WO2005061081A1 - Verfahren zum herstellen von rohrförmigen membranen - Google Patents

Verfahren zum herstellen von rohrförmigen membranen Download PDF

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Publication number
WO2005061081A1
WO2005061081A1 PCT/EP2004/010434 EP2004010434W WO2005061081A1 WO 2005061081 A1 WO2005061081 A1 WO 2005061081A1 EP 2004010434 W EP2004010434 W EP 2004010434W WO 2005061081 A1 WO2005061081 A1 WO 2005061081A1
Authority
WO
WIPO (PCT)
Prior art keywords
threads
connecting lines
tubular body
membrane
web
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.)
Ceased
Application number
PCT/EP2004/010434
Other languages
German (de)
English (en)
French (fr)
Inventor
Michael Kamleiter
Wilhelm-N. Gudernatsch
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.)
Poromedia GmbH
Original Assignee
Poromedia 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 Poromedia GmbH filed Critical Poromedia GmbH
Priority to JP2006543375A priority Critical patent/JP4718481B2/ja
Priority to US10/582,349 priority patent/US8393479B2/en
Priority to EP04765330A priority patent/EP1689517B1/de
Priority to CA002548409A priority patent/CA2548409A1/en
Priority to DE502004005399T priority patent/DE502004005399D1/de
Publication of WO2005061081A1 publication Critical patent/WO2005061081A1/de
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/06Tubular membrane modules
    • B01D63/061Manufacturing thereof
    • 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
    • B01D69/04Tubular membranes
    • 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
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04BKNITTING
    • D04B31/00Crocheting processes for the production of fabrics or articles
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2505/00Industrial
    • D10B2505/04Filters

Definitions

  • the invention relates to a method for producing tubular membranes.
  • EP 0 349 914 B1 discloses a method for producing tubular nonwoven bodies from a strip of a thermoplastic carrier nonwoven, which is wound up to form a nonwoven tube in the form of a spiral in such a way that the longitudinal edges of the strip along at least one in the wound area of the nonwoven tube Overlap the connecting seam, the longitudinal edges being thermally welded to one another to form this connecting seam.
  • a hollow rod is formed which has an outlet opening at its free end through which a coating solution can be applied to the inner wall of the wound nonwoven tube, a tubular membrane being formed by the subsequent contact with a coagulation solution.
  • tubular membranes are particularly suitable for ultrafiltration and nanofiltration, the membranes in question form microporous filter media, the passage pores of which are so small that they not only form a barrier for particles of all types and shapes, such as impurities, heavy metals etc. but also for all microorganisms, for example in the form of bacteria, parasites and viruses.
  • the active layer of the membranes is also referred to in technical terminology as a semipermeable layer.
  • a disadvantage of the tubular membranes produced in this way is that they often tear open under the pressure load of the fluid to be filtered in the area of the thermal connecting seams and accordingly fail.
  • German Offenlegungsschrift 2 255 989 to surround the otherwise thin and fragile, semi-permeable membrane tubes on the outer circumference with a reinforcement in the form of a fiber braid structure in order to counteract the high hydraulic internal pressure Act; only the known method is complex and therefore expensive to manufacture, and the reinforcing fiber braiding structure lying directly against the semipermeable membrane adversely affects the flow and filtration behavior of the tubular membrane. bran.
  • DE 199 09 930 A1 proposes a tubular composite made of a braid of thread bundles and / or wires, preferably in the form of an electron-conducting material and a layer of an ion-conducting material arranged above, as a fuel cell element.
  • a so-called PEM fuel cell it is proposed, among other things, for producing a so-called PEM fuel cell, to produce the tubular inner electrode consisting of carbon fibers and / or metal wires by means of a braiding machine.
  • This tubular braid runs for centering on a mandrel up to an application nozzle for the catalyst coating, the nozzle diameter determining the thickness of the catalyst layer.
  • a short drying section through e.g. B. ceramic the coated braid passes through an annular gap nozzle through which the ion-conductive membrane is applied in the form of a polymer solution. This step is followed by a longer drying section to drive off the solvent.
  • a second catalyst layer is applied with an application nozzle and then the outer electrode is braided around the still pasty catalyst layer.
  • the paste-like consistency of the catalyst layer allows the braided strands to penetrate and thus an intimate bond between the catalyst and the electrode.
  • this tubular composite consisting at least partially of a flat thread mesh is exposed to correspondingly high fluid pressures, it cannot be ruled out that the longitudinal and transverse tensile stresses in the thread mesh cause the threads to shift relative to one another, and this can lead to undesirable stretching effects, in particular also in the manufacture of the braid before the actual coating with the membrane material, which has the consequence that the known tubular membrane takes on a shape, in particular changes in the diameter range in such a way that it can become unsuitable for later use.
  • the object of the invention is to further improve the known technical process solutions for the production of tubular membranes in such a way that functionally reliable tubular membranes can be obtained at high production speed and at low cost, neither during their manufacture nor during later operation exhibit undesirable stretching effects with changes in the membrane geometry.
  • a related problem is solved by a method with the features of claim 1 in its entirety.
  • a tubular body is constructed from several threads in such a way that along web-like connecting lines there is an essentially firm connection of at least some of the threads, that between the web-like connecting lines at least some of the threads make the cross-connection between the adjacent connecting lines, and that a specifiable membrane material is applied to the tubular body, this results in a great deal Cost-effective manufacturing process with which very high ejection rates on tubular membranes can be obtained.
  • tubular bodies can be obtained prior to the application of the membrane material, in the manner of a knitted conductor or circular conductor knitting and with the mentioned knitted conductor pattern, any longitudinal tensile stresses that occur can be reliably absorbed by means of continuous longitudinal threads along the web-like connecting lines.
  • the looping at the crossing points of the conductor knitting pattern that is to say at the points of the essentially fixed connection between the connecting lines and the above-mentioned cross-connections, prevents the thread systems from shifting against one another and the undesired stretching effect described during the coating is minimized, with the fabric-reinforced in this way Filtration capillary withstands very high internal pressures and mechanically applied longitudinal tensile forces.
  • the wrapping at the points of the fixed link between connecting lines and cross connections means that there can be no displacements, so that any longitudinal or transverse movements of the thread system are determined solely by the inherent elasticity of the thread material used.
  • using the method according to the invention results in tubular bodies that are very stable in shape and pressure, both in the manufacture of the membrane tubes and in their later ones Use in the ultra or nanofiltration range of fluids of any kind, including in the areas of water and beverage treatment.
  • the tubular body designed as a knitted conductor is created by means of a mechanical crochet device, with each thread used being assigned its own hook or crochet needle.
  • crocheting is a process of hanging, whereby with the help of the hook or crochet needle the thread is formed into loops "in the air", ie without a base, whereby the intertwined loops can be combined into patterns.
  • the crochet device it is possible to insert supporting or holding threads continuously along the web-like connecting lines in order to create a kind of basic structure in order to then use the further threads for the looping at the crossing points along the connecting lines and to produce the cross thread connection between the mentioned connecting lines.
  • the tubular body is preferably created by crocheting in such a way that fluid passage points with a high flow rate are formed between the individual cross connections, the web-like connecting lines being essentially fluid-tight or with a lower flow rate.
  • the threads mentioned are selected from the group
  • plastic materials such as polyester, polyaramides, other polymers, carbon, Kevlar etc. or
  • the metal materials such as nickel, platinum, palladium, gold, silver, stainless steels etc. or -
  • the catalytically active materials such as ruthenium, rhodium, iridium, nickel etc. or
  • the other materials such as cellulose acetate, glass fibers, graphite powder, activated carbon etc. or
  • thread is to be drawn broadly and, in addition to the usual monofilament and multifilament threads, also includes other linear elements such as yarns, wires or rod-like components, also made from powders.
  • the adjacent cross connections that are arranged in this way between two connecting lines delimit an angle between them of 10 ° to 70 °, preferably of approximately 25 ° to 45 °, particularly preferably of approximately 30 °.
  • the tubular body is coated with a membrane-activatable substance which is passed through a precipitation bath, the substance being converted into a microporous membrane layer.
  • Particularly suitable membrane materials are those from the group of plastic materials, such as polyether sulfone (PES), polysulfone (PSU), polyacrylonitrile (PAN) or polyvinylidene fluoride (PVDF).
  • PES polyether sulfone
  • PSU polysulfone
  • PAN polyacrylonitrile
  • PVDF polyvinylidene fluoride
  • the method according to the invention for producing tubular membranes provides that a tubular body, designated as a whole by 10, is constructed from a plurality of threads 12 in such a way that an essentially firm connection of at least part of the threads 12 takes place along web-like connecting lines 14, between the web-like connecting lines 14 at least some of the threads 12 make the cross connection 16 between the adjacent connecting lines 14, and a predeterminable membrane material 18 is applied to the tubular body 10.
  • the web-like connecting lines 14 form a type of longitudinal thread system that forms a type of knitted conductor, in particular circular knitted fabric, via the transverse threads 12 of the respective transverse connection 16.
  • the tubular body 10 is produced by means of an industrial crochet device, with each thread used being assigned its own hook or crochet needle. Since mechanical crochet devices are state of the art, no further reference is made to the crochet production of the tubular body 10. In any case, the tubular body 10 is created by the aforementioned crochet in such a way that fluid passage points 20 with a high flow rate are formed between the individual cross connections 16 in the form of the transverse threads 12 in question, the web-like connecting lines 14 as longitudinal thread system being designed to be essentially fluid-tight or with a correspondingly lower flow rate.
  • the threads 12 used for the cross-connections 16 and for their connection to one another along the points 22 in the transition region to the web-like connecting lines 14 consist of multifilament plastic threads, for example of polyester or polyaramides, whereby other polymers can also be used here.
  • the longitudinal threads along the web-like connecting lines 14 are made of carbon fiber materials. If, for example, one wants to use the tubular membrane in question as a fuel cell element or the like, it is possible to construct part of the threads from an electron-conducting material and another part of the threads from an ion-conducting material.
  • the thread system which acts as an ion conductor can be provided with a catalyst layer which can additionally be provided with hydrophobicizing agents and / or proton conductor material. It is also possible in this way to use the tubular membrane described as a bipolar ion exchange membrane in order to obtain lactic acid or the like in this way.
  • the electrical charge potential of the tubular membrane can also be specified.
  • the tubular body 10 consists of eight connecting lines 14 and eight cross-connecting surfaces 16.
  • tubular bodies 10 which are constructed from six connecting lines 14 and six cross-connections 16, have proven to be particularly advantageous. The minimum requirement for building a tubular body 10 with a triangular cross section (not shown) is to build it from three connecting lines 14 with three cross connections 16.
  • the tubular body 10 produced in this way is passed through a precipitation bath, the substance being converted into a microporous membrane layer.
  • a precipitation bath Such a method is disclosed by way of example in WO 03/076055 A1, so that it will not be discussed in detail here.
  • the known solution according to the WO publication relates to a process for the production of fabric-reinforced capillary membranes, in particular for ultrafiltration, in which a fabric tube is coated with a polymer solution and passed through a precipitation bath, the conversion of the polymer solution into a microporous layer in the precipitation bath he follows. In this way, a membrane reinforced by the fabric tube is formed.
  • the fabric hose coated with the polymer solution passes through the precipitation bath without mechanical contact from top to bottom and exits through a nozzle on the underside. Liquid flows out through the nozzle and exerts a tensile force which stabilizes the running of the coated fabric tube on the capillary membrane leaving the precipitation bath.
  • the relevant coating process is only selected as an example and there are a large number of other coating processes including immersion bath processes which can be used here.
  • the membrane material is one from the group of plastic materials. selects like polyether sulfone (PES), polysulfone (PSU), polyacrylonitrile (PAN) or polyvinylidene fluoride (PVDF).
  • the tubular membrane according to the invention can be produced continuously and therefore inexpensively, ie. H. the tubular body 10 is permanently provided via the crochet process for the subsequent coating process with the membrane material 18.
  • the filter material in the form of a knitted conductor or circular conductor knit using conventional crochet technology, a filter pipe is formed in which the longitudinal tensile stresses occurring during the filtration are created are taken up by the continuous longitudinal threads along the web-like connecting lines 14, the tensions on the circumference being reliably absorbed by the transverse threads 12 of the fabric layer composite by means of the flat cross connections 16.
  • the looping at the crossing points (balls 22) reduces the displacement of the threads 12 against one another, so that undesirable stretching effects in the longitudinal direction as well as in the transverse direction of the tubular body 10 are significantly minimized during the coating with the membrane material and the filtration capillary, which is reinforced in this way, withstands very high internal pressures and Longitudinal lines in the filtration.
  • threads 12 with a diameter of 20 to 200 ⁇ m can be used as thread thickness and the number of threads along lines 14 is preferably three to six pieces.
  • the technical solution selected as a circular conductor knit tensile strengths of 100 N / mm 2 can be achieved with an elongation at break of 1 to 5% and in the dynamic pressure test such pipes hold a burst pressure of approx without further ado, with a shortening of the tube of only 1% being observed, so that the membrane tube according to the invention, which is designed as a circular conductor knit, is securely fixed in a holding device, in particular in the form of at least one module (not shown) of an overall filtration system.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Textile Engineering (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Shaping Of Tube Ends By Bending Or Straightening (AREA)
PCT/EP2004/010434 2003-12-11 2004-09-17 Verfahren zum herstellen von rohrförmigen membranen Ceased WO2005061081A1 (de)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP2006543375A JP4718481B2 (ja) 2003-12-11 2004-09-17 管状メンブレインの製造方法
US10/582,349 US8393479B2 (en) 2003-12-11 2004-09-17 Method for the production of tubular membranes
EP04765330A EP1689517B1 (de) 2003-12-11 2004-09-17 Verfahren zum herstellen von rohrförmigen membranen
CA002548409A CA2548409A1 (en) 2003-12-11 2004-09-17 Method for the production of tubular membranes
DE502004005399T DE502004005399D1 (de) 2003-12-11 2004-09-17 Verfahren zum herstellen von rohrförmigen membranen

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10358477A DE10358477B3 (de) 2003-12-11 2003-12-11 Verfahren zum Herstellen von rohrförmigen Membranen
DE10358477.3 2003-12-11

Publications (1)

Publication Number Publication Date
WO2005061081A1 true WO2005061081A1 (de) 2005-07-07

Family

ID=34353508

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2004/010434 Ceased WO2005061081A1 (de) 2003-12-11 2004-09-17 Verfahren zum herstellen von rohrförmigen membranen

Country Status (8)

Country Link
US (1) US8393479B2 (https=)
EP (1) EP1689517B1 (https=)
JP (1) JP4718481B2 (https=)
AT (1) ATE376874T1 (https=)
CA (1) CA2548409A1 (https=)
DE (2) DE10358477B3 (https=)
ES (1) ES2293325T3 (https=)
WO (1) WO2005061081A1 (https=)

Cited By (7)

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EP2411127A4 (en) * 2009-03-26 2013-08-21 Bl Technologies Inc NON-BRAIDED REINFORCED HOLLOW FIBER MEMBRANE
US8993081B2 (en) 2006-04-10 2015-03-31 Vlaamse Instelling Voor Technologish Onderzoek N.V. (Vito) Knitted support for tubular membranes
US8999454B2 (en) 2012-03-22 2015-04-07 General Electric Company Device and process for producing a reinforced hollow fibre membrane
US9022229B2 (en) 2012-03-09 2015-05-05 General Electric Company Composite membrane with compatible support filaments
US9221020B2 (en) 2010-09-15 2015-12-29 Bl Technologies, Inc. Method to make yarn-reinforced hollow fiber membranes around a soluble core
US9227362B2 (en) 2012-08-23 2016-01-05 General Electric Company Braid welding
US9321014B2 (en) 2011-12-16 2016-04-26 Bl Technologies, Inc. Hollow fiber membrane with compatible reinforcements

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US20080292912A1 (en) * 2006-05-02 2008-11-27 The Penn State Research Foundation Electrodes and methods for microbial fuel cells
US7491453B2 (en) * 2004-07-14 2009-02-17 The Penn State Research Foundation Bio-electrochemically assisted microbial reactor that generates hydrogen gas and methods of generating hydrogen gas
US8962165B2 (en) * 2006-05-02 2015-02-24 The Penn State Research Foundation Materials and configurations for scalable microbial fuel cells
US7922878B2 (en) * 2004-07-14 2011-04-12 The Penn State Research Foundation Electrohydrogenic reactor for hydrogen gas production
US8277984B2 (en) * 2006-05-02 2012-10-02 The Penn State Research Foundation Substrate-enhanced microbial fuel cells
JP4757310B2 (ja) 2005-11-29 2011-08-24 コーロン インダストリーズ インク 編物により補強された複合中空繊維膜
JP2009297641A (ja) * 2008-06-12 2009-12-24 Sepratek Inc ブレード強化中空糸膜
MX2011006971A (es) * 2008-12-30 2011-08-15 Penn State Res Found Catodos para celdas de electrolisis y celdas de combustible microbiano.
KR101714103B1 (ko) * 2009-06-26 2017-03-09 비엘 테크놀러지스 인크. 텍스타일-강화된 비-편조 중공사 막
US9643129B2 (en) 2011-12-22 2017-05-09 Bl Technologies, Inc. Non-braided, textile-reinforced hollow fiber membrane
TWI432499B (zh) * 2011-12-26 2014-04-01 Ind Tech Res Inst 複合原料、碳纖維材料及其形成方法
SG11201500210WA (en) * 2012-08-15 2015-03-30 Univ Nanyang Tech Reinforced membranes for producing osmotic power in pressure retarded osmosis
US9546426B2 (en) 2013-03-07 2017-01-17 The Penn State Research Foundation Methods for hydrogen gas production
CN105080356B (zh) * 2015-08-04 2018-01-19 天津工业大学 疏水亲油中空纤维复合膜及其制备方法
EP4182062A4 (en) * 2020-07-17 2024-08-21 New Mexico Tech University Research Park Corporation METHOD FOR PRODUCING TWO-LAYER POLYVINYLIDE FLUORIDE HOLLOW FIBER MEMBRANES AND USES THEREOF
CN116407955B (zh) * 2023-03-10 2025-09-16 清华大学 双极膜及其制备方法

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EP1059114A2 (en) * 1999-06-08 2000-12-13 Nitto Denko Corporation Liquid separation membrane module and method of producing the same
WO2003076055A1 (de) * 2002-03-12 2003-09-18 Puron Ag Verfahren zur herstellung gewebeverstärkter kapillarförmiger membranen, insbesondere für die ultrafiltration

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US5342434A (en) * 1992-12-14 1994-08-30 W. L. Gore & Associates, Inc. Gas permeable coated porous membranes
EP1059114A2 (en) * 1999-06-08 2000-12-13 Nitto Denko Corporation Liquid separation membrane module and method of producing the same
WO2003076055A1 (de) * 2002-03-12 2003-09-18 Puron Ag Verfahren zur herstellung gewebeverstärkter kapillarförmiger membranen, insbesondere für die ultrafiltration

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8993081B2 (en) 2006-04-10 2015-03-31 Vlaamse Instelling Voor Technologish Onderzoek N.V. (Vito) Knitted support for tubular membranes
EP2411127A4 (en) * 2009-03-26 2013-08-21 Bl Technologies Inc NON-BRAIDED REINFORCED HOLLOW FIBER MEMBRANE
US9132390B2 (en) 2009-03-26 2015-09-15 Bl Technologies Inc. Non-braided reinforced holow fibre membrane
CN104941459A (zh) * 2009-03-26 2015-09-30 Bl科技公司 非编织的增强中空纤维膜
AU2010228091B2 (en) * 2009-03-26 2016-06-16 Bl Technologies, Inc. Non-braided reinforced hollow fibre membrane
CN104941459B (zh) * 2009-03-26 2017-09-22 Bl 科技公司 非编织的增强中空纤维膜
US9221020B2 (en) 2010-09-15 2015-12-29 Bl Technologies, Inc. Method to make yarn-reinforced hollow fiber membranes around a soluble core
US9321014B2 (en) 2011-12-16 2016-04-26 Bl Technologies, Inc. Hollow fiber membrane with compatible reinforcements
US9022229B2 (en) 2012-03-09 2015-05-05 General Electric Company Composite membrane with compatible support filaments
US8999454B2 (en) 2012-03-22 2015-04-07 General Electric Company Device and process for producing a reinforced hollow fibre membrane
US9227362B2 (en) 2012-08-23 2016-01-05 General Electric Company Braid welding

Also Published As

Publication number Publication date
US8393479B2 (en) 2013-03-12
JP4718481B2 (ja) 2011-07-06
JP2007513755A (ja) 2007-05-31
EP1689517B1 (de) 2007-10-31
US20080251445A1 (en) 2008-10-16
CA2548409A1 (en) 2005-07-07
ATE376874T1 (de) 2007-11-15
DE10358477B3 (de) 2005-04-21
EP1689517A1 (de) 2006-08-16
DE502004005399D1 (de) 2007-12-13
ES2293325T3 (es) 2008-03-16

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