WO2010059327A2 - Membrane microporeuse et procédé de fabrication de celle-ci - Google Patents

Membrane microporeuse et procédé de fabrication de celle-ci Download PDF

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Publication number
WO2010059327A2
WO2010059327A2 PCT/US2009/061572 US2009061572W WO2010059327A2 WO 2010059327 A2 WO2010059327 A2 WO 2010059327A2 US 2009061572 W US2009061572 W US 2009061572W WO 2010059327 A2 WO2010059327 A2 WO 2010059327A2
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WIPO (PCT)
Prior art keywords
microporous membrane
dope
zone
relative humidity
humidity level
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PCT/US2009/061572
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English (en)
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WO2010059327A3 (fr
Inventor
Ilyess H. Romdhane
Mikhail S. Mezhirov
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3M Innovative Properties Company
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Application filed by 3M Innovative Properties Company filed Critical 3M Innovative Properties Company
Priority to KR1020117013951A priority Critical patent/KR101701524B1/ko
Priority to JP2011537474A priority patent/JP5698140B2/ja
Priority to CN200980154711.1A priority patent/CN102281938B/zh
Priority to US13/129,145 priority patent/US8540801B2/en
Priority to EP09827952.4A priority patent/EP2365869B1/fr
Priority to BRPI0921970A priority patent/BRPI0921970A2/pt
Publication of WO2010059327A2 publication Critical patent/WO2010059327A2/fr
Publication of WO2010059327A3 publication Critical patent/WO2010059327A3/fr
Priority to US13/974,121 priority patent/US8663372B2/en

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/08—Polysaccharides
    • 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
    • B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
    • B01D67/0013—Casting processes
    • 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
    • B01D69/06—Flat membranes
    • 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
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • 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
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • B01D69/1213—Laminated layers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/30—Polyalkenyl halides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/30—Polyalkenyl halides
    • B01D71/301—Polyvinylchloride
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/48—Polyesters
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/56—Polyamides, e.g. polyester-amides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/58—Other polymers having nitrogen in the main chain, with or without oxygen or carbon only
    • B01D71/62—Polycondensates having nitrogen-containing heterocyclic rings in the main chain
    • B01D71/64—Polyimides; Polyamide-imides; Polyester-imides; Polyamide acids or similar polyimide precursors
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/58—Other polymers having nitrogen in the main chain, with or without oxygen or carbon only
    • B01D71/62—Polycondensates having nitrogen-containing heterocyclic rings in the main chain
    • B01D71/64—Polyimides; Polyamide-imides; Polyester-imides; Polyamide acids or similar polyimide precursors
    • B01D71/643—Polyether-imides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/66—Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only
    • B01D71/68—Polysulfones; Polyethersulfones
    • 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
    • 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
    • B01D2325/0283—Pore size
    • B01D2325/02834—Pore size more than 0.1 and up to 1 µm
    • 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
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/249921—Web or sheet containing structurally defined element or component
    • Y10T428/249953—Composite having voids in a component [e.g., porous, cellular, etc.]

Definitions

  • the present disclosure relates to a method for forming a microporous membrane.
  • Microporous membranes with diverse properties are used in many modern products, including such things as filters, breathable articles, absorbent articles, and medical articles.
  • microporous membranes are further described in U.S. Patent Nos. 6,736,971 (Sale et al); 5,869,174 (Wang); 6,632,850 (Hughes et al.); 4,992,221 (Malon et al.); 6,596,167 (Ji et al.); 5,510,421 (Dennis et al.); 5,476,665 (Dennison et al.); and U.S. Patent Application Publication Nos. 2003/0209485; 2004/0084364 (Kools).
  • Coagulation of dope layers with coagulation baths has been described.
  • Another known method for coagulating dope layers includes introducing a non solvent to the dope layer in the form of a vapor.
  • the present disclosure describes a method for forming a microporous membrane. More specifically, vapor induced phase separation techniques are used for forming multizone microporous membranes having improved material throughput.
  • a method for forming microporous membranes having two or more zones (e.g., multizone).
  • the membrane is suitable for high material throughput applications.
  • the method includes casting a plurality of dope formulations on a support to provide a multilayer sheet having a first major surface, and exposing the multilayer sheet to a first relative humidity level so that water vapor diffuses into the first major surface.
  • the method includes exposing the multilayer sheet to a second relative humidity level greater than the first relative humidity level so that additional water vapor diffuses into the multilayer sheet effecting a phase separation to provide the microporous membrane.
  • the method also includes washing and drying the microporous membrane.
  • a multizone microporous membrane comprising a first zone and a second zone.
  • the multizone microporous membrane independently comprises pores having average pore diameters, such that the average pore diameters of the first zone are greater than the average pore diameters of the second zone.
  • the multizone microporous membrane has a water flux measurement of at least 3,000 lmh / psi and a forward flow bubble point measurement comprising a first zone pressure peak less than 5 psi and an initial bubble point pressure measurement less than 15 psi.
  • FIG. 1 is a schematic representation of a process for forming a multizone microporous membrane.
  • FIG. 2 is schematic representation of a multizone microporous membrane.
  • FIG. 3 is a schematic representation of a ternary phase diagram.
  • FIG. 4 is a SEM micrograph (cross-section) of a multizone microporous membrane of Example 1 having a first zone and a second zone.
  • FIG. 5a is a SEM micrograph (planar view) of a first major surface of the first zone of the multizone microporous membrane of FIG. 4.
  • FIG. 5b is a SEM micrograph (planar view) of a second major surface of the second zone of the multizone microporous membrane of FIG. 4.
  • FIG. 6 is a graphical illustration of a Forward Flow Bubble Point graph of a multizone microporous membrane (FIG. 4) of Example 1.
  • FIG. 7 is a SEM micrograph (cross-section) of a monozone microporous membrane of Example 4.
  • FIG. 8 is a graphical illustration of a Forward Flow Bubble Point graph of a monozone microporous membrane (FIG. 7) of Example 4.
  • doctor formulation refers to a composition comprising polymeric material and an adjuvant in a solvent.
  • casting refers to die forming and depositing dope formulations in layers to form a multilayered sheet.
  • relative humidity level refers to the concentration of water vapor in air and is defined as the ratio of the partial pressure of water vapor in the mixture to the saturated vapor pressure of water at the same temperature. Relative humidity is normally expressed as a percentage.
  • phase separation refers to the transformation of a homogenous system (e.g., dope formulation) into two or more phases.
  • phase separation mechanisms include vapor induced phase separation (VIPS), thermal induced phase separation (TIPS) and liquid-liquid phase separation (LIPS).
  • adjuvant refers to an additive(s) for a dope formulation.
  • multizone microporous membrane refers to a membrane having at least two distinct porous portions, each of the porous portions referred to as a "zone” or a "microporous zone.”
  • the present disclosure uses a VIPS process to form microporous membranes.
  • the process includes casting dope formulations on a support to provide a multilayered sheet, and exposing the multilayered sheet to water vapor at two different relative humidity levels.
  • the multilayered sheet is first exposed to water vapor at a first relative humidity level.
  • the water vapor diffuses into the multilayered sheet along the first major surface thereof.
  • exposure to water vapor at a first relative humidity is believed to transform the dope formulations in the multilayered sheet into a metastable state.
  • the multilayered sheet is then exposed to water vapor at a second relative humidity level greater than the first relative humidity level.
  • the water vapor at the second relative humidity level also diffuses into the multilayered sheet to increase the concentration of water therein and induce a phase separation in the dope formulations.
  • each of the original layers of the sheet become distinct microporous zones which are joined to one another along a common interface and which, together, form a multizone microporous membrane.
  • FIG. 1 is a process flow diagram for forming microporous membranes by the above described method.
  • dope formulations are first cast on a support to form a multilayered sheet.
  • the multilayered sheet is then exposed to water vapor at a first relative humidity level followed by a second exposure to water vapor at a second relative humidity level.
  • the microporous membrane is typically washed and dried to provide a multizone microporous membrane.
  • FIG. 2 illustrates a multizone microporous membrane 200 according to the present disclosure.
  • Multizone microporous membrane 200 has a first zone 210 and a second zone 220.
  • First zone 210 and second zone 220 are joined to one another along a common interface 230.
  • Both the first zone 210 and the second zone 220 include a plurality of micropores (not shown) formed as a result of the VIPS process.
  • the first zone 210 includes a pore structure with average pore dimensions that are larger than the average pore dimensions of the pores in the second zone 220.
  • a first major surface 240 of the first zone 210 is located opposite the common interface 230, and a second major surface 250 of the second zone 220 is located opposite the common interface 230 of the multizone microporous membrane 200.
  • Multizone microporous membranes formed herein are generated without the use of coagulation baths or from the construction of multiple monozone membrane layers.
  • the elimination of coagulation baths reduces the overall costs previously associated with the formation of microporous membranes by eliminating the need for filtering and cleaning such baths and related equipment.
  • the resulting multizone microporous membranes have a combination of high material throughput, fast water flow and robust hydrophilicity.
  • the dope formulations comprise polymeric material, an adjuvant, solvent and additives for controlling the rate and depth of phase separation throughout the thickness of a multilayer sheet and to influence the formation of a specific microstructure in the final multizone microporous membrane.
  • concentration of the polymeric materials and/or the adjuvant of the dope formulations can influence the formation of the final micro structure within each of the zones, facilitate the degree of diffusion of water vapor into the multilayer at first and second relative humidity levels, and influence the integrity of the resulting microporous membrane. Simply stated, if the concentration of the polymeric material of the dope formulation is too low, a membrane will not be formed. Similarly, if the concentration of the polymeric material in a dope formulation is too high, an undesired or irregular microstructure may result.
  • the concentration of the polymeric material can be selected, in part, to provide a desired viscosity and/or surface tension for the dope formulation in order to facilitate casting of the formulation as a layer in a multilayered sheet.
  • Suitable polymeric materials generally comprise materials capable of forming micropores (e.g., microstructures) upon exposure to water vapor.
  • dope formulations include polymeric materials having a concentration within the range from about 5 weight percent to about 15 weight percent based on the total weight of the dope formulation.
  • the concentration of the polymeric material is in a range from about 7 weight percent to about 14 weight percent, or in a range from about 9 weight percent to about 14 weight percent based on the total weight of the dope formulation.
  • the second dope formulation may have a concentration of polymeric material greater than the concentration of polymeric material in the first dope formulation.
  • a number of polymeric materials are suitable to include in a dope formulation, and suitable dope formulations can comprise a single polymeric material or a blend of polymeric materials.
  • the polymeric materials can be amorphous, crystalline, or partially crystalline.
  • the polymeric material in a first dope formulation is the same as the polymeric material in a second dope formulation. In other embodiments, the polymeric material in a first dope formulation is different than the polymeric material in a second dope formulation.
  • suitable polymeric materials include, for example, polyethersulfones, polyetherimides, polyimides, polyamides, polysulfones, polyarylsulphones, polyvinyl chloride, polyethylene terephthalate, polycarbonates, polyolefins such as polyethylene or polypropylene, cellulose esters such as cellulose acetate or cellulose nitrate, polystyrenes, acrylic polymers, methacrylic polymers, copolymers of acrylic or methacrylic polymers, and combinations thereof.
  • the polymeric material of a dope formulation is a polyethersulfone according to Formula (I).
  • the polymeric material of a dope formulation is a polyetherimide according to Formula (II).
  • suitable dope formulations are formulated to have a viscosity that is high enough to permit the formulation to be cast as a layer in a multilayered sheet.
  • a suitable viscosity for a dope formulation may depend on certain process conditions such as the actual or anticipated line speed of a substrate supporting the molten dope formulations following the casting step. Similarly, factors such as surface tension, general bead stability and other fluid properties of the dope formulations are considered for ensuring coating uniformity. The foregoing factors can also affect the diffusion of water vapor into a dope formulation layer according to the VIPS process utilized herein.
  • an appropriate viscosity for a dope formulation is within the range from about 2,000 centipoises to about 8,000 centipoises. In some embodiments, the viscosity of the dope formulation is in a range from about 2,000 centipoises to about 7,000 centipoises, or in a range from about 3,000 centipoises to about 6,500 centipoises.
  • the dope formulations herein include at least one solvent. Suitable solvents are those that dissolve the polymeric material to provide a homogeneous solution. In various embodiments, the solvent is compatible with the polymeric material, adjuvant and any optional additives present in the dope formulation.
  • the selection of a solvent can be made by one skilled in the art to influence one or more steps in the VIPS process as well as the properties of the resulting microporous membrane. For example, the selection of a solvent can influence the rate of phase separation for the multilayered sheet, the type of micro structure formed in the finished membrane, or the depth of the microstructure formation within a layer of the dope formulation.
  • solvents for dope formulations useful in the present disclosure include, for example, water, dimethyl formamide (DMF), N, N- dimethylacetamide, N-methyl-2- pyrrolidinone (NMP), tetramethylurea, acetone, methyl ethyl ketone (MEK), methyl acetate, ethylacetate and other alkyl acetates, dimethylsulfoxide (DMSO), and combinations thereof.
  • the solvent is N-methyl-2-pyrrolidinone.
  • a solvent can be oligomeric or polymeric in nature.
  • the dope formulation can comprise more than one solvent, or a blend of solvents.
  • the solvent provides a stable homogeneous solution for casting a dope formulation to form a microporous membrane.
  • Solvents are categorized as 'good' solvents, 'nonsolvents', and 'poor' solvents, depending on their ability to dissolve the selected polymer therein.
  • Solvents categorized as 'good' are those in which the interactions (forces of attraction) between the polymer molecules and solvent molecules are greater than the forces of attraction between polymer molecules. The reverse is true for nonsolvents.
  • Solvents described as 'poor' are those in which the interactions between the polymer and solvent are equal to the forces of attraction between polymer molecules.
  • a stable homogeneous dope formulation can be obtained by first dissolving the chosen polymer in a good solvent.
  • suitable 'good' solvents include, for example, N- methyl-2- pyrrolidinone, dimethylacetamide, dioxane, dimethylsulfoxide, chloroform, tetramethylurea, and tetrachloroethane.
  • good solvents are able to dissolve substantial amounts of polymeric material.
  • a 'good' solvent is one that is miscible with the polymeric material at polymer concentrations of at least about 5 weight percent based on the total weight of the dope formulation.
  • Hildebrand solubility parameters refer to a solubility parameter represented by the square root of the cohesive energy density of a material, having units of (pressure) 1 ' 2 , and being equal to
  • ⁇ H is the molar vaporization enthalpy of the material
  • R is the universal gas constant
  • T is the absolute temperature
  • V is the molar volume of the solvent.
  • Hildebrand solubility parameters are tabulated for solvents in: Barton, A. F. M., “Handbook of Solubility and Other Cohesion Parameters", 2 nd Ed., CRC Press, Boca Raton, FIa. (1991); for monomers and representative polymers in "Polymer Handbook", 4 l Ed., J. Brandrup & E. H. Immergut, Eds. John Wiley, NY, pp. VII 675-714 (1999); and for many commercially available polymers in Barton, A. F. M., “Handbook of Polymer- Liquid Interaction Parameters and Solubility Parameters", CRC Press, Boca Raton, FIa. (1990).
  • Adjuvants selected for the dope formulations are generally soluble in the solvent and are compatible with the polymeric material. Adjuvants can be added to dope formulations to adjust the viscosity of a dope formulation prior to casting it as a layer in a multilayer sheet. Similarly, the concentration of adjuvant in a dope formulation can influence the diffusion of water vapor into layers of dope formulations during the VIPS process. Adjuvants can also be added to dope formulations to control the rate (kinetics) of the phase separation in a VIPS process. Some useful adjuvants include, for example, poly(alkylene) glycols, polyethers, or combinations thereof. In some embodiments, the adjuvant is poly (ethylene) glycol.
  • Adjuvants added to dope formulations at selected concentrations can effect phase separation at a predetermined depth within a layer of a dope formulation.
  • the depth of the phase separation within a layer of dope formulation is in a range from about 5 percent to about 100 percent of the thickness of the layer.
  • the concentrations of adjuvant(s) in a plurality of dope formulations are selected to influence phase separation and provide different pore size distributions and different porosities for each of the different zones within the multizone microporous membrane.
  • Multizone microporous membranes having zones with different average pore diameters are useful in certain high material throughput and high flux filtration applications.
  • the adjuvant concentration in a dope formulation can be in a range from about 60 weight percent to 70 weight percent based on the total weight of the dope formulation. In some embodiments, the concentration of the adjuvant is in a range from about 60 weight percent to about 68 weight percent, or in a range from about 62 weight percent to about 68 weight percent based on the total weight of the dope formulation.
  • the dope formulations are first cast on a support to provide a multilayer sheet.
  • the support can be a plastic or a metal sheet, and it can be continuous or discontinuous (e.g., discrete).
  • the selected support provides stability for the stacked layers of dope formulations while casting and during transport through the first and second humidified environments, and during the washing and drying steps.
  • a plurality of dope formulations is typically cast to form a multilayered sheet on a support.
  • a first dope formulation layer is stacked onto a second dope formulation layer with an interface formed between the layers.
  • the second dope formulation layer lays directly on the support and the first dope formulation layer is positioned on top of the second dope formulation, opposite the support.
  • the resulting multilayered sheet has a first major surface that coincides with the exposed surface on the first dope formulation layer.
  • two dope formulation layers are cast simultaneously to provide the aforementioned configuration.
  • Simultaneous casting of multiple dope formulations can be accomplished using any of a number of known techniques and devices. Some useful devices include a multipath applicator, a dual-knife over roll device, a dual layer slot fed knife die, and other related devices known in the art for casting dope formulations.
  • any dope formulation layer is dependent on several variables, as known by those skilled in the art.
  • the thickness of a layer can depend on the equipment settings as well as on the rheology and viscosity of the respective dope formulations.
  • the foregoing methods for casting typically involve the use of a die to shape the dope formulations as they are cast into a multilayered sheet. Consequently, the thicknesses of the dope formulation layers are directly affected by the gap dimensions of the particular die slots that are used for the casting operation.
  • gap dimensions may be adjusted, in part, to accommodate the viscosity of a dope formulation. In casting dope formulations using a dual knife over roll device, the gap dimensions can be in a range from about 150 micrometers to about 300 micrometers.
  • the multilayer sheet After casting the dope formulation layers to form the multilayer sheet, the multilayer sheet is exposed to at least two humidified environments to induce phase separation and the formation of microstructures within the layered dope formulation layers.
  • dope formulations that are suitable for forming microporous membranes is better understood through a consideration of principles of polymer solubility, the miscibility of components, and the concentrations of polymer, solvent, and water. At certain concentrations, polymeric material is completely miscible with solvent. At other concentrations, a region of phase separation exists.
  • FIG. 3 a ternary phase diagram 300 is shown for the components of an exemplary dope formulation, i.e., polymer concentration, water concentration and solvent concentration.
  • FIG. 3 illustrates a relationship between the three components.
  • binodal curve 305 delineates the regions 320 and 330.
  • Each region represents areas of component concentrations for a dope formulation, with region 320 representing a thermodynamically stable concentration of components and region 330 representing a thermodynamically unstable concentration of components.
  • the relationship of the polymer concentration to solvent and water concentrations is delineated by the binodal curve 305.
  • Region 330 is further divided to include area 340 between spinodal curve 310 and binodal curve 305.
  • Spinodal curve 310 and binodal curve 305 intersect at point 315 which represents the so-called theta condition ( ⁇ ).
  • ⁇ the interaction forces between the polymeric material molecules and the solvent molecules equal the interaction forces of polymer molecules for other molecules of the same polymer.
  • a dope formulation having component concentrations within area 340 represents a composition believed to be in a metastable state prior to phase separation.
  • a dope formulation having component concentrations within area 330 but outside of area 340 represents a phase separated composition.
  • the formulation In the processing of a dope formulation via a VIPS process, the formulation is exposed to water vapor to increase the water content of the formulation and thereby alter the concentrations of solvent and polymer.
  • the VIPS process seeks to induce a phase separation of a homogeneous solution by adding water (e.g., as water vapor) to the dope formulation and altering the component concentrations of the formulation until the component concentrations migrate from region 320, where the formulation is thermodynamically stable (e.g., a solution), to region 340 where it is believed to exist in a metastable state.
  • a sufficient amount of water vapor will be diffused into the dope formulation so that the component concentrations of the formulation move it out of region 340 and further into the region 330 where phase separation occurs.
  • Humidified environments may be used for delivering water vapor to the dope formulations of a multilayered sheet.
  • water vapor can be delivered by injecting steam into humidified chambers.
  • Sensors placed within the chambers can be used to monitor the actual air temperature and percent relative humidity (e.g., relative humidity level).
  • Exposure times to water vapor can vary within a useful range depending on factors such as the relative humidity levels being employed, air temperature, and gas phase (e.g., steam) velocity.
  • the exposure time for the multilayered sheet can be, for example, in a range from about 7.5 minutes to about 25 minutes.
  • exposure time can be, for example, in a range from about 10 minutes to about 22.5 minutes, in a range from about 10 minutes to about 20 minutes, or in a range from about 12.5 minutes to about 20 minutes.
  • the first relative humidity level can be in a range from about 45 percent to about 55 percent. In some embodiments, the first relative humidity level can be in a range from about 46 percent to about 54 percent, in a range from about 46 percent to about 53 percent, or in a range from about 46 percent to about 52 percent.
  • the multilayered sheet After exposure to water vapor at a first humidity level for a period of time, the multilayered sheet is exposed to a second relative humidity level to induce a phase separation.
  • the second relative humidity level is at least 5 percent greater than the first relative humidity level.
  • the second relative humidity level is at least 6 percent greater, at least 7 percent greater, at least 8 percent greater, at least 9 percent greater, or at least 10 percent greater than the first relative humidity level.
  • the second relative humidity level can be in a range from about 60 percent to about 80 percent. In some embodiments, the second relative humidity level is in a range from about 60 percent to about 75 percent, in a range from about 62 percent to about 75 percent, or in a range from about 65 percent to about 75 percent.
  • dope formulations in a multilayered sheet are exposed to water at a relative humidity level intermediate to the first relative humidity level and to the second relative humidity level.
  • the intermediate relative humidity level may be desired for certain dope formulation or under certain processing conditions in order to gradually increase the water content of the dope formulations.
  • the first relative humidity level can be in a range from about 45 percent to 50 percent
  • the intermediate relative humidity level (e.g., intermediate) can be in a range from about 50 percent to 55 percent
  • the second relative humidity level can be in a range from about 55 percent to 65 percent.
  • Humidified environments used for the delivery of water vapor and the aforementioned relative humidity levels are typically maintained within a desired temperature range between about 15°C to about 55°C.
  • the temperature can be, for example, between about 20 0 C to about 50 0 C, between about 20 0 C to about 47°C, or between about 20 0 C to about 45°C.
  • the resulting phase separated microporous membrane is subjected to washing and drying processes. Washing of the microporous membrane aids in removal of solvents, including water, used in the dope formulations.
  • the washing step described helps to prevent the microstructure of the membrane from collapsing. Washing can be accomplished by spraying, immersing, and other techniques for removing solvents and water.
  • the membrane is moved through a tank with fluid bearing rollers. After washing, the microporous membrane can be dried by convection, air drying and vacuum processing. In some embodiments, the membrane is dried at ambient conditions in air.
  • Effective pore sizes (e.g., average pore diameters) formed in the multizone microporous membranes can range from about 0.05 micrometer to about 2 micrometers.
  • the pore dimensions from the microporous membrane can be, for example, in a range of about 0.1 micrometer to about 1.5 micrometers, or in a range of about 0.2 micrometer to about 0.8 micrometer.
  • the pore dimensions of the microporous membrane can be nearly uniform or symmetrical through a thickness of one or more of the zones. Zones can have a symmetrical distribution of pores extending through a portion of the thickness of the zone or through the entire thickness of the zone.
  • multizone microporous membranes formed by the method described comprise at least two zones having nearly symmetrical pore distributions extending through the thicknesses of their respective zones.
  • Pore size of the membranes refers to the average diameter of an opening within a microstructure formed during phase separation. Pore sizes can be measured, for example, by bubble point pressure methods. Some other pore size and pore size distribution measurement methods can include, for example, solute retention, and flow/pressure techniques. Pore diameter can also be estimated by porometry analysis and by a separate measurement of the bubble point, with a higher bubble point indicative of tighter or smaller pores.
  • Multizone microporous membranes can be formed comprising at least two zones having different pore dimensions within each of their respective zones.
  • Microporous membranes formed by the method described herein provide for multizone microporous membranes having a first zone and a second zone. Pores of the first zone provide a first microstructure having larger pore dimensions than the pores formed in the second zone providing a second microstructure
  • the microstructures formed can depend on the dope formulation and the processing parameters.
  • the first and second microstructures can provide a continuous or discontinuous path through the membrane.
  • the formation of the microstructures can depend on the concentration of some of the components (e.g., polymeric material, coating adjuvant, nonsolvent) of the dope formulation and the water vapor concentration.
  • the morphology (e.g., symmetric or asymmetric) of the microstructures can further depend on the metering (e.g., layer thickness) of the dope formulations, relative humidity level and/or the rate of phase separation.
  • the morphology can also depend on the phase separation mechanism, and related pressure and temperature processing conditions.
  • the first zone of the microporous membrane has average pore dimensions which are greater than the average pore dimensions of the second zone.
  • the ratio of the average pore dimensions of the first zone to the second zone can be, for example, in a range of about 10: 1 to about 2: 1.
  • Thickness of the microporous membranes formed can be dependent on the thickness of the dope formulation layers when cast, and subsequent removal of solvents followed by the steps of washing and drying the microporous membrane.
  • the thickness of the microporous membrane can be, for example, in a range of about 125 micrometers to about 150 micrometers.
  • the thickness of the microporous membrane can be in a range of about 125 micrometers to about 145 micrometers, in a range of about 125 micrometers to about 140 micrometers, or in a range of about 125 micrometers to about 135 micrometers.
  • the thickness of the first zone is greater than the thickness of the second zone of the multizone microporous membrane. In another embodiment, the thickness of the first zone is equal to the thickness of the second zone of the multizone microporous membrane.
  • Multizone microporous membranes formed by the method of the present application can be used in filtration applications.
  • the first zone can act as a pre-filter for capturing larger particles and the second zone can capture smaller particles.
  • Multizone microporous membranes comprising a first zone and a second zone comprise pores having average pore diameters.
  • the average pore diameters of the first zone are generally greater than the average pore diameters of the second zone.
  • the multizone microporous membrane formed herein has a water flux measurement of at least 3,000 lmh / psi and a forward flow bubble point measurement comprising a first zone pressure peak less than 5 psi and an initial bubble point pressure measurement less than 15 psi.
  • a combination microporous membrane can be formed comprising a multizone microporous membrane, as already described, laminated to a mono zone microporous membrane.
  • the term "monozone microporous membrane” refers to a microporous membrane having at least one porous zone resulting from the vapor induced phase separation of a single dope formulation.
  • a monozone membrane can have two or more layers, but the resulting membrane zones will have average pore diameters that are substantially the same.
  • Such a monozone membrane is made in the same manner as described herein for multizone microporous membranes but using first and second dope formulations that are identical or at least are substantially the same. While the monozone membrane includes two 'zones,' both zones are of the same morphology and average pore size and, consequently form a single filtration zone.
  • Lamination of the multizone microporous membrane and the monozone microporous membrane can be accomplished using known lamination techniques including pressure or thermal methods and/or using a suitable additive or an adhesive.
  • the resulting article is referred to as a combination microporous membrane comprised of a multilayered microporous membrane having a monozone membrane affixed (e.g., laminated) to the major surface of the second zone.
  • Multizone membranes formed herein eliminate the need for combination membranes formed by lamination of at least two membranes.
  • Microporous membranes formed by the described methods can reduce manufacturing costs and increases manufacturing efficiency.
  • the use of humidified environments to deliver water vapor to sheets for inducing phase separation in multilayer sheets eliminates the need for a coagulation bath and multiple washing steps.
  • the multizone microporous membranes disclosed herein have high material throughput.
  • the multizone microporous membranes can be used in pharmaceutical, biological, medical, food and beverage applications.
  • a filter assembly comprising a cartridge, an inlet, an outlet, and a multizone microporous membrane residing in the cartridge can be used in residential, commercial and industrial applications.
  • IBP Initial Bubble Point Pressure
  • WFR Water Flow Rate
  • RMT Robust Molasses Throughput
  • FFBP Forward Flow Bubble Point
  • CEl - Sterile High Capacity SHC
  • CE2 - DuraPES TM-600 Membrana, Wuppertal, Germany
  • Dope formulations were prepared and delivered to a dual-knife over roll device.
  • the first dope formulation (first dope) comprised 9.7 wt. % polyethersulfone (Radel H-2000P; Solvay, Alpharetta, Georgia) dissolved in a solution blend (27.3 / 63 wt. %) of l-methyl-2- pyrrolidinone (NMP) (Sigma- Aldrich, St. Louis, Missouri) / polyethylene glycol (PEG-400, (Sigma-Aldrich, St. Louis, Missouri)).
  • the second dope formulation (e.g., second dope) comprised 14 wt. % polyethersulfone (Sigma-Aldrich, St. Louis, Missouri) dissolved in a solution blend (17 / 69 wt. %) of l-methyl-2-pyrrolidinone (NMP) / polyethylene glycol (PEG-400).
  • the first and second dope formulations were co-cast onto a 125 micrometer thick polyethylene terephthalate (PET) film (3M Company, St. Paul, Minnesota) conveyed at a line speed of 0.41 meters (m) /minute.
  • PET polyethylene terephthalate
  • the gap dimensions of the dual knife over roll device were set at 150 micrometers for the second dope formulation and the gap dimension was set at 225 micrometers for the first dope formulation.
  • the viscosities of the first dope formulation and the second dope formulation were 3,000 centipoises (cps) and 7,500 cps, respectively.
  • the first dope and the second dope formulations were cast as layers on one another forming an interface between the two formulations to provide the multilayer sheet.
  • the multilayer sheet was introduced into a 7.31 meter long air-floatation dryer line having first and second humidified environmental chambers, and a washing and drying section. Each of the first and second humidified environmental chambers had a length of approximately 2.45 m. Steam was injected into the chambers to achieve the first and second relative humidity levels. The relative humidity of the humidified chambers was controlled by needle valves placed downstream of the steam injectors. Humidity sensors were used to monitor the actual temperature and percent relative humidity in the chambers. The multilayer sheet was exposed to a first relative humidity level of 56 percent at 45 0 C in a first humidified chamber for water vapor to diffuse into the first major surface. The multilayer sheet was then exposed to a second relative humidity level of 65 percent at 43.3 0 C in a second humidified chamber to effect a phase separation. The resulting article was washed and dried to provide a multizone microporous membrane.
  • FIG. 4 is an SEM micrograph illustrating, in cross-section, the microporous structure of the multizone microporous membrane 400 according to Example 1.
  • the multizone microporous membrane 400 includes two individual zones having two distinct pore sizes.
  • the first zone 405 has pore sizes of about 0.6 micrometers, and the second zone 410 has pore sizes of about 0.2 micrometers separated by an interface 415.
  • First zone 405 of the multizone microporous membrane 400 can provide a prefiltering membrane feature and the second zone 410 can provide a sterilizing membrane feature in high throughput filtering applications, for example.
  • FIG. 5a is an SEM micrograph (planar view) illustrating a first major surface of the first zone 405 of FIG. 4.
  • FIG. 5b is a SEM micrograph (planar view) illustrating the second major surface of the second zone 410 of FIG. 4.
  • a FFBP curve for Example 1 is illustrated in FIG. 6.
  • the curve supports a multizone morphology having a first zone and a second zone.
  • a first zone pressure peak is exhibited at about 4 psi when nitrogen clears the first zone.
  • the bulk flow at about 11.34 psi indicates that adequate nitrogen pressure was reached to clear the second zone of the multizone microporous membrane.
  • Test results from Example 1 are shown in Table 1.
  • a multizone microporous membrane was formed in a manner similar to Example 1 with the following exceptions: polyethersulfone polymer (Ultrson E-6020; BASF, location) was used for the first and the second dope formulations; the first humidity level was 50 percent at 45°C and the second humidity level was 65 percent at 43°C.
  • the resulting FFBP profile (not shown) supported a multizone morphology having a first zone pressure peak of 4.5 psi. Test results from Example 2 are illustrated in Table 1.
  • a multizone microporous membrane was formed in a manner similar to Example 1 with the following exceptions: the gap dimension of the dual knife over roll device for delivering the first dope layer was set at 350 micrometers; the gap dimension for delivering the second dope layer was set at 125 micrometers; the first relative humidity level was 48 percent at 47.2 0 C; the second relative humidity level was 70 percent at 45.6 0 C.
  • the resulting FFBP profile (not shown) supported a multizone morphology having a first zone pressure peak of 4.5 psi. Test results from Example 3 are illustrated in Table 1.
  • a single-layer monozone microporous membrane (sterilizing-grade membrane) was prepared for use in the construction of a combination membrane.
  • the monozone microporous membrane was formed using the dual knife over roll device of Example 1.
  • the second dope formulation of Example 2 was cast and exposed to a first relative humidity level of 43 percent and 45°C.
  • the single dope formulation layer was then exposed to a second relative humidity level of 65 percent and 43.3 0 C.
  • the resulting material was washed and dried.
  • FIG. 7 is an SEM micrograph of a cross-section of the monozone microporous membrane, showing a symmetrical morphology through the entire thickness of the monozone microporous membrane.
  • FIG. 8 A FFBP curve for Example 4 is illustrated in FIG. 8.
  • the curve supports a monozone morphology.
  • nitrogen (g) clears the single zone at a peak of about 35 psi.
  • the monozone microporous membrane was tested, and the results are illustrated in Table 1.
  • Monozone microporous membranes of FIG. 7 can be applied (e.g., laminated) to multizone microporous membranes for forming combination microporous membranes.
  • the combination microporous membrane can have the monozone membrane (first layer) as a sterilizing membrane and a multizone microporous membrane (second layer) functioning as a pre- filtering membrane.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Laminated Bodies (AREA)

Abstract

La présente invention concerne un procédé de fabrication de membranes microporeuses, et plus particulièrement des techniques de séparation de phase induite par la vapeur utilisées pour former des membranes microporeuses multizones offrant un débit de matière amélioré.
PCT/US2009/061572 2008-11-21 2009-10-22 Membrane microporeuse et procédé de fabrication de celle-ci WO2010059327A2 (fr)

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KR1020117013951A KR101701524B1 (ko) 2008-11-21 2009-10-22 미세다공성 막 및 그 형성 방법
JP2011537474A JP5698140B2 (ja) 2008-11-21 2009-10-22 微多孔性膜及び形成法
CN200980154711.1A CN102281938B (zh) 2008-11-21 2009-10-22 微孔膜和形成方法
US13/129,145 US8540801B2 (en) 2008-11-21 2009-10-22 Microporous membrane and method for forming
EP09827952.4A EP2365869B1 (fr) 2008-11-21 2009-10-22 Procédé de fabrication d'une membrane microporeuse
BRPI0921970A BRPI0921970A2 (pt) 2008-11-21 2009-10-22 membrana microporosa e método para sua formação.
US13/974,121 US8663372B2 (en) 2008-11-21 2013-08-23 Microporous membrane and method for forming

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EP2365869B1 (fr) 2017-10-04
US20130334123A1 (en) 2013-12-19
JP2012509171A (ja) 2012-04-19
EP3281689A1 (fr) 2018-02-14
US20110225940A1 (en) 2011-09-22
CN102281938B (zh) 2016-08-03
BRPI0921970A2 (pt) 2018-06-05
JP5698140B2 (ja) 2015-04-08
EP2365869A2 (fr) 2011-09-21
CN102281938A (zh) 2011-12-14
US8663372B2 (en) 2014-03-04
KR20110095372A (ko) 2011-08-24
WO2010059327A3 (fr) 2010-07-22
KR101701524B1 (ko) 2017-02-01
US8540801B2 (en) 2013-09-24
EP2365869A4 (fr) 2012-09-19

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