JPS56136605A - Selective gas permeable membrane cell - Google Patents
Selective gas permeable membrane cellInfo
- Publication number
- JPS56136605A JPS56136605A JP3930380A JP3930380A JPS56136605A JP S56136605 A JPS56136605 A JP S56136605A JP 3930380 A JP3930380 A JP 3930380A JP 3930380 A JP3930380 A JP 3930380A JP S56136605 A JPS56136605 A JP S56136605A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- port
- vanes
- membranes
- chamber
- 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
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
PURPOSE: To decrease boundary layers and the use amount of unpermeated gas and obtain the intended rich gas efficiently by providing freely turnable vanes in the space between permeable membrane cells in order to decrease the flow speed of inflow gas and increasing the flow speed of the internal gas.
CONSTITUTION: Plural sheets of the vane units which are mounted to rotating shafts 21 and consist of the vanes 23 reinforced with frames 22 and the cell units 20 of which the take-out ports 25 are mounted to the side faces of doughnut- shaped permeable gas chambers 26 consisting of selective gas permeable membranes 24 on both sides are laminated by maintaining spaces. This cell constitution is provided in an unpermeated gas chamber 27 and if mixed gases are introduced through a lead-in port 29 by rotating the vanes 23 with a motor 28, the gases pass through the surfaces of the membranes 24 from, for example, the outer side, go toward the center and flow upward and downward along the shafts 21. On the other hand, the gases permeate through the membranes 24 from the chamber 27 on account of the pressure difference between the rooms 26, 27 and enter the chamber 26 as the rich gas. This gas is taken out through a lead-out port 31 past the port 25. Here, the velocity of flow on the membrane surfaces is made higher than the flow speed from the port 29 to the port 30.
COPYRIGHT: (C)1981,JPO&Japio
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3930380A JPS56136605A (en) | 1980-03-26 | 1980-03-26 | Selective gas permeable membrane cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3930380A JPS56136605A (en) | 1980-03-26 | 1980-03-26 | Selective gas permeable membrane cell |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS56136605A true JPS56136605A (en) | 1981-10-26 |
Family
ID=12549345
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3930380A Pending JPS56136605A (en) | 1980-03-26 | 1980-03-26 | Selective gas permeable membrane cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56136605A (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7833314B2 (en) * | 2008-04-30 | 2010-11-16 | Praxair Technology, Inc. | Purification method and junction for related apparatus |
| US9611144B2 (en) | 2013-04-26 | 2017-04-04 | Praxair Technology, Inc. | Method and system for producing a synthesis gas in an oxygen transport membrane based reforming system that is free of metal dusting corrosion |
| US9776153B2 (en) | 2013-10-07 | 2017-10-03 | Praxair Technology, Inc. | Ceramic oxygen transport membrane array reactor and reforming method |
| US9839899B2 (en) | 2013-04-26 | 2017-12-12 | Praxair Technology, Inc. | Method and system for producing methanol using an integrated oxygen transport membrane based reforming system |
| US9938145B2 (en) | 2013-04-26 | 2018-04-10 | Praxair Technology, Inc. | Method and system for adjusting synthesis gas module in an oxygen transport membrane based reforming system |
| US9938146B2 (en) | 2015-12-28 | 2018-04-10 | Praxair Technology, Inc. | High aspect ratio catalytic reactor and catalyst inserts therefor |
| US9969645B2 (en) | 2012-12-19 | 2018-05-15 | Praxair Technology, Inc. | Method for sealing an oxygen transport membrane assembly |
| US10005664B2 (en) | 2013-04-26 | 2018-06-26 | Praxair Technology, Inc. | Method and system for producing a synthesis gas using an oxygen transport membrane based reforming system with secondary reforming and auxiliary heat source |
| US10118823B2 (en) | 2015-12-15 | 2018-11-06 | Praxair Technology, Inc. | Method of thermally-stabilizing an oxygen transport membrane-based reforming system |
| US10441922B2 (en) | 2015-06-29 | 2019-10-15 | Praxair Technology, Inc. | Dual function composite oxygen transport membrane |
| US10822234B2 (en) | 2014-04-16 | 2020-11-03 | Praxair Technology, Inc. | Method and system for oxygen transport membrane enhanced integrated gasifier combined cycle (IGCC) |
| US11052353B2 (en) | 2016-04-01 | 2021-07-06 | Praxair Technology, Inc. | Catalyst-containing oxygen transport membrane |
| US11136238B2 (en) | 2018-05-21 | 2021-10-05 | Praxair Technology, Inc. | OTM syngas panel with gas heated reformer |
-
1980
- 1980-03-26 JP JP3930380A patent/JPS56136605A/en active Pending
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7883571B1 (en) * | 2008-04-30 | 2011-02-08 | Praxair Technology, Inc. | Purification method and junction for related apparatus |
| US7833314B2 (en) * | 2008-04-30 | 2010-11-16 | Praxair Technology, Inc. | Purification method and junction for related apparatus |
| US9969645B2 (en) | 2012-12-19 | 2018-05-15 | Praxair Technology, Inc. | Method for sealing an oxygen transport membrane assembly |
| US9611144B2 (en) | 2013-04-26 | 2017-04-04 | Praxair Technology, Inc. | Method and system for producing a synthesis gas in an oxygen transport membrane based reforming system that is free of metal dusting corrosion |
| US9839899B2 (en) | 2013-04-26 | 2017-12-12 | Praxair Technology, Inc. | Method and system for producing methanol using an integrated oxygen transport membrane based reforming system |
| US9938145B2 (en) | 2013-04-26 | 2018-04-10 | Praxair Technology, Inc. | Method and system for adjusting synthesis gas module in an oxygen transport membrane based reforming system |
| US10005664B2 (en) | 2013-04-26 | 2018-06-26 | Praxair Technology, Inc. | Method and system for producing a synthesis gas using an oxygen transport membrane based reforming system with secondary reforming and auxiliary heat source |
| US9776153B2 (en) | 2013-10-07 | 2017-10-03 | Praxair Technology, Inc. | Ceramic oxygen transport membrane array reactor and reforming method |
| US10822234B2 (en) | 2014-04-16 | 2020-11-03 | Praxair Technology, Inc. | Method and system for oxygen transport membrane enhanced integrated gasifier combined cycle (IGCC) |
| US10441922B2 (en) | 2015-06-29 | 2019-10-15 | Praxair Technology, Inc. | Dual function composite oxygen transport membrane |
| US10118823B2 (en) | 2015-12-15 | 2018-11-06 | Praxair Technology, Inc. | Method of thermally-stabilizing an oxygen transport membrane-based reforming system |
| US9938146B2 (en) | 2015-12-28 | 2018-04-10 | Praxair Technology, Inc. | High aspect ratio catalytic reactor and catalyst inserts therefor |
| US11052353B2 (en) | 2016-04-01 | 2021-07-06 | Praxair Technology, Inc. | Catalyst-containing oxygen transport membrane |
| US11136238B2 (en) | 2018-05-21 | 2021-10-05 | Praxair Technology, Inc. | OTM syngas panel with gas heated reformer |
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