JPS54138868A - Mixed gas separating and refining apparatus - Google Patents
Mixed gas separating and refining apparatusInfo
- Publication number
- JPS54138868A JPS54138868A JP4644578A JP4644578A JPS54138868A JP S54138868 A JPS54138868 A JP S54138868A JP 4644578 A JP4644578 A JP 4644578A JP 4644578 A JP4644578 A JP 4644578A JP S54138868 A JPS54138868 A JP S54138868A
- Authority
- JP
- Japan
- Prior art keywords
- adsorbent
- room
- fluid
- adsorption
- component
- 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
Abstract
PURPOSE: To eliminate the adsorbent inactive part as usual method and to miniaturize the apparatus and also, to enable to reduce separating and refining cost, by flowing all sorts of fluid countercurrent in rotating direction of adsorption room member, at the rotary type mixed gas separating apparatus.
CONSTITUTION: The adsorption rooms 6aW6l packed the adsorbent selectively adsorbing at least one component in mixed gas containing more than two components, are provided with the rotating body 6 and the partition boards 18 are provided between each room and then, the body 6 is rotated in the arrow mark direction. The one side opened rooms 4aW4l selectively charging and discharging all sorts of fluid, are provided with the fixed body 4. The raw material gas A is supplied to the room 4l and easy adsorptive component is adsorbed on the adsorbent and also, difficult adsorptive component is taken out as the product B. Next, the fluid E for regeneration is supplied from the room 4e and the adsorbent is regenerated and then, the fluid E is discharged with desorbed component from F. Also, the gas C for exhaust is supplied from the room 4g and remaining fluid e is discharged from D and then, the above mentioned adsorption, regeneration and exhaust, are repeated. Thus, defect of usual method such as transferring the adsorption band for outlet side, is eliminated and the adsorbent is utilized effectively. Also, the apparatus is made compact and cost is reduced.
COPYRIGHT: (C)1979,JPO&Japio
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4644578A JPS54138868A (en) | 1978-04-21 | 1978-04-21 | Mixed gas separating and refining apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4644578A JPS54138868A (en) | 1978-04-21 | 1978-04-21 | Mixed gas separating and refining apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS54138868A true JPS54138868A (en) | 1979-10-27 |
Family
ID=12747355
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4644578A Pending JPS54138868A (en) | 1978-04-21 | 1978-04-21 | Mixed gas separating and refining apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS54138868A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5487775A (en) * | 1994-05-09 | 1996-01-30 | The Boc Group, Inc. | Continuous pressure difference driven adsorption process |
| CN113144810A (en) * | 2020-01-07 | 2021-07-23 | 万华化学集团股份有限公司 | Mixed exhaust separation equipment and separation method of diisocyanate product containing light components |
-
1978
- 1978-04-21 JP JP4644578A patent/JPS54138868A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5487775A (en) * | 1994-05-09 | 1996-01-30 | The Boc Group, Inc. | Continuous pressure difference driven adsorption process |
| CN113144810A (en) * | 2020-01-07 | 2021-07-23 | 万华化学集团股份有限公司 | Mixed exhaust separation equipment and separation method of diisocyanate product containing light components |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5198001A (en) | Apparatus and process for removing organic compounds from a gas stream | |
| ZA862098B (en) | Pressure swing adsorption process and apparatus | |
| AU5212079A (en) | Adsorbent fractionator flow control system | |
| EP0391718A3 (en) | Heaterless adsorption system for combined purification and fractionation of air | |
| EP0205709A3 (en) | Process for enriching a component gas | |
| GB1234862A (en) | Separating gas mixtures by selective absorption in liquids | |
| JPS5678615A (en) | Adsorption type gas refining method and its appratus utilizing pressure difference | |
| EP0004465A3 (en) | Method of regenerating adsorbents | |
| KR880003662A (en) | Continuous removal of sulfur from fuel gas | |
| JPS54138868A (en) | Mixed gas separating and refining apparatus | |
| JPS57183304A (en) | Ozonizer | |
| JPS54145372A (en) | Continuous adsorption and desorption device | |
| US3847572A (en) | Apparatus for desulfurizing flue gas | |
| JPS56111021A (en) | Dry type exhaust gas desulfurizing apparatus | |
| JPS54138869A (en) | Gas separating and refining apparatus | |
| GB2135899B (en) | Apparatus for adsorbing adsorbable constituents in a fluid stream | |
| JPS54125180A (en) | Gas separation purifying method | |
| JPS5395872A (en) | Treating method for tail gas | |
| JPS5458681A (en) | Treating apparatus for malodor | |
| JPS56136621A (en) | Desulfurizer of waste gas | |
| JPS56136622A (en) | Stack gas desulfurizer | |
| JPS57175702A (en) | Method and apparatus for separating oxygen from air | |
| JPS55139829A (en) | Orthogonal flow type gas-solid contact apparatus | |
| JPS5597206A (en) | Adsorption-separator | |
| JPS55132618A (en) | Separator for gas component |