JPS6351919A - Gas adsorption separating device - Google Patents
Gas adsorption separating deviceInfo
- Publication number
- JPS6351919A JPS6351919A JP61195606A JP19560686A JPS6351919A JP S6351919 A JPS6351919 A JP S6351919A JP 61195606 A JP61195606 A JP 61195606A JP 19560686 A JP19560686 A JP 19560686A JP S6351919 A JPS6351919 A JP S6351919A
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- selective adsorbent
- low
- storage container
- gas
- 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
- 238000001179 sorption measurement Methods 0.000 title claims description 20
- 239000003463 adsorbent Substances 0.000 claims abstract description 30
- 238000000926 separation method Methods 0.000 claims description 15
- 229910021536 Zeolite Inorganic materials 0.000 abstract description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 abstract description 2
- 239000010457 zeolite Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 38
- 238000009423 ventilation Methods 0.000 description 28
- 238000000034 method Methods 0.000 description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000000203 mixture Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
Landscapes
- Separation Of Gases By Adsorption (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は気体吸着分離装置、特に選択的吸着剤により
混合気体中の特定気体成分の濃度を高めるのに好適な気
体吸着分離装置に関するものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a gas adsorption separation device, particularly a gas adsorption separation device suitable for increasing the concentration of a specific gas component in a mixed gas using a selective adsorbent. be.
病院や研究所或は一般住居用ビルにおいても。 Also in hospitals, research institutes, and general residential buildings.
ビル全体を酸素富化空気環境とし、当該ビルでの勤務者
や居住者の生活環境を健康の面から改善しようとする試
みがなされている。Attempts have been made to provide an oxygen-enriched air environment to the entire building in order to improve the living environment of workers and residents in the building from a health perspective.
このために、当該ビルの空調設備に対し気体吸着分離装
置を取り付け、当該ビル内に送入される空気中の酸素濃
度を高めようとする方式が、例えば特開昭58−151
304号公報、特開昭58−135106号公報に開示
されている。For this purpose, a method has been proposed in which a gas adsorption separation device is attached to the air conditioning equipment of the building in order to increase the oxygen concentration in the air fed into the building.
This method is disclosed in Japanese Patent Application Laid-open No. 304 and Japanese Patent Application Laid-open No. 135106/1983.
これらに開示されている方式は、いずれも選択的吸着剤
が充填された固定円筒に混合気体を通過させ、固定円筒
の前後に弁が設けられ、これらの弁の操作によつ℃加圧
、吸着、均圧分離、減圧及び再生の各工程を行なわせる
ものである。従って固定円筒の前後に多数の弁が配設さ
れ、とわらの弁を顆次制御することが必要で、装置は大
規模なものとなる。In each of the methods disclosed in these documents, a mixed gas is passed through a fixed cylinder filled with a selective adsorbent, and valves are provided before and after the fixed cylinder, and by operating these valves, the gas mixture is pressurized by °C, Each step of adsorption, pressure equalization separation, depressurization and regeneration is carried out. Therefore, a large number of valves are arranged before and after the fixed cylinder, and it is necessary to control the valves condylarly, resulting in a large-scale device.
また、特開昭58−30322号公報には、ストローク
の異なる2個のピストンを使用して、固定円筒を通過す
る混合気体に対する加圧、減圧を行なわせて、固定円筒
を通過する混合気体に対して所定の気体成分濃度を高め
る方式が開示されている。In addition, Japanese Patent Application Laid-Open No. 58-30322 discloses that two pistons with different strokes are used to pressurize and depressurize a gas mixture passing through a fixed cylinder. On the other hand, a method of increasing the concentration of a predetermined gas component has been disclosed.
この方式では機械的な方向転換要素が多い構造となり、
装置全体が機構的に複雑となる。This method has a structure with many mechanical direction changing elements,
The entire device becomes mechanically complex.
特開昭58−151304号公報や特開昭58−135
106号公報に開示されている方式には、多数の制御弁
を用いるため装置が大規模となり、設備費用や維持管理
費用が増大し、比較的小規模な範囲での使用には適さな
いという難点がある。また、特開昭58−30322号
公報に開示されている方式は2機械的な方向転換要素が
多い複雑な構造となる難点がある。JP-A-58-151304 and JP-A-58-135
The method disclosed in Publication No. 106 has the disadvantage that it uses a large number of control valves, resulting in a large-scale device, increasing equipment costs and maintenance costs, and is not suitable for use in a relatively small scale. There is. Furthermore, the method disclosed in Japanese Patent Application Laid-Open No. 58-30322 has the disadvantage that it has a complicated structure with many two mechanical direction changing elements.
この発明は、前述のようなこの種の気体吸着分離装置の
現状に鑑入てなされたものであり、その目的は比較的簡
単な構成で小規模な範囲に対して適用可能な気体吸着分
離装置を提供することにある。This invention was made in consideration of the current state of gas adsorption separation devices of this type as described above, and its purpose is to provide a gas adsorption separation device that has a relatively simple configuration and is applicable to small-scale areas. Our goal is to provide the following.
前述の目的を達成するために、この発明の気体吸着分離
装置は、収納容器に選択的吸着剤が収容され、前記収納
容器に収容された選択的吸着剤に混合気体を通過させ、
前記混合気体中の特定気体成分の濃度を高める気体吸着
分離装置において。In order to achieve the above object, the gas adsorption separation device of the present invention includes a storage container containing a selective adsorbent, a mixed gas passing through the selective adsorption agent contained in the storage container,
In a gas adsorption separation device that increases the concentration of a specific gas component in the gas mixture.
高圧混合気体が流される高圧通気路と、低圧混合気体が
流される低圧通気路と1選択的吸着剤が収容される収納
容器と、前記選択的吸着剤を前記高圧通気路と、前記低
圧通気路と九交互に挿入するように、前記収納容器を駆
動する駆動手段とを有する構成とされている。a high-pressure ventilation passage through which a high-pressure mixed gas flows; a storage container in which a selective adsorbent is accommodated; and a driving means for driving the storage containers so that the storage containers are inserted alternately.
この発明の気体吸着分離装置では1選択的吸着剤が収容
された収納容器が、駆動手段により高圧混合気体が流さ
れる高圧通気路と、低圧混合気体が流される低圧通気路
とに交互に挿入される。このために、高圧混合気体中の
特定気体成分が選択的吸着剤に吸着され、高圧混合気体
中の他の特定気体取分濃度が高められた混合気体が、所
定の被供給領域に供給さねる。In the gas adsorption separation device of the present invention, storage containers containing one selective adsorbent are inserted alternately into a high-pressure ventilation path through which a high-pressure mixed gas is flowed and a low-pressure ventilation path through which a low-pressure mixed gas is flowed by a driving means. Ru. For this purpose, the specific gas component in the high-pressure mixed gas is adsorbed by the selective adsorbent, and the mixed gas in which the fractional concentration of other specific gases in the high-pressure mixed gas is increased is not supplied to a predetermined supply area. .
次いで駆動手段により、特定気体成分が吸着された選択
的吸着剤が低圧混合気体が流される低圧通気路に挿入さ
れ、吸着剤の再生が行なわれる。Next, the selective adsorbent on which the specific gas component has been adsorbed is inserted by the driving means into the low-pressure ventilation path through which the low-pressure mixed gas flows, and the adsorbent is regenerated.
このようにして、制御弁も少ない簡単な構成で。In this way, a simple configuration with fewer control valves is possible.
自動的に繰り返し工程が連続して行なわれる。The process is automatically repeated in succession.
以下、この発明の気体吸着分離装置を、その実施例に基
づき図面を使用して詳細に説明する。EMBODIMENT OF THE INVENTION Hereinafter, the gas adsorption separation apparatus of this invention will be explained in detail based on the embodiment using the drawings.
第1図はこの発明の実施例の構成を示す縦断面図で、第
2図は第1図の1−1矢視図、第3図は第1図の■−■
矢視図であり、高圧混合気体が流される高圧通気路2と
、低圧混合気体が流される低圧通気路3と1選択的吸着
剤が収容される収納容器4と1選択的吸着剤を高圧通気
路と低圧通気路とに交互に挿入するように収納容器4を
駆動する駆動手段8とで、この発明の気体吸着分離装置
が構成されている。FIG. 1 is a vertical cross-sectional view showing the configuration of an embodiment of the present invention, FIG. 2 is a view taken along arrows 1-1 in FIG. 1, and FIG.
This is a view from the direction of the arrow, showing a high-pressure ventilation passage 2 through which a high-pressure mixed gas flows, a low-pressure ventilation passage 3 through which a low-pressure mixed gas flows, a storage container 4 in which a selective adsorbent is accommodated, and a selective adsorption agent through high-pressure ventilation. The gas adsorption separation device of the present invention is constituted by a driving means 8 for driving the storage container 4 so as to be inserted alternately into the air passage and the low-pressure ventilation passage.
この発明の具体的構成を、実施例の製造工程に基づいて
説明する。A specific configuration of the present invention will be explained based on the manufacturing process of an embodiment.
実施例は駆動手段として回転枠体10を用いた例であり
1回転軸7を中心に回動自在に外形がほぼ円板状の回転
枠体10が形成される。回転枠体10には板面を貫通し
て1選択的吸着剤1が収容されろ収納容器4が複数個1
回転軸7に対して放射状に形成される。実施例では、各
収納容器4の断面は。In this embodiment, a rotating frame 10 is used as the driving means, and the rotating frame 10 is formed so as to be rotatable about the rotation axis 7 and has a substantially disk-shaped outer shape. The rotary frame body 10 has a plurality of storage containers 4 that penetrate through the plate surface and accommodate the selective adsorbent 1.
It is formed radially with respect to the rotating shaft 7. In the embodiment, the cross section of each storage container 4 is as follows.
角が丸められた台形状に形成される。It is formed into a trapezoid shape with rounded corners.
高圧通気管5及び低圧通気管6が、板面に直角に一体に
突出形成された蓋体11が形成され、この蓋体11が回
転軸7の廻りに1回転枠体10を挾持するようにして配
設される。この状態で、固定配設される二つの蓋体11
に挾まれて、回転枠体10は回転軸7を中心に回動自在
に取り付けられる。A lid 11 is formed in which the high-pressure ventilation pipe 5 and the low-pressure ventilation pipe 6 are integrally formed to protrude at right angles to the plate surface, and this lid 11 clamps the one-rotation frame 10 around the rotating shaft 7. It will be arranged as follows. In this state, the two lid bodies 11 fixedly disposed
The rotating frame body 10 is mounted so as to be rotatable about the rotating shaft 7.
蓋体11ICは回転軸7に対称に、それぞれ2個の:・
、収納容器4の開口を被う形状のカバー12が、高圧通
気管5及び低圧通気管6の配役位置に形成されている。The lid body 11IC has two pieces each symmetrically about the rotation axis 7:
A cover 12 shaped to cover the opening of the storage container 4 is formed at a position where the high pressure ventilation pipe 5 and the low pressure ventilation pipe 6 are arranged.
高圧通気管5の入口には、図示していない高圧発生装置
が接続され、この高圧発生装置で高圧化された高圧通気
、例えば1.2kV/crnGの高圧空気が流入可能に
設定される。高圧通気管5の出口は所定の被供給場所1
例えばビルの空調装置の入力側に接続される。低圧通気
管60入口には1例えば空調装置の0.7kV/cm
Gの低圧排気管が接続される。A high-pressure generator (not shown) is connected to the inlet of the high-pressure ventilation pipe 5, and is set to allow high-pressure ventilation, for example, high-pressure air of 1.2 kV/crnG, to flow in, which is increased in pressure by the high-pressure generator. The outlet of the high pressure ventilation pipe 5 is located at a predetermined supply location 1.
For example, it is connected to the input side of a building's air conditioner. At the inlet of the low-pressure ventilation pipe 60, for example, 0.7 kV/cm of an air conditioner.
G's low pressure exhaust pipe is connected.
回転枠体100回転軸7には図示していない駆動モータ
の回転軸に連結された伝達機構が接続され。A transmission mechanism connected to the rotation shaft of a drive motor (not shown) is connected to the rotation shaft 7 of the rotation frame 100.
回転枠体10は毎分1〜2回転の低回転速度で回転可能
に設定される。The rotating frame 10 is set to be rotatable at a low rotational speed of 1 to 2 revolutions per minute.
このように構成されたこの発明の気体吸着分離装置の動
作を説明する。The operation of the gas adsorption separation apparatus of the present invention configured as described above will be explained.
回転枠体10の各収納容器4に、所定量のゼオライトな
どの選択的吸着剤を充填し1回転枠体10は。Each storage container 4 of the rotating frame 10 is filled with a predetermined amount of selective adsorbent such as zeolite.
毎分1〜2回転程度の低回転速度で回転される。It rotates at a low rotation speed of about 1 to 2 revolutions per minute.
高圧通気管5の入口に、 1.2k)/ωGの高圧空気
を。High pressure air of 1.2k)/ωG is supplied to the inlet of the high pressure ventilation pipe 5.
また低圧通気管6の入口には、Q、7 kP/an”
Qの低圧排気を通気する。Also, at the entrance of the low pressure vent pipe 6, there is a pressure of Q, 7 kP/an”
Vent the low pressure exhaust of Q.
駆動手段を構成する回転枠体】0は低速度で回転し、こ
の回転に伴って収納容器4が低速度で高圧通気管5の高
圧通気路内に挿入さね、収納容器4内の選択的吸着剤1
に高圧空気が接触し、高圧空気中の凡を選択的吸着剤1
が選択的に吸着し、高圧通気管5の出口には、o1濃度
の高い空気が得られる。このような酸素富化空気が、空
調装置から該ビル内に供給され、該ビルの勤務者或は居
住者圧は健康の面から優れた環境が与えられる。The rotating frame 0 constituting the driving means rotates at a low speed, and as a result of this rotation, the storage container 4 is inserted at a low speed into the high-pressure ventilation path of the high-pressure ventilation pipe 5. Adsorbent 1
When high pressure air comes into contact with the
is selectively adsorbed, and air with a high o1 concentration is obtained at the outlet of the high-pressure ventilation pipe 5. Such oxygen-enriched air is supplied into the building from an air conditioner, and the building's employees or residents are provided with an environment that is excellent in terms of health.
N、を吸着した選択的吸着剤lは、収納容器4の移動と
共に高圧通気路外に位置し1回転枠体10の回転が進む
と低圧通気管6と対向する。この位置で収納容器4内の
選択的吸着剤lは、低圧通気管6の低圧通気路内に挿入
され1選択的板着剤1ONの放出即ち選択的吸着剤1の
再生が行なわれる。The selective adsorbent l adsorbing N is located outside the high-pressure ventilation path as the storage container 4 moves, and faces the low-pressure ventilation pipe 6 as the frame 10 rotates once. At this position, the selective adsorbent 1 in the storage container 4 is inserted into the low-pressure ventilation path of the low-pressure ventilation pipe 6, and the selective adsorbent 1ON is discharged, that is, the selective adsorbent 1 is regenerated.
第4図に示すように、圧力が増大すると選択的吸着剤1
へのN、の吸着量が、O!の吸着量に比して大幅に上昇
するので、高圧空気を選択的吸着剤1に接触させること
により、N1を多量に吸着させて放出空気のO1濃度を
大幅に高めることが出来る。As shown in Figure 4, as the pressure increases, the selective adsorbent 1
The adsorption amount of N is O! By bringing high-pressure air into contact with the selective adsorbent 1, a large amount of N1 can be adsorbed and the O1 concentration of the released air can be significantly increased.
また、空気圧を低下させるとほぼ直線的にN、の吸着量
が低下するので、N2を放出して選択的吸着剤lを回復
させることが出来る。Furthermore, since the amount of N adsorbed decreases almost linearly when the air pressure is lowered, the selective adsorbent 1 can be recovered by releasing N2.
このようにして、簡単な構成で運転操作も容易で1例え
ば空気中の酸素濃度を高めた混合気体が効率よく得られ
る。In this way, the configuration is simple, the operation is easy, and a mixed gas with an increased oxygen concentration in the air, for example, can be efficiently obtained.
第5図は収納容器の他の例の構成を示し、収納容器9は
両端面を開放面とした円筒状に形成されている。この収
納容器9は1例えば回転枠体に形成された収容孔に嵌合
されて使用される。FIG. 5 shows the structure of another example of the storage container 9, in which the storage container 9 is formed into a cylindrical shape with both ends open. This storage container 9 is used by being fitted into a storage hole formed in, for example, a rotating frame.
実施例では、駆動手段として回転枠体10を使用した場
合を説明したが1例えば第5図に示すような収納容器9
が直線往復運動をして、高圧通気路内と低圧通気路内に
顆次挿入されるような駆動手段とすることも出来る。In the embodiment, a case was explained in which a rotary frame body 10 was used as the driving means.1 For example, a storage container 9 as shown in FIG.
It is also possible to use a driving means that makes a linear reciprocating motion and is inserted condyle into the high-pressure air passage and the low-pressure air passage.
以上詳細に説明したように、この発明によると構造が簡
単且つ堅固であり、簡単な操作で駆動されて、混合気体
中から特定気体成分を高い効率で吸収し、他の特定気体
成分濃度の高い混合気体を小規模な設備でも効率的に得
ることが可能な、気体吸着分離装置を提供することがで
きる。As explained in detail above, according to the present invention, the structure is simple and strong, and it is driven by simple operation, absorbs a specific gas component from a mixed gas with high efficiency, and absorbs a high concentration of other specific gas components. It is possible to provide a gas adsorption separation device that can efficiently obtain a mixed gas even with small-scale equipment.
第1図はこの発明の実施例の構成を示す縦断面図、第2
図は第1図の1−1矢視図、第3図は第1図の■−■矢
視図、第4図は窒素及び酸素に対する圧力と吸着量との
関係を示す図、第5図は収納容器の他の形状を示す斜視
Vである。
1・・・・・・選択的吸着剤、2・・・・・・高圧通気
路、3・・・・・・低圧通気路、4・・・・・・収納容
器、5・・・・・・高圧通気管、6・・・・・・低圧通
気管、7・・・・・・回転軸、8・・・・・・駆動手段
、10・・・・・・回転枠体、 11・・・・・・蓋体
、 12・・・・・・カバー。
第1図
第3図Fig. 1 is a vertical sectional view showing the configuration of an embodiment of the present invention;
The figure is a 1-1 arrow view in Figure 1, Figure 3 is a ■-■ arrow view in Figure 1, Figure 4 is a diagram showing the relationship between pressure and adsorption amount for nitrogen and oxygen, and Figure 5 is a perspective view V showing another shape of the storage container. 1... Selective adsorbent, 2... High pressure ventilation path, 3... Low pressure ventilation path, 4... Storage container, 5... - High pressure ventilation pipe, 6... Low pressure ventilation pipe, 7... Rotating shaft, 8... Drive means, 10... Rotating frame, 11... ...Lid body, 12...Cover. Figure 1 Figure 3
Claims (1)
容された選択的吸着剤に混合気体を通過させ、前記混合
気体中の特定気体成分の濃度を高める気体吸着分離装置
において、高圧混合気体が流される高圧通気路と、低圧
混合気体が流される低圧通気路と、選択的吸着剤が収容
される収納容器と、前記選択的吸着剤を前記高圧通気路
と前記低圧通気路とに交互に挿入するように、前記収納
容器を駆動する駆動手段とを有することを特徴とする気
体吸着分離装置。A gas adsorption separation device in which a selective adsorbent is accommodated in a storage container, and a mixed gas is passed through the selective adsorbent accommodated in the storage container to increase the concentration of a specific gas component in the mixed gas. a high-pressure air passage through which a gas is flowed, a low-pressure air passage through which a low-pressure mixed gas is flowed, a storage container in which a selective adsorbent is stored, and the selective adsorbent is alternately distributed between the high-pressure air passage and the low-pressure air passage. A gas adsorption/separation device comprising a driving means for driving the storage container so as to insert the storage container.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61195606A JPS6351919A (en) | 1986-08-22 | 1986-08-22 | Gas adsorption separating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61195606A JPS6351919A (en) | 1986-08-22 | 1986-08-22 | Gas adsorption separating device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6351919A true JPS6351919A (en) | 1988-03-05 |
Family
ID=16343954
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61195606A Pending JPS6351919A (en) | 1986-08-22 | 1986-08-22 | Gas adsorption separating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6351919A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6361585B1 (en) * | 1999-09-06 | 2002-03-26 | Fujitsu Limited | Rotor-type dehumidifier, starting method for rotor-type dehumidifier and an electronic device mounting the rotor-type dehumidifier |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5615820A (en) * | 1979-07-20 | 1981-02-16 | Nippon Steel Corp | Separator for mixed gases |
JPS57190640A (en) * | 1981-05-18 | 1982-11-24 | Hitachi Zosen Corp | Denitrating reaction apparatus |
-
1986
- 1986-08-22 JP JP61195606A patent/JPS6351919A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5615820A (en) * | 1979-07-20 | 1981-02-16 | Nippon Steel Corp | Separator for mixed gases |
JPS57190640A (en) * | 1981-05-18 | 1982-11-24 | Hitachi Zosen Corp | Denitrating reaction apparatus |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6361585B1 (en) * | 1999-09-06 | 2002-03-26 | Fujitsu Limited | Rotor-type dehumidifier, starting method for rotor-type dehumidifier and an electronic device mounting the rotor-type dehumidifier |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP3725391B1 (en) | High troughput direct air capture device for capturing co2 from air and method of its operation | |
ES2295503T3 (en) | ADSORTION SYSTEM BY PRESSURE CHANGE FOR GAS SEPARATION. | |
US5891217A (en) | Process and apparatus for gas separation | |
AU710281B2 (en) | Device and process for separating gases by adsorption | |
US5807423A (en) | Process and apparatus for gas separation | |
US5827358A (en) | Rapid cycle pressure swing adsorption oxygen concentration method and apparatus | |
US6500236B2 (en) | Method for decarbonating waste gas and decarbonating apparatus | |
CN1231282C (en) | Low air-gap adsorption system and its application | |
JP3312055B2 (en) | Rotary adsorption / desorption type gas processing equipment | |
EP0368435A3 (en) | Dehumidified air generator employing adsorbent | |
JPH0339729B2 (en) | ||
EP0853967A2 (en) | Valve apparatus for gas separation and adsorption system | |
JP4477630B2 (en) | Air storage slide valve | |
WO2023247482A1 (en) | Direct air capture device | |
CN216654003U (en) | Zeolite runner adsorbs concentrated purifier | |
JP5184850B2 (en) | Gas separator, oxygen concentrator and exercise bike | |
JPS6351919A (en) | Gas adsorption separating device | |
JP4040581B2 (en) | Vacuum-pressurized pressure fluctuation adsorption type oxygen concentrator | |
US4761236A (en) | Coordinated sorptive strand contactor | |
JP3269626B2 (en) | Improved fluid separation device and method | |
KR20180129218A (en) | Method for adsorpting and concentrating toxic compound | |
JP2948367B2 (en) | Gas separation equipment | |
KR102716777B1 (en) | Portable oxygen generator by pressure swing adsorption | |
CN217549421U (en) | Nitrogen-oxygen separation tower for oxygenerator | |
JPS61209025A (en) | Gas adsorbing and separation apparatus |