WO2005052040A1

WO2005052040A1 - Polymer electrolyte membranes crosslinked by nitrile trimerization

Info

Publication number: WO2005052040A1
Application number: PCT/US2004/033808
Authority: WO
Inventors: Michael A. Yandrasits; Steven J. Hamrock; Werner M. A. Grootaert; Miguel A. Guerra; Naiyong Jing
Original assignee: 3M Innovative Properties Company
Priority date: 2003-11-13
Filing date: 2004-10-13
Publication date: 2005-06-09
Also published as: US7074841B2; JP2007513219A; US20060205829A1; US7435498B2; KR20060107779A; EP1694751A1; CN1882642A; CA2545173A1; US20050107489A1; TW200524961A

Abstract

A method is provided for making a crosslinked polymer electrolyte, typically in the form of a membrane for use as a polymer electrolyte membrane in an electrolytic cell such as a fuel cell, by trimerization of nitrile groups contained on groups pendant from the polymer. The resulting polymer electrolyte membrane comprises a highly fluorinated polymer comprising: a perfluorinated backbone, first pendent groups which comprise sulfonic acid groups, and crosslinks comprising trivalent groups according to the formula I The first pendent groups are typically according to the formula: -R1-SO3H, where R1 is a branched or unbranched perfluoroalkyl or perfluoroether group comprising 1-15 carbon atoms and 0-4 oxygen atoms, most typically -O-CF2-CF2-CF2-CF2-SO3H or O-CF2-CF(CF3)-O-CF2-CF2 SO3H.

Description

Polymer Electrolyte Membranes Crosslinked by Nitrile Trimerization

Field of the Invention This invention relates to a method of making a crosslinked polymer electrolyte, typically in the form of a membrane for use as a polymer electrolyte membrane in an electrolytic cell such as a fuel cell, by trimerization of nitrile groups contained on groups pendant from the polymer.

Background of the Invention International Patent Application Publication No. WO 02/50142 Al purportedly discloses fluorosulphonated nitrile crosslinkable elastomers based on vinylidene fluoride with low Tg. U.S. Patent No. 5,260,351 purportedly discloses perfluoroelastomers cured by radiation in the absence of curing agents. The reference purportedly relates to curing of fully fluorinated polymers, such as those prepared from tetrafluoroethylene, a perfluoralkyl perfluorovinyl ether, and cure site or crosslinking units providing at least one of nitrile, perfluorophenyl, bromine or iodine in the resulting terpolymer. U.S. Patent No. 5,527,861 purportedly discloses nitrile containing perfluoroelastomers cured by a combination of a peroxide, a coagent, and a catalyst which causes crosslinks to form using the nitrile groups. U.S. Patent Nos. 4,334,082, 4,414,159, 4,440,917, and 4,454,247 purportedly disclose an ion exchange membrane for use in a chlor-alkali electrolysis cell formed from a copolymer of a vinyl ether monomer of the formula: Y₂CFO(CF(CF3)CF₂O)_nCF=CF2 where Y is selected from the group consisting of CF2CN, CF2CO2R, CF2CO2H, CF2CO2M, CF2CONH2 and CF2CONR; a perfluorinated comonomer selected from tetrafluoroethylene, hexafluoropropylene, and perfluoroalkylvinyl ether; and CF₂=CF(OCF2CF(CF3))_nOCF CF2SO2F where n is 1 or 2. (4,454,247 at claim 1). These references purportedly disclose a method of curing fluoroelastomers by trimerization of nitriles to form triazine rings. (4,454,247 at col. 10, Ins. 60-68).

Summary of the Invention Briefly, the present invention provides a polymer electrolyte membrane comprising a highly fluorinated polymer comprising: a perfluorinated backbone, first pendent groups which comprise sulfonic acid groups, and crosslinks comprising rivalent groups according to the formula:

[lie first pendent groups are typically according to the formula: -RI-SO3H, where R! s a branched or unbranched perfluoroalkyl or perfluoroether group comprising 1-15 ;arbon atoms and 0-4 oxygen atoms, most typically -O-CF2-CF2-CF2-CF2-SO3H or

O-CF₂-CF(CF₃)-O-CF2-CF₂-SO₃H. In another aspect, the present invention provides a method of making a polymer jlectrolyte membrane comprising the steps of: a) providing a highly fluorinated )θlymer comprising: a perfluorinated backbone, first pendent groups which comprise lfonyl halide groups, and second pendent groups which comprise nitrile groups; b) rming the fluoropolymer into a membrane; c) forming crosslinks by trimerization of he nitrile groups; and d) converting the sulfonyl halide groups to sulfonic acid groups.

[Tie second pendent groups are typically according to the formula: -CsN or -R *-G≡N, vhere R* 1 is a branched or unbranched perfluoroalkyl or perfluoroether group ;omprising 1-15 carbon atoms and 0-4 oxygen atoms. The first pendent groups ypically according to the formula: -RI-SO2X, where X is a halogen and where R! is a >ranched or unbranched perfluoroalkyl or perfluoroether group comprising 1-15 carbon itoms and 0-4 oxygen atoms, most typically -O-CF2-CF2-CF2-CF2-SO2X or -O-CF₂- F(CF₃)-O-CF₂-CF₂-SO₂X. In another aspect, the present invention provides crosslinked polymers made according to any of the methods of the present invention. In this application: "equivalent weight" (EW) of a polymer means the weight of polymer which will neutralize one equivalent of base; "hydration product" (HP) of a polymer means the number of equivalentsmoles) of water absorbed by a membrane per equivalent of sulfonic acid groups present in the membrane multiplied by the equivalent weight of the polymer; and "highly fluorinated" means containing fluorine in an amount of 40 wt% or more, ypically 50 wt% or more and more typically 60 wt% or more.

Detailed Description The present invention provides a crosslinked polymer electrolyte membrane, rhe membrane is derived from a polymer comprising: a highly fluorinated backbone, ϊrst pendent groups which include a group according to the formula -SO2X, where X is

1 halogen and second pendent groups which include a nitrile group (-C≤N) which may )e trimerized to form crosslinks comprising trivalent groups according to the formula:

such crosslinked polymer electrolyte membranes (PEM's) may be used in electrolytic ;ells such as fuel cells. PEM's manufactured from the crosslinked polymer according to the present nvention may be used in the fabrication of membrane electrode assemblies (MEA's) or use in fuel cells. An ME A is the central element of a proton exchange membrane uel cell, such as a hydrogen fuel cell. Fuel cells are electrochemical cells which nroduce usable electricity by the catalyzed combination of a fuel such as hydrogen and in oxidant such as oxygen. Typical MEA's comprise a polymer electrolyte membrane PEM) (also known as an ion conductive membrane (ICM)), which functions as a solid slectrolyte. One face of the PEM is in contact with an anode electrode layer and the pposite face is in contact with a cathode electrode layer. Each electrode layer includes lectrochemical catalysts, typically including platinum metal. Gas diffusion layers 3DL's) facilitate gas transport to and from the anode and cathode electrode materials nd conduct electrical current. The GDL may also be called a fluid transport layer FTL) or a diffuser/current collector (DCC). The anode and cathode electrode layers lay be applied to GDL's in the form of a catalyst ink, and the resulting coated GDL's andwiched with a PEM to form a five-layer MEA. Alternately, the anode and cathode lectrode layers maybe applied to opposite sides of the PEM in the form of a catalyst tik, and the resulting catalyst-coated membrane (CCM) sandwiched with two GDL's to brm a five-layer MEA. The five layers of a five-layer MEA are, in order: anode GDL, node electrode layer, PEM, cathode electrode layer, and cathode GDL. In a typical 'EM fuel cell, protons are formed at the anode via hydrogen oxidation and transported tcross the PEM to the cathode to react with oxygen, causing electrical current to flow in tn external circuit connecting the electrodes. The PEM forms a durable, non-porous, ilectrically non-conductive mechanical barrier between the reactant gases, yet it also

>asses H⁺ ions readily. The polymer to be crosslinked comprises a backbone, which may be branched )r unbranched but is typically unbranched. The backbone is highly fluorinated and nore typically perfluorinated. The backbone may comprise units derived from :etrafluoroethylene (TFE), i.e., typically -CF2-CF2- units, and units derived from

:o-monomers, typically including at least one according to the formula CF2=CY-R where Y is typically F but may also be CF3, and where R is a first pendant group which includes a group according to the formula -SO2X which is a sulfonyl halide. X is most typically F. In an alternative embodiment, first side groups R may be added to the backbone by grafting. Typically, first side groups R are highly fluorinated and more typically perfluorinated. R may be aromatic or non-aromatic. Typically, R is

-RI-SO2 , where Rl is a branched or unbranched perfluoroalkyl or perfluoroether group comprising 1-15 carbon atoms and 0-4 oxygen atoms, R! is typically -O-R^- wherein R^ is a branched or unbranched perfluoroalkyl or perfluoroether group comprising 1-15 carbon atoms and 0-4 oxygen atoms. R* is more typically -O-R-3- wherein R^ is a perfluoroalkyl group comprising 1-15 carbon atoms. Examples of R! include: -(CF₂)_n- where n is 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14 or 15 (-CF₂CF(CF₃)-)_n where n is 1, 2, 3, 4, or 5 (-CF(CF₃)CF2-)_n where n is 1, 2, 3, 4, or 5(-CF2CF(CF3)-)_n-CF2- where n is 1, 2, 3 or 4 (-O-CF2CF2-)_n where n is 1, 2, 3, 4, 5, 6 or 7 (-O-CF2CF2CF₂-)_n where n is 1, 2, 3, 4, or 5 (-O-CF2CF2CF₂CF2-)_n where n is 1, 2 or 3 (-O-CF₂CF(CF₃)-)_n where n is 1, 2, 3, 4, or 5 (-O-CF2CF(CF₂CF3)-)_n where n is 1, 2 or 3 (-O-CF(CF₃)CF₂-)_n where n is 1, 2, 3, 4 or 5 (-O-CF(CF2CF3)CF2-)_n where n is 1, 2 or 3 (-O-CF2CF(CF₃)-)_n-O-CF₂CF2- where n is 1, 2, 3 or 4 (-O-CF₂CF(CF2CF3)-)_n-O-CF₂CF2- where n is 1, 2 or 3 (-O-CF(CF3)CF₂-)_n-O-CF₂CF2- where n is 1, 2, 3 or 4 (~O-CF(CF₂CF3)CF2-)_n-O-CF2CF₂- where n is 1, 2 or 3 -O-(CF₂)_n- where n is 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13 or 14 R is typically -O-CF2CF2CF2CF2-SO2X or -O-CF₂-CF(CF₃)-O-CF₂- UF2-SO2X and most typically -O-CF2CF2CF2CF2-SO2X. The -SO2X group is most ypically -SO2F during polymerization, i.e., X is F. The -SO2X group is typically ;onverted to -SO3H at some point prior to use of the fluoropolymer as an polymer slectrolyte. The fluoromonomer providing first side group R may be synthesized by any suitable means, including methods disclosed in U.S. Pat. No. 6,624,328. In addition, the fluoropolymer includes second pendant groups Q containing a CsN group. The second pendant group may be derived from a co-monomer according 0 the formula CF2=CY-Q where Y is typically F but may also be CF3, and where Q is . second pendent group which includes a group according to the formula -C≡N. In an Iternative embodiment, second pendant groups Q may be added to the backbone by [rafting. Typically, second pendant groups Q are highly fluorinated and more typically lerfluorinated, other than at the bromine position. Typically, Q is -R¹ !-C≡N, where i.11 can be any Rl described above but is selected independently from R! . Most typically, the fluoropolymer is a terpolymer of TFE, CF2=CY-R as lescribed above, and CF2=CY-Q as described above. The polymer to be crosslinked may be made by any suitable method, including mulsion polymerization, extrusion polymerization, polymerization in supercritical :arbon dioxide, solution or suspension polymerization, and the like. In one typical jolymerization, CF2=CF-O-CF2CF2CF2CF2-SO2F (MV4S) is preemulsified in water vith an emulsifier (ammonium perfluorooctanoate, C7F15COONH4) under high shear

24,000 rpm). An oxygen-free polymerization kettle equipped with an impeller agitator system is charged with deionized water and heated to 50°C and then the preemulsion is diarged into the polymerization kettle. The kettle is charged with a nitrile-functional nonomer such as

typically in a preemulsion. The kettle is further charged with gaseous tetrafluoroethylene (TFE) to 6-8 bar absolute reaction Dressure. At 50°C and 240 rpm agitator speed polymerization is initiated by addition of sodium disulfite and ammonium peroxodisulfate. During the course of the reaction, the ^•eaction temperature is maintained at 50 °C. Reaction pressure is maintained at 6-8 bar ibsolute by feeding additional TFE into the gas phase. A second portion of MV4S preemulsion may be continuously fed into the liquid phase during the course of the reaction. Additional nitrile-functional monomer may also be continuously fed into the reactor during the course of the reaction. After feeding sufficient TFE, the monomer feed may be interrupted and the continuing polymerization allowed to reduce the pressure of the monomer gas phase. The reactor may then be vented and flushed with nitrogen gas. Typically, the polymer is formed into a membrane prior to crosslinking. Any suitable method of forming the membrane may be used. The polymer is typically cast from a suspension. Any suitable casting method may be used, including bar coating, ipray coating, slit coating, brush coating, and the like. Alternately, the membrane may )e formed from neat polymer in a melt process such as extrusion. After forming, the nembrane may be annealed. Typically the membrane has a thickness of 90 microns or ess, more typically 60 microns or less, and most typically 30 microns or less. A thinner nembrane may provide less resistance to the passage of ions. In fuel cell use, this ^•esults in cooler operation and greater output of usable energy. Thinner membranes nust be made of materials that maintain their structural integrity in use. In one typical )rocess, membranes are cast by knife coating out of a water suspension containing 20% solids onto a glass plate and dried at 80 °C for 10 minutes to form films having a hickness of approximately 30 microns. The step of crosslinking (nitrile trimerization) may be accomplished by any suitable method. Typically, crosslinking is accomplished by application of heat, ypically to a temperature of 160 °C or more, in the presence of suitable initiators or catalysts. Suitable initiators or catalysts may include ammonia, ammonium compounds, including salts of ammonium and salts of quaternary ammonium compounds, including cyclic compounds such as salts of l,8-diazabicyclo[5.4.0]undec- 7-ene (DBU), including salts of fluorinated carboxylates, Lewis acids, and the like. The step of crosslinking the polymer may occur in whole or part during annealing of the membrane or may be carried out separate from any annealing step. During the crosslinking step, nitrile groups trimerize to form linkages comprising triazine groups, i.e., trivalent groups according to the formula:

LΛΛKΛ ( π ). After crosslinking, the sulfur-containing functions of the first pendant groups may be converted to sulfonic acid form by any suitable process. Sulfonyl halide groups may be converted by hydrolysis. In one typical process, the polymer is immersed in an aqueous solution of a strong base and subsequently acidified. In one typical embodiment, a polymer membrane is immersed in 15% KOH in water at 80 °C for 1 hour, then washed twice in 20% nitric acid at 80 °C, then boiled in deionized water twice. The acid-functional pendent groups typically are present in an amount sufficient 3 result in an hydration product (HP) of greater than 15,000, more typically greater an 18,000, more typically greater than 22,000, and most typically greater than 25,000. n general, higher HP correlates with higher ionic conductance. The acid-functional pendent groups typically are present in an amount sufficient 3 result in an equivalent weight (EW) of less than 1200, more typically less than 1100, nd more typically less than 1000, and more typically less than 900. In a further embodiment, the polymer may be imbibed into a porous supporting tiatrix prior to crosslinking, typically in the form of a thin membrane having a hickness of 90 microns or less, more typically 60 microns or less, and most typically 30 microns or less. Any suitable method of imbibing the polymer into the pores of the lUpporting matrix may be used, including overpressure, vacuum, wicking, immersion, md the like. The blend becomes embedded in the matrix upon crosslinking. Any suitable supporting matrix may be used. Typically the supporting matrix is electrically ion-conductive. Typically, the supporting matrix is composed of a fluoropolymer, vhich is more typically perfluorinated. Typical matrices include porous )olytetrafluoroethylene (PTFE), such as biaxially stretched PTFE webs. It will be understood that polymers and membranes made according to the nethod of the present invention may differ in chemical structure from those made by 3ther methods, in the structure of crosslinks, the placement of crosslinks, the placement 3f acid-functional groups, the presence or absence of crosslinks on pendent groups or of icid-functional groups on crosslinks, and the like. This invention is useful in the manufacture of strengthened polymer electrolyte membranes for use in electrolytic cells such as fuel cells. Various modifications and alterations of this invention will become apparent to those skilled in the art without departing from the scope and principles of this invention, and it should be understood that this invention is not to be unduly limited to the illustrative embodiments set forth hereinabove.

Claims

e claim:

A polymer electrolyte membrane comprising a highly fluorinated polymer omprising: a perfluorinated backbone, first pendent groups which comprise sulfonic cid groups, and crosslinks comprising trivalent groups according to the formula:

The polymer electrolyte membrane according to claim 1 wherein said first endent groups are according to the formula: -RI-SO3H, where R* is a branched or nbranched perfluoroalkyl or perfluoroether group comprising 1-15 carbon atoms and '-4 oxygen atoms.

A method of making a polymer electrolyte membrane comprising the steps of: a) providing a highly fluorinated polymer comprising: a perfluorinated backbone, first pendent groups which comprise sulfonyl halide groups, and second pendent groups which comprise nitrile groups; b) forming said fluoropolymer into a membrane; c) trimerizing said nitrile groups to form crosslinks; and d) converting said sulfonyl halide groups to sulfonic acid groups. The method according to claim 3 wherein said second pendent groups are elected from -C≡N and groups according to the formula: -R^-C≡N, where R! is a (ranched or unbranched perfluoroalkyl or perfluoroether group comprising 1-15 carbon itoms and 0-4 oxygen atoms.

>. The method according to claim 3 or 4 wherein said first pendent groups are iccording to the formula: -RI-SO2X, where X is a halogen and where R! is a

>ranched or unbranched perfluoroalkyl or perfluoroether group comprising 1-15 carbon itoms and 0-4 oxygen atoms. A polymer electrolyte membrane made according to the method of any of claims 3 - 5.

A polymer membrane comprising a highly fluorinated polymer comprising: a erfluorinated backbone, first pendent groups which comprise groups according to the

)rmula -SO2X, where X is F, Cl, Br, OH, or -O"M⁺, where M⁺ is a monovalent cation, rid crosslinks comprising trivalent groups according to the formula:

The polymer membrane according to claim 7 wherein said first pendent groups re according to the formula: -R^I-SO2X, where Rl is a branched or unbranched erfluoroalkyl or perfluoroether group comprising 1-15 carbon atoms and 0-4 oxygen toms.

A polymer comprising a highly fluorinated polymer comprising: a erfluorinated backbone, first pendent groups which comprise groups according to the

)rmula -SO2X, where X is F, Cl, Br, OH, or -O"M⁺, where M⁺ is a monovalent cation, ad crosslinks comprising trivalent groups according to the formula:

0. The polymer according to claim 9 wherein said first pendent groups are ccording to the formula: -RI-SO2X, where R! is a branched or unbranched erfluoroalkyl or perfluoroether group comprising 1-15 carbon atoms and 0-4 oxygen toms.