JPS58222A - Gas supply device utilizing gas-selective high-polymer film - Google Patents
Gas supply device utilizing gas-selective high-polymer filmInfo
- Publication number
- JPS58222A JPS58222A JP9947081A JP9947081A JPS58222A JP S58222 A JPS58222 A JP S58222A JP 9947081 A JP9947081 A JP 9947081A JP 9947081 A JP9947081 A JP 9947081A JP S58222 A JPS58222 A JP S58222A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- flow rate
- components
- air
- supply device
- 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
Links
- 229920006254 polymer film Polymers 0.000 title 1
- 229920005597 polymer membrane Polymers 0.000 claims description 8
- 239000012466 permeate Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 5
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 239000012141 concentrate Substances 0.000 abstract 1
- 239000012528 membrane Substances 0.000 description 14
- 238000009423 ventilation Methods 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- 238000007664 blowing Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000011796 hollow space material Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はある物質を選択的に透過する気体選択性高分子
膜を利用して、必要な成分を豊富に含む気体を供給する
気体供給装置に関し、供給される気体の成分濃度を簡単
に調節出来るようにすることを目的とする。Detailed Description of the Invention The present invention relates to a gas supply device that supplies a gas rich in necessary components by using a gas-selective polymer membrane that selectively permeates a certain substance. The purpose is to allow the concentration of ingredients to be easily adjusted.
従来の気体供給装置においては、高分子膜を透過して得
られた気体に含まれる成分は一定であるため、成分濃度
を変えるためには高分子膜の成分透過性量を変えなけれ
ばならなかったので、簡単に成分濃度の調節が出来ない
欠点があった。In conventional gas supply devices, the components contained in the gas obtained by permeating the polymer membrane are constant, so in order to change the component concentration, the amount of component permeability of the polymer membrane must be changed. Therefore, there was a drawback that the component concentration could not be easily adjusted.
本発明は上記従来の欠点を解消するもので、以下にその
実施例を第1図〜第3図にもとづいて説明する。The present invention solves the above-mentioned conventional drawbacks, and embodiments thereof will be described below with reference to FIGS. 1 to 3.
図において、1は吸気室2と排気室3を仕切板4により
仕切り形成した筐体状の気体供給装置の本体で防音材に
より形成されている。6は吸気室2に連通ずるように本
体1に設けられた大気の吸気口、6は吸気口5に設けら
れたフィルター、7は吸気室2と排気室3を連通ずるよ
うに仕切板4に設けられた通気口、8は排気室3に連通
ずるように設けられた排気口、9は吸気室2に設けられ
鐵。In the figure, reference numeral 1 denotes a main body of a gas supply device in the form of a housing in which an intake chamber 2 and an exhaust chamber 3 are partitioned by a partition plate 4, and is made of a soundproof material. Reference numeral 6 indicates an air intake port provided in the main body 1 so as to communicate with the intake chamber 2, 6 indicates a filter provided in the intake port 5, and 7 indicates an air intake port provided in the partition plate 4 so as to communicate the intake chamber 2 with the exhaust chamber 3. A ventilation port 8 is provided to communicate with the exhaust chamber 3, and a reference numeral 9 is an exhaust port provided in the intake chamber 2.
た送風外で、前記通気ロアを介して吸気口6から排気口
8に向かう空気流を形成している。1oは吸気口6と送
風機9間に設けられる膜セルで、補強板11に必要な成
分に対し高い透過性を有する気体選択性高分子膜12を
補強板11との間に中空が形成されるように内部に通気
性材を設は周囲を接着し、一部に中空部と連通ずる接続
口13を形成した平膜モジー−ル14を間隔をおいて多
数並設して構成されている。16は排気室3内に通気ロ
アと連通ずるように防音壁16で区画したポンプ室で排
気口8に向かい排気される連通口17が形成されている
。18はポンプ室15内に防電ゴム19上に載置して設
けられる真空ポンプで、膜モジュール14の接続口13
とノ(イブ2oを介して接続され、膜モジーール14の
中空部を真空にして膜12を通して必要な成分濃度の高
い気体が得られるように設けられている。21は)くイ
ブ20に接続された大気混合口で、大気空気流量を調節
する混合流量調節弁22が設けられている。Outside of the air blowing, an air flow is formed from the intake port 6 to the exhaust port 8 via the ventilation lower. 1o is a membrane cell provided between the intake port 6 and the blower 9, in which a hollow space is formed between the reinforcing plate 11 and a gas-selective polymer membrane 12 having high permeability to components necessary for the reinforcing plate 11. It is constructed by installing a large number of flat membrane modules 14 at intervals, each of which has a ventilating material inside and is bonded around the periphery, and has a connecting port 13 communicating with a hollow part formed in a part thereof. Reference numeral 16 denotes a pump chamber partitioned by a soundproof wall 16 so as to communicate with the ventilation lower in the exhaust chamber 3, and a communication port 17 for exhausting the air toward the exhaust port 8 is formed. Reference numeral 18 denotes a vacuum pump installed on the electrically insulating rubber 19 in the pump chamber 15, and connected to the connection port 13 of the membrane module 14.
21 is connected to the tube 20 and is provided so that the hollow part of the membrane module 14 is evacuated and a gas having a high concentration of necessary components is obtained through the membrane 12. A mixing flow rate control valve 22 for adjusting the flow rate of atmospheric air is provided at the atmospheric mixing port.
23はコイル状の熱交換器で送風機9により形成される
空気流路内に設けられ、一端は前記真空ポンプ18の吐
出側に接続され、他端は水分離器24に接続されている
。25は本体1に設けられた濃縮成分気体の供給口で、
水分離器24で水分が除去された濃縮成分気体が流量調
整器26、流量計27、活性炭層28、フィルター29
を通過して供給されるように接続されている。30は水
分離器24で分離された水分を受けて蒸発する水分蒸発
皿で、ポンプ室15の連通ロシアから排気口8に向かう
空気流により水分が蒸発するように設けられている。A coil-shaped heat exchanger 23 is provided in the air flow path formed by the blower 9, and one end is connected to the discharge side of the vacuum pump 18, and the other end is connected to the water separator 24. 25 is a supply port for concentrated component gas provided in the main body 1;
The concentrated component gas from which water has been removed in the water separator 24 is transferred to a flow rate regulator 26, a flow meter 27, an activated carbon layer 28, and a filter 29.
connected to be supplied through the Reference numeral 30 denotes a moisture evaporation plate that receives and evaporates the moisture separated by the water separator 24, and is provided so that the moisture is evaporated by the air flow from the communicating part of the pump chamber 15 toward the exhaust port 8.
上記構成において、送風機9並びに真空ポンプ18を運
転すると、送風機9により本体1の吸気口5から大気が
フィルタ6を介して吸気され、吸気された大気は膜セル
1oに設けられた膜モジーール14間を通過する。この
とき真空ポンプ18により膜モジュール14の中空部内
の空気が真空状態になろうとするので、膜モジユール1
4間を通過する大気の一部は必要な成分を透過しやすい
膜12により必要な成分が多量 透過し、中空部内は必
要な成分を多量に含む気体となる。そして膜セル1oで
得られた高温の気体は真空ポンプ18により熱交換器2
3に送られ、送風機9により形成される空気流が熱交換
器23を冷却して水分が凝縮され、水分と共に水分離器
24に送られて水分が分離される。水分が分離された気
体は流量調整器26により流量が調整され活性炭層28
に送られて脱臭され、更にフィルタ29により浄化され
て供給口25より所定の成分が濃縮された気体が供給さ
れる。In the above configuration, when the blower 9 and the vacuum pump 18 are operated, air is sucked in from the air inlet 5 of the main body 1 by the blower 9 via the filter 6, and the sucked air is passed between the membrane module 14 provided in the membrane cell 1o. pass through. At this time, the air in the hollow part of the membrane module 14 attempts to become a vacuum state by the vacuum pump 18, so the membrane module 1
A large amount of the necessary components permeate through the membrane 12, which allows the necessary components to pass through the membrane 12, and the inside of the hollow portion becomes a gas containing a large amount of the necessary components. The high temperature gas obtained in the membrane cell 1o is transferred to the heat exchanger 2 by a vacuum pump 18.
The air flow generated by the blower 9 cools the heat exchanger 23 to condense the moisture, and is sent together with the moisture to the water separator 24 where the moisture is separated. The flow rate of the gas from which the moisture has been separated is adjusted by a flow rate regulator 26, and the gas is transferred to an activated carbon layer 28.
The gas is deodorized by the filter 29, and then purified by the filter 29, and a gas enriched with predetermined components is supplied from the supply port 25.
一方水分離器24により分離された水分は水分蒸発皿3
0に送られる。そして熱交換器23を経て更に通気ロア
よりポンプ室15内に入り真空ポンプ18に接触して温
度の高くなった送風機9からの空気流が水分蒸発皿全0
の水分に接して蒸発し、排気口8より装置外に排出され
る。On the other hand, the water separated by the water separator 24 is transferred to the water evaporating dish 3.
Sent to 0. After passing through the heat exchanger 23, the airflow from the blower 9 enters the pump chamber 15 through the ventilation lower, contacts the vacuum pump 18, and reaches a high temperature.
It evaporates when it comes into contact with moisture, and is discharged from the apparatus through the exhaust port 8.
次に必要な成分の含まれる濃度を調節したい場合には大
気混合口21に設けられた混合流量調節弁22を開口を
調整し所定量の大気を通過可能とすることにより、必要
虚成分が一定量渓縮されている気体が通るパイプ2o内
に大気が混合して必要な成分濃度が低くなる。従って混
合流量調節弁22により大気の混合度を調節することに
より簡単に必要な成分の濃度を調節することが出来るも
のである。Next, when it is desired to adjust the concentration of the necessary components, the opening of the mixing flow rate control valve 22 provided at the air mixing port 21 is adjusted to allow a predetermined amount of air to pass through, thereby keeping the necessary imaginary component constant. Air is mixed in the pipe 2o through which the gas whose volume is being reduced is mixed, and the concentration of the necessary components is lowered. Therefore, by adjusting the degree of mixing of the atmosphere using the mixing flow control valve 22, the concentration of the necessary components can be easily adjusted.
このように本発明によれば必要な成分を所定量透過させ
る気体選択性高分子膜を利用し、混合流量調整弁を設け
ることによって必要な成分を濃縮した気体中の成分濃度
を連続して簡単に調゛〜節出来る効果が発揮されるもの
である。As described above, according to the present invention, by using a gas-selective polymer membrane that allows a predetermined amount of necessary components to pass through, and by providing a mixing flow rate adjustment valve, it is possible to continuously and easily adjust the concentration of the necessary components in the concentrated gas. It has the effect of being adjustable.
第1図は本発明の一実施例における気体供給装置の概略
断面図、第2図は同装置の膜モジーールの一部断面した
側面図、第3図は同装置の膜セルの斜視図である。
12 ++w+a気体選択性高分子膜、18 、、、、
、、真空ポンプ、21 、、、、、大気混合口、22
、、、、、、混−合流量調節弁。
代理人の氏名 弁理士 中 尾 敏 男 ほか1名第2
図
@3図FIG. 1 is a schematic sectional view of a gas supply device according to an embodiment of the present invention, FIG. 2 is a partially sectional side view of a membrane module of the same device, and FIG. 3 is a perspective view of a membrane cell of the same device. . 12 ++w+a gas selective polymer membrane, 18...
, Vacuum pump, 21 , Atmospheric mixing port, 22
, , , , Mixed flow control valve. Name of agent: Patent attorney Toshio Nakao and 1 other person 2nd
Figure @3 figure
Claims (1)
吸気し、必要成分を選択透過して選択成分濃度の高まっ
た気体を供給する気体供給装置において、気体選択性高
分子膜を透過し、真空ポンプに吸引される吸引回路の途
中に混合流量調節弁を有した大気混合口を設け、選択成
分濃度の調節を行なわせることを特徴とする気体選択性
高分子膜を利用した気体供給装置。A gas supply device that sucks gas through a gas-selective polymer membrane using the suction force of a vacuum pump, selectively permeates necessary components, and supplies gas with an increased concentration of selected components. , a gas supply device using a gas-selective polymer membrane, characterized in that an air mixing port having a mixing flow rate control valve is provided in the middle of a suction circuit sucked by a vacuum pump to adjust the concentration of selected components. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9947081A JPS58222A (en) | 1981-06-25 | 1981-06-25 | Gas supply device utilizing gas-selective high-polymer film |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9947081A JPS58222A (en) | 1981-06-25 | 1981-06-25 | Gas supply device utilizing gas-selective high-polymer film |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58222A true JPS58222A (en) | 1983-01-05 |
Family
ID=14248194
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9947081A Pending JPS58222A (en) | 1981-06-25 | 1981-06-25 | Gas supply device utilizing gas-selective high-polymer film |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58222A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02121750A (en) * | 1987-10-30 | 1990-05-09 | Daimler Benz Ag | Hardening method for moulding formed by sand mould |
-
1981
- 1981-06-25 JP JP9947081A patent/JPS58222A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02121750A (en) * | 1987-10-30 | 1990-05-09 | Daimler Benz Ag | Hardening method for moulding formed by sand mould |
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