FR2222134A1 - Appts for permeation through hollow fibres - allows simple construction and efficient separation and mixing processes - Google Patents
Appts for permeation through hollow fibres - allows simple construction and efficient separation and mixing processesInfo
- Publication number
- FR2222134A1 FR2222134A1 FR7309752A FR7309752A FR2222134A1 FR 2222134 A1 FR2222134 A1 FR 2222134A1 FR 7309752 A FR7309752 A FR 7309752A FR 7309752 A FR7309752 A FR 7309752A FR 2222134 A1 FR2222134 A1 FR 2222134A1
- Authority
- FR
- France
- Prior art keywords
- shell
- hollow fibres
- discs
- appts
- end plates
- 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.)
- Granted
Links
- 238000000926 separation method Methods 0.000 title abstract 3
- 238000000034 method Methods 0.000 title abstract 2
- 238000010276 construction Methods 0.000 title 1
- 239000012530 fluid Substances 0.000 abstract 5
- 239000012466 permeate Substances 0.000 abstract 4
- 239000004744 fabric Substances 0.000 abstract 1
- 238000001223 reverse osmosis Methods 0.000 abstract 1
- 238000000108 ultra-filtration Methods 0.000 abstract 1
- 238000009834 vaporization Methods 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/02—Hollow fibre modules
- B01D63/021—Manufacturing thereof
- B01D63/0232—Manufacturing thereof using hollow fibers mats as precursor, e.g. wound or pleated mats
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/02—Hollow fibre modules
- B01D63/026—Wafer type modules or flat-surface type modules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/02—Hollow fibre modules
- B01D63/04—Hollow fibre modules comprising multiple hollow fibre assemblies
- B01D63/043—Hollow fibre modules comprising multiple hollow fibre assemblies with separate tube sheets
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Appts. for sepn. or mixing of fluids consists of a stack of discs in a shell. The discs are made of hollow fibres, woven into a fabric, mounted in a frame so that the ends of the fibres emerge at its outer circumference. The discs are stacked and the stack is enclosed between perforated end plates and surrounded by a porous casing. The whole is fitted into the shell so that there is a space between the porous casing and the wall of the shell. The end plates of the shell have feed and discharge nozzles respectively and the bear on to the perforated end plates of thestack and are held tight by bolts drawing them together. There is a permeate nozzle in the shell wall. In separation processes, feed fluid flows perpendicularly across the discs and permeate flows through the walls of the hollow fibres and out across the porous casing and through the permeate nozzle. In mixing processes one fluid enters through the permeate nozzle, flows across the walls of the hollow fibres and mixes with the other fluid outside them. Separation processes envisaged are ultra-filtration, reverse osmosis gaseous permeation. Mixing operations are solution of gas in liq. vaporisation into gas. The appts. is simple to make and ensures good contact between circulating fluid and hollow fibres.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7309752A FR2222134A1 (en) | 1973-03-19 | 1973-03-19 | Appts for permeation through hollow fibres - allows simple construction and efficient separation and mixing processes |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7309752A FR2222134A1 (en) | 1973-03-19 | 1973-03-19 | Appts for permeation through hollow fibres - allows simple construction and efficient separation and mixing processes |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2222134A1 true FR2222134A1 (en) | 1974-10-18 |
FR2222134B1 FR2222134B1 (en) | 1975-10-31 |
Family
ID=9116502
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR7309752A Granted FR2222134A1 (en) | 1973-03-19 | 1973-03-19 | Appts for permeation through hollow fibres - allows simple construction and efficient separation and mixing processes |
Country Status (1)
Country | Link |
---|---|
FR (1) | FR2222134A1 (en) |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4231879A (en) * | 1977-10-17 | 1980-11-04 | Gambro Dialysatoren Gmbh & Co. Kg | Apparatus for selective separation of matter through semi-permeable membranes |
US4261829A (en) * | 1977-10-17 | 1981-04-14 | Gambro Dialysatoren Gmbh & Co. Kg | Apparatus for selective separation of matter through semi-permeable membranes |
DE3508382A1 (en) * | 1985-03-08 | 1986-09-11 | Akzo Gmbh, 5600 Wuppertal | DEVICE FOR THE TRANSFER OF HEAT AND / OR FABRIC WITH THE AID OF CAVE THREADS |
EP0160268A3 (en) * | 1984-04-24 | 1987-10-21 | Mitsubishi Rayon Co. Ltd. | Blood oxygenator using a hollow-fiber membrane |
DE3823858A1 (en) * | 1988-07-14 | 1990-02-22 | Akzo Gmbh | METHOD AND DEVICE FOR FILTERING GASEOUS OR LIQUID DISPERSIONS |
DE3839567A1 (en) * | 1988-11-24 | 1990-06-07 | Akzo Gmbh | HOLLOW THREAD MODULE FOR SEPARATING GAS |
US4959152A (en) * | 1989-03-24 | 1990-09-25 | The Standard Oil Company | Hollow fiber separation module and method for the use thereof |
EP0374873A3 (en) * | 1988-12-20 | 1991-01-23 | The Dow Chemical Company | Efficient vapor- liquid mass transfer by microporous membrane fibers |
EP0443206A3 (en) * | 1990-02-17 | 1991-10-02 | Akzo N.V. | Process for preparing hollow filament stacks |
EP0464945A1 (en) * | 1990-07-03 | 1992-01-08 | Shell Internationale Researchmaatschappij B.V. | Counter-current flow membrane module for liquid separations |
US5100556A (en) * | 1989-07-21 | 1992-03-31 | The Standard Oil Company | Transverse sheet membrane separation module, components thereof and related methods |
US5164081A (en) * | 1989-03-24 | 1992-11-17 | The Standard Oil Company | Apparatus for separation and for treatment of fluid feedstreams, wafers for use therein and related methods |
US5174900A (en) * | 1989-03-24 | 1992-12-29 | The Standard Oil Company | Apparatus for separation and for treatment of fluid feedstreams, wafers for use therein and related methods |
DE4308697A1 (en) * | 1993-03-18 | 1994-09-22 | Durst Franz Prof Dr Dr H C | Process for enriching a first gaseous or liquid medium with a second gas or a second liquid and a reactor for carrying out the process |
US5747138A (en) * | 1995-11-30 | 1998-05-05 | Minnesota Mining And Manufacturing Company | Multilayer hollow-fiber body and method of making |
EP1360984A3 (en) * | 2002-05-07 | 2004-06-23 | Gkss-Forschungszentrum Geesthacht Gmbh | Apparatus for separating a component from a gas mixture or a liquid mixture |
WO2006081059A2 (en) | 2005-01-26 | 2006-08-03 | Celgard Llc | Hollow fiber module |
EP2296792A4 (en) * | 2008-06-05 | 2012-08-15 | Celgard Llc | A wafer-shaped hollow fiber module for in-line use in a piping system |
-
1973
- 1973-03-19 FR FR7309752A patent/FR2222134A1/en active Granted
Non-Patent Citations (1)
Title |
---|
NEANT * |
Cited By (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4231879A (en) * | 1977-10-17 | 1980-11-04 | Gambro Dialysatoren Gmbh & Co. Kg | Apparatus for selective separation of matter through semi-permeable membranes |
US4261829A (en) * | 1977-10-17 | 1981-04-14 | Gambro Dialysatoren Gmbh & Co. Kg | Apparatus for selective separation of matter through semi-permeable membranes |
EP0160268A3 (en) * | 1984-04-24 | 1987-10-21 | Mitsubishi Rayon Co. Ltd. | Blood oxygenator using a hollow-fiber membrane |
DE3508382A1 (en) * | 1985-03-08 | 1986-09-11 | Akzo Gmbh, 5600 Wuppertal | DEVICE FOR THE TRANSFER OF HEAT AND / OR FABRIC WITH THE AID OF CAVE THREADS |
DE3823858A1 (en) * | 1988-07-14 | 1990-02-22 | Akzo Gmbh | METHOD AND DEVICE FOR FILTERING GASEOUS OR LIQUID DISPERSIONS |
DE3839567A1 (en) * | 1988-11-24 | 1990-06-07 | Akzo Gmbh | HOLLOW THREAD MODULE FOR SEPARATING GAS |
EP0374873A3 (en) * | 1988-12-20 | 1991-01-23 | The Dow Chemical Company | Efficient vapor- liquid mass transfer by microporous membrane fibers |
US4959152A (en) * | 1989-03-24 | 1990-09-25 | The Standard Oil Company | Hollow fiber separation module and method for the use thereof |
US5174900A (en) * | 1989-03-24 | 1992-12-29 | The Standard Oil Company | Apparatus for separation and for treatment of fluid feedstreams, wafers for use therein and related methods |
EP0454918A1 (en) * | 1989-03-24 | 1991-11-06 | The Standard Oil Company | Hollow fibre separation module and method for the use thereof |
US5164081A (en) * | 1989-03-24 | 1992-11-17 | The Standard Oil Company | Apparatus for separation and for treatment of fluid feedstreams, wafers for use therein and related methods |
US5100556A (en) * | 1989-07-21 | 1992-03-31 | The Standard Oil Company | Transverse sheet membrane separation module, components thereof and related methods |
US5126053A (en) * | 1990-02-17 | 1992-06-30 | Akzo N.V. | Method for manufacturing hollow fiber piles |
EP0443206A3 (en) * | 1990-02-17 | 1991-10-02 | Akzo N.V. | Process for preparing hollow filament stacks |
US5143613A (en) * | 1990-07-03 | 1992-09-01 | Shell Oil Company | Counter-current membrane module for liquid separation |
EP0464945A1 (en) * | 1990-07-03 | 1992-01-08 | Shell Internationale Researchmaatschappij B.V. | Counter-current flow membrane module for liquid separations |
DE4308697A1 (en) * | 1993-03-18 | 1994-09-22 | Durst Franz Prof Dr Dr H C | Process for enriching a first gaseous or liquid medium with a second gas or a second liquid and a reactor for carrying out the process |
US5747138A (en) * | 1995-11-30 | 1998-05-05 | Minnesota Mining And Manufacturing Company | Multilayer hollow-fiber body and method of making |
US5888611A (en) * | 1995-11-30 | 1999-03-30 | Leonard; Ronald J. | Multilayer hollow fiber body and method of making |
EP1360984A3 (en) * | 2002-05-07 | 2004-06-23 | Gkss-Forschungszentrum Geesthacht Gmbh | Apparatus for separating a component from a gas mixture or a liquid mixture |
WO2006081059A2 (en) | 2005-01-26 | 2006-08-03 | Celgard Llc | Hollow fiber module |
CN101287539A (en) * | 2005-01-26 | 2008-10-15 | 赛尔格有限责任公司 | Hollow fiber module |
EP1850949A4 (en) * | 2005-01-26 | 2009-09-02 | Celgard Llc | Hollow fiber module |
US7628916B2 (en) | 2005-01-26 | 2009-12-08 | Celgard Llc | Hollow fiber module |
EP2296792A4 (en) * | 2008-06-05 | 2012-08-15 | Celgard Llc | A wafer-shaped hollow fiber module for in-line use in a piping system |
Also Published As
Publication number | Publication date |
---|---|
FR2222134B1 (en) | 1975-10-31 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
ST | Notification of lapse |