DE3920562C1 - Plate membrane used in micro- and ultra-filtration - obtd. by forming polymer membrane layer on rigid and porous plate through phase inversion process - Google Patents

Plate membrane used in micro- and ultra-filtration - obtd. by forming polymer membrane layer on rigid and porous plate through phase inversion process

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Publication number
DE3920562C1
DE3920562C1 DE3920562A DE3920562A DE3920562C1 DE 3920562 C1 DE3920562 C1 DE 3920562C1 DE 3920562 A DE3920562 A DE 3920562A DE 3920562 A DE3920562 A DE 3920562A DE 3920562 C1 DE3920562 C1 DE 3920562C1
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DE
Germany
Prior art keywords
plate
microns
porous
rigid plate
rigid
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
DE3920562A
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German (de)
Inventor
Robert Dr. 3000 Hannover De Kohlheb
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
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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.)
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Publication date
Application filed by Amafilter Membrantechnik GmbH filed Critical Amafilter Membrantechnik GmbH
Priority to DE3920562A priority Critical patent/DE3920562C1/en
Application granted granted Critical
Publication of DE3920562C1 publication Critical patent/DE3920562C1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • B01D69/108Inorganic support material
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002Organic membrane manufacture
    • B01D67/0009Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002Organic membrane manufacture
    • B01D67/0009Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
    • B01D67/0016Coagulation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/04Characteristic thickness

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

A plate membrane for use in micro- and ultra-filtration is made by producing a polymer membrane layer on a rigid and porous plate through a phase inversion process. The plate is passed at an angle of under 90 deg. and with a distance of 20-1000 microns from the solution pouring device into the precipitating bath. The plate is a porous sinter product or a mat of glass-, carbon- or metal fibres. The pref. polymer material is PES,PVF or polyamide. ADVANTAGE - This eliminates the difficulty of handling flexible plate membrances.

Description

Die Erfindung bezieht sich auf Polymer Anorganische-Composite­ membranen zum Einsatz in der Mikro- und Ultrafiltration und ein Verfahren zu deren Herstellung.The invention relates to polymer inorganic composites membranes 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 are from the various materials known:

- Holzefasermembranen
- Kapillarmembranen
- Rohrmembranen
- Flachmembranen.
- Wood fiber membranes
- capillary membranes
- tubular membranes
- flat membranes.

Diese werden bei Membrantrennverfahren einge­ setzt. Außer Rohrmembranen sind diese Membranarten im allge­ meinen durch große Flexibilität charakterisiert. These are used in membrane separation processes puts. In addition to tubular membranes, these membrane types are common mean characterized by great flexibility.  

Es ist bekannt, daß insbesondere bei der Montage von Plattenmo­ duln die Handhabung flexibler Flachmembranen sehr schwierig ist. Es sei auf die Rolleigenschaften der Membranen hinge­ wiesen. Oft werden deshalb die flexiblen Membranen auf Platten geklebt.It is known that especially when mounting Plattenmo It is very difficult to handle flexible flat membranes is. It depends on the rolling properties of the membranes grasslands. That is why the flexible membranes are often placed on plates glued.

Die vorliegende Erfindung löst das Problem auf einfache Weise. Erfindungsgemäß wird dieses dadurch erreicht, daß die Membran­ bildung (2) direkt auf einer porösen und starren Platte (1) erfolgt, die gleichzeitig eine gleichmäßige Permeatabfuhr ge­ währleistet. Hierbei kann die starre Trägerplatte (1) ein po­ röses Sintermetall, Sinterglas oder Sinterkeramik sein, aber auch faserige Gewebe und Vliese, insbesonder aus Glas-, Kohle- oder Metallfaser. Bei diesen Materialien werden vor­ teilhaft zur Verstärkung Polymerharze benutzt, die mit Pyro­ lyseverfahren porös und starr gemacht werden können.The present invention solves the problem in a simple manner. According to the invention this is achieved in that the membrane formation ( 2 ) takes place directly on a porous and rigid plate ( 1 ) which at the same time ensures uniform permeate removal. Here, the rigid carrier plate ( 1 ) can be a porous sintered metal, sintered glass or sintered ceramic, but also fibrous fabrics and nonwovens, in particular made of glass, carbon or metal fibers. In these materials, polymeric resins are used before for reinforcement, which can be made porous and rigid with 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 Per­ meataufnahme sichergestellt werden. Other advantages of the rigid insert are the good ones Conditions for double-sided membrane polymer coatings. The radial continuation of the permeate in the direction of the larger one Radii, due to an even and congestion-free per can be ensured.  

Die Membranbildung erfolgt nach dem sogenannten Phaseninver­ sionsprozeß. Dazu sollte ein Polymer in an sich bekannter Weise in einem oder mehreren Lösungsmitteln gelöst werden. Bei Bedarf können Nichtlösungsmittel oder Salze zugefügt werden.The membrane formation takes place after the so-called phase inverter process. For this purpose, a polymer should be known per se Be solved in one or more solvents. If necessary, non-solvents or salts can be added will.

Die so entstandene homogene Gießlösung wird flächenhaft auf die starre und poröse Platte aufgetragen, wobei die Beschich­ tungsstärke 20 bis 1000 µm beträgt.The resulting homogeneous pouring solution is spread over a large area applied the rigid and porous plate, the Beschich thickness is 20 to 1000 µm.

Die Viskosität der Gießlösung soll so eingestellt werden, daß die Gießlösung in den Plattenquerschnitt nur teilweise ein­ dringt aber nicht durchläuft.The viscosity of the casting solution should be adjusted so that only partially pour the casting solution into the plate cross-section does not penetrate.

Die Gießlösung wird mit Hilfe der Auftragseinrichtung (3) auf die poröse und starre Platte (1) aufgetragen, wobei zwischen der Auftragseinrichtung und der porösen Platte ein fester Abstand von 20 bis 1000 µm eingestellt wird. Die so beschichtete Platte wird anschließend mit einem Winkel zwischen Plattenoberfläche und Oberfläche der Fällflüssigkeit von kleiner gleich 90° in das Fällbad eingeführt (Fig. I). The casting solution is applied to the porous and rigid plate ( 1 ) with the aid of the application device ( 3 ), a fixed distance of 20 to 1000 μm being set between the application device and the porous plate. The plate coated in this way is then introduced into the precipitation bath at an angle between the plate surface and the surface of the precipitation liquid of less than or equal to 90 ° ( FIG. I).

Alternativ hierzu wird die Gießlösung auf der porösen und starren Platte (1) beidseitig aufgetragen, so daß die Platte senkrecht mit zwischen 20 und 1000 µm fest eingestelltem Abstand zu der stehenden Polymerauftrags­ einrichtung nach unten in das Fällbad (4) geführt wird (Fig. II).Alternatively, the casting solution is applied to the porous and rigid plate ( 1 ) on both sides, so that the plate is guided vertically with a fixed distance between 20 and 1000 microns to the standing polymer application device down into the precipitation bath ( 4 ) ( Fig. II ).

Die Tauchzeit im Fällbad kann zwischen 1 und 120 min betragen.The immersion time in the precipitation bath can be between 1 and 120 min be.

Das unerwünschte Aufrollen der Membran im Zuge der Trocknung wird mit Plattenmembranen unterbunden.The unwanted rolling up of the membrane in the course of Drying is prevented with plate membranes.

In diesem Fall kann das in der vom Polymer nicht durchgedrun­ gende freien Querschnittszone gewonnene Permeat in Richtung des Außenrandes der Membranplatte abgeführt werden.In this case, the polymer cannot run through it permeate obtained in the direction of the free cross-sectional zone of the outer edge of the membrane plate.

Claims (4)

1. Plattenmembranen, gekennzeichnet durch eine Polymermembranschicht (2), mit einer porösen und starren Platte (1) mechanisch unlösbar verbunden, wobei je nach Auswahl die Dicke der Platte (1) zwischen 50 µm und 5000 µm, die Porengröße der starren Platte (1) zwischen 5 µm und 500 µm, die Porosität der starren Platte (1) zwischen 0,1 und 0,9 sowie die Stärke der verbundenen Polymermembranschicht (2) zwischen 20 und 1000 µm liegen, dadurch erhältlich, daß die Polymermembran­ schicht (2) auf der porösen und starren Platte (1) mittels Phaseninversionsprozeß erzeugt wird, indem die Platte (1) mit einem Winkel von kleiner gleich 90° zur Waagerechten vorteilhaft in schräg eingestellter Position mit zwischen 20 und 1000 µm fest eingestelltem Abstand zu der stehenden Auftragseinrichtung der Gießlösung (3) nach unten in das Fällbad (4) geführt wird. 1. plate membranes, characterized by a polymer membrane layer ( 2 ) with a porous and rigid plate ( 1 ) mechanically insoluble, depending on the selection, the thickness of the plate ( 1 ) between 50 microns and 5000 microns, the pore size of the rigid plate ( 1 ) of between 5 microns and 500 microns, the porosity of the rigid plate (1) between 0.1 and 0.9 and the strength of the bonded polymeric membrane layer (2) is between 20 and 1000 microns, obtainable by the polymer membrane layer (2) is generated on the porous and rigid plate ( 1 ) by means of a phase inversion process, in that the plate ( 1 ) is at an angle of less than or equal to 90 ° to the horizontal, advantageously in an inclined position with a fixed distance between 20 and 1000 μm to the standing application device of the casting solution ( 3 ) is led down into the precipitation bath ( 4 ). 2. Plattenmembranen nach Anspruch 1, gekennzeichnet durch zweiseitige Beschichtung einer porösen und starren Platte (1) mit einer Polymermembranschicht (2), wobei je nach Auswahl die Dicke der Platte (1) zwischen 50 µm und 5000 µm, die Porengröße der starren Platte (1) zwischen 5 µm und 500 µm, die Porosität der starren Platte (1) zwischen 0,1 und 0,9 sowie die Stärke der verbundenen Polymermembranschicht (2) zwischen 20 und 1000 µm liegen, dadurch erhältlich, daß die Polymer­ schicht (2) auf der porösen und starren Platte (1) beid­ seitig mittels Phaseninversionsprozeß erzeugt wird, indem die beidseitig mit Gießlösung beschichtete Platte (1) senkrecht nach unten in das Fällbad (4) geführt wird.2. plate membranes according to claim 1, characterized by two-sided coating of a porous and rigid plate ( 1 ) with a polymer membrane layer ( 2 ), wherein depending on the selection, the thickness of the plate ( 1 ) between 50 microns and 5000 microns, the pore size of the rigid plate ( 1) microns between 5 and 500 micrometers, the porosity of the rigid plate (1) between 0.1 and 0.9 and the strength of the bonded polymeric membrane layer (2) are between 20 and 1000 microns, obtainable in that the polymer layer (2 ) is produced on both sides of the porous and rigid plate ( 1 ) by means of a phase inversion process, in that the plate ( 1 ) coated on both sides with casting solution is guided vertically downward into the precipitation bath ( 4 ). 3. Plattenmembran nach Anspruch 1 und 2, gekennzeichnet durch eine Polymermembranschicht (2) mit einer porösen und starren Platte (1) mechanisch unlösbar verbunden, wobei der Werkstoff der porösen und starren Platte (1) eine chemisch und pyrolytisch verstärkte symmetrische oder asymmetrische Struktur hat und aus Glas- oder Kohle- oder Keramik- oder Metall-Faser, oder -Vlies, oder -Sinter besteht. 3. plate membrane according to claim 1 and 2, characterized by a polymer membrane layer ( 2 ) with a porous and rigid plate ( 1 ) mechanically non-detachably, the material of the porous and rigid plate ( 1 ) has a chemically and pyrolytically reinforced symmetrical or asymmetrical structure and consists of glass or carbon or ceramic or metal fiber, or fleece, or sinter. 4. Plattenmembran nach einem der Ansprüche 1 bis 3, dadurch gekennzeichnet, daß das Polymermaterial aus Polyethersulfon, Polyvinylidenfluorid oder Polyamid besteht.4. Plate membrane according to one of claims 1 to 3, characterized characterized in that the polymer material Polyether sulfone, polyvinylidene fluoride or polyamide consists.
DE3920562A 1989-06-23 1989-06-23 Plate membrane used in micro- and ultra-filtration - obtd. by forming polymer membrane layer on rigid and porous plate through phase inversion process Expired - Lifetime DE3920562C1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DE3920562A DE3920562C1 (en) 1989-06-23 1989-06-23 Plate membrane used in micro- and ultra-filtration - obtd. by forming polymer membrane layer on rigid and porous plate through phase inversion process

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Application Number Priority Date Filing Date Title
DE3920562A DE3920562C1 (en) 1989-06-23 1989-06-23 Plate membrane used in micro- and ultra-filtration - obtd. by forming polymer membrane layer on rigid and porous plate through phase inversion process

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0674937A2 (en) * 1994-03-30 1995-10-04 Corning Incorporated Non-porous polymeric membrane on a porous inorganic support

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2037186A1 (en) * 1969-07-31 1971-02-18 Hydronautics, Ine , Laurel, Md (VStA) Tubular component and process for its manufacture and use
DE1767543A1 (en) * 1967-05-22 1971-04-29 American Standard Inc Method and device for attaching a highly effective membrane filter body to the inside of a porous support tube
DE2432049A1 (en) * 1974-07-04 1976-01-22 Boehringer Sohn Ingelheim COMPOSITE OF MEMBRANE FILTERS AND POROESE MATERIAL AND ITS USE
DE3029153A1 (en) * 1980-07-31 1982-03-04 Siemens AG, 1000 Berlin und 8000 München Gas permeable polymer membrane for analysis devices - has perforated metal or glass backing disc
DE3546328A1 (en) * 1984-12-29 1986-07-03 NGK Insulators Ltd., Nagoya, Aichi FILTER AND METHOD FOR PRODUCING THE FILTER
DE3515025A1 (en) * 1985-04-25 1986-10-30 Altenburger Electronic Gmbh, 7633 Seelbach Process for producing a filter having pores of a predetermined and roughly equal micro size and a filter produced by this process

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1767543A1 (en) * 1967-05-22 1971-04-29 American Standard Inc Method and device for attaching a highly effective membrane filter body to the inside of a porous support tube
DE2037186A1 (en) * 1969-07-31 1971-02-18 Hydronautics, Ine , Laurel, Md (VStA) Tubular component and process for its manufacture and use
DE2432049A1 (en) * 1974-07-04 1976-01-22 Boehringer Sohn Ingelheim COMPOSITE OF MEMBRANE FILTERS AND POROESE MATERIAL AND ITS USE
DE3029153A1 (en) * 1980-07-31 1982-03-04 Siemens AG, 1000 Berlin und 8000 München Gas permeable polymer membrane for analysis devices - has perforated metal or glass backing disc
DE3546328A1 (en) * 1984-12-29 1986-07-03 NGK Insulators Ltd., Nagoya, Aichi FILTER AND METHOD FOR PRODUCING THE FILTER
DE3515025A1 (en) * 1985-04-25 1986-10-30 Altenburger Electronic Gmbh, 7633 Seelbach Process for producing a filter having pores of a predetermined and roughly equal micro size and a filter produced by this process

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0674937A2 (en) * 1994-03-30 1995-10-04 Corning Incorporated Non-porous polymeric membrane on a porous inorganic support
EP0674937A3 (en) * 1994-03-30 1995-11-22 Corning Inc Non-porous polymeric membrane on a porous inorganic support.

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