US20130153485A1 - Filter membrane module, and method for its production - Google Patents

Filter membrane module, and method for its production Download PDF

Info

Publication number
US20130153485A1
US20130153485A1 US13/591,089 US201213591089A US2013153485A1 US 20130153485 A1 US20130153485 A1 US 20130153485A1 US 201213591089 A US201213591089 A US 201213591089A US 2013153485 A1 US2013153485 A1 US 2013153485A1
Authority
US
United States
Prior art keywords
housing
filter elements
filter
membrane module
plastic
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.)
Abandoned
Application number
US13/591,089
Inventor
Christian Goebbert
Manfred Volz
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.)
Nanostone Water GmbH
Original Assignee
KSM Water 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
Priority claimed from DE102010008869A external-priority patent/DE102010008869A1/en
Application filed by KSM Water GmbH filed Critical KSM Water GmbH
Assigned to KSM WATER GMBH reassignment KSM WATER GMBH ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: VOLZ, MANFRED, GOEBBERT, CHRISTIAN
Publication of US20130153485A1 publication Critical patent/US20130153485A1/en
Assigned to NANOSTONE WATER GMBH reassignment NANOSTONE WATER GMBH CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: KSM WATER GMBH
Priority to US15/154,793 priority Critical patent/US10226741B2/en
Priority to US16/257,824 priority patent/US20190151802A1/en
Abandoned legal-status Critical Current

Links

Images

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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02Hollow fibre modules
    • B01D63/021Manufacturing thereof
    • 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
    • B01D63/066Tubular membrane modules with a porous block having membrane coated passages
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/54Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms
    • B01D46/543Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms using membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/56Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
    • B01D46/58Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in parallel
    • B01D46/60Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in parallel arranged concentrically or coaxially
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02Hollow fibre modules
    • B01D63/021Manufacturing thereof
    • B01D63/022Encapsulating hollow fibres
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02Hollow fibre modules
    • B01D63/021Manufacturing thereof
    • B01D63/022Encapsulating hollow fibres
    • B01D63/023Encapsulating materials
    • 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
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/06Tubular membrane modules
    • B01D63/062Tubular membrane modules with membranes on a surface of a support tube
    • B01D63/063Tubular membrane modules with membranes on a surface of a support tube on the inner surface thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/003Membrane bonding or sealing
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2313/00Details relating to membrane modules or apparatus
    • B01D2313/04Specific sealing means
    • B01D2313/041Gaskets or O-rings

Definitions

  • the present disclosure relates to a filter membrane module and a method for producing a filter membrane module.
  • One such membrane module includes an elongated filter element, which is penetrated by at least one longitudinal conduit and comprises a porous material, such as ceramic.
  • the module further includes a housing, which surrounds the filter element and with it forms a collection chamber.
  • Such a module functions as follows: Into one end of each longitudinal conduit, the medium to be treated, the so-called unfiltrate, is introduced. Along the course of the unfiltrate, filtrate passes through the wall surface of the longitudinal conduit, enters the aforementioned collection chamber between the filter element and the housing, and is carried away from there as filtrate. The unfiltrate emerges from the other end of the longitudinal conduits and is optionally returned to the first end of the longitudinal conduit, so as to form a cycle.
  • the wall surfaces of the longitudinal conduits are coated with a material that is also permeable to a certain extent. This usually very thin film usually forms the actual filtration device.
  • a single filter element has a plurality of longitudinal conduits (multi-conduit element). A plurality of such multi-conduit elements is combined to form a membrane module from them.
  • each face end of the filter elements there is a face-end plate. It defines the annular chamber between the housing and the filter elements, specifically in such a way that the annular chamber is sealed off from the outer environment at least in fluid-tight fashion. Sealing it off can be problematic, since during operation varying temperatures prevail, which lead to expansion and contraction of structural parts, in fact in different ways.
  • the face-end boundary plates may for instance be of special steel.
  • EP 1 374 979 A2 describes a filter membrane module having a multitude of spaghetti-type individual filter capillaries, which are bundled at theirs ends by means of a potting material.
  • DE 600 24 966 T2 discloses a thermoplastic filter cartouche with a plurality of concentric filter tubes.
  • US 2008/0035270 A1 relates to a filter membrane module having a multitude of fibers, the ends of which are bundled by means of a potting material.
  • US 2007/0144716 A1 describes a device with porous membranes, the ends of which being unitarily combined by potting.
  • the object of the invention is to provide a filter membrane module having a high filter performance and offering more simple and thus cheaper manufacturing.
  • a plastic potting material such as a thermoplastic, in particular a polymer
  • the plastic thus blocks off the interstices between the filter elements. It forms a mounting ring, which in turn surrounds the filter elements in their end region.
  • thermoset plastics or dual-component plastics such as epoxies or acrylates can be considered.
  • This method is performed on both ends of the bundle of filter elements, so that two mounting rings are created. Then the housing is slipped onto both mounting rings and thus onto the filter element bundle.
  • a mounting ring again comprising a plastic potting material, is first applied to one end and then to the other end of the filter element. After the application, in both cases the plastic potting material is made to harden. The same is done on the other end. Then the housing is again slipped onto the two mounting rings.
  • the housing can be formed of the same material as the mounting rings.
  • the housing can even be in one piece with one of the two mounting rings, by being produced in a single potting operation.
  • the bearing of the housing on at least one of the mounting rings be embodied as a loose bearing, so that impermissible thermal stresses do not occur between the ceramic part and the housing.
  • the housing can be provided with connections for supplying or removing medium, for example for the medium to be treated (so-called unfiltrate) or for the treated medium (filtrate). If the housing is made from thermoplastic material, then potting the connection ports integrally with it is an attractive option.
  • FIG. 1 shows a single hollow ceramic fiber (spaghetti) in perspective.
  • FIG. 2 in an axially vertical cross section, shows three pieces of spaghetti filter elements combined in a bundle.
  • FIG. 3 shows a bundle of spaghetti filter elements surrounded by a sleeve.
  • FIG. 4 schematically shows the subject of FIG. 3 , with one end dipped into a tub that contains a potting material.
  • FIG. 5 shows the bundle with the sleeve of FIG. 3 after the potting material has hardened.
  • FIG. 6 shows the end region of a multi-conduit element in perspective.
  • FIG. 7 shows the subject of FIG. 6 , provided with a mounting ring.
  • FIG. 8 shows the complete filter device in an elevation view and partly cut away, including a plurality of filter elements in one housing.
  • FIG. 9 shows a further filter apparatus in an elevation view and partly cut away.
  • FIG. 10 shows the apparatus of FIG. 9 in a plan view.
  • FIG. 11 shows an embodiment of an inventive filter device in cross section, with five flat membranes.
  • a spaghetti element 1 shown in FIG. 1 is of ceramic. It surrounds a longitudinal conduit 1 . 1 .
  • the spaghetti bundle shown in FIG. 2 includes three pieces of spaghetti 1 , each with a longitudinal conduit 1 . 1 .
  • the three pieces of spaghetti enclose a hollow space 1 . 2 between them.
  • FIG. 3 shows a bundle of spaghetti 1 surrounded by a sleeve 2 .
  • the sleeve 2 has a plurality of openings 2 . 1 , so that there is a conductive connection between the hollow spaces 1 . 2 , each located between pieces of spaghetti 1 adjacent one another, and the external environment.
  • FIG. 4 schematically illustrates the application of a mounting ring 3 —see also FIG. 5 .
  • the subject of FIG. 3 is dipped by one of its ends into a potting material 4 , which is located in a tub 5 .
  • the potting material 4 comprises plastic, such as a thermoplastic material, or synthetic resin.
  • the potting material penetrates through the openings 2 . 1 into the hollow spaces 1 . 2 in the spaghetti 1 and fills them up.
  • the result is the subject shown in FIG. 5 , that is, the spaghetti bundle, surrounded by the sleeve 2 , with the mounting ring 3 .
  • the longitudinal conduits 1 . 1 remain open. This can be achieved in various ways. If the lower end face of the bundle is absolutely flat and flush with the bottom of the tub 5 , then the penetration of potting material into the longitudinal conduits 1 . 1 can be prevented. The ends of the longitudinal conduits 1 . 1 could also be provided with plugs, but this is tedious and expensive. Finally, after the state shown in FIG. 5 is reached, the bundle can be shortened, by cutting off a desired piece at its lower end, since because the diameter of the longitudinal conduits is so slight, the potting material does not penetrate them overly much.
  • FIG. 6 shows the end region of a multi-conduit element 6 having a plurality of longitudinal conduits 6 . 1 .
  • the element 6 is of ceramic. It is hexagonal in cross section. Still other cross sections are also possible here, such as round or oval ones.
  • the mounting rings 3 are seated solidly on the spaghetti bundle, or on the multi-conduit element. Now a union with a housing must be established.
  • the finished filter apparatus is seen in FIG. 8 . In it, a plurality of multi-conduit elements 6 are surrounded by a housing 7 . Instead of the multi-conduit elements 6 , spaghetti elements could also be provided.
  • the housing 7 in the embodiment shown comprises a thermoplastic material. This is the same material that comprises the mounting ring 3 .
  • the housing 7 and mounting ring 3 are produced in a single potting operation and are thus in one piece. This is true in any case for the lower mounting ring 3 . 1 , which in a sense forms the bottom of the housing 7 . It does not apply to the upper mounting ring 3 . 2 , however. There is a seam between it and the upper end of the housing, so that an axial relative motion between the upper mounting ring 3 . 2 and the housing 7 is possible. It is thus also ensured that during the operation of the filter apparatus, the housing 7 can expand to different extents compared to the structural parts surrounded by the housing, namely the multi-conduit elements 6 .
  • the individual multi-conduit elements 6 are surrounded by a collection chamber 9 .
  • the housing 7 includes a lower cap 7 . 1 and an upper cap 7 . 2 .
  • Two connection stubs namely a lower connection stub 7 . 3 and an upper connection stub 7 . 4 , are also formed integrally with the cylindrical part of the housing.
  • the filter apparatus of FIG. 8 functions as follows:
  • medium to be filtered flows to the lower face ends of the multi-conduit elements 6 . There, it enters the longitudinal conduits 6 . 1 and flows through them. It then emerges from the upper ends of the longitudinal conduits 6 . 1 and reaches the upper cap 7 . 2 .
  • filtrate passes crosswise to the flow direction into the longitudinal conduits 6 . 1 through the porous ceramic material of the individual multi-conduit element 6 and reaches the collection chamber 9 . From there, it reaches the lower outlet 7 . 3 and the upper outlet 7 . 4 .
  • the unfiltrate entering the upper cap 7 . 2 can be carried in circulatory fashion and delivered to a further filter apparatus, or the same one, where it passes through further filtration operations.
  • the filtration apparatus shown in FIGS. 9 and 10 again has a housing of a thermoplastic material.
  • the filter elements 1 are of the spaghetti type.
  • FIG. 11 An alternative embodiment of a filtration apparatus, shown in FIG. 11 , has a housing, not shown in this drawing, similar to that of FIGS. 9 and 10 .
  • the multi-conduit elements are not round (“tubular membrane”) but instead are embodied in the form of five elements 6 a - 6 e , all of them flat (“flat membranes”) between which shallow, wide interstices 10 are present.
  • the flat membranes 6 a and 6 e and the flat membranes 6 b and 6 d are embodied identically, but are disposed mirror-symmetrically to one another. Overall, the outer contours of the flat membranes 6 a - 6 e are adapted to insertion into the tubular housing. It is understood that in other embodiments, not shown, a different number of flat membranes can also be used.
  • the cross sections of the two outer flat membranes 6 a and 6 e are in the form of classical circular segments, which are bounded on one side by a circular arc and on the other by a chord.
  • the inner flat membranes 6 b , 6 c and 6 d are each bounded by two circular arcs and two chords.
  • the height h of all five flat membranes 6 a - 6 e is identical. For the sake of simplicity, the height is shown in FIG. 11 only for the upper flat membrane 6 b in FIG. 11 .
  • still other cross sections such as oval or even free-form cross sections, can also occur.
  • each flat membrane 6 a - 6 e there are many longitudinal conduits 6 . 1 , of which for the sake of simplicity only one is provided with a reference numeral in FIG. 11 . In the present instance, the longitudinal conduits 6 . 1 have an approximately square cross section, but they can have a different cross section instead.
  • the production and material of the embodiment of FIG. 11 are identical to the foregoing embodiments.
  • the flat membranes 6 a - 6 e are disposed in the desired manner and at the desired spacing from one another.
  • the axial ends of the flat membranes 6 a - 6 e are potted with a plastic material, as shown as an example in conjunction with a different exemplary embodiment in FIGS. 4 and 5 and described above with reference to them.
  • the result on the axial ends is equivalent mounting rings, of which only one mounting ring 3 . 1 on the end is visible in FIG. 11 .
  • the plastic material on the axial ends of the flat membranes 6 a - 6 e is also present in the interstices 10 , and as a result, they are produced reliably and durably.
  • the function is also essentially equivalent to the function that has already been described above in conjunction with the tubular membranes 6 : While the medium to be filtered is being conducted through the longitudinal conduits 6 . 1 , the filtrate is conducted away via the interstices 10 and the interstice, between the housing and the flat membranes 6 a - 6 e , that is formed by the mounting ring 3 . 1 .

Landscapes

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

Abstract

The invention relates to a method for producing a membrane module, comprising a plurality of elongated filter elements disposed in parallel adjacent to one another, each element comprising a longitudinal channel, a housing enclosing the filter elements, and a collector chamber between the housing and the filter elements.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • This application is a continuation of International Application No. PCT/EP2011/052074 filed on Feb. 11, 2011, which claims the benefit of DE 10 2010 008 869.2, filed Feb. 22, 2010, and DE 20 2010 005 971.2, filed Apr. 22, 2010. The disclosures of the above applications are incorporated herein by reference.
  • FIELD
  • The present disclosure relates to a filter membrane module and a method for producing a filter membrane module.
  • BACKGROUND
  • The statements in this section merely provide background information related to the present disclosure and may not constitute prior art.
  • One such membrane module includes an elongated filter element, which is penetrated by at least one longitudinal conduit and comprises a porous material, such as ceramic. The module further includes a housing, which surrounds the filter element and with it forms a collection chamber.
  • Such a module functions as follows: Into one end of each longitudinal conduit, the medium to be treated, the so-called unfiltrate, is introduced. Along the course of the unfiltrate, filtrate passes through the wall surface of the longitudinal conduit, enters the aforementioned collection chamber between the filter element and the housing, and is carried away from there as filtrate. The unfiltrate emerges from the other end of the longitudinal conduits and is optionally returned to the first end of the longitudinal conduit, so as to form a cycle. The wall surfaces of the longitudinal conduits are coated with a material that is also permeable to a certain extent. This usually very thin film usually forms the actual filtration device.
  • A single filter element has a plurality of longitudinal conduits (multi-conduit element). A plurality of such multi-conduit elements is combined to form a membrane module from them.
  • On each face end of the filter elements, there is a face-end plate. It defines the annular chamber between the housing and the filter elements, specifically in such a way that the annular chamber is sealed off from the outer environment at least in fluid-tight fashion. Sealing it off can be problematic, since during operation varying temperatures prevail, which lead to expansion and contraction of structural parts, in fact in different ways. The face-end boundary plates may for instance be of special steel.
  • Exemplary embodiments have become known from EP 0 270 051 B1 and DE 690 19 552 T2. EP 1 374 979 A2 describes a filter membrane module having a multitude of spaghetti-type individual filter capillaries, which are bundled at theirs ends by means of a potting material. DE 600 24 966 T2 discloses a thermoplastic filter cartouche with a plurality of concentric filter tubes. US 2008/0035270 A1 relates to a filter membrane module having a multitude of fibers, the ends of which are bundled by means of a potting material. US 2007/0144716 A1 describes a device with porous membranes, the ends of which being unitarily combined by potting.
  • SUMMARY
  • The object of the invention is to provide a filter membrane module having a high filter performance and offering more simple and thus cheaper manufacturing.
  • This object is attained by the features of the independent claims.
  • One fundamental concept of the invention is that a plastic potting material, such as a thermoplastic, in particular a polymer, is applied to the end region of the filter elements. The plastic thus blocks off the interstices between the filter elements. It forms a mounting ring, which in turn surrounds the filter elements in their end region.
  • The term “plastic” should be understood in the broadest sense. For instance, thermoset plastics or dual-component plastics such as epoxies or acrylates can be considered.
  • This method is performed on both ends of the bundle of filter elements, so that two mounting rings are created. Then the housing is slipped onto both mounting rings and thus onto the filter element bundle.
  • In an inventive multi-conduit element, a mounting ring, again comprising a plastic potting material, is first applied to one end and then to the other end of the filter element. After the application, in both cases the plastic potting material is made to harden. The same is done on the other end. Then the housing is again slipped onto the two mounting rings.
  • Flat membranes can be manufactured at low cost. By means of the flat and large interstices formed between the filter elements, the filtrate can be bled off very efficiently.
  • The housing can be formed of the same material as the mounting rings. The housing can even be in one piece with one of the two mounting rings, by being produced in a single potting operation.
  • In filter devices of the aforementioned structural type with ceramic filter elements, one known problem is the variably pronounced expansion under the influence of heat. This problem arises when materials with different coefficients of thermal expansion are used.
  • It is therefore recommended that the bearing of the housing on at least one of the mounting rings be embodied as a loose bearing, so that impermissible thermal stresses do not occur between the ceramic part and the housing.
  • The housing can be provided with connections for supplying or removing medium, for example for the medium to be treated (so-called unfiltrate) or for the treated medium (filtrate). If the housing is made from thermoplastic material, then potting the connection ports integrally with it is an attractive option.
  • Further areas of applicability will become apparent from the description provided herein. It should be understood that the description and specific examples are intended for purposes of illustration only and are not intended to limit the scope of the present disclosure.
  • DRAWINGS
  • The drawings described herein are for illustration purposes only and are not intended to limit the scope of the present disclosure in any way.
  • FIG. 1 shows a single hollow ceramic fiber (spaghetti) in perspective.
  • FIG. 2, in an axially vertical cross section, shows three pieces of spaghetti filter elements combined in a bundle.
  • FIG. 3 shows a bundle of spaghetti filter elements surrounded by a sleeve.
  • FIG. 4 schematically shows the subject of FIG. 3, with one end dipped into a tub that contains a potting material.
  • FIG. 5 shows the bundle with the sleeve of FIG. 3 after the potting material has hardened.
  • FIG. 6 shows the end region of a multi-conduit element in perspective.
  • FIG. 7 shows the subject of FIG. 6, provided with a mounting ring.
  • FIG. 8 shows the complete filter device in an elevation view and partly cut away, including a plurality of filter elements in one housing.
  • FIG. 9 shows a further filter apparatus in an elevation view and partly cut away.
  • FIG. 10 shows the apparatus of FIG. 9 in a plan view.
  • FIG. 11 shows an embodiment of an inventive filter device in cross section, with five flat membranes.
  • DETAILED DESCRIPTION
  • The following description is merely exemplary in nature and is not intended to limit the present disclosure, application, or uses. It should be understood that throughout the drawings, corresponding reference numerals indicate like or corresponding parts and features. It should also be understood that various cross-hatching patterns used in the drawings are not intended to limit the specific materials that may be employed with the present disclosure. The cross-hatching patterns are merely exemplary of preferable materials or are used to distinguish between adjacent or mating components illustrated within the drawings for purposes of clarity.
  • A spaghetti element 1 shown in FIG. 1 is of ceramic. It surrounds a longitudinal conduit 1.1. The spaghetti bundle shown in FIG. 2 includes three pieces of spaghetti 1, each with a longitudinal conduit 1.1. The three pieces of spaghetti enclose a hollow space 1.2 between them.
  • FIG. 3 shows a bundle of spaghetti 1 surrounded by a sleeve 2. The sleeve 2 has a plurality of openings 2.1, so that there is a conductive connection between the hollow spaces 1.2, each located between pieces of spaghetti 1 adjacent one another, and the external environment.
  • FIG. 4 schematically illustrates the application of a mounting ring 3—see also FIG. 5. For that purpose, the subject of FIG. 3 is dipped by one of its ends into a potting material 4, which is located in a tub 5. The potting material 4 comprises plastic, such as a thermoplastic material, or synthetic resin. After the subject of FIG. 3 has been dipped, the potting material penetrates through the openings 2.1 into the hollow spaces 1.2 in the spaghetti 1 and fills them up. After the potting material has hardened, the result is the subject shown in FIG. 5, that is, the spaghetti bundle, surrounded by the sleeve 2, with the mounting ring 3.
  • For the filtration process, it is necessary that the longitudinal conduits 1.1 remain open. This can be achieved in various ways. If the lower end face of the bundle is absolutely flat and flush with the bottom of the tub 5, then the penetration of potting material into the longitudinal conduits 1.1 can be prevented. The ends of the longitudinal conduits 1.1 could also be provided with plugs, but this is tedious and expensive. Finally, after the state shown in FIG. 5 is reached, the bundle can be shortened, by cutting off a desired piece at its lower end, since because the diameter of the longitudinal conduits is so slight, the potting material does not penetrate them overly much.
  • FIG. 6 shows the end region of a multi-conduit element 6 having a plurality of longitudinal conduits 6.1. The element 6 is of ceramic. It is hexagonal in cross section. Still other cross sections are also possible here, such as round or oval ones.
  • The application of mounting rings is done for the multi-conduit element in precisely the same way as for the spaghetti element. See FIGS. 4 and 5. However, what is crucial here is solely the application of the mounting ring 3. Conversely, it is no longer crucial to fill up hollow spaces analogously to the hollow spaces 1.2 in the bundle shown in FIG. 2.
  • In each case, the mounting rings 3 are seated solidly on the spaghetti bundle, or on the multi-conduit element. Now a union with a housing must be established. The finished filter apparatus is seen in FIG. 8. In it, a plurality of multi-conduit elements 6 are surrounded by a housing 7. Instead of the multi-conduit elements 6, spaghetti elements could also be provided.
  • The housing 7 in the embodiment shown comprises a thermoplastic material. This is the same material that comprises the mounting ring 3. The housing 7 and mounting ring 3 are produced in a single potting operation and are thus in one piece. This is true in any case for the lower mounting ring 3.1, which in a sense forms the bottom of the housing 7. It does not apply to the upper mounting ring 3.2, however. There is a seam between it and the upper end of the housing, so that an axial relative motion between the upper mounting ring 3.2 and the housing 7 is possible. It is thus also ensured that during the operation of the filter apparatus, the housing 7 can expand to different extents compared to the structural parts surrounded by the housing, namely the multi-conduit elements 6.
  • At this point, however, a seal is required. See the O-ring 8. This ring is let into the outer circumference of the upper mounting ring 3.2. It can already be potted integrally with the mounting ring 3.2 in the operation of potting the mounting ring.
  • The individual multi-conduit elements 6 are surrounded by a collection chamber 9.
  • The housing 7 includes a lower cap 7.1 and an upper cap 7.2. Two connection stubs, namely a lower connection stub 7.3 and an upper connection stub 7.4, are also formed integrally with the cylindrical part of the housing.
  • The filter apparatus of FIG. 8 functions as follows:
  • Through the lower cap 7.1, medium to be filtered (unfiltrate) flows to the lower face ends of the multi-conduit elements 6. There, it enters the longitudinal conduits 6.1 and flows through them. It then emerges from the upper ends of the longitudinal conduits 6.1 and reaches the upper cap 7.2.
  • Over this course, filtrate passes crosswise to the flow direction into the longitudinal conduits 6.1 through the porous ceramic material of the individual multi-conduit element 6 and reaches the collection chamber 9. From there, it reaches the lower outlet 7.3 and the upper outlet 7.4.
  • In a known manner, the unfiltrate entering the upper cap 7.2 can be carried in circulatory fashion and delivered to a further filter apparatus, or the same one, where it passes through further filtration operations.
  • The filtration apparatus shown in FIGS. 9 and 10 again has a housing of a thermoplastic material. The filter elements 1 are of the spaghetti type.
  • An alternative embodiment of a filtration apparatus, shown in FIG. 11, has a housing, not shown in this drawing, similar to that of FIGS. 9 and 10. However, the multi-conduit elements are not round (“tubular membrane”) but instead are embodied in the form of five elements 6 a-6 e, all of them flat (“flat membranes”) between which shallow, wide interstices 10 are present. The flat membranes 6 a and 6 e and the flat membranes 6 b and 6 d are embodied identically, but are disposed mirror-symmetrically to one another. Overall, the outer contours of the flat membranes 6 a-6 e are adapted to insertion into the tubular housing. It is understood that in other embodiments, not shown, a different number of flat membranes can also be used.
  • The cross sections of the two outer flat membranes 6 a and 6 e are in the form of classical circular segments, which are bounded on one side by a circular arc and on the other by a chord. The inner flat membranes 6 b, 6 c and 6 d are each bounded by two circular arcs and two chords. The height h of all five flat membranes 6 a-6 e is identical. For the sake of simplicity, the height is shown in FIG. 11 only for the upper flat membrane 6 b in FIG. 11. Here again, it is understood that in an embodiment that is not shown, still other cross sections, such as oval or even free-form cross sections, can also occur. In each flat membrane 6 a-6 e, there are many longitudinal conduits 6.1, of which for the sake of simplicity only one is provided with a reference numeral in FIG. 11. In the present instance, the longitudinal conduits 6.1 have an approximately square cross section, but they can have a different cross section instead.
  • The production and material of the embodiment of FIG. 11 are identical to the foregoing embodiments. First, the flat membranes 6 a-6 e are disposed in the desired manner and at the desired spacing from one another. Then the axial ends of the flat membranes 6 a-6 e are potted with a plastic material, as shown as an example in conjunction with a different exemplary embodiment in FIGS. 4 and 5 and described above with reference to them. The result on the axial ends is equivalent mounting rings, of which only one mounting ring 3.1 on the end is visible in FIG. 11. The plastic material on the axial ends of the flat membranes 6 a-6 e is also present in the interstices 10, and as a result, they are produced reliably and durably.
  • The function is also essentially equivalent to the function that has already been described above in conjunction with the tubular membranes 6: While the medium to be filtered is being conducted through the longitudinal conduits 6.1, the filtrate is conducted away via the interstices 10 and the interstice, between the housing and the flat membranes 6 a-6 e, that is formed by the mounting ring 3.1.
  • The description of the disclosure is merely exemplary in nature and, thus, variations that do not depart from the substance of the disclosure are intended to be within the scope of the disclosure. Such variations are not to be regarded as a departure from the spirit and scope of the disclosure.

Claims (9)

What is claimed is:
1. A filter membrane module, including: a plurality of elongated filter elements, which each have a plurality of longitudinal conduits; and a housing surrounding the filter elements; wherein the filter elements are potted in both of their end regions with a material, which forms after hardening a mounting ring surrounding the plurality of filter elements; wherein either the housing is slipped over the mounting ring and sealingly joined to it or is unitary with one of the two mounting rings by being manufactured in a single potting operation, wherein the filter elements are formed as flat membranes, which preferably have a segment of a circle type cross section, between which flat and large interstices are provided, and in that the wall surfaces of the longitudinal conduits are coated with a filtration material such that the medium to be filtrated can be conducted through the longitudinal conduits and the filtered medium can be discharged through the interstices and a collecting space which is formed by means of the mounting ring between housing and the flat membranes.
2. The filter membrane module according to claim 1, wherein the housing comprises a plastic, for instance thermoplastic, a thermoset plastic or a dual-component plastic, such as epoxy or acrylate.
3. The filter membrane module according to claim 1, wherein the housing has one connection each for the unfiltrate and for the filtrate.
4. The filter membrane module according to claim 1, wherein three sealing elements are potted integrally with the mounting rings.
5. A method for producing a filter membrane module according to claim 1, wherein the method comprises: applying a potting material of plastic, in particular a thermoplastic, a thermoset plastic or a dual-component plastic such as an epoxy or acrylate, to one end region of the plurality of filter elements such that it sheathes the filter elements on their ends and thereby forms a mounting ring; hardening the potting material; doing the same to the other end; if necessary: slipping the housing over the mounting rings; sealing off the mounting rings from the housing.
6. The method according to claim 5, wherein the end regions of the filter elements are dipped into the potting material.
7. The method according to claim 5, wherein a sleeve is used for forming the mounting rings.
8. The method according to claim 5, wherein at least the jacket faces of the mounting rings are mechanically machined.
9. The method according to claim 5, wherein at least one sealing ring each is potted integrally into a mounting ring.
US13/591,089 2010-02-22 2012-08-21 Filter membrane module, and method for its production Abandoned US20130153485A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US15/154,793 US10226741B2 (en) 2010-02-22 2016-05-13 Filter membrane module, and method for its production
US16/257,824 US20190151802A1 (en) 2010-02-22 2019-01-25 Filter membrane module, and method for its production

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
DE102010008869A DE102010008869A1 (en) 2010-02-22 2010-02-22 Method for manufacturing membrane module, involves combining multiple filter elements into bundle, and applying melt made of plastic, particularly thermoplastic resin on end area of bundle
DE102010008869.2 2010-02-22
DE202010005971 2010-04-22
DE202010005971.2 2010-04-22
PCT/EP2011/052074 WO2011101295A1 (en) 2010-02-22 2011-02-11 Method for producing a membrane module and membrane module

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2011/052074 Continuation WO2011101295A1 (en) 2010-02-22 2011-02-11 Method for producing a membrane module and membrane module

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US15/154,793 Continuation US10226741B2 (en) 2010-02-22 2016-05-13 Filter membrane module, and method for its production

Publications (1)

Publication Number Publication Date
US20130153485A1 true US20130153485A1 (en) 2013-06-20

Family

ID=43857992

Family Applications (3)

Application Number Title Priority Date Filing Date
US13/591,089 Abandoned US20130153485A1 (en) 2010-02-22 2012-08-21 Filter membrane module, and method for its production
US15/154,793 Active 2031-10-20 US10226741B2 (en) 2010-02-22 2016-05-13 Filter membrane module, and method for its production
US16/257,824 Pending US20190151802A1 (en) 2010-02-22 2019-01-25 Filter membrane module, and method for its production

Family Applications After (2)

Application Number Title Priority Date Filing Date
US15/154,793 Active 2031-10-20 US10226741B2 (en) 2010-02-22 2016-05-13 Filter membrane module, and method for its production
US16/257,824 Pending US20190151802A1 (en) 2010-02-22 2019-01-25 Filter membrane module, and method for its production

Country Status (7)

Country Link
US (3) US20130153485A1 (en)
EP (1) EP2539052B1 (en)
KR (1) KR101738202B1 (en)
CN (2) CN105597546B (en)
CA (1) CA2790599A1 (en)
DE (1) DE202011110920U1 (en)
WO (1) WO2011101295A1 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016174373A1 (en) 2015-04-29 2016-11-03 Saint-Gobain Centre De Recherches Et D'etudes Europeen Assembled filters for the filtration of liquids
JP2017056427A (en) * 2015-09-18 2017-03-23 日本特殊陶業株式会社 Separation membrane structure, and separation membrane structure module
WO2017027626A3 (en) * 2015-08-10 2017-05-04 Nanostone Water Inc. Ceramic membrane module with recessed membrane and related methods
WO2017182276A1 (en) * 2016-04-22 2017-10-26 Nanostone Water Gmbh Ceramic membrane module with external frame assembly and related methods
WO2017185033A1 (en) * 2016-04-22 2017-10-26 Nanostone Water Us Ceramic membrane module with drive plate and related methods
WO2017185035A1 (en) * 2016-04-22 2017-10-26 Nanostone Water Us Ceramic membrane module with inflatable assembly and related methods
US20180333687A1 (en) * 2016-01-25 2018-11-22 Noritake Co., Limited Apparatus for generating fine-bubble-containing liquid
US10226741B2 (en) 2010-02-22 2019-03-12 Nanostone Water Gmbh Filter membrane module, and method for its production
WO2019141498A1 (en) * 2018-01-16 2019-07-25 Nanostone Water Inc. Membrane modules with limited defects and related methods

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11041565B2 (en) * 2013-11-19 2021-06-22 1934612 Ontario Inc. Filtration methods, apparatus, and systems using a ceramic seal gasket
US20150246305A1 (en) * 2014-03-02 2015-09-03 Johannes A. Thomassen Plastic membrane housing for ceramic membranes
EP2933010B1 (en) * 2014-04-17 2019-12-25 Gambro Lundia AB Thermoforming of fiber bundles
CN106669427B (en) * 2016-11-18 2019-12-10 江苏坤奕环境工程有限公司 Integrated wear-resistant, crystal-resistant and corrosion-resistant cross-flow microfiltration membrane element

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4781831A (en) * 1986-12-19 1988-11-01 Goldsmith Robert L Cross-flow filtration device with filtrate flow conduits and method of forming same
US5855781A (en) * 1992-07-23 1999-01-05 Noritake Co., Ltd. Monolithic ceramic filter
US6077436A (en) * 1997-01-06 2000-06-20 Corning Incorporated Device for altering a feed stock and method for using same
US6328777B1 (en) * 1998-12-23 2001-12-11 Thomas Josef Heimbach Gesellschaft Mit Beschrankter Haftung & Co. Filter system
US20020038536A1 (en) * 2000-09-29 2002-04-04 Walter Best Filter device
US20040035786A1 (en) * 2002-08-21 2004-02-26 Goldsmith Robert L. Airlift membrane device and membrane bioreactor and bioreactor process containing same
US20050279693A1 (en) * 2004-06-22 2005-12-22 Ngk Insulators, Ltd. Ceramic filter
US7294267B2 (en) * 2002-09-27 2007-11-13 Mitsubishi Rayon Co., Ltd. Hollow fiber membrane module, hollow fiber membrane module unit, membrane filtration device using the same and method of operating the same

Family Cites Families (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2607880B1 (en) 1986-12-03 1989-02-03 Ceramiques Tech Soc D METHOD FOR ASSEMBLING A MODULE OF SEPARATING ELEMENTS WITH CERAMIC SUPPORT AND MODULE OBTAINED BY THIS METHOD
US4758341A (en) 1987-04-20 1988-07-19 The Dow Chemical Company Membrane separation device
US4980060A (en) 1987-07-13 1990-12-25 Asahi Kasei Kogyo Kabushiki Kaisha Hollow fiber membranes with fusion-bonded end portions
DD272608A1 (en) 1988-05-30 1989-10-18 Akad Wissenschaften Ddr CROSS POWER FILTER MODULE
FR2642328B1 (en) 1989-01-27 1991-04-12 Ceramiques Tech Soc D METHOD FOR ASSEMBLING A RIGID ELEMENT WITH A SEPARATING, FILTERING, OR CATALYTIC TRANSFORMATION MEMBRANE IN A MODULE
DE3916511A1 (en) 1989-05-20 1990-12-13 Seitz Filter Werke MEMBRANE FILTER DEVICE FOR MICRO AND ULTRAFILTRATION OF FLUIDS IN THE CROSSFLOW PROCESS
CH681281A5 (en) 1990-04-12 1993-02-26 Johannes Wieser Linhart Dipl I Particle filter for sepg. process materials - comprises particulate porous elongated block with 1st channel for raw mixt. and 2nd channel for permeate
JPH05146609A (en) 1991-12-02 1993-06-15 Toshiba Ceramics Co Ltd Ceramic filter device
US5779897A (en) 1996-11-08 1998-07-14 Permea, Inc. Hollow fiber membrane device with inert filaments randomly distributed in the inter-fiber voids
US6074559A (en) 1996-11-21 2000-06-13 Fresenius Medical Care Deutschland Gmbh Filter device having a hollow fiber bundle and associated sealing devices
DE19846041A1 (en) * 1998-10-07 2000-04-20 Membraflow Gmbh & Co Kg Filter Membrane module
DE60024966T2 (en) 1999-01-29 2006-08-17 Mykrolis Corp., Billerica PERFLUORED, THERMOPLASTIC FILTER CARTRIDGE
US6126833A (en) 1999-02-22 2000-10-03 Ceramem Corporation Cross-flow filtration device with filtrate conduit network and method of making same
JP3277918B2 (en) * 1999-06-15 2002-04-22 住友電気工業株式会社 Filter using porous ceramics
NL1013465C2 (en) 1999-11-02 2001-05-03 Stork Friesland Bv Membrane filtration element with sleeve element and sleeve members.
DE10026344A1 (en) 2000-04-01 2001-10-04 Membraflow Gmbh & Co Kg Filter Filter module
JP4599656B2 (en) 2000-04-26 2010-12-15 宇部興産株式会社 Hollow fiber separation membrane element, hollow fiber separation membrane module, and manufacturing method thereof
DE10113465A1 (en) * 2001-03-19 2002-10-02 Aaflowsystems Gmbh & Co Kg filtration unit
DE10227721B4 (en) * 2002-06-21 2008-03-13 Hermsdorfer Institut Für Technische Keramik E.V. Process for producing a bundle of ceramic capillaries for a separation module
DE20321132U1 (en) 2003-02-13 2006-02-16 Itn Nanovation Gmbh Filtration device for e.g. separating oil-water emulsions comprises a pressure-resistant housing with a liquid inlet opening and a filtrate outlet opening
EP1706699B1 (en) 2003-12-22 2011-02-09 Entegris, Inc. Exchange device with potted hollow conduits and methods of application
DE102005008900B4 (en) 2005-02-26 2008-02-14 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Process for producing gastight and temperature-resistant modules with ceramic hollow fiber or capillary membranes
GB2431154B (en) * 2005-10-15 2011-05-18 Daniel Stefanini Purification treatment of water
CN100479904C (en) * 2005-12-14 2009-04-22 南京九思高科技有限公司 Ceramic film filtering element
DE102006008453A1 (en) 2006-02-17 2007-08-23 Itn Nanovation Ag Cleaning process for wastewater
DE102006022502A1 (en) 2006-05-08 2007-11-29 Ltn Nanovation Ag Filter unit for wastewater treatment and drinking water production
DE102006036498A1 (en) 2006-07-28 2008-02-07 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Composite honeycomb structure, e.g. useful as a filter or catalytic converter, comprises comprises prismatic segments whose sides are bonded together over their whole length parallel to the direction of flow
US7662333B2 (en) 2006-08-14 2010-02-16 Generon Igs, Inc. Vacuum-assisted potting of fiber module tubesheets
US7614505B2 (en) * 2006-11-08 2009-11-10 Ngk Insulators, Ltd. Ceramic filter and regenerating method thereof
DE102007052088A1 (en) 2007-10-31 2009-05-07 M. Mannesmann Gmbh & Co. Kg Membrane filter for producing Legionella-free water, comprises tubular housing comprising water inlet, water outlet and bundle of membrane hollow fibers, and silver layer provided in a part of the inner surface of the housing
JP2009160561A (en) 2008-01-10 2009-07-23 Sumitomo Electric Fine Polymer Inc Filtration module
DE102008036920A1 (en) 2008-08-04 2010-02-11 Itn Nanovation Ag Filtration unit for the treatment of water
DE202011110920U1 (en) 2010-02-22 2017-03-31 Nanostone Water Gmbh membrane module

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4781831A (en) * 1986-12-19 1988-11-01 Goldsmith Robert L Cross-flow filtration device with filtrate flow conduits and method of forming same
US5855781A (en) * 1992-07-23 1999-01-05 Noritake Co., Ltd. Monolithic ceramic filter
US6077436A (en) * 1997-01-06 2000-06-20 Corning Incorporated Device for altering a feed stock and method for using same
US6328777B1 (en) * 1998-12-23 2001-12-11 Thomas Josef Heimbach Gesellschaft Mit Beschrankter Haftung & Co. Filter system
US20020038536A1 (en) * 2000-09-29 2002-04-04 Walter Best Filter device
US20040035786A1 (en) * 2002-08-21 2004-02-26 Goldsmith Robert L. Airlift membrane device and membrane bioreactor and bioreactor process containing same
US7294267B2 (en) * 2002-09-27 2007-11-13 Mitsubishi Rayon Co., Ltd. Hollow fiber membrane module, hollow fiber membrane module unit, membrane filtration device using the same and method of operating the same
US20050279693A1 (en) * 2004-06-22 2005-12-22 Ngk Insulators, Ltd. Ceramic filter

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10226741B2 (en) 2010-02-22 2019-03-12 Nanostone Water Gmbh Filter membrane module, and method for its production
WO2016174373A1 (en) 2015-04-29 2016-11-03 Saint-Gobain Centre De Recherches Et D'etudes Europeen Assembled filters for the filtration of liquids
FR3035599A1 (en) * 2015-04-29 2016-11-04 Saint-Gobain Centre De Rech Et D'Etudes Europeen ASSEMBLED FILTERS FOR FILTERING LIQUIDS
WO2017027626A3 (en) * 2015-08-10 2017-05-04 Nanostone Water Inc. Ceramic membrane module with recessed membrane and related methods
JP2017056427A (en) * 2015-09-18 2017-03-23 日本特殊陶業株式会社 Separation membrane structure, and separation membrane structure module
US20180333687A1 (en) * 2016-01-25 2018-11-22 Noritake Co., Limited Apparatus for generating fine-bubble-containing liquid
WO2017182276A1 (en) * 2016-04-22 2017-10-26 Nanostone Water Gmbh Ceramic membrane module with external frame assembly and related methods
WO2017185033A1 (en) * 2016-04-22 2017-10-26 Nanostone Water Us Ceramic membrane module with drive plate and related methods
WO2017185035A1 (en) * 2016-04-22 2017-10-26 Nanostone Water Us Ceramic membrane module with inflatable assembly and related methods
US10744464B2 (en) 2016-04-22 2020-08-18 Nanostone Water Inc. Ceramic membrane module with drive plate and related methods
US10758870B2 (en) 2016-04-22 2020-09-01 Nanostone Water Gmbh Ceramic membrane module with external frame assembly and related methods
WO2019141498A1 (en) * 2018-01-16 2019-07-25 Nanostone Water Inc. Membrane modules with limited defects and related methods

Also Published As

Publication number Publication date
CN102834166A (en) 2012-12-19
KR20130004302A (en) 2013-01-09
WO2011101295A1 (en) 2011-08-25
CN105597546A (en) 2016-05-25
US10226741B2 (en) 2019-03-12
DE202011110920U1 (en) 2017-03-31
CN102834166B (en) 2016-02-03
US20160361689A1 (en) 2016-12-15
EP2539052A1 (en) 2013-01-02
CA2790599A1 (en) 2011-08-25
EP2539052B1 (en) 2017-07-26
CN105597546B (en) 2018-08-24
KR101738202B1 (en) 2017-05-29
US20190151802A1 (en) 2019-05-23

Similar Documents

Publication Publication Date Title
US10226741B2 (en) Filter membrane module, and method for its production
JP2015506269A5 (en)
RU2641127C2 (en) Hollow fibre cartridge, its components and method of their manufacture
US7264725B2 (en) Hollow fiber membrane contactor and method of making same
EP2825296B1 (en) Method for sealing hollow fiber membranes
CN111514759B (en) Hollow fiber membrane module and method for manufacturing hollow fiber membrane module
JPH0312928B2 (en)
KR20140049421A (en) Hollow fiber membrane module and method for repairing the same
CN109641180A (en) Diffusion and/or Filtration Equipment
JP2018536537A (en) Hollow fiber membrane filtration device and manufacturing method thereof
US20180250853A1 (en) Membrane Potting Methods
JP6252281B2 (en) Method for producing hollow fiber membrane module
JP2003236347A (en) Hollow fiber membrane assembled body and method for manufacturing the same
CN111330448B (en) Casting end cap, casting device and casting method of ultrafiltration membrane
CN114206478B (en) Device for exchanging material and/or energy between two media and method for producing said device
CN110740803B (en) Hollow fiber membrane device for mass transfer between two fluids, method for the production thereof, and coil and core assembly therefor
JP2017039122A (en) Hollow fiber membrane module
CN212262914U (en) Casting end cover and casting device of milipore filter
EP1530996B1 (en) Hollow fiber membrane separation device
JP2836791B2 (en) Method for manufacturing hollow fiber bundle cartridge and cartridge case used in the method
KR101629613B1 (en) Hollow fiber membrane module and method for repairing the same
HK40064318A (en) Device for material and/or energy exchange between two media and method for the production thereof
JP6835538B2 (en) A method of fixing at least one end of a hollow fiber membrane bundle to a tubular module case
JP5385523B2 (en) Method for manufacturing separation membrane module

Legal Events

Date Code Title Description
AS Assignment

Owner name: KSM WATER GMBH, GERMANY

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:GOEBBERT, CHRISTIAN;VOLZ, MANFRED;SIGNING DATES FROM 20120806 TO 20120808;REEL/FRAME:028829/0220

AS Assignment

Owner name: NANOSTONE WATER GMBH, GERMANY

Free format text: CHANGE OF NAME;ASSIGNOR:KSM WATER GMBH;REEL/FRAME:037233/0468

Effective date: 20140814

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION