JPS6127609Y2 - - Google Patents
Info
- Publication number
- JPS6127609Y2 JPS6127609Y2 JP1981068930U JP6893081U JPS6127609Y2 JP S6127609 Y2 JPS6127609 Y2 JP S6127609Y2 JP 1981068930 U JP1981068930 U JP 1981068930U JP 6893081 U JP6893081 U JP 6893081U JP S6127609 Y2 JPS6127609 Y2 JP S6127609Y2
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- gas permeable
- selective gas
- porous body
- elastic porous
- 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.)
- Expired
Links
- 239000012528 membrane Substances 0.000 claims description 48
- 239000002131 composite material Substances 0.000 claims description 17
- 239000011148 porous material Substances 0.000 claims 1
- 239000007789 gas Substances 0.000 description 23
- 239000010408 film Substances 0.000 description 4
- -1 polyethylene Polymers 0.000 description 4
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000010409 thin film Substances 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000004205 dimethyl polysiloxane Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000012948 isocyanate Substances 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Description
【考案の詳細な説明】
本考案は選択性気体透過膜を用い、この膜を通
して二種以上の混合気体から、特定の気体を濃縮
分離する膜式気体分離法において、これを工業的
に実用性を有ぜしめるモジユール構造を提供する
ものである。特に本考案は、均質な1μ以下の超
薄膜を選択性気体透過膜として用いた場合に有効
な平板状モジユール構造に関する。[Detailed description of the invention] The present invention uses a selective gas permeable membrane to concentrate and separate a specific gas from a mixture of two or more gases through the membrane. This provides a modular structure that has the following features. In particular, the present invention relates to a flat module structure that is effective when a homogeneous ultra-thin film of 1 μm or less is used as a selective gas permeable membrane.
従来平板状構造のモジユールは種々提案されて
おり、代表的な例はS.A・Sternによる米国特許
3332216号明細書に記載のものがある。 Various modules with a flat plate structure have been proposed in the past, and a typical example is the US patent by SA Stern.
There is one described in specification No. 3332216.
これは、膜に繊維質のシートで内張りをし、こ
れを金属の金網の両側に張付け、周囲をシールし
たものを一単位とし、これを積層した構造であ
る。 This is a structure in which the membrane is lined with a fibrous sheet, which is pasted on both sides of a metal wire mesh, and the periphery is sealed, forming a unit that is laminated.
上記の構造では、透過膜が十分に機械的強度を
有し、且つ膜厚が厚い場合、及び被分離気体が不
活性気体の場合には十分な効果があるが、本考案
に用いる場合のように、透過膜が、1μ以下であ
る超薄膜の場合は、入口側と出口側の圧力差によ
つて、この膜が変形し損傷する危険がある。また
被分離気体の性質によつては、内部の金網が腐蝕
劣化する場合がある。本考案者らはこのような点
を改善し、気体透過膜に損傷を与えず、また腐蝕
その他の劣化を惹き起こさない構造を提供するも
のである。本考案の特徴は超薄膜から成る選択性
気体透過均質膜部分を多孔性膜と一体化した選択
性気体透過複合膜を形成し、この複合膜によつ
て、弾性を有し、内部の一部または全部が連続気
泡で構成されている弾力性多孔体を多孔性膜側が
多孔体と対向するごとく気密に覆つて形成したも
のである。 The above structure is sufficiently effective when the permeable membrane has sufficient mechanical strength and thickness, and when the gas to be separated is an inert gas. Furthermore, if the permeable membrane is an ultra-thin membrane with a thickness of 1 μm or less, there is a risk that the membrane will be deformed and damaged due to the pressure difference between the inlet and outlet sides. Furthermore, depending on the properties of the gas to be separated, the internal wire mesh may deteriorate due to corrosion. The inventors of the present invention have improved these points and provided a structure that does not damage the gas permeable membrane and does not cause corrosion or other deterioration. The feature of this invention is that a selective gas permeable homogeneous membrane part consisting of an ultra-thin membrane is integrated with a porous membrane to form a selective gas permeable composite membrane. Alternatively, it is formed by airtightly covering an elastic porous body composed entirely of open cells so that the porous membrane side faces the porous body.
以下図面を用いて本考案の一実施例を説明する
と、第1図は本モジユールの全体の構成を示す斜
視図で、1は金属またはプラスチツクあるいは木
材などから形成される断面コ字状の外枠、2は内
部の一部又は全部が通気性を有する連続気泡構造
から成る多孔性弾性体、3は前記した選択性気体
透過複合膜、4は被分離気体透過口である。第2
図は、モジユールの断面をを示し、選択性気体透
過複合膜3は、弾性体2の表面を覆い、枠1にd
点において気密を保つように接着されている。第
3図は膜の動作時、すなわち膜の前後に圧力差の
生じている場合の動作説明図で、イは金網を用い
た従来例の場合、ロは本考案の弾性体を用いた場
合である。イの場合、繊維質シートで内張りした
選択性気体透過膜複合膜5は網6の形に沿つて
c′に示すように変形し、圧力差を取り除くと、も
とのcの位置に復帰する。この動作の繰り返しが
生じるため、膜5は次第に延び始め、約20回の繰
り返しで、膜5は網目部分から外側に、初期に比
べて約5mm膨らんだ。他の例では、約45回の繰り
返しで、ピンホールの発生する場合が生じた。一
方ロの構成では500回の繰り返しにも複合膜3の
変形は認められず、初期性能を充分に維持した。
ここで弾性体2として用いうるものは、圧力変形
が小さく、内部が通気性を有しており、表面が適
度の軟らかさを有するもので、次のごときものが
使用し得る。軟質ウレタンをプレスしたもので、
プレスによる圧縮率が5〜15倍程度のもの、また
は、上記軟質ウレタンを、イソシアネートにより
再硬化したもの、もしくは、適当な樹脂、例え
ば、ポリ塩化ビニルを一部含浸硬化させたもの、
あるいはポリエチレン、ポリプロピレンなどのポ
リオレフイン系樹脂の焼結体が好適な結果を示し
た。 One embodiment of the present invention will be described below with reference to the drawings. Fig. 1 is a perspective view showing the overall structure of this module, and 1 is an outer frame with a U-shaped cross section made of metal, plastic, wood, etc. , 2 is a porous elastic body having an open cell structure whose interior is partly or entirely breathable, 3 is the aforementioned selective gas permeable composite membrane, and 4 is a gas permeation port to be separated. Second
The figure shows a cross section of the module, in which the selective gas permeable composite membrane 3 covers the surface of the elastic body 2 and is attached to the frame 1.
It is glued to keep it airtight at the points. Figure 3 is an explanatory diagram of the operation when the membrane is in operation, that is, when there is a pressure difference between the front and rear sides of the membrane. be. In the case of A, the selective gas permeable membrane composite membrane 5 lined with a fibrous sheet follows the shape of the net 6.
It deforms as shown at c' and returns to its original position at c when the pressure difference is removed. As this action was repeated, the membrane 5 gradually began to expand, and after about 20 repetitions, the membrane 5 expanded outward from the mesh portion by about 5 mm compared to the initial size. In another example, pinholes occurred after about 45 repetitions. On the other hand, in the configuration B, no deformation of the composite membrane 3 was observed even after 500 repetitions, and the initial performance was sufficiently maintained.
The elastic body 2 that can be used here has a small pressure deformation, is breathable inside, and has a moderately soft surface, and the following can be used. Made of pressed soft urethane,
A material with a compression rate of about 5 to 15 times by pressing, or a material obtained by re-curing the above-mentioned soft urethane with isocyanate, or a material obtained by partially impregnating and curing a suitable resin such as polyvinyl chloride,
Alternatively, sintered bodies of polyolefin resins such as polyethylene and polypropylene showed suitable results.
第1図のモジユール構造では角型の場合を示し
たが、丸型、楕円形その他用途に応じて任意の形
状に構成することが可能であり、また、被分離気
体透過口4は、外枠1を工夫することによつて外
枠1の任意の部分より、任意の数だけ、任意の形
で、例えば、スリツト形状などで取り出すことが
出来る。 Although the modular structure shown in Fig. 1 is square, it can be configured in any shape depending on the purpose, such as round or oval. 1, it is possible to take out an arbitrary number and arbitrary shape from an arbitrary part of the outer frame 1, for example, in the form of a slit.
第2図において、弾性体2は、外枠1に接する
形で設置されているが、弾性体2の周縁部は、外
枠1の内面に設けられた凹部に、被分離気体の通
路となる空間を残してはめ込むようにしてもよ
い。 In FIG. 2, the elastic body 2 is installed in contact with the outer frame 1, and the peripheral edge of the elastic body 2 forms a passage for the gas to be separated into a recess provided on the inner surface of the outer frame 1. It may be fitted leaving a space.
なお外枠断面はコ字形に限らず、丸形、角形い
ずれでもよく、中空状にすることが好ましい。ま
た、膜3は外枠1に対して、dの部分で接着され
ているが、接着法に対しても、特に制限は無く、
気密性が保持される限り如何なる接着法も利用可
能である。 The cross section of the outer frame is not limited to a U-shape, but may be round or rectangular, and is preferably hollow. The membrane 3 is bonded to the outer frame 1 at the portion d, but there is no particular restriction on the bonding method.
Any adhesive method can be used as long as the airtightness is maintained.
また外枠1として縦30cm、横70cm、奥行0.5cm
枠の巾1cmの角形外枠を作り、弾性体2として、
井上MTP(株)製軟化ウレタンFS−10を10倍プレス
したものを用い、複合膜3として25μの多孔性ポ
リプロピレン(商品名ジユラガード)に均質膜と
して約2000Å厚のポリジメチルシロキサン膜を設
置した複合膜を用いて第1図に示した構成のモジ
ユールを作つた。複合膜3は外枠1に対して、d
の部分で、ゴム系接着剤で接着した。このような
モジユールを用い、気体透過口4より真空ポンプ
で、150mmHgに減圧吸引し、空気を吸引した結
果、酸素濃度が32%に濃縮された酸素富化空気
が、毎分7の割合で得ることが出来た。この構
成で真空ポンプのオンーオフを500回繰り返した
が、モジユール、複合膜には何らの異常も発生し
なかつた。また、80℃の恒温下で500時間連続運
転を行なつたが、同様に何らの変化も認められな
かつた。このように本考案のモジユールは、軽量
で、製造が簡単であり、且つコストも安く、しか
も、膜部分に何らの損傷も与えず、長期にわたつ
て安定な特性を維持する秀れた性能を示した。以
上のように本考案は選択性気体透過膜と支持体で
ある多孔性薄膜より成る選択性気体透過複合膜を
有し、この複合膜を弾性を有し、内部の一部また
は全部が連続気泡で構成されている弾力性多孔体
によつて上記複合膜の多孔性薄膜側と上記弾力性
多孔体がするように保持したものであり、軽量
で、製造が簡単であり且つコストも安く、しかも
膜部分に何らの損傷を与えず、長期にわたつて安
定な性能を維持する選択性気体透過膜モジユール
を提供するものである。 Also, as outer frame 1, height 30cm, width 70cm, depth 0.5cm
Make a square outer frame with a frame width of 1 cm, and use it as elastic body 2.
Using 10 times pressed softened urethane FS-10 manufactured by Inoue MTP Co., Ltd., a composite film in which a polydimethylsiloxane film with a thickness of about 2000 Å is installed as a homogeneous film on 25μ porous polypropylene (trade name Jyuraguard) as the composite film 3. A module having the configuration shown in FIG. 1 was made using the membrane. The composite membrane 3 is d relative to the outer frame 1.
The part was glued with rubber adhesive. Using such a module, a vacuum pump is used to vacuum the air through the gas permeation port 4 to 150 mmHg, and as a result of sucking air, oxygen-enriched air with an oxygen concentration of 32% is obtained at a rate of 7 per minute. I was able to do it. With this configuration, the vacuum pump was turned on and off 500 times, but no abnormalities occurred in the module or composite membrane. Furthermore, although continuous operation was performed for 500 hours at a constant temperature of 80°C, no change was observed. In this way, the module of the present invention is lightweight, easy to manufacture, and inexpensive, and has excellent performance that does not cause any damage to the membrane part and maintains stable characteristics over a long period of time. Indicated. As described above, the present invention has a selective gas permeable composite membrane consisting of a selective gas permeable membrane and a porous thin film as a support. The porous thin film side of the composite membrane and the elastic porous body are held together by the elastic porous body composed of the above, and it is lightweight, easy to manufacture, and low in cost. The present invention provides a selective gas permeable membrane module that maintains stable performance over a long period of time without causing any damage to the membrane portion.
第1図は本考案による選択性気体透過膜モジユ
ールの実施例を示す分解斜視図、第2図は本考案
による選択性気体透過膜モジユールの実施例にお
ける一部拡大断面側面図、第3図イ,ロは従来例
および本考案による選択性気体透過膜モジユール
の動作説明図である。
1……外枠、2……弾性体、3……選択気体透
過複合膜、4……気体透過口。
FIG. 1 is an exploded perspective view showing an embodiment of the selective gas permeable membrane module according to the present invention, FIG. 2 is a partially enlarged cross-sectional side view of the selective gas permeable membrane module according to the present invention, and FIG. , b are explanatory diagrams of the operation of the selective gas permeable membrane module according to the conventional example and the present invention. 1...Outer frame, 2...Elastic body, 3...Selective gas permeation composite membrane, 4...Gas permeation port.
Claims (1)
泡で構成された弾力性多孔体と、超薄膜から成
る選択性気体透過膜および多孔性膜より成る選
択性気体透過複合膜と、上記複合膜の多孔性膜
側が上記弾力性多孔体と対向するごとく気密に
覆う手段と、上記弾力性多孔体を含む空間を、
上記複合膜の外側の空間から隔離させ、上記隔
離された弾力性多孔体を含む空間から気体を取
り出す手段とを具備することを特徴とする選択
性気体透過膜モジユール。 (2) 弾力性多孔体の周囲を外枠で囲み、外枠の両
面の一部に選択性気体透過複合膜を接着させ、
選択性気体透過複合膜で上記弾力性多孔体を気
密的に挾持させた実用新案登録請求の範囲第1
項記載の選択性気体透過膜モジユール。[Claims for Utility Model Registration] (1) Consists of an elastic porous body that has elasticity and is partially or entirely composed of open cells, a selective gas permeable membrane made of an ultra-thin membrane, and a porous membrane. a selective gas permeable composite membrane, a means for airtightly covering the porous membrane side of the composite membrane so that it faces the elastic porous body, and a space containing the elastic porous body,
A selective gas permeable membrane module characterized by comprising means for isolating gas from a space outside the composite membrane and extracting gas from the space containing the isolated elastic porous body. (2) Surround the elastic porous material with an outer frame, adhere selective gas permeable composite membranes to parts of both sides of the outer frame,
Utility model registration claim 1 in which the elastic porous body is airtightly sandwiched between selective gas permeable composite membranes.
Selective gas permeable membrane module as described in .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1981068930U JPS6127609Y2 (en) | 1981-05-13 | 1981-05-13 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1981068930U JPS6127609Y2 (en) | 1981-05-13 | 1981-05-13 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57181332U JPS57181332U (en) | 1982-11-17 |
JPS6127609Y2 true JPS6127609Y2 (en) | 1986-08-18 |
Family
ID=29864823
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1981068930U Expired JPS6127609Y2 (en) | 1981-05-13 | 1981-05-13 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6127609Y2 (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53116284A (en) * | 1977-03-18 | 1978-10-11 | Rhone Poulenc Ind | Osmosis apparatus and manufacture thereof |
-
1981
- 1981-05-13 JP JP1981068930U patent/JPS6127609Y2/ja not_active Expired
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53116284A (en) * | 1977-03-18 | 1978-10-11 | Rhone Poulenc Ind | Osmosis apparatus and manufacture thereof |
Also Published As
Publication number | Publication date |
---|---|
JPS57181332U (en) | 1982-11-17 |
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