CA2385346A1 - Heterogeneous ion exchange membrane and method of manufacturing thereof - Google Patents
Heterogeneous ion exchange membrane and method of manufacturing thereof Download PDFInfo
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- CA2385346A1 CA2385346A1 CA002385346A CA2385346A CA2385346A1 CA 2385346 A1 CA2385346 A1 CA 2385346A1 CA 002385346 A CA002385346 A CA 002385346A CA 2385346 A CA2385346 A CA 2385346A CA 2385346 A1 CA2385346 A1 CA 2385346A1
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- ion exchange
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/20—Manufacture of shaped structures of ion-exchange resins
- C08J5/22—Films, membranes or diaphragms
- C08J5/2206—Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds
- C08J5/2275—Heterogeneous 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/30—Extrusion nozzles or dies
- B29C48/305—Extrusion nozzles or dies having a wide opening, e.g. for forming sheets
- B29C48/31—Extrusion nozzles or dies having a wide opening, e.g. for forming sheets being adjustable, i.e. having adjustable exit sections
- B29C48/313—Extrusion nozzles or dies having a wide opening, e.g. for forming sheets being adjustable, i.e. having adjustable exit sections by positioning the die lips
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92009—Measured parameter
- B29C2948/92114—Dimensions
- B29C2948/92152—Thickness
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92323—Location or phase of measurement
- B29C2948/92428—Calibration, after-treatment, or cooling zone
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92609—Dimensions
- B29C2948/92647—Thickness
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92904—Die; Nozzle zone
-
- 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
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/0001—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor characterised by the choice of material
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2031/00—Other particular articles
- B29L2031/755—Membranes, diaphragms
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
- C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2327/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
- C08J2327/16—Homopolymers or copolymers of vinylidene fluoride
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
- C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2327/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
- C08J2327/18—Homopolymers or copolymers of tetrafluoroethylene
Abstract
A heterogeneous ion exchange material is provided which comprises an ion exchange resin incorporated within a binder, the binder comprising a material selected from the group consisting of: (i) a Metallocene catalyzed linear low density polyethylene, (ii) a very low density polyethylene or ultra low density polyethylene processed using either Ziegler-Natta catalysts or Metallocene catalysts, (iii) a thermoplastic elastomeric olefin comprising a polypropylene continuous phase with an ethylene-propylene-diene monomer or ethylene-propylene rubber rubbery phase dispersed through the polypropylene continuous phase, and (iv) a thermoplastic vulcanizate comprising a polypropylene continuous phase with an ethylene-propylene-diene monomer, ethylene-propylene rubber, nitrile-butadiene rubber, natural rubber, ethylene vinyl acetate rubbery phase dispersed through the polypropylene continuous phase, a co-polymer of vinylidene fluoride and hexafluoropropylene, or a co-polymer of vinylidene fluoride and hexafluoropropylene and tetrafluoroethylene. The ion exchange membrane can be manufactured using advanced extrusion techniques, including computer-controlled material feed, computer-controlled automatic die thickness adjustment with independently adjustable lip segments and nuclear gauge detection with feed-back control. It can also be manufactured by injection molding.
Description
HETEROGENEOUS ION EXCHANGE MEMBRANE
AND METHOD OF MANUFACTURING THEREOF
Field of Invention The present invention relates to novel heterogeneous ion exchange membranes, methods for producing such membranes, and apparatus employing such membranes.
Background of the Invention Membranes that selectively allow diffusion and adsorption of ions while excluding certain other ions and non-ionized solutes and solvents, typically referred to as ion exchange membranes, have numerous important industrial applications. Such membranes are used in electrodialysis and electrodeionization equipment as well as in devices for fractionation, transport depletion and electro-regeneration, and purification or treatment of water, food, beverages, chemicals and waste streams. The membranes are also used in electrochemical devices such as caustic/chlorine electrolysis equipment, electropaint purification equipment, and electro-organic synthesis equipment. Additionally, ion exchange membranes are used in electrophoresis devices and analytical equipment as adsorbents, and as suppressor devices for ion chromatography. They are used in chemical treatment and concentration applications via the processes of Donnan dialysis and diffusion dialysis, and they are also used in batteries and fuel cells for the production of electricity.
In each of the applications described above, numerous membrane properties must be balanced against one another in order to achieve a membrane that satisfies the desired objectives of the particular application. Among these, it is an objective to employ ion exchange membranes that have high selectivity, low solvent and non-ionized solute transfer, low diffusion resistance of the ions selected, high physical strength, and good chemical resistance.
Additionally, it is desirable that such membranes be easily manufactured at low cost without the use of hazardous substances. Furthermore, ideal membranes should be easy to handle and process and should also be amenable to low cost assembly techniques during the production of devices containing such membranes.
Current commercially available ion exchange membranes are primarily of two general types: homogeneous membranes and heterogeneous membranes. A homogeneous membrane is one in which the entire volume of the membrane (excluding any support material that may be used to improve strength) is made from the reactive polymer. Examples include membranes made of sulfonated or aminated styrene-divinylbenzene polymers (SDVB
membranes), polymerized perfluorosulfonic acids (PFSO membranes) or various thermoplastics with active groups grafted onto the base polymer.
Unfortunately, homogeneous membranes tend to be difficult to manufacture. They also tend to employ the use of hazardous materials during their manufacturing process since, for the most part, they must be made from base monomers. Additionally, they are difficult to modify chemically because each modification requires a change in the fundamental chemistry of the membrane.
Homogeneous membranes also tend to have limited physical strength (therefore often requiring a screen or cloth support) because the polymer produced cannot readily combine both the required physical and electrochemical properties to operate efficiently in a fabricated device.
Homogeneous membranes may be either crosslinked (to provide the membrane with dimensional stability, but increased brittleness and sensitivity upon drying), or they may be non-crosslinked (to provide membranes which may be dried, but lack dimensional stability and resistance to swelling and various solvents).
In contrast, heterogeneous membranes are formed of 1) a composite containing an ion exchange resin to impart electrochemical properties and 2) a binder to impart physical strength and integrity. Heterogeneous membrane may also include inert support material to impart extra strength and stability. Typical heterogeneous membranes may be produced as "micro-heterogeneous" membranes by the paste method (in which ion exchange resin monomers are reacted to form the ultimate ion exchange resin polymer in the presence of a finely-ground inert binder polymer), or in the alternative, as "macro-heterogeneous"
membranes by the physical blending of pre-polymerized ion exchange resin and binder.
Present macro-heterogeneous membranes tend to have inferior electrochemical properties as compared to micro-heterogeneous membranes, but they do offer a number of advantages as compared to membranes of the micro-heterogeneous variety. In particular, macro-heterogeneous membranes are easy to manufacture and can be readily chemically modified since, within limits, the binder and resin types and content can be varied without significantly modifying the manufacturing process. Notably, with micro-heterogeneous membranes, the binder must be compatible with the pre-cursor ion exchange monomers such that the binder does not interfere with the polymerization of the ion exchange monomer or, as a consequence of such polymerization, becomes chemically altered with undesirable properties.
In some plate-and-frame type unit operations, ion exchange membranes are typically interposed between adj acent frame members to assist in defining individual chambers or compartments. For example, in filter-press type electrodeionization units, ion exchange membranes are interposed between adjacent frame members or spacers to form separate diluting and concentrating chambers. In assembling such units, a plurality of frame members are provided in a parallel manner with ion exchange membranes interposed between the frame members. The resulting structure is then forced together by clamping means with a view to providing a closed, tightly sealed unit. Tears and pinholes also contribute to poor deionization performance.
Unfortunately, present ion exchange membrane materials do not possess entirely adequate sealing characteristics. During prolonged operation of the afore-mentioned unit operations, ion exchange membrane materials have a tendency to creep, thereby receding from contact with adjacent frame members and potentially compromising positive sealing of the unit. Present ion exchange membranes also tend to be brittle and prone to tearing or pinhole formation, thereby further potentially compromising the sealing of the unit.
In addition, present ion exchange materials are not particularly suitable for high temperature applications. As a result, unit operations having ion exchange membranes are unlikely candidates for pharmaceutical applications, where the constituent membranes would be exposed to high temperatures during cleaning for purposes of disinfection.
With respect to membrane manufacturing, the prior methods used to make heterogeneous ion exchange membranes typically involved standard equipment for sheet extrusion. This equipment is very common. However, extruding filled materials like heterogeneous ion exchange membranes involves special difficulties. Gauge control, gear pump pressure limits and uniformity of dispersion of the phases axe all special difficulties encountered when extruding the materials in question. Yield rates as low as 30% are common.
Summary of Invention A heterogeneous ion exchange material is provided comprising an ion exchange resin incorporated within a binder, the binder comprising a material selected from the group consisting of (i) a Metallocene catalyzed linear low density polyethylene, (ii) a very low density polyethylene or ultra low density polyethylene processed using either Ziegler-Natta catalysts or Metallocene catalysts, (iii) a thermoplastic elastomeric olefin comprising a polypropylene continuous phase with an ethylene-propylene-dime monomer or ethylene-propylene rubber rubbery phase dispersed through the polypropylene continuous phase, and (iv) a thermoplastic vulcanizate comprising a polypropylene continuous phase with an ethylene-propylene-dime monomer, ethylene-propylene rubber, nitrile-butadiene rubber, natural rubber, ethylene vinyl acetate rubbery phase dispersed through the polypropylene continuous phase, a co-polymer of vinylidene fluoride and hexafluoropropylene, or a co-polymer of vinylidene fluoride and hexafluoropropylene and tetrafluoroethylene.
In one aspect, the binder is a Metallocene catalyzed linear low density polyethylene.
In another aspect, the binder is a very low density polyethylene or ultra low density polyethylene processed using either Ziegler-Natta catalysts or Metallocene catalysts.
In a further aspect, the binder is a thermoplastic elastomeric olefin comprising a 1 S polypropylene continuous phase with an ethylene-propylene-dime monomer or ethylene propylene rubber rubbery phase dispersed through the polypropylene continuous phase.
In yet a further aspect, the binder is a thermoplastic vulcanizate comprising a polypropylene continuous phase with an ethylene-propylene-dime monomer, ethylene-propylene rubber, nitrite-butadiene rubber, natural rubber or ethylene vinyl acetate rubbery phase dispersed through the polypropylene continuous phase.
A method for manufacturing an ion exchange membrane is also provided using advanced extrusion techniques, including computer-controlled material feed, computer-controlled automatic die thickness adjustment with independently adjustable lip segments and nuclear gauge detection with feed-back control. In one aspect, the method comprises the steps of: (i) extruding polymeric material through an auto-die, having a first lip block with a plurality of segments and a second lip block, at least one of the first lip block segments spaced from said second lip block, the at least one of the first lip block segments disposed at a first position, (ii) measuring a first thickness of the extruded polymeric material with a sensor, (iii) providing an input signal corresponding to the first thickness to a central processing unit (CPU), processing the input signal in said CPU by comparing said input signal to a setpoint corresponding to a desired thickness, (iv) providing an output signal, and (v) moving the at least one first lip block segment to a second position in response to said output signal to change the spacing between the at least one first lip block segment and the second lip block.
A method for manufacturing an ion exchange membrane is also provided by injection molding.
Brief Description of Drawings The present invention will be better understood with reference to the appended drawings in which:
Figure 1 is an illustration of an auto-die;
Figure 2 is a schematic of a method of manufacturing an ion exchange membrane.
Detailed Description of the Invention The composite membrane of the present invention may be employed in various applications, including but not limited to, polarity-based chemical separations, such as electrodeionization and electrodialysis, electrolysis, fuel cells and batteries, pervaporation, gas separation, dialysis separation and industrial electrochemistry, such as chloralkali production and other electrochemical applications.
Heterogeneous ion exchange membranes are provided comprising typical ground ion exchange resin such as Rohm and Haas AMBERLITET"~ IR120 and AMBERLITET"~ IRA
bound by a polymeric binder selected from: (i) a Metallocene-catalyzed linear low density polyethylene (M-LLDDE), (ii) a very low density polyethylene (VLDPE) or ultra low density polyethylene (ULDPE) processed using either Ziegler-Natta catalysts or Metallocene catalysts, (iii) a thermoplastic elastomeric olefin comprising a polypropylene continuous phase with an ethylene-propylene-dime monomer (EPDM) or ethylene-propylene rubber (EPR) rubbery phase dispersed through the polypropylene continuous phase, and (iv) a thermoplastic vulcanizate comprising a polypropylene continuous phase with an EPDM, EBR, nitrite-butadiene rubber (NBR), natural rubber (NR), ethylene vinyl acetate (EVA) rubbery phase dispersed through the polypropylene continuous phase, a co-polymer of vinylidene fluoride and hexafluoropropylene, or a co-polymer of vinylidene fluoride and hexafluoropropylene and tetrafluoroethylene. The M-LLDPE can be an ethylene alpha olefin copolymerized using Metallocene catalysts or ' ~ 8 882 788 ...
, , ~___.....
r constrained geometry catalysts such as YNST1'E'~'u. The thermoplastic vulcanizate can be AES
r SANTOPRBNEz'M or DSM S.ARLIN1~TM, ox AES TREFSIrT~. ' in one embodiment, the thcrmop fastic based elastvmer is sn alloy comprising M-LLDPE
and any of polypropylene (PP), low density polygthylene (LDPE), high density polyethylene (1-1DPE), EDPM (cross-linked, partially icmss-linked, or non-cross-linked), EPR (cross-linked, partially cross-linked, or non-cross-linked), EVA or other synthetic robbers such as a co-polymer of vinylidene fluoride and hexafluoropropyle'ne or a co polynner of vinylidene fluoride and ! .
htxafluvropmpylcnc and tetrafluvrvethylenc. .
In another embodiment, the thermoplastic based elastomer is an alloy of VLDPE
or . .. _.
' !
ULDPE and any ofPP, LDPE, I;IDPE, M LLDPE, EPDM, (cross-linked, partially cross-naked, or non~ross-linked), EPR (cross-linked, partially cross-linked, or non-cross-Iink~) or EVA. ' In another embodiment, the thermoplastic based elastomer is an alloy of (r) a ~ .
thcrmopiastic elastomeric olefin comprising a polypropylene continuous phase with an EPDM
r or EPR rubbery phase dispersed through the polypropylene continuous phase, and ('u) any of LDPE, I~PE, M-LLDPE, or linear low(density polyethylene (LLDPE)_ .
In another embodiment, the . thermoplastic based elagtor~aer is an alloy of (r) a ' thermoplastic vulcanizate comprising a poiypmpylene continuous phase with an EPDM EPR, NBlt, NR or EVA robbery phase dispersed through the polypropylene continuous phase, and ('u) anyof LDPE,.HDPE, M-LLDPE, or lin ~ar low density polyethyleuo (LLDPE). ' The heterogen~us ion exchange membrane ofthe present invention can be manufacttued with advanced extrusion technology including computer controlled material ~eed, computer cornrolled automatic die thiclmcss adjustment with independently adjustable lip segments. and nuclear gauge detection with feed back control. Alternatively, the heterogeneous ion exchange . . E
membrane of the present invention can be mauerfactured using iqjection molding.
' Referring to Figures l arid 2, ~in done embodiment, the ion exchange membrane of the present invention is manufsctuted by advanced sheet extrusion technology to manufacture . . exchange membranes. The inventive process involves the use of 'very accurate nuclear gauge measuring instruments feeding back to a;control computer that automatically adjusts an "auta dic" 10 (see Figure 1). This auto-die has a first lip block 12 and a second lip block 14. The second lip block 14 is split into many individually adjustable segments or zones I6 for precise AMENDED ~SHE~T
C..n~...,s.....~i ~9 A.~s ~0~~,A
gauge control. Other extruder parameters and gear pump parameters can also be automatically adjusted.
Membrane ingredients, including the polymeric binder and the ion exchange resin, are fed by an extruder 8 into the auto-die 10 through gate slot 18 in the direction indicated by arrow 11. After exiting the autodie 10, the extruded material is fed through calendaring rolls 26a, 26b for flattening and solidifying the extruded sheet and smoothing its surface.
Thickness of the extruded and calendared material is measured by a nuclear gauge sensor 24. At this time, the first lip block 12 is at a first position. The sensor provides an electrical input signal corresponding to the thickness of the extruded and calendared material to a central processing unit (CPU) 22. The CPU 22 compares the input signal with a setpoint corresponding to a desired thickness of the extruded and calendared material. The CPU 22 then provides an output signal to one or more of the zones 16 of the second lip block 14 of the auto-die 10.
In response to this output signal, the zones 16 are actuated and move relative to the first lip block 12 from a first position to a second position in the direction indicated by arrows 20, thereby adjusting the spacing between the zone or zones 16 and the first lip block 12 and achieving the desired spacing A second embodiment of the invention involves the injection molding of ion exchange membranes. This reduces the production cost and further ensures dimensional consistency and adequate phase dispersion. Injection molding eases the processing of beneficial binder materials that may not be ideally suited to extrusion with a filler material such as ion exchange resin particles.
It will be understood, of course, that modification can be made in the embodiments of the invention described herein without departing from the scope and purview of the invention as defined by the appended claims.
AND METHOD OF MANUFACTURING THEREOF
Field of Invention The present invention relates to novel heterogeneous ion exchange membranes, methods for producing such membranes, and apparatus employing such membranes.
Background of the Invention Membranes that selectively allow diffusion and adsorption of ions while excluding certain other ions and non-ionized solutes and solvents, typically referred to as ion exchange membranes, have numerous important industrial applications. Such membranes are used in electrodialysis and electrodeionization equipment as well as in devices for fractionation, transport depletion and electro-regeneration, and purification or treatment of water, food, beverages, chemicals and waste streams. The membranes are also used in electrochemical devices such as caustic/chlorine electrolysis equipment, electropaint purification equipment, and electro-organic synthesis equipment. Additionally, ion exchange membranes are used in electrophoresis devices and analytical equipment as adsorbents, and as suppressor devices for ion chromatography. They are used in chemical treatment and concentration applications via the processes of Donnan dialysis and diffusion dialysis, and they are also used in batteries and fuel cells for the production of electricity.
In each of the applications described above, numerous membrane properties must be balanced against one another in order to achieve a membrane that satisfies the desired objectives of the particular application. Among these, it is an objective to employ ion exchange membranes that have high selectivity, low solvent and non-ionized solute transfer, low diffusion resistance of the ions selected, high physical strength, and good chemical resistance.
Additionally, it is desirable that such membranes be easily manufactured at low cost without the use of hazardous substances. Furthermore, ideal membranes should be easy to handle and process and should also be amenable to low cost assembly techniques during the production of devices containing such membranes.
Current commercially available ion exchange membranes are primarily of two general types: homogeneous membranes and heterogeneous membranes. A homogeneous membrane is one in which the entire volume of the membrane (excluding any support material that may be used to improve strength) is made from the reactive polymer. Examples include membranes made of sulfonated or aminated styrene-divinylbenzene polymers (SDVB
membranes), polymerized perfluorosulfonic acids (PFSO membranes) or various thermoplastics with active groups grafted onto the base polymer.
Unfortunately, homogeneous membranes tend to be difficult to manufacture. They also tend to employ the use of hazardous materials during their manufacturing process since, for the most part, they must be made from base monomers. Additionally, they are difficult to modify chemically because each modification requires a change in the fundamental chemistry of the membrane.
Homogeneous membranes also tend to have limited physical strength (therefore often requiring a screen or cloth support) because the polymer produced cannot readily combine both the required physical and electrochemical properties to operate efficiently in a fabricated device.
Homogeneous membranes may be either crosslinked (to provide the membrane with dimensional stability, but increased brittleness and sensitivity upon drying), or they may be non-crosslinked (to provide membranes which may be dried, but lack dimensional stability and resistance to swelling and various solvents).
In contrast, heterogeneous membranes are formed of 1) a composite containing an ion exchange resin to impart electrochemical properties and 2) a binder to impart physical strength and integrity. Heterogeneous membrane may also include inert support material to impart extra strength and stability. Typical heterogeneous membranes may be produced as "micro-heterogeneous" membranes by the paste method (in which ion exchange resin monomers are reacted to form the ultimate ion exchange resin polymer in the presence of a finely-ground inert binder polymer), or in the alternative, as "macro-heterogeneous"
membranes by the physical blending of pre-polymerized ion exchange resin and binder.
Present macro-heterogeneous membranes tend to have inferior electrochemical properties as compared to micro-heterogeneous membranes, but they do offer a number of advantages as compared to membranes of the micro-heterogeneous variety. In particular, macro-heterogeneous membranes are easy to manufacture and can be readily chemically modified since, within limits, the binder and resin types and content can be varied without significantly modifying the manufacturing process. Notably, with micro-heterogeneous membranes, the binder must be compatible with the pre-cursor ion exchange monomers such that the binder does not interfere with the polymerization of the ion exchange monomer or, as a consequence of such polymerization, becomes chemically altered with undesirable properties.
In some plate-and-frame type unit operations, ion exchange membranes are typically interposed between adj acent frame members to assist in defining individual chambers or compartments. For example, in filter-press type electrodeionization units, ion exchange membranes are interposed between adjacent frame members or spacers to form separate diluting and concentrating chambers. In assembling such units, a plurality of frame members are provided in a parallel manner with ion exchange membranes interposed between the frame members. The resulting structure is then forced together by clamping means with a view to providing a closed, tightly sealed unit. Tears and pinholes also contribute to poor deionization performance.
Unfortunately, present ion exchange membrane materials do not possess entirely adequate sealing characteristics. During prolonged operation of the afore-mentioned unit operations, ion exchange membrane materials have a tendency to creep, thereby receding from contact with adjacent frame members and potentially compromising positive sealing of the unit. Present ion exchange membranes also tend to be brittle and prone to tearing or pinhole formation, thereby further potentially compromising the sealing of the unit.
In addition, present ion exchange materials are not particularly suitable for high temperature applications. As a result, unit operations having ion exchange membranes are unlikely candidates for pharmaceutical applications, where the constituent membranes would be exposed to high temperatures during cleaning for purposes of disinfection.
With respect to membrane manufacturing, the prior methods used to make heterogeneous ion exchange membranes typically involved standard equipment for sheet extrusion. This equipment is very common. However, extruding filled materials like heterogeneous ion exchange membranes involves special difficulties. Gauge control, gear pump pressure limits and uniformity of dispersion of the phases axe all special difficulties encountered when extruding the materials in question. Yield rates as low as 30% are common.
Summary of Invention A heterogeneous ion exchange material is provided comprising an ion exchange resin incorporated within a binder, the binder comprising a material selected from the group consisting of (i) a Metallocene catalyzed linear low density polyethylene, (ii) a very low density polyethylene or ultra low density polyethylene processed using either Ziegler-Natta catalysts or Metallocene catalysts, (iii) a thermoplastic elastomeric olefin comprising a polypropylene continuous phase with an ethylene-propylene-dime monomer or ethylene-propylene rubber rubbery phase dispersed through the polypropylene continuous phase, and (iv) a thermoplastic vulcanizate comprising a polypropylene continuous phase with an ethylene-propylene-dime monomer, ethylene-propylene rubber, nitrile-butadiene rubber, natural rubber, ethylene vinyl acetate rubbery phase dispersed through the polypropylene continuous phase, a co-polymer of vinylidene fluoride and hexafluoropropylene, or a co-polymer of vinylidene fluoride and hexafluoropropylene and tetrafluoroethylene.
In one aspect, the binder is a Metallocene catalyzed linear low density polyethylene.
In another aspect, the binder is a very low density polyethylene or ultra low density polyethylene processed using either Ziegler-Natta catalysts or Metallocene catalysts.
In a further aspect, the binder is a thermoplastic elastomeric olefin comprising a 1 S polypropylene continuous phase with an ethylene-propylene-dime monomer or ethylene propylene rubber rubbery phase dispersed through the polypropylene continuous phase.
In yet a further aspect, the binder is a thermoplastic vulcanizate comprising a polypropylene continuous phase with an ethylene-propylene-dime monomer, ethylene-propylene rubber, nitrite-butadiene rubber, natural rubber or ethylene vinyl acetate rubbery phase dispersed through the polypropylene continuous phase.
A method for manufacturing an ion exchange membrane is also provided using advanced extrusion techniques, including computer-controlled material feed, computer-controlled automatic die thickness adjustment with independently adjustable lip segments and nuclear gauge detection with feed-back control. In one aspect, the method comprises the steps of: (i) extruding polymeric material through an auto-die, having a first lip block with a plurality of segments and a second lip block, at least one of the first lip block segments spaced from said second lip block, the at least one of the first lip block segments disposed at a first position, (ii) measuring a first thickness of the extruded polymeric material with a sensor, (iii) providing an input signal corresponding to the first thickness to a central processing unit (CPU), processing the input signal in said CPU by comparing said input signal to a setpoint corresponding to a desired thickness, (iv) providing an output signal, and (v) moving the at least one first lip block segment to a second position in response to said output signal to change the spacing between the at least one first lip block segment and the second lip block.
A method for manufacturing an ion exchange membrane is also provided by injection molding.
Brief Description of Drawings The present invention will be better understood with reference to the appended drawings in which:
Figure 1 is an illustration of an auto-die;
Figure 2 is a schematic of a method of manufacturing an ion exchange membrane.
Detailed Description of the Invention The composite membrane of the present invention may be employed in various applications, including but not limited to, polarity-based chemical separations, such as electrodeionization and electrodialysis, electrolysis, fuel cells and batteries, pervaporation, gas separation, dialysis separation and industrial electrochemistry, such as chloralkali production and other electrochemical applications.
Heterogeneous ion exchange membranes are provided comprising typical ground ion exchange resin such as Rohm and Haas AMBERLITET"~ IR120 and AMBERLITET"~ IRA
bound by a polymeric binder selected from: (i) a Metallocene-catalyzed linear low density polyethylene (M-LLDDE), (ii) a very low density polyethylene (VLDPE) or ultra low density polyethylene (ULDPE) processed using either Ziegler-Natta catalysts or Metallocene catalysts, (iii) a thermoplastic elastomeric olefin comprising a polypropylene continuous phase with an ethylene-propylene-dime monomer (EPDM) or ethylene-propylene rubber (EPR) rubbery phase dispersed through the polypropylene continuous phase, and (iv) a thermoplastic vulcanizate comprising a polypropylene continuous phase with an EPDM, EBR, nitrite-butadiene rubber (NBR), natural rubber (NR), ethylene vinyl acetate (EVA) rubbery phase dispersed through the polypropylene continuous phase, a co-polymer of vinylidene fluoride and hexafluoropropylene, or a co-polymer of vinylidene fluoride and hexafluoropropylene and tetrafluoroethylene. The M-LLDPE can be an ethylene alpha olefin copolymerized using Metallocene catalysts or ' ~ 8 882 788 ...
, , ~___.....
r constrained geometry catalysts such as YNST1'E'~'u. The thermoplastic vulcanizate can be AES
r SANTOPRBNEz'M or DSM S.ARLIN1~TM, ox AES TREFSIrT~. ' in one embodiment, the thcrmop fastic based elastvmer is sn alloy comprising M-LLDPE
and any of polypropylene (PP), low density polygthylene (LDPE), high density polyethylene (1-1DPE), EDPM (cross-linked, partially icmss-linked, or non-cross-linked), EPR (cross-linked, partially cross-linked, or non-cross-linked), EVA or other synthetic robbers such as a co-polymer of vinylidene fluoride and hexafluoropropyle'ne or a co polynner of vinylidene fluoride and ! .
htxafluvropmpylcnc and tetrafluvrvethylenc. .
In another embodiment, the thermoplastic based elastomer is an alloy of VLDPE
or . .. _.
' !
ULDPE and any ofPP, LDPE, I;IDPE, M LLDPE, EPDM, (cross-linked, partially cross-naked, or non~ross-linked), EPR (cross-linked, partially cross-linked, or non-cross-Iink~) or EVA. ' In another embodiment, the thermoplastic based elastomer is an alloy of (r) a ~ .
thcrmopiastic elastomeric olefin comprising a polypropylene continuous phase with an EPDM
r or EPR rubbery phase dispersed through the polypropylene continuous phase, and ('u) any of LDPE, I~PE, M-LLDPE, or linear low(density polyethylene (LLDPE)_ .
In another embodiment, the . thermoplastic based elagtor~aer is an alloy of (r) a ' thermoplastic vulcanizate comprising a poiypmpylene continuous phase with an EPDM EPR, NBlt, NR or EVA robbery phase dispersed through the polypropylene continuous phase, and ('u) anyof LDPE,.HDPE, M-LLDPE, or lin ~ar low density polyethyleuo (LLDPE). ' The heterogen~us ion exchange membrane ofthe present invention can be manufacttued with advanced extrusion technology including computer controlled material ~eed, computer cornrolled automatic die thiclmcss adjustment with independently adjustable lip segments. and nuclear gauge detection with feed back control. Alternatively, the heterogeneous ion exchange . . E
membrane of the present invention can be mauerfactured using iqjection molding.
' Referring to Figures l arid 2, ~in done embodiment, the ion exchange membrane of the present invention is manufsctuted by advanced sheet extrusion technology to manufacture . . exchange membranes. The inventive process involves the use of 'very accurate nuclear gauge measuring instruments feeding back to a;control computer that automatically adjusts an "auta dic" 10 (see Figure 1). This auto-die has a first lip block 12 and a second lip block 14. The second lip block 14 is split into many individually adjustable segments or zones I6 for precise AMENDED ~SHE~T
C..n~...,s.....~i ~9 A.~s ~0~~,A
gauge control. Other extruder parameters and gear pump parameters can also be automatically adjusted.
Membrane ingredients, including the polymeric binder and the ion exchange resin, are fed by an extruder 8 into the auto-die 10 through gate slot 18 in the direction indicated by arrow 11. After exiting the autodie 10, the extruded material is fed through calendaring rolls 26a, 26b for flattening and solidifying the extruded sheet and smoothing its surface.
Thickness of the extruded and calendared material is measured by a nuclear gauge sensor 24. At this time, the first lip block 12 is at a first position. The sensor provides an electrical input signal corresponding to the thickness of the extruded and calendared material to a central processing unit (CPU) 22. The CPU 22 compares the input signal with a setpoint corresponding to a desired thickness of the extruded and calendared material. The CPU 22 then provides an output signal to one or more of the zones 16 of the second lip block 14 of the auto-die 10.
In response to this output signal, the zones 16 are actuated and move relative to the first lip block 12 from a first position to a second position in the direction indicated by arrows 20, thereby adjusting the spacing between the zone or zones 16 and the first lip block 12 and achieving the desired spacing A second embodiment of the invention involves the injection molding of ion exchange membranes. This reduces the production cost and further ensures dimensional consistency and adequate phase dispersion. Injection molding eases the processing of beneficial binder materials that may not be ideally suited to extrusion with a filler material such as ion exchange resin particles.
It will be understood, of course, that modification can be made in the embodiments of the invention described herein without departing from the scope and purview of the invention as defined by the appended claims.
Claims
8. A method for manufacturing an ion exchange membrane using injection molding wherein the ion exchange resin membrane comprises an ion exchange resin incorporated within a binder, the binder comprising a material selected from the group consisting of (i) Metallocene catalyzed linear low deputy polyethylene, (ii) a very low density polyethylene or ultra low density polyethylene processed using either Ziegler-Natta catalysts or Metallocene catalysts, (iii) a thermoplastic elastomeric olefin comprising a polypropylene continuous phase with an ethylene-propylene-diene monomer or ethylene-propylene rubber rubbery phase dispersed through the polypropylene continuous phase, and (iv) a thermoplastic vulcanizate comprising a polypropylene continuous phase with an ethylene-propylene-diene monomer, ethylene-propylene rubber, nitrile-butadiene rubber, natural rubber, ethylene vinyl acetate rubber phase dispersed through the polypropylene continuous phase, a co-polymer of vinylidene fluoride and hexafluoropropylene, or a co-polymer of vinylidene fluoride and hexafluoropropylene and tetrafluoroethylene.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002385346A CA2385346A1 (en) | 1999-06-21 | 2000-06-21 | Heterogeneous ion exchange membrane and method of manufacturing thereof |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA2275999 | 1999-06-21 | ||
| CA2,275,999 | 1999-06-21 | ||
| CA002385346A CA2385346A1 (en) | 1999-06-21 | 2000-06-21 | Heterogeneous ion exchange membrane and method of manufacturing thereof |
| PCT/CA2000/000741 WO2000078849A1 (en) | 1999-06-21 | 2000-06-21 | Heterogeneous ion exchange membrane and method of manufacturing thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2385346A1 true CA2385346A1 (en) | 2000-12-28 |
Family
ID=25681019
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002385346A Abandoned CA2385346A1 (en) | 1999-06-21 | 2000-06-21 | Heterogeneous ion exchange membrane and method of manufacturing thereof |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA2385346A1 (en) |
-
2000
- 2000-06-21 CA CA002385346A patent/CA2385346A1/en not_active Abandoned
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| FZDE | Discontinued |