気管の回りにスパイラル状に巻回した気
体分離膜モジュールで、巻始めの一端は原料気体流路と
給排気管の給気管が連通し、かつ、透過気体流路と給排
気管の排気管が連通するように給排気管に第1及び第2
の気体分離複合膜を接着し、巻終わりの一端は透過気体
流路を閉じるように第1及び第2の気体分離複合膜を接
着し、巻回方向の両側端部は原料気体流路と透過気体流
路を気密に隔てるように封止したことを特徴とする気体
分離膜モジュール。
2. A raw material gas flow channel material, a flat membrane-shaped first gas separation composite membrane, a permeation gas flow channel material, and a flat membrane-shaped second gas separation composite membrane are stacked in the order described above. A gas separation membrane module that is spirally wound around an air supply / exhaust pipe that integrates an air supply pipe that supplies raw air and an exhaust pipe that exhausts permeated gas. The first and second supply / exhaust pipes are connected so that the gas flow passage and the supply / exhaust pipes communicate with each other, and the permeate gas flow passage and the exhaust pipes of the supply / exhaust pipe communicate with each other.
The gas separation composite membrane is adhered, the first and second gas separation composite membranes are adhered so that one end of the winding end closes the permeation gas flow passage, and both side ends in the winding direction permeate the raw material gas flow passage. A gas separation membrane module, characterized in that a gas channel is hermetically sealed.
【請求項3】 給排気管の長さ方向に対して水平に給気
管と排気管を設けた給排気管を有する請求項1または2
記載の気体分離膜モジュール。
3. An air supply / exhaust pipe having an air supply pipe and an exhaust pipe provided horizontally to the length direction of the air supply / exhaust pipe.
The gas separation membrane module described.
【請求項4】 給排気管内を仕切り、給気管と排気管を
設けた給排気管を有する請求項1または2記載の気体分
離膜モジュール。
4. The gas separation membrane module according to claim 1, further comprising a supply / exhaust pipe provided with an air supply pipe and an exhaust pipe, which partition the interior of the supply / exhaust pipe.
JP3158693A 1993-02-22 1993-02-22 Gas separation membrane module Pending JPH06246125A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3158693A JPH06246125A (en) 1993-02-22 1993-02-22 Gas separation membrane module

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3158693A JPH06246125A (en) 1993-02-22 1993-02-22 Gas separation membrane module

Publications (1)

Publication Number Publication Date
JPH06246125A true JPH06246125A (en) 1994-09-06

Family

ID=12335301

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3158693A Pending JPH06246125A (en) 1993-02-22 1993-02-22 Gas separation membrane module

Country Status (1)

Country Link
JP (1) JPH06246125A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010044961A1 (en) * 2008-10-17 2010-04-22 General Electric Company Spirally wound membrane separator assembly
WO2010044970A1 (en) * 2008-10-17 2010-04-22 General Electric Company Spirally wound membrane separator assembly
US8021550B2 (en) 2008-10-17 2011-09-20 General Electric Company Central core element for a separator assembly
US8961790B2 (en) 2008-10-17 2015-02-24 General Electric Company Separator assembly
US8968566B2 (en) 2008-10-17 2015-03-03 General Electric Company Separator assembly
US9795924B2 (en) 2011-10-31 2017-10-24 General Electric Company Central core element for a separator assembly
EP3135366A4 (en) * 2014-04-21 2018-01-24 Picogram Co., Ltd. Reverse osmosis membrane filter having fluid channel formed on side surface thereof

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010044961A1 (en) * 2008-10-17 2010-04-22 General Electric Company Spirally wound membrane separator assembly
WO2010044970A1 (en) * 2008-10-17 2010-04-22 General Electric Company Spirally wound membrane separator assembly
US8021550B2 (en) 2008-10-17 2011-09-20 General Electric Company Central core element for a separator assembly
US8961790B2 (en) 2008-10-17 2015-02-24 General Electric Company Separator assembly
US8968566B2 (en) 2008-10-17 2015-03-03 General Electric Company Separator assembly
AU2009303747B2 (en) * 2008-10-17 2016-03-03 Bl Technologies, Inc. Spirally wound membrane separator assembly
US9795924B2 (en) 2011-10-31 2017-10-24 General Electric Company Central core element for a separator assembly
EP3135366A4 (en) * 2014-04-21 2018-01-24 Picogram Co., Ltd. Reverse osmosis membrane filter having fluid channel formed on side surface thereof

Similar Documents

Publication Publication Date Title
JP5501897B2 (en) Oxygen-enriched air separation and recovery device
US5104532A (en) Flat stack permeator
US4789480A (en) Membrane module and the use thereof for the separation of liquids according to the pervaporation process
KR930009641A (en) Membrane oxygen process and system
JPH06339613A (en) Membrane aggregate for removing gaseous substance from air stream, device containing the same and removing method
US20090200226A1 (en) Multifiltration cartridge filtration apparatus
US5284583A (en) Fiber membrane elements and modules and methods of fabrication for fluid separation
WO1994009189A1 (en) Fiber membrane structures and methods of fabrication
JPH06246125A (en) Gas separation membrane module
JP2005262211A (en) Method for separating/collecting oxygen-rich air from air and gas separation membrane module
JPH06262026A (en) Air separation membrane module
JPH06190249A (en) Membrane module and preparation thereof
JPH0699016A (en) Gas separation membrane module
JP2573670B2 (en) Spiral type membrane separation device
JPH06227803A (en) Nitrogen generator
JPH02135117A (en) Gas separation module and multistage gas separator
JPS6260923B2 (en)
JPS621405A (en) Fluid separator
FR2216000A1 (en) Compact gas permeation filter - with alternate porous layers faced with membranes on both sides giving high area to volume ratio
JPH06246124A (en) Gas separation membrane module
JPH01288303A (en) Fluid separation element
JPH0328104A (en) Inline oxygen enriching film device
JP2878297B2 (en) Method for producing nitrogen-enriched air
JPH0810367Y2 (en) Spiral type membrane separation device
CN114849483B (en) Membrane element for water in and out in same direction and production process