US20050082717A1 - Methods of making stretched filtering membranes and modules - Google Patents
Methods of making stretched filtering membranes and modules Download PDFInfo
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- US20050082717A1 US20050082717A1 US11/006,627 US662704A US2005082717A1 US 20050082717 A1 US20050082717 A1 US 20050082717A1 US 662704 A US662704 A US 662704A US 2005082717 A1 US2005082717 A1 US 2005082717A1
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- 238000000034 method Methods 0.000 title claims abstract description 63
- 238000001914 filtration Methods 0.000 title abstract description 11
- 239000000835 fiber Substances 0.000 claims abstract description 155
- 238000004382 potting Methods 0.000 claims abstract description 41
- 239000012815 thermoplastic material Substances 0.000 claims abstract description 19
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- 239000012510 hollow fiber Substances 0.000 claims 2
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- 239000011148 porous material Substances 0.000 description 5
- 239000004698 Polyethylene Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 230000035699 permeability Effects 0.000 description 4
- 229920000573 polyethylene Polymers 0.000 description 4
- 239000012466 permeate Substances 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 2
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- 230000001070 adhesive effect Effects 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
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- -1 polypropylene Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 125000006850 spacer group Chemical group 0.000 description 2
- 229920001169 thermoplastic Polymers 0.000 description 2
- 239000004416 thermosoftening plastic Substances 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
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- 229910000831 Steel Inorganic materials 0.000 description 1
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- 239000002184 metal Substances 0.000 description 1
- 210000001724 microfibril Anatomy 0.000 description 1
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- 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
- B01D63/08—Flat membrane modules
- B01D63/087—Single membrane modules
-
- 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
- B01D63/021—Manufacturing thereof
-
- 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
- B01D63/021—Manufacturing thereof
- B01D63/022—Encapsulating hollow fibres
-
- 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
- B01D63/021—Manufacturing thereof
- B01D63/022—Encapsulating hollow fibres
- B01D63/0221—Encapsulating hollow fibres using a mould
-
- 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
- B01D63/024—Hollow fibre modules with a single potted end
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0023—Organic membrane manufacture by inducing porosity into non porous precursor membranes
- B01D67/0025—Organic membrane manufacture by inducing porosity into non porous precursor membranes by mechanical treatment, e.g. pore-stretching
- B01D67/0027—Organic membrane manufacture by inducing porosity into non porous precursor membranes by mechanical treatment, e.g. pore-stretching by stretching
-
- 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
- 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
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
- B29C55/04—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique
- B29C55/06—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique parallel with the direction of feed
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/24—Formation of filaments, threads, or the like with a hollow structure; Spinnerette packs therefor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/50—Control of the membrane preparation process
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/02—Details relating to pores or porosity of the membranes
- B01D2325/022—Asymmetric membranes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/02—Details relating to pores or porosity of the membranes
- B01D2325/022—Asymmetric membranes
- B01D2325/0231—Dense layers being placed on the outer side of the cross-section
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/04—Condition, form or state of moulded material or of the material to be shaped cellular or porous
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Textile Engineering (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
A method for stretching a hollow fibre while making a stretched filtering membrane from a precursor involves wrapping the hollow fibre around a structure and modifying the structure such that at least portions of the hollow fibre are forced to elongated. For example, the hollow fibre may be wrapped around around two or more supports and the distance between adjacent supports increased. This produces first portions of the hollow fibre stretched to a first elongation and porous to a first porosity and second portions of the hollow fibre that are not stretched or are stretched to a second elongation less than the first elongation and that remain non-porous or become porous to a second porosity which is less than the first porosity. The membrane may be made into a module with second portions of the membranes located at points where the membranes exit the potting material or at turns in loops of the fibres, if any. In various embodiments, the fibre is potted into modules before or after it is stretched. Some methods of potting involve applying a hot melt adhesive to the second portions. Some embodiments are made entirely of thermoplastic material and can be easily recycled.
Description
- This is a continuation of U.S. Ser. No. 10/314,334 filed Dec. 9, 2002, which is an application claiming the benefit under 35 USC 119(e) of U.S. Ser. No. 60/338,676 filed Dec. 11, 2001. U.S. Ser. No. 10/314,334 and 60/338,676 are incorporated herein, in their entirety, by this reference to them.
- This invention relates to filtering membranes and in particular to a method of making stretched filtering membranes, a module of stretched filtering membranes and a method of making such a module.
- Stretched membranes are a class of filtering membranes. Stretched membranes are typically made by first forming a non-porous hollow fibre of an appropriate membrane material. The membrane material is typically a thermoplastic such as polypropylene (PP), polyethylene (PE) or, less frequently, PVDF. The membrane material can be formed into a non-porous hollow fibre by various methods such as extruding or melt-spinning. The non-porous hollow fibre (often called a precursor) is then treated by a variety of processes which typically include annealing steps and stretching steps (typically at specified temperatures, rates of elongation, and total elongation) to produce pores within a desired size range in the fibres. The processes generally share a common strategy of providing a non-uniform composition in the fibre with areas having a crystalline structure dispersed throughout the fibre. When the fibre is stretched, the membrane material between the crystalline structures tears into a series of microfibrils alternating with elongated pores oriented along the length of the fibres.
- A large number of specific processes have been described in the art. While following the generally strategy outlined above, these processes may differ, among other things, in the number of annealing or stretching steps, the order of the annealing or stretching steps and the temperature, changes in temperature, total elongation or rate of elongation specified for any particular stretching step.
- A typical plant for making stretched membranes allows for generally continuous production. For example, in one area of the plant, precursor may be formed by extruding a continuous fibre that passes over a series of rollers designed to stretch the fibres to a final dimension (but without producing pores) and allow the fibre to cool before it is wound around a take up spool. Once full, the take up spools are then mounted into the head of a stretching apparatus. The stretching apparatus may consist of a series of chambers each having a plurality of rollers of differing diameters and turning at different speeds. The fibre is threaded through the various rollers of the chambers in series to a take up roll at the tail end of the stretching apparatus. The different speeds and diameters of the rollers in each chamber causes the fibre to be stretched (or not stretched for annealing) at selected speeds and to selected elongations as it passes through each chamber. The temperature of each chamber is individually set as desired for stretching or annealing. The total length of the path (around the various rollers) in each chamber and the average speed of the fibre through each chamber can be chosen to achieve a desired length of time that the fibre is exposed to the temperature prevalent in each chamber. As long as the fibre does not break, a continuous fibre of stretched filtering membrane winds continuously onto the take up roll at the tail end of the plant. Once a roll of fibre is produced, membrane modules can be made by various techniques.
- It is an object of the present invention to improve on the prior art and provide a method of making stretched filtering membranes, a module of stretched filtering membranes and a method of making such a module. The invention achieves these goals through the combinations or sub-combinations of features specified in the claims, this summary or the description of embodiments.
- The inventors have observed various problems with the existing art. Some problems relate to the existing methods of making stretched fibres. Expensive and intrusive capital equipment is required to make large amounts of stretched fibres. Changes to any part of the process may require difficult design changes to the various chambers, rollers, or roller drive mechanisms in a plant. Further, the residence time in each chamber is significant and so the rate of production, even with multiple fibres simultaneously moving through a plant, is low in relation to the size of a plant. A break in a fibre also causes significant down time since the fibre must be re-threaded through the plant.
- Others problems relate to the stretched fibres themselves. Stretched membranes are somewhat delicate, kink easily and may break prematurely in use. In particular, when individual fibres are folded over into a loop, for example with both open ends of the fibre potted into the same header, the stretched membranes may kink or break at the turn of the loop. The fibres may also break where they exit the resin of the header, particular in applications where the modules are heavily agitated to encourage the fibres to sway. The stretched membranes are also easily damaged by heat. These problems increase with the porosity of the membranes, with microfiltration membranes in particular being prone to damage during handling.
- The inventors have addressed these and other problems by creating new methods for stretching the precursor and new ways of using the membranes created by this method to make modules.
- To stretch the precursor, one or more strands of precursor are wound around a structure and the structure is modified such that at least portions of the hollow fibre are forced to elongate. For example, the precursor may be wound around two or more supports. The supports are mounted onto a support moving apparatus adapted to move the one or more supports away from each other at one or more speeds, for one or more times or to hold the supports apart from each other at one or more distances as required according to a selected regimen for making stretched membranes.
- Where the stretching regimen requires a non-ambient environment, the fibre is subjected to the required environment, for example an increased temperature, by locating the supports with the fibre wrapped around them inside of a controlled environment chamber. Surprisingly, such a batch method can produce a higher output of stretched material than a continuous process for the same size of controlled environment chambers. Since the precursor is tougher and 2 to 10 times shorter than the stretched fibre, thousands of turns can be wound around a set of supports quickly. Such a method also allows easy modification to the regimen for making the stretched membranes and exceptional control. The displacement of the supports from each other, the tension on the fibre, the speed that the supports move at any particular displacement, the temperature or changes in temperature and other parameters can be easily achieved through a wide variety of mechanisms, for example, a motor and heater controlled by a PLC attached to force, temperature and distance sensors. Finally, broken fibres do not significantly disrupt the process.
- In the methods described above, portions of the precursor that contact a support do not stretch significantly. Friction against the support and adjacent turns of the fibre cause the tension in the fibre to rapidly drop off after the points of tangency between the fibre and the support. Areas between the points of tangency may have some elongation, and may even become porous to a small degree, but at least a portion of the fibres has sufficiently small elongation and porosity that its mechanical properties are appreciably better than the mechanical properties of portions of the fibre from between adjacent supports. To provide a further variation in the mechanical properties of a fibre that is to be stretched while heated, the atmospheric chamber may be configured to heat areas between the supports more intensely or the supports may be heat sinked so that portions adjacent the support remain cooler.
- The resulting fibre has unstretched or less stretched portions (which will collectively be referred to as unstretched portions for brevity) and stretched portions. The stretched portions are useful as a filter media. The unstretched portions can be cut out and discarded leaving individual stretched hollow fibre membranes. The unstretched, however, retain some or all of the qualities of the precursor which can be used to advantage. In particular, the unstretched portions are less brittle and are more resistant to kinking and heating. By locating the unstretched portions of the fibre at one or more high stress points in a module, the overall reliability or service life of the module can be greatly increased with very little loss in filtration capacity. For example, unstretched portions can be located at the turn of the loop of a looped fibre or at the point where the fibre exists the potting material of a header or both. The unstretched portions, because of their better heat resistance, can also be used with potting methods in which a hot melt adhesive is attached to the fibre.
- Locating the unstretched portions in selected locations can be done after a strand of partially stretched and partially unstretched fibre is produced. Alternately, precursor can be first arranged in a geometrical configuration appropriate for use in a module and then stretched. Further alternately, the precursor can be potted into a header before the fibres are stretched, the header becoming one of the supports. Because the precursor is tougher than the stretched fibre, the precursor can be arranged in a desired geometrical configuration or potted faster and with less breakage. The precursor can also be potted with hot melt adhesives.
- Modules with the stretched and unstretched portions of fibres at the appropriate places can be made by various methods. In some methods, the stretched or unstretched portions form a regular alternating pattern. A point on the fibre can then be indexed or registered to a bundle, fabric or array forming apparatus so that a bundle, fabric or array is formed with the unstretched portions in the desired places. In another method, the supports and support moving apparatus are configured, and the precursor wound around them, to produce membranes in the approximate geometrical configfuration that they will have in the module. The supports can be kept with the fibres or replaced with a smaller replacement support. For a module of looped fibres, for example, a support or replacement support can remain with the fibres at the turn of the loop. For potting, a small replacement support can be used which leaves unstretched portions long enough to give sufficient contact with the potting resin. The replacement support can then be immersed in potting material with the fibres. After the potting material hardens, the replacement support can be cut out, which also cuts open and exposes the ends of the fibres. For this method, the fibre may be wound around the supports such that the adjacent lengths of fibre are separated from each other at the support by a distance at least sufficient to allow the potting medium to surround the fibre and provide a good seal.
- In other methods, a hot melt adhesive is used. For example, the fibre may be cut into individual fibres of a desired length and potted according to the fugitive potting method described in U.S. Pat. No. 5,639,373 which is incorporated into this document by this reference. According to this method, a hot melt adhesive temporarily holds the fibres together. By placing unstretched portions where the hot melt adhesive will be applied, the fibre is able to withstand the heat of the adhesive.
- In other methods, the fibres are not potted in a resin, but rather in a hot melt adhesive alone. The hot melt adhesive may be applied to the supports or precursor as the precursor is wrapped onto the supports. Alternately, the hot melt adhesive may be applied to the hollow fibre membrane after it is stretched but still wound on the supports. Further alternately, the fibres may be transferred to a drum having a diameter chosen so that unstretched portions of the fibres are adjacent each other, ie one or more lines of unstretched portions extends across the width of the drum for application of the hot melt adhesive. In these methods, one or more bands of hot melt adhesive are melted across a band of unstretched portions or precursor which will be at the unstretched portions. Further layers of fibre or precursor and hot melt adhesive may be added and adhered to a first layer of fibre or precursor. The fibre is later cut, for example through or adjacent to a band of glue, to provide distinct fibres with open ends held in relation to each other by a mass of hot melt adhesive. The mass of hot melt adhesive may then be glued into a pan, optionally of a thermoplastic material, to create a header or manifold. Optionally, the mass of hot melt adhesive itself forms a header or manifold. For example, a the hot melt adhesive may be cut to both expose open ends of the fibres and create a channel in the hot melt adhesive which permits fluid connection of the ends of the fibres to one or more pipes. By either method, modules may be made entirely of thermoplastic material. Such modules can be easily recycled.
- FIGS. 1 to 3 are schematic representations of a method of making stretched membranes.
-
FIG. 4 is a schematic representation of methods of producing short fibres for potting from a set of supports. -
FIG. 5 is a schematic representation of a support moving apparatus located inside of a controlled environment chamber. -
FIG. 6 is a cross section of a looped fibre potted into a header. -
FIG. 7 is a schematic representation of a method for using replacement supports to create a module. -
FIG. 8 is a representation of a fibre being transferred from a set of supports to a drum. -
FIG. 9-11 are representations of a process for potting fibres into a permeate pan using a hot melt adhesive. -
FIGS. 12-15 are representations of a process for potting fibres using a hot melt adhesive without a permeate pan. -
FIG. 17 is a representations of an alternate method of forming collections of distinct fibres on a drum. -
FIGS. 17 and 18 are representations of methods in which fibres are first potted and then stretched. - FIGS. 1 to 3 give a schematic representation of a method of making stretched membranes.
- In
FIG. 1 ,precursor 10 is wound off of aprecursor spool 12 and wrapped around a plurality of supports 14. For example, thesupports 14 may be metal rods with their ends slipped into notches in an opposed pair ofsupport holding plates 16. Two, three, four ormore supports 14 may be used. To provide a reasonably consistent tension in theprecursor 10, a dancer arm assembly may be used between theprecursor spool 12 and thesupports 14. With the use of a dancer arm or other means to account for variations in take up speed of the supports,precursor 10 may be wrapped directly around the plurality ofsupports 14 as it is made. In this way aprecursor spool 12 is not required. By any technique, theprecursor 10 may be wound around thesupports 14 to multiple layers to increase the output of the process. - In
FIG. 2 , thesupports 14 have been removed from the support holding plates and mounted into asupport moving apparatus 18. Alternately,precursor 10 may be wound directly ontosupports 14 already on thesupport moving apparatus 18. For steps requiring non-ambient conditions, thesupport moving apparatus 18 is placed inside a controlledenvironment chamber 20, for example a heating chamber, as shown inFIG. 2A . To stretch theprecursor 10, thesupport moving apparatus 18 is operated to moveadjacent supports 14 away from each other. As shown inFIG. 2B for example, thesupports 14 are driven away from the center of thesupport moving apparatus 18 by a driving device (not illustrated). According to many regimens for making stretched membranes, this step would be performed while the controlledenvironment chamber 20 is heated and there may be multiple stretching steps. InFIG. 2C , theprecursor 10 has been stretched to its desired elongation. According to many regimens, the precursor may be annealed at a selected temperature as it is held at its maximum elongation.FIGS. 2A, 2B and 2C are illustrative only and thesupport moving apparatus 18 can be placed in or removed from one or more controlledenvironment chambers 20 or other treatment areas as desired for any particular regimen. For example, thesupports 14 may be held at a fixed distance from each other, may be moved away from each other at steady speeds or unsteady speeds, may be moved away from each other in one or more steps taken at various temperatures or may be moved towards or away from each other at a constant force or strain rate, etc. - Moving
adjacent supports 14 away from each other creates tension in theprecursor 10. Due to friction between theprecursor 10 and thesupports 14 and between adjacent turns of theprecursor 10, this tension decreases sharply a short distance behind the points of tangency between the fibre and the supports. For example, with PE precursor on a cylindrical,unpolished steel support 14, tension in the fibre may be reduced in half only 20 degrees behind the points of tangency and is further reduced towards a minimum at halfway between the points of tangency. Further, as the precursor stretches, it work hardens and requires more force to produce a further elongation. As a result, portions of the fibre between the two points of tangency will be less stretched than portions of the fibre held between adjacent supports. - As shown in
FIG. 3 , amembrane fibre 22 is produced having, over a sufficient length, alternating stretchedareas 24 andunstretched areas 26. The term unstretched areas is used for simplicity, but may include portions of themembrane fibre 22 that are stretched to less elongation and porosity compared to the stretchedareas 24. For example, the stretchedareas 24 may have elongations of over 200% while theunstretched areas 26 have elongations of less than 50% or less than 25%. Similarly, the stretched areas are highly porous and have pore sizes and permeability sufficient to make them useful as a filtration media, for example as a microfiltration or ultrafiltration membrane. Theunstretched areas 26 may also have some pores, but their permeability is minimal. Theunstretched areas 26 retain the mechanical properties of theprecursor 10 to a large extent, and are appreciably more durable and flexible than the stretchedareas 24. - The length of the
unstretched areas 26 may be a few or several centimeters, for example 3-12 cm. The length and degree of elongation or permeability of theunstretched areas 26 can be altered by changing the size of acylindrical support 14 or by using asupport 14 of altered size or cross-section. For example, a rectangular support, with rounded edges to avoid damaging themembrane fibre 22, can be used to produce a longunstretched area 26 of minimal or no elongation and permeability. By altering the initial spacing betweensupports 14 in relation to the desired percentage elongation, the length of the stretchedareas 24 can also be altered. The lengths of the stretchedareas 24 andunstretched areas 26 may each be constant, or may be made to vary along amembrane fibre 22. - The stretched
areas 26 are typically visibly distinct from theunstretched areas 24. For example, with PE, the stretchedareas 26 are an opaque white whereas theunstretched areas 24 remain semi-translucent like theprecursor 10. If individual hollow fibre membranes having onlyunstretched areas 24 are desired, the stretchedareas 26 can be cut out and discarded. - The
membrane fibre 22 can be cut into distinct hollow fibre membranes for potting into a module. For example, inFIG. 4 , themembrane fibre 22 is cut while it is still wrapped around thesupports 14. Cutting themembrane fibre 22 reveals a plurality of individual hollow fibre membranes that can be collected together into a bundle. The bundle can be inserted, for example, into a liquid potting resin or other potting material and centrifuged. By cutting at location A, the resulting hollow fibre membranes will haveunstretched areas 26 in their middles. If used to make a looped fibre, theunstretched areas 26 can be located at the turns of the loops. By cutting, for example with a knife, at B through theunstretched area 26, the resulting hollow fibre membranes will haveunstretched areas 26 at their ends. If used in a module having membranes potted between a pair of headers, such membranes can be potted to haveunstretched areas 26 where they exit the potting material. By cutting at C through theunstretched areas 26, the resulting hollow fibre membranes will haveunstretched areas 26 in their middles and their ends. If used to make a looped fibre, theunstretched areas 26 can be located at the turns of the loops and where the membranes exit the potting material. Since the turn of a loop and the point where a membrane exits potting material are high stress areas in a module, the additional durability of theunstretched areas 26 increases the durability of a module. - The
membrane fibre 22 may also be transferred from thesupport moving apparatus 18 to other conventional devices for preparing themembrane fibre 22 for potting. The membrane fibre may be first transferred to a spool so that thesupport moving apparatus 18 may be returned touse stretching precursor 10. By either method, the location of theunstretched areas 26 should be tracked in whatever machine takes up themembrane fibre 22. For example, if themembrane fibre 22 will be made into a fabric, theunstretched areas 26 can be located to advantage at turns in themembrane fibre 22. -
FIG. 5 shows asupport moving apparatus 18 and controlledenvironment chamber 20 in greater detail. Thesupport moving apparatus 18 is adapted for use with twosupports 18 and a plurality of such support moving apparatuses may be located in a single controlledenvironment chamber 20. Theprecursor 10 is shown loosely wrapped around the supports to allow it to stick out in the drawing although it would typically be taut between thesupports 14. Afirst support 14A rests in a notchedplate 44 attached to one side of the controlledenvironment chamber 20. Thesecond support 14B rests in a channel of a channeledplate 46. A pair ofhooks 48 are hooked to thesecond support 14B and also slide in the channel. Threadedrods 50 are threaded onto thehooks 48 at each side of thesecond support 14B and may be turned bymotors 52 which cause thesecond support 14B to move within the channel. Themotors 52 are controlled by a programmable logic controller (PLC) 54 connected to various sensors. The sensors may include astrain sensor 56 to measure the strain in (and force exerted by) the threadedrod 50, atemperature sensor 58 and aposition sensor 60. ThePLC 54 may also be used to control one ormore heating elements 62 which may be turned on an off individually. Heat may be provided to areas between thesupports 14 more intensely by, for example, turning on only thoseheating elements 62 between thesupports 14, by shielding or insulating an area near thesupports 14 or heat-sinking thesupports 14 so that an area near or adjacent thesupports 14 remains cooler. Such an apparatus allows almost any stretching regimen to be followed. -
FIG. 6 shows a cross section of a header ormanifold 32 of amodule 34. The header includes apan 36 and a solidifiedpotting material 38 defining aplenum 40. Apipe 42 allows feed or permeate to flow into or out of theplenum 40. Ahollow fibre membrane 42 made according to one or more of the methods described above has its ends potted in thepotting material 38 and open to theplenum 40.Unstretched areas 26 are located at the turn of a loop in thehollow fibre membrane 42 and where thehollow fibre membrane 42 exits the pottingmaterial 38. - To make a
module 34 as shown inFIG. 6 , amembrane fibre 22 can be cut to produce distincthollow fibre membranes 42 withunstretched areas 26 in the appropriate places. For example, cuts can be made at points C inFIG. 4 to producehollow fibre membranes 42 which can be potted using any suitable method for potting distinct fibres. To produce a module with a pair of opposed headers, cuts can be made at points B as shown inFIG. 4 . Alternately, a plurality of separate lengths ofprecursor 10 can be first arranged in a geometrical configuration appropriate for use in themodule 32 and then stretched. In this case, the open ends of the lengths ofprecursor 10 are held in a clamp rather than wrapped around asupport 14 for stretching. -
FIG. 7 shows another method of making amodule 34 like the one inFIG. 6 . One or more lengths ofmembrane fibre 22 are wrapped around a pair of replacement supports 64 withunstretched areas 26 located near the replacement supports 64. At one end, theunstretched areas 26 are sufficiently long on either side of thereplacement support 64 for potting an area of themembrane fibre 22 near themembrane support 64. To ensure that the pottingmaterial 38 surrounds and seals each part of themembrane fibre 22 that passes through it, themembrane fibre 22 may be wrapped around the replacement supports 64 so that adjacentunstretched areas 26 are spaced a minimum distance apart. Alternately, a limited number of layers ofmembrane fibre 22 may be wrapped around the replacement supports 64, but the replacement supports 64 positioned close enough to each other to cause adjacent turns ofmembrane fibre 22 to spread out. Themembrane fibre 22 is also made sufficiently loose in relation to the surface energy between the pottingmaterial 38 andmembrane fibre 22 to ensure that pottingmaterial 38 surrounds each length ofmembrane fibre 22. - To pot the
module 34, onereplacement support 64 with themembrane fibre 22 wrapped around it may be inserted into aliquid potting material 38 held in apotting container 66. After thepotting material 38 hardens, it is cut along thecut line 68 to create and expose open ends ofhollow fibre membranes 42. Alternately, a fugitive potting method may be used in which the area below thecut line 68 is filled with a fugitive material instead of thepotting material 38. After thepotting material 38 hardens, the fugitive material andcontainer 66 are removed. Themembrane fibre 22 can then be cut as described above. - To wrap the
membrane fibre 22 around the replacement supports 64, a dancer arm assembly may be used to transfer themembrane fibre 22 from anysupport moving apparatus 18. Alternately, thesupport moving apparatus 18 may be configured to producemembrane fibre 22 in a geometrical configuration appropriate for use in themodule 34. For example, thesupport moving apparatus 18 ofFIG. 5 will producemembrane fiber 22 in a configuration appropriate for themodule 34 ofFIGS. 6 and 7 . Theprecursor 10 may be wrapped around thesupports 14 at the same spacing or number of layers that will be used around the replacement supports 64. The replacement supports 64 can then be slipped directly into the place occupied by thesupports 18 to transfer themembrane fibre 22 to the replacement supports 64. -
FIG. 8 shows another method of transferring themembrane fibre 22. The membrane fibre is unwound from asupport moving apparatus 18 and onto amembrane fibre drum 28 through adancer arm assembly 70. Themembrane fibre 22 may be wound in one or more layers, and randomly or orderly. For example, a random winding may be appropriate when themembrane fibre 22 will alter be fed from thedrum 28 into another machines for preparing themembrane fibre 22 for potting. When feeding into another rmachine, the location of theunstretched areas 26 is tracked by the machine to make best use of theunstretched areas 26. For example, if themembrane fibre 22 will be made into a fabric, theunstretched areas 26 can be located to advantage at turns in themembrane fibre 22, for example at the edge of the fabric. - To produce an orderly arrangement of the
membrane fibre 22 on thedrum 28, the diameter of thedrum 28 may be chosen so that theunstretched areas 26 are located generally across the width of the drum but at a limited number of angular positions on thedrum 28. Replacement supports 64 may be slipped under theunstretched portions 26 or into channels in thedrum 28 under theunstretched portions 26. The drum can then be removed and themembrane fibre 22 will be transferred to the replacement supports 64. This method can be used, for example, to transfermembrane fibre 22 from more than twosupports 14 onto two replacement supports 64. To produce a more orderly arrangement, aguide 30 moving across the width of themembrane fibre spool 28 at an appropriate speed may be used to space adjacent turns ofmembrane fibre 22 apart from each other. The spacedmembrane fibre 22 may then be transferred to replacement supports 64 as described above. - With the
membrane fibre 22 transferred to adrum 28, other potting methods may also be used. The following potting methods may also be used without adrum 28 by applying hot melt adhesive to theprecursor 10 orhollow fibre membrane 42 while it is on or being wrapped onto thesupport moving apparatus 18 either before or after stretching. - FIGS. 9 to 11 show one method. In
FIG. 9 ,membrane fibre 22 is wrapped around adrum 28 withunstretched sections 26 located in two bands on the circumference of thedrum 28. Themembrane fibre 22 is wrapped such that adjacent turns are a minimum spacing away from each other. A hot melt adhesive 72, formulated for low viscosity and melt temperature, is placed on one of the bands ofunstretched sections 26. In the area where the hot melt adhesive 72 is applied, thedrum 28 may have arecess 74 to allow hot melt adhesive 72 to surround themembrane fibre 22. Alternately or additionally, a band of hot melt adhesive can be placed on thedrum 28 before the membrane fibre is wound on. If the hot melt adhesive 72 does not fully surround eachunstretched area 26 of themembrane fibre 22, it can be re-melted with a hot press to achieve a fluid tight seal around each turn of themembrane fibre 22. Multiple layers ofmembrane fibre 22 can be applied to thedrum 28 by alternating layers of hot melt adhesive 72 withmembrane fibres 22. Alternately, a similar result can be achieved by wrapping theprecursor 10 as described above around thesupports 14 which may haveindents 74 or be provided with a flat face under where theunstretched portions 26 will be to assist in applying the hot melt adhesive 72. If only one layer ofprecursor 10 ormembrane fibre 22 is desired, the hot melt adhesive 72 may be applied either before or after stretching. If multiple layers ormembrane fibre 22 are desired, the hot melt adhesive 72 can be applied in layers surrounding theprecursor 10 as theprecursor 10 is wound onto thesupports 14 before stretching. The hot melt adhesive 72 can be melted to theprecursor 10 either before, during or after stretching. If necessary, the area around thesupports 14 can be heat sinked, insulated or protected by baffles and the controlledenvironment chamber 20 can be configured so that the hot melt adhesive 72 is not heated too much during stretching. In the following paragraphs, further steps will be described in relation tomembrane fibre 22 wrapped onto adrum 28, but similar steps can be used formembrane fibre 22 wrapped around supports 14. - After the
membrane fibre 22 is wound onto thedrum 28 and sealed with hot melt adhesive 72, it can be cut as shown at D and removed from thedrum 28. The cutting also creates a plurality of distincthollow fibre membranes 42 with open ends. As shown inFIG. 10 , thehollow fibre membranes 42 can be folded over to make a loop with opposed open ends adjacent each other. The two masses of hot melt adhesive 72 associated with the ends of thehollow fibre membranes 42 can be joined to each other, for example, by placing a melted mass of hot melt adhesive 72 in between them and allowing it to solidify. Alternately, as shown inFIG. 10 ,hot plates 76 can be used to re-melt the hot melt adhesive 72 and fuse the two parts together. As shown inFIG. 11 , this entire assembly can be glued with more hot melt adhesive 72 into apan 36 to produce a header ormanifold 32. If thepan 36 is made of an appropriate thermoplastic, the resultingmodule 34 will be made entirely of thermoplastic materials and will be easily recyclable. -
FIGS. 12-15 show another method of making amodule 34. As shown inFIG. 12 ,membrane fibre 22 is wound around adrum 28 as inFIG. 9 . As forFIG. 9 , the following method can also be performed on thesupports 14 directly with hot melt adhesive 72 applied to either theprecursor 10 ormembrane fibre 22 either before, during or after winding theprecursor 10 onto thesupports 14 and before or after stretching. The following description will refer tomembrane fibre 22 wrapped onto adrum 28 but will apply tomembrane fibre 22 wrapped around supports 14.Unstretched portions 26 are located in four bands about the circumference of the drum and hot melt adhesive 72 is applied in two opposed locations ofunstretched portions 26. Thedrum 28 is then removed. As shown inFIG. 13 , the two opposed masses of hot melt adhesive 72 are brought together to produce opposed loops ofmembrane fibre 22. The two masses of hot melt adhesive 72 are glued together with more hot melt adhesive or fused together byheated plates 76.Heated plates 76 are also used to create two generally smooth roughly paralle opposed sides 78 of the hot melt adhesive 72, as shown inFIG. 14 . The hot melt adhesive 72 andmembrane fibre 22 is cut along the cut lines 80 shown inFIG. 14 to create distincthollow fibre membranes 42 with open ends. As shown inFIG. 15 , two such assemblies can be fused or glued together to create anelement 84 having achannel 82 in fluid connection with the open ends of thehollow fibre membranes 42. A plurality of theseelements 84 can be placed together back to back and a cap optionally of thermoplastic material glued to theelements 84 to provide a header or manifold in communication with thechannels 82. Such an assembly can be made entirely of compatible materials such that it is easily recyclable. -
FIG. 16 shows an alternate methods of forming collections of distinct fibres on adrum 28. In this method, two bands of hot melt adhesive 72 are placed across a single band of unstretched portions. Theunstretched prtions 26 are then cut in between the two bands of hot melt adhesive. The resulting distincthollow fibre membranes 42 can be used in methods analogous to the ones described above or the fugitive potting method described in U.S. Pat. No. 5,639,373 which is incorporated into this document by this reference. According to this method, the individual lengths of fibre are laid at a minimum distance from each other onto a spacers. A hot melt adhesive is place over the fibres, near but not at their ends, to attach them to the spacing means. Further layers (or arrays) of fibres may be made and stacked onto the first layer. The layers are then bundled together. The ends of the fibres are held in a fugitive material while a potting resin is poured over a portion of the fibres including a portion containing the adhesive and spacers. After the potting resin hardens, the fugitive material is removed to re-open the ends of the membranes. -
FIGS. 18 and 19 show methods in whichprecursor 10 is first potted and then stretched. In both cases, theprecursor 10 is potted into aheader 32 is made by any appropriate method. Asupport 14 is then placed through loops of theprecursor 10. The entire assembly can then be placed in a controlledenvironment chamber 20, if necessary, and thesupports 14 attached to a device for moving thesupports 14 to stretch theprecursor 10.Heating elements 62 may be configured to avoid heating theheader 32 to much. Optionally or additionally, insulation, baffling or heat sinking can also be used to avoid overheating theheader 32. Pre-cut lengths ofprecursor 10 may also be potted into pairs ofopposed headers 32 and stretched by mounting theheaders 32 into asupport moving apparatus 18 as if they were supports 14. Because theprecursor 10 is tougher than themembrane fibre 22, theprecursor 10 can be arranged in a desired geometrical configuration or potted faster and with less breakage. - The invention may be practiced with many variations from the embodiments described above without departing from the scope of the invention which is defined by the following claims.
Claims (10)
1. A process of potting hollow fiber membranes to produce a header or manifold of a membrane module composing the steps of
a) forming a mass of thermoplastic material with a plurality of hollow fiber membranes secured in and passing through the mass of thermoplastic material, ends of the membranes being open;
b) securing the mass of thermoplastic material and membranes into a pan in a manner that creates a sealed plenum in the pan with the open ends of the membranes in fluid communication with the plenum.
2. The process of claim 1 wherein the mass of thermoplastic material is secured to the pan with a second quantity of a thermoplastic material.
3. The process of claim 2 wherein the pan is made of a thermoplastic material.
4. The process of claim 3 wherein the fibers are made of a thermoplastic material.
5. The process of claim 1 wherein the step of forming the mass of thermoplastic material further comprises laying lengths of membrane fiber onto a supporting surface such that adjacent lengths of membrane fiber are spaced from each other by at least a minimum spacing, applying a thermoplastic material in liquid state around a portion of the outer surface, the length of membrane fibers and allowing the thermoplastic material to solidify.
6. The process of claim 5 further comprising the steps of laying additional lengths of membrane fibers onto the lengths of membrane fiber of claim 5 , applying additional thermoplastic material in liquid state around the additional lengths of membrane fiber and allowing the additional thermoplastic material to solidify.
7. The process of claim 5 wherein the supporting surface is a drum.
8. The process of claim 5 wherein the lengths of membranes are cut after the steps of claim 5 to provide distinct lengths of membrane fiber with open ends.
9. The process of claim 5 wherein the lengths of membrane fiber are cut through the solidified thermoplastic material.
10. The process of claim 8 wherein the lengths of membrane fiber are cut near the solidified thermoplastic material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/006,627 US20050082717A1 (en) | 2001-12-11 | 2004-12-08 | Methods of making stretched filtering membranes and modules |
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US33867601P | 2001-12-11 | 2001-12-11 | |
CA002365817A CA2365817A1 (en) | 2001-12-11 | 2001-12-21 | Methods of making stretched filtering membranes and membrane modules |
CA2,365,817 | 2001-12-21 | ||
US10/314,334 US6878276B2 (en) | 2001-12-11 | 2002-12-09 | Methods of making stretched filtering membranes and modules |
US11/006,627 US20050082717A1 (en) | 2001-12-11 | 2004-12-08 | Methods of making stretched filtering membranes and modules |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US10/314,334 Continuation US6878276B2 (en) | 2001-12-11 | 2002-12-09 | Methods of making stretched filtering membranes and modules |
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US20050082717A1 true US20050082717A1 (en) | 2005-04-21 |
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US10/314,334 Expired - Fee Related US6878276B2 (en) | 2001-12-11 | 2002-12-09 | Methods of making stretched filtering membranes and modules |
US11/006,627 Abandoned US20050082717A1 (en) | 2001-12-11 | 2004-12-08 | Methods of making stretched filtering membranes and modules |
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US10/314,334 Expired - Fee Related US6878276B2 (en) | 2001-12-11 | 2002-12-09 | Methods of making stretched filtering membranes and modules |
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CA (1) | CA2365817A1 (en) |
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DE602004013731D1 (en) * | 2003-03-05 | 2008-06-26 | Hydranautics | DIPLOCKABLE MEMBRANE MODULE WITH REPLACEABLE MEMBRANE ELEMENTS |
EP1882512A1 (en) * | 2006-07-26 | 2008-01-30 | Vlaamse Instelling Voor Technologisch Onderzoek (Vito) | Planar capillary membrane filtration module and method of its production |
DE102006057101A1 (en) * | 2006-12-04 | 2008-06-05 | Fresenius Medical Care Deutschland Gmbh | Fiber strand i.e. hollow-fiber membrane strand, winding up device for producing e.g. filter for hemodialysis, has two reels rotatably mounted on reel support, where reels have axes of rotation extending perpendicular to main axis of support |
DE102007009208B4 (en) * | 2007-02-26 | 2010-01-28 | Fresenius Medical Care Deutschland Gmbh | Hollow fiber, hollow fiber bundles, filters and processes for producing a hollow fiber or a hollow fiber bundle |
DE102015225668A1 (en) * | 2015-12-17 | 2017-06-22 | Mahle International Gmbh | Process for producing a capillary membrane bundle |
CN113663522B (en) * | 2020-05-15 | 2022-12-20 | 三达膜科技(厦门)有限公司 | Casting method of hollow fiber membrane filaments |
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Also Published As
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US6878276B2 (en) | 2005-04-12 |
US20030111407A1 (en) | 2003-06-19 |
CA2365817A1 (en) | 2003-06-11 |
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