SE8904133A - - Google Patents
Info
- Publication number
- SE8904133A SE8904133A SE8904133A SE8904133A SE8904133A SE 8904133 A SE8904133 A SE 8904133A SE 8904133 A SE8904133 A SE 8904133A SE 8904133 A SE8904133 A SE 8904133A SE 8904133 A SE8904133 A SE 8904133A
- Authority
- SE
- Sweden
- Prior art keywords
- hollow fibres
- filter
- liquid
- permeate
- exterior
- Prior art date
Links
- 239000007788 liquid Substances 0.000 abstract 4
- 239000012466 permeate Substances 0.000 abstract 3
- 238000001914 filtration Methods 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
Classifications
-
- 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
- B01D63/0233—Manufacturing thereof forming the bundle
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/18—Apparatus therefor
-
- 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
- B01D63/024—Hollow fibre modules with a single potted end
-
- 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
- B01D63/024—Hollow fibre modules with a single potted end
- B01D63/0241—Hollow fibre modules with a single potted end being U-shaped
-
- 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
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/48—Biological material, e.g. blood, urine; Haemocytometers
- G01N33/483—Physical analysis of biological material
- G01N33/487—Physical analysis of biological material of liquid biological material
- G01N33/49—Blood
- G01N33/491—Blood by separating the blood components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/16—Specific vents
Abstract
A disposable filter comprises a bundle of hollow fibres arranged in a housing having an inlet for a particle-laden volume of liquid to be filtered, as well as an outlet or a collecting chamber for the permeate. The inlet communicates with the interior of the hollow fibres, and the outlet or collecting chamber communicates with the exterior thereof. Before the filter is used, the moisture content of the hollow fibres is below 0.1 %, preferably below 0.05 %. In a separation method for removing particles from a particle-laden volume of liquid by means of such a filter, a pressure difference is generated between the interior and the exterior of the hollow fibres when the liquid is supplied to the filter, thus increasing the yield of permeate and reducing the filtering time. The total area of the hollow fibres is dimensioned such that a major part of the maximum permeate volume available can be obtained when the liquid flows once along the entire length of the hollow fibres, so that the filter can be discarded after a single use.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE8904133A SE465355B (en) | 1989-12-07 | 1989-12-07 | DISPOSABLE AND PROCEDURE FOR FILTERING OF A PARTICULATED WATER VOLUME |
PCT/SE1990/000811 WO1991008782A1 (en) | 1989-12-07 | 1990-12-07 | Disposable filter and separation method using this filter |
AU69553/91A AU6955391A (en) | 1989-12-07 | 1990-12-07 | Disposable filter and separation method using this filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE8904133A SE465355B (en) | 1989-12-07 | 1989-12-07 | DISPOSABLE AND PROCEDURE FOR FILTERING OF A PARTICULATED WATER VOLUME |
Publications (3)
Publication Number | Publication Date |
---|---|
SE8904133D0 SE8904133D0 (en) | 1989-12-07 |
SE8904133A true SE8904133A (en) | 1991-06-08 |
SE465355B SE465355B (en) | 1991-09-02 |
Family
ID=20377713
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE8904133A SE465355B (en) | 1989-12-07 | 1989-12-07 | DISPOSABLE AND PROCEDURE FOR FILTERING OF A PARTICULATED WATER VOLUME |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU6955391A (en) |
SE (1) | SE465355B (en) |
WO (1) | WO1991008782A1 (en) |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2713091B1 (en) * | 1993-12-06 | 1996-02-09 | Hemodia Sa | Method and device for measuring the concentration of at least one substance contained in a complex medium. |
GB9426251D0 (en) * | 1994-12-24 | 1995-02-22 | Fsm Technologies Ltd | Device |
AU4657696A (en) * | 1995-01-25 | 1996-08-14 | Therakos, Inc. | Disposable hemolysis detector |
US6936473B2 (en) | 2000-01-05 | 2005-08-30 | Leisure, Inc. | Method of preparing a biological sample for quantification |
US6406672B1 (en) * | 2000-01-28 | 2002-06-18 | Roche Diagnostics | Plasma retention structure providing internal flow |
AUPR064800A0 (en) * | 2000-10-09 | 2000-11-02 | Usf Filtration And Separations Group Inc. | Improved membrane filtration system |
DE60116723T2 (en) * | 2001-01-05 | 2006-10-26 | Leisure, Inc. | Apparatus and method for blood separation and preparation method, quantification method and preservation container for a biological sample |
AU2006284524B2 (en) * | 2005-08-22 | 2011-04-21 | Evoqua Water Technologies Llc | An assembly for water filtration using a tube manifold to minimise backwash |
SG140229A1 (en) * | 2005-08-22 | 2008-03-28 | Siemens Water Tech Corp | An assembly for water filtration using a tube manifold to minimise backwash |
EP2735359B1 (en) | 2012-11-26 | 2017-02-08 | Gambro Lundia AB | Integrated device for liver support systems |
EP2735326B1 (en) | 2012-11-26 | 2017-03-08 | Gambro Lundia AB | Liver support system |
EP2735360B1 (en) * | 2012-11-26 | 2017-04-12 | Gambro Lundia AB | Adsorber device combining beads and hollow fiber membranes |
DE102014114544B4 (en) * | 2014-10-07 | 2016-06-02 | Sartorius Stedim Biotech Gmbh | filtration device |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5949018B2 (en) * | 1976-10-15 | 1984-11-30 | 旭化成株式会社 | drug syringe |
US4707268A (en) * | 1982-10-18 | 1987-11-17 | Baxter Travenol Laboratories, Inc. | Hollow fiber potted microfilter |
US4639316A (en) * | 1984-12-14 | 1987-01-27 | Becton, Dickinson And Company | Automatic liquid component separator |
JPS62181056A (en) * | 1985-10-07 | 1987-08-08 | アメリカン・ホスピタル・サプライ・コ−ポレイシヨン | Blood filter apparatus having filter element coated with heparin |
DE3600527A1 (en) * | 1986-01-10 | 1987-07-16 | Fresenius Ag | FILTER FOR OBTAINING PLASMA OR PLASMA WATER AND METHOD FOR THE PRODUCTION THEREOF |
DE3636583A1 (en) * | 1986-10-28 | 1988-05-05 | Draegerwerk Ag | METHOD FOR PRODUCING A HOLLOW FIBER FABRIC EXCHANGE MODULE AND MODULE PRODUCED BY THIS METHOD |
US4995967A (en) * | 1987-11-06 | 1991-02-26 | Akzo N.V. | Separator for cell-containing liquids |
-
1989
- 1989-12-07 SE SE8904133A patent/SE465355B/en not_active IP Right Cessation
-
1990
- 1990-12-07 WO PCT/SE1990/000811 patent/WO1991008782A1/en unknown
- 1990-12-07 AU AU69553/91A patent/AU6955391A/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
AU6955391A (en) | 1991-07-18 |
SE465355B (en) | 1991-09-02 |
SE8904133D0 (en) | 1989-12-07 |
WO1991008782A1 (en) | 1991-06-27 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
NUG | Patent has lapsed |
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