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DE8907667U1 - Plate membrane - Google Patents

Plate membrane

Info

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
Application number
DE8907667U
Other languages
German (de)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Amafilter Membrantechnik GmbH
Original Assignee
Amafilter Membrantechnik GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Amafilter Membrantechnik GmbH filed Critical Amafilter Membrantechnik GmbH
Priority to DE8907667U priority Critical patent/DE8907667U1/en
Publication of DE8907667U1 publication Critical patent/DE8907667U1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/10Supported membranes; Membrane supports
    • B01D69/106Membranes 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

BeschreibungDescription

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

MembrantechnikMembrane technology

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

MembrantechnikMembrane technology

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

MembrantechnikMembrane technology

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)

AnsprücheExpectations 1. Plattenmembran1. Plate membrane bestehend aus einer Polymermembranschicht (2), mit einer porösen und starren Platte (1) mechanisch unlösbar verbunden, wobei je nach Auswahl dife Dicke der Platte (1) zwischen 50 um und 5000 pm, die Porengröße der starren Platte (1) zwischen 5 um und 500 pm, die Porosität der starren Platte (1) zwischen 0,1 und 0,9 sowie die Stärke der verbundenen PolymermeF>hranschicht (2) zwischen 20 pm und IÖ00 pm liegen, dadurch gekennzeichnet, daß die öffnungen der starren und porösen Platte (1) in Richtung der größeren Radien miteinander verbunden sind.consisting of a polymer membrane layer (2) mechanically inseparably connected to a porous and rigid plate (1), whereby, depending on the selection, the thickness of the plate (1) is between 50 µm and 5000 µm, the pore size of the rigid plate (1) is between 5 µm and 500 µm, the porosity of the rigid plate (1) is between 0.1 and 0.9 and the thickness of the connected polymer membrane layer (2) is between 20 µm and 100 µm, characterized in that the openings of the rigid and porous plate (1) are connected to one another in the direction of the larger radii. amafitteramafitter Aif|fif|iterJ.::4 Membrantechnik GmbHAif|fif|iterJ.::4 Membrane Technology GmbH amafilteramafilter 2. Plattenmembran nach Anspruch 1,2. Plate membrane according to claim 1, bestehend aus zwei Polymermembranschichten (2) mit einerconsisting of two polymer membrane layers (2) with a porösen und starren Platte (1) mechanisch unlösbarporous and rigid plate (1) mechanically insoluble verbunden, wobei je nach Auswahl die Dicke der Platte (1)connected, whereby depending on the selection the thickness of the plate (1) zwischen 50 um und 5000 um, die Porengroße der starrenbetween 50 um and 5000 um, the pore size of the rigid Platte (1) zwischen 5 um und 500 pm, die Porosität der '& Plate (1) between 5 um and 500 pm, the porosity of the '& starren Platte (1) zwischen 0,1 und 0,9 sowie die Stärke £rigid plate (1) between 0.1 and 0.9 and the thickness £ der verbundenen Polymermembranschicht (2) zwischen 20 umthe bonded polymer membrane layer (2) between 20 um und 1000 pm liegen, dadurch gekennzeichnet, daß die ,';and 1000 pm, characterized in that the '; Offnungen der porösen und starren Platte (1) in Richtung !')Openings of the porous and rigid plate (1) in direction !') der größeren Radien miteinander verbunden sind. ^of the larger radii are connected. ^
DE8907667U 1989-06-23 1989-06-23 Plate membrane Expired - Lifetime DE8907667U1 (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (17)

* Cited by examiner, † Cited by third party
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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