DE8907667U1 - Plate membrane - Google Patents
Plate membraneInfo
- Publication number
- DE8907667U1 DE8907667U1 DE8907667U DE8907667U DE8907667U1 DE 8907667 U1 DE8907667 U1 DE 8907667U1 DE 8907667 U DE8907667 U DE 8907667U DE 8907667 U DE8907667 U DE 8907667U DE 8907667 U1 DE8907667 U1 DE 8907667U1
- Authority
- DE
- Germany
- Prior art keywords
- plate
- rigid
- porous
- membrane
- rigid plate
- 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.)
- Expired - Lifetime
Links
- 239000012528 membrane Substances 0.000 title claims description 23
- 229920005597 polymer membrane Polymers 0.000 claims 4
- 239000011148 porous material Substances 0.000 claims 2
- 229920000642 polymer Polymers 0.000 description 8
- 238000000034 method Methods 0.000 description 5
- 239000012466 permeate Substances 0.000 description 4
- 238000005266 casting Methods 0.000 description 3
- 238000000576 coating method Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 210000001601 blood-air barrier Anatomy 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002952 polymeric resin Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
- B01D69/106—Membranes in the pores of a support, e.g. polymerized in the pores or voids
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Description
Die Erfindung besieht sich auf Folymer-Anorganisch-Composite- »eisbrsneR zum Sinsat^: in hikro- und Ultrafiltration und ein verfahren zu deren Herstellung.The invention relates to polymer-inorganic composite filters for use in micro- and ultrafiltration and a process for their production.
Bis heute sind folgende synthetische Membranarten aus den unterschiedlichsten Materialien bekannt:To date, the following synthetic membrane types made from a wide variety of materials are known:
- Hohlfasermembranen- Hollow fiber membranes
- Kapillarmembranen- Capillary membranes
- Rohrmembranen- Tubular membranes
- Flachmembranen- Flat membranes
Diese werden bei mechanischen Membrantrennverfahren eingesetzt. Außer Rohrmembranen sind diese Membranarten im allgemeinen durch große Flexibilität charakterisiert.These are used in mechanical membrane separation processes. Except for tubular membranes, these types of membranes are generally characterized by great flexibility.
AmafilterAmafilter
GmbHGmbH
Es ist bekannt, dsjä insbesondere bsi Montage von Plattenmoduln die Handhabung flexibler Flachmembranen sehr schwierig ist. Es ist auf die Rolleigenschaften der Membranen hinweisen. Oft wird deshalb die flexible Membran auf e'iie Platte geklebt.It is known that handling flexible flat membranes is very difficult, especially when assembling plate modules. The rolling properties of the membranes must be taken into account. The flexible membrane is therefore often glued to the plate.
Die vorliegende Erfindung löst das Problem auf einfache Weise. Erfindungsgemäß wird dieses dadurch erreicht, daß die Membranbildung (2) direkt auf eirer porösen und starren Platte (1) erfolgt, die gleichzeitig eine gleichmäßige Permeatabfuhr gewährleistet. Hierbei kann die starre Trägerplatte (1) ein poröses Sintermetall, Sinterglas oder Sinterkeramik sein, aber auch faserige Gewebe und Vliese, insbesondere aus Glas-, Kohle-,oder Metallfaser. Bei diesen Materialien werden vorteilhaft zur Verstärkung Polymerharze benutzt, die mit £yrolyseverfahren porös und starr gemacht werden können.The present invention solves the problem in a simple way. According to the invention, this is achieved by forming the membrane (2) directly on a porous and rigid plate (1), which at the same time ensures uniform permeate removal. The rigid carrier plate (1) can be a porous sintered metal, sintered glass or sintered ceramic, but also fibrous fabrics and fleeces, in particular made of glass, carbon or metal fibers. With these materials, polymer resins are advantageously used for reinforcement, which can be made porous and rigid using pyrolysis processes.
Weitere Vorteile des starren Platteneinsatzes sind die guten Gegebenheiten für beidseitige Membranpolymerbeschichtungen. Die radiale Fortführung des Permeates in Richtung der größeren Radien, kann aufgrund einer gleichmäßigen und staufreien Permeataufnähme sichergestellt werden.Further advantages of the rigid plate insert are the good conditions for membrane polymer coatings on both sides. The radial continuation of the permeate in the direction of the larger radii can be ensured due to a uniform and jam-free permeate uptake.
amafilteramafilter
ÄmafiiterAmafiiter
GmbHGmbH
Die Membranbildung erfolgt nach dem sogenannten Phaseninversionsprozess. Dazu sollte ein Polymer in an sich bekannter WHiKR in einem oder mehreren Lösungsmitteln gelöst werden. Bei Bedarf können Nichtlösungsmittel oder Salze zugefügt werden.The membrane is formed according to the so-called phase inversion process. For this, a polymer in a known WHiKR should be dissolved in one or more solvents. If necessary, non-solvents or salts can be added.
Die so entstandene homogene Gießlösung wird flächenhaft auf die starre und poröse Platte aufgetragen, wobei die Beschichtungsstärke von 20 pm bis 1000 um beträgt.The resulting homogeneous casting solution is applied evenly to the rigid and porous plate, with the coating thickness ranging from 20 pm to 1000 µm.
Die Viskosität der Gießlösung soll so eingestellt werden, daß die Gießlösung in den Plattenquerschnitt nur teilweise eindringt aber nicht durchläuft.The viscosity of the casting solution should be adjusted so that the casting solution only partially penetrates the plate cross-section but does not pass through.
Dig Pct-Vineirsciiiciit \2/ wird suf cisr pcrcssn und stsrrsn Plstts (1) mittels Phaseninversionsprozess aufgetragen, so daß die Platte zwischen 0 rad und 0,5 &pgr; rad zur Waagerechten vorteilhaft in schräg eingestellter Position in Richtung der Stellung der Plattenoberfläche mit zwischen 20 um und 1000 &mgr;&idiagr;&eegr; fest eingestelltem Abstand zu der stehenden Polymerauftragseinrichtung (3) nach unten in das Fällbad (4) geführt wird (Fig.I).The polymer is applied to the polymer and the solid particles (1) by means of a phase inversion process, so that the plate is guided downwards into the precipitation bath (4) at an angle of between 0 rad and 0.5 π rad to the horizontal in the direction of the position of the plate surface at a fixed distance of between 20 μm and 1000 μm from the stationary polymer application device (3) (Fig. I).
amafilteramafilter
ÄmafiBterÄmafiBter
GmbHGmbH
Im anderen Fall wird die Polymerschicht (2) auf der porösen und starren Platte (1) beidseitig mittels Phaseninversionsprozess aufgetragen, so daß die Platte 0,5 &pgr; rad zur Waagerechten in senkrecht eingestellter Position in Richtung der Stellung der Plattenoberfläche mit zwischen 20 ym und 1000 pm fest eingestelltem Abstand zu der stehenden Polymerauftragseinrichtung nach unten in das Fallbad geführt wird (Fig. II).In the other case, the polymer layer (2) is applied to both sides of the porous and rigid plate (1) using a phase inversion process, so that the plate is guided downwards into the falling bath at a distance of 0.5 π rad from the horizontal in a vertical position in the direction of the position of the plate surface with a distance of between 20 μm and 1000 μm to the stationary polymer application device (Fig. II).
Die auf diese Weise beschichtete Platte wird in ein Fällungsbad getaucht (4). Die Tauchzeit kann von 1 min bis 120 min betragen. Das unerwünschte Aufrollen der Membran im Zuge der Trockung wird mit Plattenmembrane unterbunden.The plate coated in this way is immersed in a precipitation bath (4). The immersion time can be from 1 min to 120 min. The undesirable rolling up of the membrane during drying is prevented by the plate membrane.
Es ist möglich.· daß die poröse und starre Platte beidKeltis beschichtet wird.It is possible that the porous and rigid plate is coated on both sides.
In diesem Fall kann das in der vom Polymer nicht durchgedrungende freien Querschnittszone gewonnene Permeat in Richtung des Außenrandes der Membranplatte abgeführt werden.In this case, the permeate obtained in the free cross-sectional zone not penetrated by the polymer can be discharged towards the outer edge of the membrane plate.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE8907667U DE8907667U1 (en) | 1989-06-23 | 1989-06-23 | Plate membrane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE8907667U DE8907667U1 (en) | 1989-06-23 | 1989-06-23 | Plate membrane |
Publications (1)
Publication Number | Publication Date |
---|---|
DE8907667U1 true DE8907667U1 (en) | 1990-03-29 |
Family
ID=6840402
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE8907667U Expired - Lifetime DE8907667U1 (en) | 1989-06-23 | 1989-06-23 | Plate membrane |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE8907667U1 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999047335A1 (en) * | 1998-03-18 | 1999-09-23 | Cuno, Inc. | Process of making reinforced, three zone microporous membrane |
US6264044B1 (en) | 1997-04-11 | 2001-07-24 | Cuno, Inc. | Reinforced, three zone microporous membrane |
US6280791B1 (en) | 1997-04-11 | 2001-08-28 | Cuno, Inc. | Process of making a three-region reinforced microporous filtration membrane |
US6413070B1 (en) | 1997-04-11 | 2002-07-02 | Cuno Incorporated | System for manufacturing reinforced three-zone microporous membrane |
KR20140085525A (en) * | 2011-10-20 | 2014-07-07 | 파이브라케스트 리미티드 | Coating device and process for coating formed sheet membrane element |
US10478777B2 (en) | 2010-04-20 | 2019-11-19 | Fibracast Ltd. | Formed sheet membrane element and filtration system |
-
1989
- 1989-06-23 DE DE8907667U patent/DE8907667U1/en not_active Expired - Lifetime
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6264044B1 (en) | 1997-04-11 | 2001-07-24 | Cuno, Inc. | Reinforced, three zone microporous membrane |
US6280791B1 (en) | 1997-04-11 | 2001-08-28 | Cuno, Inc. | Process of making a three-region reinforced microporous filtration membrane |
US6413070B1 (en) | 1997-04-11 | 2002-07-02 | Cuno Incorporated | System for manufacturing reinforced three-zone microporous membrane |
US6513666B2 (en) | 1997-04-11 | 2003-02-04 | Cuno Incorporated | Reinforced, three zone microporous membrane |
US6776940B2 (en) | 1997-04-11 | 2004-08-17 | Cuno Incorporated | Process for making a three-zone microporous membrane |
WO1999047335A1 (en) * | 1998-03-18 | 1999-09-23 | Cuno, Inc. | Process of making reinforced, three zone microporous membrane |
US6090441A (en) * | 1998-03-18 | 2000-07-18 | Cuno, Inc. | Process of making reinforced, three zone microporous membrane |
US10478777B2 (en) | 2010-04-20 | 2019-11-19 | Fibracast Ltd. | Formed sheet membrane element and filtration system |
US11642628B2 (en) | 2010-04-20 | 2023-05-09 | Fibracast Ltd. | Formed sheet membrane element and filtration system |
EP2768604A4 (en) * | 2011-10-20 | 2015-09-02 | Fibracast Ltd | Coating device and process for coating formed sheet membrane element |
US10105651B2 (en) | 2011-10-20 | 2018-10-23 | Fibracast Ltd. | Formed sheet membrane element and filtration system |
KR20190060000A (en) * | 2011-10-20 | 2019-05-31 | 파이브라케스트 리미티드 | Coating device and process for coating formed sheet membrane element |
KR102015613B1 (en) | 2011-10-20 | 2019-08-28 | 파이브라케스트 리미티드 | Coating device and process for coating formed sheet membrane element |
KR20140085525A (en) * | 2011-10-20 | 2014-07-07 | 파이브라케스트 리미티드 | Coating device and process for coating formed sheet membrane element |
KR102244592B1 (en) | 2011-10-20 | 2021-04-26 | 파이브라케스트 리미티드 | Coating device and process for coating formed sheet membrane element |
US11154817B2 (en) | 2011-10-20 | 2021-10-26 | Fibracast Ltd. | Formed sheet membrane element and filtration system |
US12053743B2 (en) | 2011-10-20 | 2024-08-06 | Fibracast Ltd. | Formed sheet membrane element and filtration system |
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