WO2010108285A1 - Non-braided reinforced hollow fibre membrane - Google Patents
Non-braided reinforced hollow fibre membrane Download PDFInfo
- Publication number
- WO2010108285A1 WO2010108285A1 PCT/CA2010/000469 CA2010000469W WO2010108285A1 WO 2010108285 A1 WO2010108285 A1 WO 2010108285A1 CA 2010000469 W CA2010000469 W CA 2010000469W WO 2010108285 A1 WO2010108285 A1 WO 2010108285A1
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- WIPO (PCT)
- Prior art keywords
- filaments
- reinforcing
- needle
- reinforcing structure
- membrane
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/08—Hollow fibre membranes
- B01D69/085—Details relating to the spinneret
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/08—Hollow fibre membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/02—Hollow fibre modules
- B01D63/04—Hollow fibre modules comprising multiple hollow fibre assemblies
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/40—Fibre reinforced membranes
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T29/00—Metal working
- Y10T29/49—Method of mechanical manufacture
- Y10T29/49826—Assembling or joining
Definitions
- This specification relates to reinforced hollow fiber membranes, to reinforcement structures for hollow fiber membranes, and to methods of making hollow fiber membranes and reinforcement structures for them.
- Polymeric separation membranes in the form of small capillary tubes or hollow fibres can be made from a variety of polymers by different methods that can be categorized as NIPS (non-solvent induced phase separation), or TIPS (thermally induced phase separation).
- the membranes may have a separation layer on the outside and may be used, for example, for microfiltration (MF) or ultrafiltration (UF).
- the simplest approach is to make the hollow fiber from a single material that provides mechanical properties (tensile resistance, burst or collapse resistance, and resistance to fatigue by cracking), separation properties (rejection and permeability) and chemical properties (tolerance to chemicals in the feed or to cleaners).
- mechanical properties tensile resistance, burst or collapse resistance, and resistance to fatigue by cracking
- separation properties rejection and permeability
- chemical properties tolerance to chemicals in the feed or to cleaners.
- composite membranes are prepared.
- a microporous support structure is coated with the separation layer.
- a special case of composite hollow fibre membrane is that where a hollow textile braided sleeve is coated or impregnated with a polymeric membrane.
- the braid provides the strength and flexibility that is needed in MF/UF applications such as filtration of water suspensions where continuous or intermittent agitation (with air or otherwise) of the hollow fibers is needed to prevent fouling or accumulation of solids on the membrane surface.
- Patent 7,306,105 to Shinada et al. where the braid is coated with 2 different porous layers.
- Braid-supported hollow fibre membranes are normally prepared as follows.
- the braid is fabricated on a braider, wound on a bobbin, and transferred to a spin line where it is coated or impregnated with a polymer solution.
- Relatively thick wall braids are used in order for the final hollow fibre membrane to be round in shape. This is necessary because the braid must be round-stable, i.e., prevented from flattening out through winding and unwinding and must be round when inserted in the coating spinneret.
- Round-stable braids are thus normally made with a thick wall and have two major disadvantages.
- the ratio of inside-to-outside diameters is the normalized parameter that determines the pressure loss to conduct permeate through the lumen of the membrane. The high lumen pressure drop in thick wall braids thus limits the length of hollow fibres that can be potted in a module.
- round-stable braids are fabricated with a large number of braiding carriers. Each carrier is supplied from a different bobbin and the bobbins must cross paths in the braiding machine.
- the bobbins must start from a stop position, accelerate and decelerate and come back to a stop position every time the carriers cross each other. This is a very slow operation.
- Small diameter braids (less than 2mm) are normally made at a speed of less than 0.5 m/min. In contrast, the braid coating/impregnation operation is typically done much faster, at a speed of greater than 15 m/min.
- a reinforcing structure for a hollow fibre membrane is made with a plurality of reinforcing filaments.
- the reinforcing filaments can include longitudinally extending filaments, which may be called warp filaments, as well as one or more filaments that extend obliquely between warp filaments, which may be called "wrap" filaments.
- a wrap filament is provided in a continuous spiral around the warp filaments.
- a plurality of discontinuous wrap filament segments collectively extend between each pair of adjacent warp filaments, although individual segments might not extend completely around the reinforcing structure.
- a continuous wrap filament extends along the length of the reinforcing structure and also back and forth between two or more warp filaments.
- the reinforcing filaments are not woven or braided together, but the may be bonded together at one or more, or a plurality of, points of contact between them.
- the bonding may be by way of heat, softening with a solvent or UV-activation.
- the bonding may occur before a membrane is formed around the reinforcing structure.
- a reinforcing structure may be bonded while a membrane is formed around the reinforcing structure by way of a solvent in the membrane dope softening the reinforcing filaments or an outer layer of the reinforcing filaments.
- a reinforcing filament may be a monofilament or a multi-filament such as a yarn.
- a reinforcing filament may be made of a polymer and have an outer layer of another polymer that better responds to a bonding method.
- a reinforcing filament may have an outer layer of a polymer that is soluble in a solvent in a membrane forming dope.
- a hollow fiber membrane has a reinforcing structure embedded within a membrane wall.
- the membrane may have an ID/OD ratio of 0.6 or more.
- the membrane may have an inside diameter in a range of about 0.5 mm to 2.0 mm.
- a reinforcing structure may be formed over a needle or wire while advancing a formed portion of the structure along the needle or wire. The formed portion of the reinforcing structure may be advanced directly into a dope coating spinneret before or directly after moving the reinforcing structure past an end of the needle or wire, without first winding the reinforcing structure onto a bobbin or reel.
- a polymer dope can be injected into the dope coating spinneret such that formation of the reinforcing structure and the membrane occur one after the other at the same speed.
- One or more filaments may be bonded together as the reinforcing structure is moving along the needle or wire, or in the dope coating spinneret.
- Figure 1 is a cross section of a hollow fiber membrane showing a reinforcing structure with a single set of wrap filaments.
- Figure 2 is a side view a cage-like reinforcing structure with warp filaments and two sets of spiral wrap filaments.
- Figure 3 is a schematic representation, in elevation view, of a machine for making a non-braided reinforced hollow fiber membrane with preexisting wrap filaments.
- Figure 4 is a schematic representation, in elevation view, of a machine for making a non-braided reinforced hollow fiber membrane with in-situ filament formation.
- Figures 5A and 5B are elevation and plan view, respectively, drawings of an in-situ filament formation device for making zigzag wrap filaments.
- Figures 6A and 6B are elevation and bottom plan view, respectively, drawings of an in-situ filament formation device for making discontinuous wrap filaments.
- Figure 7 is a side view of a reinforced hollow fiber membrane with a portion of the membrane wall cut away to show a reinforcing structure with zigzag wrap filaments.
- Figure 8 is a side view of another reinforced hollow fiber membrane with a portion of the membrane wall cut away to show a reinforcing structure with discontinuous wrap filaments.
- the longitudinal axis of the hollow fibre is vertical and a reinforcing structure is formed as it moves downwards.
- a reinforced hollow fiber is described below with integral reinforcing textile filaments embedded in, preferably buried within, the wall of the hollow fibre.
- the reinforcing filaments can be monofilaments or multi-filaments, for example a yarn, or a multi-component multi-filament.
- the reinforcing filaments run i) in the longitudinal or vertical direction, preferably substantially continuously (called warp filaments herein) and ii) along the circumference, in a continuous, zigzag or discontinuous way (called wrap filaments herein).
- wrap filaments A plurality of zigzag and discontinuous wrap filaments collectively surround the warp filaments although individual zigzag or discontinuous filaments might not travel completely around the circumference of the reinforcing structure.
- the reinforcing filaments are not woven or braided together but they can, however, be attached or fused to each other at points of contact where they intersect each other.
- the filaments form a cage-like reinforcing structure that can be impregnated with a membrane dope in a continuous operation in which the dope impregnation is done shortly after the reinforcing structure is formed, with both a dope impregnation and reinforcing structure formation process operating at the same time and at the same speed.
- the reinforced hollow fibre preferably has a thin wall, with a ratio of inside-to-outside diameters larger than 0.60.
- the inside diameter of the hollow fibre can be between 0.5 to 2 mm, preferably between 0.8 to 1.5 mm.
- FIG. 1 The cross-section of a reinforced hollow fiber membrane 10 with a reinforcing structure 12 is illustrated in Figure 1.
- Two types of textile filaments 14 are embedded in the hollow fibre wall 16.
- the number of parallel warp filaments 18 may be such that the sum of their diameters divided by the inside circumference of the hollow fibre 10 is in a range from 0.2 to 0.6, preferably between 0.3 and 0.5.
- this parameter can be taken as (1 - porosity).
- the second type of filaments, called "wrap" filaments 22 extend from one warp filament 18 to another, preferably within the wall 16 immediately adjacent to and in contact with the warp filaments 18.
- one or more wrap filaments 22 may extend continuously along the length of a membrane in a spiral around all of the warp filaments 18, or a plurality of wrap filaments 22 may each extend back and forth between at least a sub-set of the warp filaments 18 and along the length of a membrane 10 in a zigzag pattern, or a collection of discontinuous wrap filaments 22 may each extend between two or more warp filaments 18 without any one of them necessarily extending completely along or around the entire membrane 10.
- a cage-like structure 12 has two layers of wrap filaments 22.
- the first layer 24 has a continuous wrap filament that was wrapped counter-clockwise (viewed from above) around the warp filaments 18 as the warp filaments 18 moved downwards.
- the second layer 26 has a continuous wrap filament that was wrapped clockwise (viewed from above) around the first layer 24 as the warp filaments 18 moved downwards.
- the warp 18 and wrap 22 filaments are bonded together at points of contact where they intersect, although it is not necessary for the filaments 18, 22 to be bonded together at every point of contact and, optionally, there may be no bonding.
- Warp 18 and wrap 22 filaments can be either mono or multi filaments or a mixture of both. They can be made from polymers such as polyethylene, polypropylene, polyester, nylon, aramid, etc. Filaments 14 can be coated with a thin, for example less than 10 ⁇ m, polymer layer which allows filament to filament bonding where they intersect. Bonding can be achieved by a number of methods known in the art including, without limitation, heating, softening with a solvent or UV-activation. Bonding can be better controlled by coating the filaments 22 with a layer that responds to the bonding method. In the case where a filament 14 is a multi-filament, only one or a few of the individual filaments might be involved in a bond with an intersecting filament 14.
- Fabrication methods can be based on pre-formed wrap filaments 22 as will be described with reference to Figure 3.
- Pre-formed wrap filaments 22 are un-wound from bobbins and wrapped around the warp filaments 18 in a continuous way.
- the wrapping pitch is defined as the distance between two points along the axis of the hollow fibre where a continuous wrap filament 22 comes back to the same circumferential (radial angle) position. It is a function of the distance between filaments 22 and the number of filaments 22.
- the centre-to- centre distance between continuous wrapping filaments 22 can be between 1-10 times their diameter, preferably between 2 to 5.
- Fabrication methods can also be based on filaments 22 produced in-situ by melt-extrusion or dry spinning as will be described with reference to Figures 4 to 6. Melt extrusion or dry spinning are herein used as commonly understood in textile yarn production. Filaments formed in-situ offer more options for delivering the wrap filaments 22 as will be described a zigzag pattern example and a chopped fiber example.
- a reinforced hollow fiber membrane is produced continuously in a machine wherein all the steps are done at the same linear speed called the spinning velocity.
- the spinning velocity for pre-formed filaments in the example of Figure 3 may range between 0.5-5 m/min, preferably between 1-3 m/min.
- the spinning velocity for filaments formed in-situ may range between 5-20 m/min, preferably between 10-15 m/min.
- FIG. 3 An example of a process and a device to fabricate a non-braided, reinforced hollow fibre membrane 10 is illustrated in Figure 3.
- the process is built around a fixed needle 30 of a diameter substantially equal to the desired inside diameter of the hollow fibre membrane 10.
- the top portion 32 of the needle 30, which is hollow, is open to atmosphere or attached to a source of a pressurized gas 34.
- the warp bobbins 38 are arranged radially (spaced angularly) around the needle 30 to distribute warp filaments 18.
- the warp bobbins 38 are stationary and there is one bobbin 38 per warp filament 18 with individual tension control.
- the warp filaments 18 are distributed evenly around the needle 30 through a warp filament die 40.
- the wrap filament die 40 is the only mechanical attachment point between the needle 30 and the structure of the spinning machine (not shown).
- a first creel 42 for wrap filaments 22 Next going down along the needle 30 is a first creel 42 for wrap filaments 22.
- the wrap filament bobbins 44 are mounted on a wheel 46 that rotates around the needle 30 without being in contact with it, and always in the same direction, which is clockwise in this example.
- Each wrap bobbin 44 is equipped with tension control.
- the wrapping velocity is equal to the spinning velocity divided by the wrapping pitch.
- a hollow fiber membrane 10 may have the following parameters:
- the wrap filaments 22 are distributed along the axis of the needle through a wrap die 48 which ensures a precise center to center distance between wrap filaments 22.
- the second wrap filament creel 50 for wrap filaments 22.
- the second wrap filament creel 50 is similar to the first filament creel 42, except that it rotates in the opposite direction, counterclockwise in this example, and can have a different number of filaments 22.
- bonding at least some of the points of contact can be achieved by heating, applying UV, etc.
- this step can be performed during application of the membrane dope if the dope solvent has the ability to soften the filament polymer or coating and promote bonding.
- the membrane impregnation step is done with a spinneret 56 used to inject the polymer dope 58 to fill the gap between the needle 30 and the spinneret 56 lumen diameter.
- the diameter of the needle 30 can be reduced in the area of the spinneret 56 to ensure that the polymer dope 58 fully impregnates the filament reinforcing structure 12 and that no filament 14 is exposed to the hollow fibre lumen. Because the needle 30 acts to restrict dope flow into the lumen of the hollow fiber membrane 10, a relatively simple dope delivery method based on pressure control can be used (as opposed to flow control as described in other processes later).
- the needle 30 ends just as the formed reinforced hollow fibre 10 exits the spinneret. A gas drawn through the needle bore prevents fibre collapse.
- the following steps performed in a post-treatment area 60 are similar to those used to make un-reinforced or braid coated hollow fibres and they vary according to the polymer coagulation method (NIPS or TIPS), and the desired membrane properties. These conditions are known in the art and typically include the steps of initial membrane formation through an air gap, coagulation, rinsing, post-treatment (e.g., chlorination), impregnation (e.g., with glycerine), bundling and drying. These can all be in-line but they are often interrupted by taking up the hollow fibre onto a bobbin or a winder 62. [0045] The spinning velocity is controlled by the finished hollow fibre take up speed. The wrapping velocity must be precisely coupled to the spinning velocity, either mechanically or electronically.
- FIG 4 Another process and a device to fabricate a non-braided, reinforced hollow fibre membrane 10 is illustrated in Figure 4. This method and device are similar to that of Figure 3, except that the rotating creels 42, 50 for wrap filaments 22 are replaced by an in-situ filament formation device 63, which is described below.
- wrap filaments 22 are produced in-situ by melt- extrusion or dry spinning.
- In-situ formed filaments 22 are preferably produced by melt-extrusion, which is described in US Patent 3,849,241 , US Patent 5,271 ,883 and US Patent 6,114,017, which are incorporated herein in their entirety.
- melt extrusion thermoplastic polymers are extruded at high temperature through small orifices using air to elongate the filaments and transport them to a moving collector.
- the warp filaments 18 moving down function as the moving collector.
- Typical process conditions for the spunbond and meltblown processes are described in the following Table 1. Polymer flow per hole can be up to 1-2 g/min.
- a first in-situ filament formation device 63A is described with reference to Figures 5A and 5B.
- Extrusion die assemblies 70 are located around the needle 30 along which travels the warp filaments 18.
- Each extrusion die assembly 70 has a molten (for melt spinning) or dissolved (for dry spinning) port 72 and extrusion holes 74, as well as high pressure air port 76 and air jet holes 78 located around the polymer extrusion hole 74.
- the filaments 22 deposit randomly on the surface of the warp fibres 18. Air flow can be pulsed to improve wrap filament 22 distribution.
- each extrusion die assembly 70 may be mounted in a way that allows rapid vibration in the horizontal plane. Vibration at a frequency of 50 to 200 Hertz can be effected by a number of means known in the art.
- the extrusion die 70 is mounted on a vertical rod 80 that acts as a spring; a small motor with an ex-centered mass 84 on its shaft is mounted on the die assembly 70 and its rotation puts the entire die assembly 70 in vibration, as taught by Culkin in US Patent 5,014,564, which is incorporated herein in its entirety.
- Figure 5B shows 4 extrusion die assemblies but the number can vary from 3 to 9, preferably 4 to 8 to ensure overlap of wrap filaments 22 around the perimeter of the reinforcing structure 12.
- Figure 5A illustrates that the extrusion die assemblies 70 (only 2 shown in Figure 5A) are positioned around the needle in different horizontal planes so that the flow of elongation air for one extrusion die 70 does not interfere with the others.
- the resulting structure of wrap filaments is a series of continuous overlapping zigzag wrap filaments 22.
- Each wrap filament 22 travels back and forth between two or more warp filaments 18.
- a single wrap filament 22 might extend around only a portion of the circumference of the reinforcing structure 12, but the wrap filaments 22 collectively surround the warp filaments.
- a membrane 10 may be made according to the following parameters:
- mass flow rate per die 0.37 g/min
- FIG. 6A Another process and a device to fabricate a non-braided, reinforced hollow fibre membrane 10 according to the general description of Figure 4 uses fixed dies and rotating air knifes as shown in Figures 6A and 6B for an in-situ filament forming device 63B.
- a ring-shaped extrusion die assembly 90 is located around the needle 30 along which travels the warp filaments 18.
- the die assembly 90 has a polymer port 92 and several, for example 4 to 8, extrusion holes 94 surrounded by air ports 95.
- an air knife assembly 96 which has a fixed part 98 and a rotating part 100.
- the rotating part 100 has one or more air knifes 102 that cut the filaments 22 as it rotates around the needle.
- the rotation speed of the air knife 102 is matched to the extrusion speed to control the length of the filaments 22.
- the air knife 102 also changes the travelling direction of the cut filaments to cause them to deposit on the warps 18 surface along the circumference, at a negative angle to horizontal.
- wrap filaments 22 are a series of chopped filaments (segments) 22 deposited on the warp filaments 18 at a small angle to horizontal. As shown in Figure 8, for example, each wrap filament 22 might not extend along the entire length or circumference of the membrane 10, but the warp filaments 22 collectively extend between all of the warp filaments 18.
- the steps described above for forming a reinforcing structure before membrane impregnation may result in a self-supporing, cylindrical structure that is strong and has a thin wall.
- the needle 30 can be replaced by a simple wire as pressure equilibration can be effected in the gap, where ambient air is sucked into the lumen of the forming hollow fiber membrane 10 to prevent collapse.
- the subsequent membrane impregnation step must be done by delivering the dope at a precise flow rate to avoid filling the lumen of the membrane 10, which is now open (not filled by the needle 30 or wire).
- a positive displacement pump can be used for that purpose. This operation can be made easier if the membrane dope spontaneously wets the reinforcing filaments 14 so that it is retained by surface tension within the cage structure 12. This can be achieved by treating the surface of the filaments 14 and/or manipulating the composition of the dope.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Nonwoven Fabrics (AREA)
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2012501101A JP2012521279A (en) | 2009-03-26 | 2010-03-26 | Non-woven reinforced hollow fiber membrane |
AU2010228091A AU2010228091B2 (en) | 2009-03-26 | 2010-03-26 | Non-braided reinforced hollow fibre membrane |
EP10755375.2A EP2411127B1 (en) | 2009-03-26 | 2010-03-26 | Non-braided reinforced hollow fibre membrane |
ES10755375T ES2906058T3 (en) | 2009-03-26 | 2010-03-26 | Non-braided reinforced hollow fiber membrane |
CN201080015946.5A CN102365125B (en) | 2009-03-26 | 2010-03-26 | Non-braided reinforced hollow fibre membrane |
US13/260,443 US9132390B2 (en) | 2009-03-26 | 2010-03-26 | Non-braided reinforced holow fibre membrane |
BRPI1006414A BRPI1006414A2 (en) | 2009-03-26 | 2010-03-26 | reinforcement structure for a hollow fiber membrane, hollow fiber membrane, method for producing a reinforcement structure and method for producing a hollow fiber reinforcement membrane |
KR1020117025178A KR101766492B1 (en) | 2009-03-26 | 2010-03-26 | Non-braided reinforced hollow fibre membrane |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US16365409P | 2009-03-26 | 2009-03-26 | |
US61/163,654 | 2009-03-26 |
Publications (1)
Publication Number | Publication Date |
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WO2010108285A1 true WO2010108285A1 (en) | 2010-09-30 |
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ID=42780118
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/CA2010/000469 WO2010108285A1 (en) | 2009-03-26 | 2010-03-26 | Non-braided reinforced hollow fibre membrane |
Country Status (9)
Country | Link |
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US (1) | US9132390B2 (en) |
EP (1) | EP2411127B1 (en) |
JP (1) | JP2012521279A (en) |
KR (1) | KR101766492B1 (en) |
CN (2) | CN104941459B (en) |
AU (1) | AU2010228091B2 (en) |
BR (1) | BRPI1006414A2 (en) |
ES (1) | ES2906058T3 (en) |
WO (1) | WO2010108285A1 (en) |
Cited By (9)
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WO2012036935A1 (en) | 2010-09-15 | 2012-03-22 | Bl Technologies, Inc. | Method to make a yarn-reinforced hollow fibre membranes around a soluble core |
WO2012082441A2 (en) * | 2010-12-15 | 2012-06-21 | General Electric Company | Supported hollow fiber membrane |
WO2013089971A1 (en) * | 2011-12-16 | 2013-06-20 | Bl Technologies, Inc. | Hollow fibre membrane with compatible reinforcements |
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 |
US9061250B2 (en) | 2009-06-26 | 2015-06-23 | Bl Technologies, Inc. | Non-braided, textile-reinforced hollow fiber membrane |
US9132390B2 (en) | 2009-03-26 | 2015-09-15 | Bl Technologies Inc. | Non-braided reinforced holow fibre membrane |
US9227362B2 (en) | 2012-08-23 | 2016-01-05 | General Electric Company | Braid welding |
US9643129B2 (en) | 2011-12-22 | 2017-05-09 | Bl Technologies, Inc. | Non-braided, textile-reinforced hollow fiber membrane |
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GB0913645D0 (en) * | 2009-08-05 | 2009-09-16 | Nano Porous Solutions Ltd | A method of forming a fluid separation filter for use in a fluid separation device |
ES2393153B1 (en) * | 2010-07-29 | 2013-11-21 | Lifitec S.L.U. | METHOD AND APPARATUS FOR ALLOWING THE CURING OF THE COATING OF A PART BY FREE RADICALS GENERATED BY ULTRAVIOLET (UV) RADIATION. |
GB2543483B (en) * | 2015-10-09 | 2022-09-28 | Flexenable Ltd | Lamination technique for producing electronic devices |
WO2017087484A1 (en) * | 2015-11-19 | 2017-05-26 | Arkema Inc. | Fluoropolymer fiber-bonding agent and articles produced therewith |
US11839857B2 (en) * | 2017-12-01 | 2023-12-12 | I2M Llc | Filtration membrane bundle, filtration membrane assembly and method of producing the same |
US20190168163A1 (en) * | 2017-12-01 | 2019-06-06 | Stuart Miller | Ultra-filtration membrane and method of forming the same |
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Also Published As
Publication number | Publication date |
---|---|
CN102365125A (en) | 2012-02-29 |
BRPI1006414A2 (en) | 2016-02-10 |
CN104941459B (en) | 2017-09-22 |
US9132390B2 (en) | 2015-09-15 |
AU2010228091B2 (en) | 2016-06-16 |
JP2012521279A (en) | 2012-09-13 |
ES2906058T3 (en) | 2022-04-13 |
US20120018371A1 (en) | 2012-01-26 |
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EP2411127B1 (en) | 2022-01-05 |
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CN104941459A (en) | 2015-09-30 |
KR20120013343A (en) | 2012-02-14 |
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