JPH033425U - - Google Patents
Info
- Publication number
- JPH033425U JPH033425U JP6235489U JP6235489U JPH033425U JP H033425 U JPH033425 U JP H033425U JP 6235489 U JP6235489 U JP 6235489U JP 6235489 U JP6235489 U JP 6235489U JP H033425 U JPH033425 U JP H033425U
- Authority
- JP
- Japan
- Prior art keywords
- separation
- gas
- pressure
- agent
- cylinder
- 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
- 238000000926 separation method Methods 0.000 claims description 23
- 239000007789 gas Substances 0.000 claims 11
- 239000003795 chemical substances by application Substances 0.000 claims 4
- 238000007599 discharging Methods 0.000 claims 2
- 238000005429 filling process Methods 0.000 claims 2
- 238000000034 method Methods 0.000 claims 2
- 230000008929 regeneration Effects 0.000 claims 2
- 238000011069 regeneration method Methods 0.000 claims 2
- 239000002250 absorbent Substances 0.000 claims 1
- 230000002745 absorbent Effects 0.000 claims 1
- 239000003463 adsorbent Substances 0.000 claims 1
- 238000010586 diagram Methods 0.000 description 2
Landscapes
- Separation Of Gases By Adsorption (AREA)
- Drying Of Gases (AREA)
Description
第１図は本考案の一実施例を適用した除湿装置
のシステム構成図、第２図はそのタイムチヤート
、第３図乃至第７図はその作動説明図であり、第
８図は他の実施例のシステム構成図である。
１ａ〜１ｃ：分離筒、５ａ〜５ｃ，６ａ〜６ｃ
，７ａ〜７ｃ，８ａ〜８ｃ，９ａ〜９ｃ，３１ａ
〜３１ｃ：開閉弁、１１：供給口、、１３：吐出
口、１５ａ〜１５ｃ：チエツク弁付絞り弁、１９
：絞り弁、２１：排気口、２２ａ〜２２ｃ：絞り
弁、３２ａ〜３２ｃ：絞り弁。
Fig. 1 is a system configuration diagram of a dehumidifying device to which an embodiment of the present invention is applied, Fig. 2 is a time chart thereof, Figs. FIG. 2 is an example system configuration diagram. 1a-1c: Separation tube, 5a-5c, 6a-6c
, 7a-7c, 8a-8c, 9a-9c, 31a
~31c: Open/close valve, 11: Supply port, 13: Discharge port, 15a~15c: Throttle valve with check valve, 19
: Throttle valve, 21: Exhaust port, 22a-22c: Throttle valve, 32a-32c: Throttle valve.
Claims (1)
筒を設け、該各分離筒が、該分離筒に分離すべき
１種または２種以上のガスの混入した混合ガスを
高圧で供給してそのガスを前記分離剤に吸着また
は吸収させることにより分離した処理済みガスを
吐出する分離工程と、該分離筒内のガスを絞り機
構を介して外部に排出して該分離筒内を低圧とす
る排気工程と、該分離筒内に分離工程にある他の
前記分離筒からの処理済みガスの一部を絞り機構
を介して減圧して供給して前記分離剤に吸着また
は吸収されていたガスを該分離剤から取り去つて
放出する再生工程と、該分離筒内に分離工程にあ
る他の前記分離筒からの処理済みガスの一部を絞
り機構を介して充填して該分離筒内を高圧とする
充填工程とを、一の前記分離筒の排気工程と充填
工程とが、他の２本の前記分離筒のいずれか一方
で分離工程を、他方で再生工程を行つている間に
行われるように、互いに位相をずらして順次に繰
り返す構成としたことを特徴とする混合ガス分離
装置。 Three separation cylinders filled with an adsorbent and an absorbent separation agent are provided, and each separation cylinder supplies a mixed gas containing one or more gases to be separated to the separation cylinder at high pressure. a separation step of discharging the separated treated gas by adsorbing or absorbing the gas in the separation agent; and a step of discharging the gas in the separation cylinder to the outside via a throttle mechanism to lower the pressure in the separation cylinder. A part of the treated gas from the other separation column in the separation process is reduced in pressure and supplied into the separation column through a throttle mechanism to remove the gas that has been adsorbed or absorbed by the separation agent. a regeneration step in which gas is removed from the separation agent and released; and a part of the treated gas from the other separation tubes in the separation step is filled into the separation tube through a throttle mechanism to fill the inside of the separation tube. The filling process in which the pressure is high is carried out while the exhausting process and filling process of one of the separation cylinders is being performed while the separation process is being performed in one of the other two separation cylinders and the regeneration process is being performed in the other. 1. A mixed gas separation device characterized in that the mixed gas separation device is configured to repeat the operations sequentially with mutually shifted phases, as shown in FIG.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6235489U JPH033425U (en) | 1989-05-29 | 1989-05-29 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6235489U JPH033425U (en) | 1989-05-29 | 1989-05-29 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH033425U true JPH033425U (en) | 1991-01-14 |
Family
ID=31591425
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6235489U Pending JPH033425U (en) | 1989-05-29 | 1989-05-29 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH033425U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2022090755A (en) * | 2020-12-08 | 2022-06-20 | 大陽日酸株式会社 | Gas adsorption and separation device |
-
1989
- 1989-05-29 JP JP6235489U patent/JPH033425U/ja active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2022090755A (en) * | 2020-12-08 | 2022-06-20 | 大陽日酸株式会社 | Gas adsorption and separation device |
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