US20070099054A1 - Sulfonated-perfluorocyclobutane polyelectrolyte membranes for fuel cells - Google Patents

Sulfonated-perfluorocyclobutane polyelectrolyte membranes for fuel cells Download PDF

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US20070099054A1
US20070099054A1 US11/264,755 US26475505A US2007099054A1 US 20070099054 A1 US20070099054 A1 US 20070099054A1 US 26475505 A US26475505 A US 26475505A US 2007099054 A1 US2007099054 A1 US 2007099054A1
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polymer
sulfonating
oleum
sulfonated
perfluorocyclobutane
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US11/264,755
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Timothy Fuller
Michael Schoeneweiss
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GM Global Technology Operations LLC
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GM Global Technology Operations LLC
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Priority to US11/264,755 priority Critical patent/US20070099054A1/en
Assigned to GM GLOBAL TECHNOLOGY OPERATIONS, INC. reassignment GM GLOBAL TECHNOLOGY OPERATIONS, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: FULLER, TIMOTHY J., SCHOENEWEISS, MICHAEL R.
Priority to JP2006295851A priority patent/JP4416778B2/en
Priority to DE102006051431A priority patent/DE102006051431B4/en
Priority to CN2006101646562A priority patent/CN101016374B/en
Publication of US20070099054A1 publication Critical patent/US20070099054A1/en
Priority to US12/144,392 priority patent/US7960046B2/en
Priority to US13/151,906 priority patent/US20110229797A1/en
Abandoned legal-status Critical Current

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    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90—Selection of catalytic material
    • H01M4/92—Metals of platinum group
    • H01M4/925—Metals of platinum group supported on carriers, e.g. powder carriers
    • H01M4/926—Metals of platinum group supported on carriers, e.g. powder carriers on carbon or graphite
    • 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
    • B01D71/76—Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74
    • B01D71/82—Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74 characterised by the presence of specified groups, e.g. introduced by chemical after-treatment
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    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F214/00—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
    • C08F214/18—Monomers containing fluorine
    • C08F214/182—Monomers containing fluorine not covered by the groups C08F214/20 - C08F214/28
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
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    • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/34—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
    • C08G65/38—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols
    • C08G65/40—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols from phenols (I) and other compounds (II), e.g. OH-Ar-OH + X-Ar-X, where X is halogen atom, i.e. leaving group
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Definitions

  • the present invention relates to electrochemical conversion cells, commonly referred to as fuel cells, which produce electrical energy by processing first and second reactants.
  • electrical energy can be generated in a fuel cell through the reduction (cathode reaction: O 2 +4H + +4e ⁇ ⁇ 2H 2 O) of an oxygen-containing gas and the oxidation (anode reaction: 2H 2 ⁇ 4H + +4e ⁇ ) of a hydrogenous gas.
  • a typical cell comprises a membrane electrode assembly positioned between a pair of flow fields accommodating respective ones of the reactants. More specifically, a cathode flowfield plate and an anode flowfield plate can be positioned on opposite sides of the membrane electrode assembly.
  • the voltage provided by a single cell unit is typically too small for useful automotive power application so it is common to arrange a plurality of cells in a conductively coupled “stack” to increase the electrical output of the electrochemical conversion assembly.
  • the conversion assembly generally comprises a membrane electrode assembly, an anode flowfield, and a cathode flowfield.
  • the membrane electrode assembly in turn comprises a proton exchange membrane separating an anode and cathode.
  • the membrane electrode assembly generally comprises, among other things, a catalyst supported by a high surface area support material and is characterized by enhanced proton conductivity under wet conditions.
  • a catalyst supported by a high surface area support material and is characterized by enhanced proton conductivity under wet conditions.
  • the present invention is directed to particular polyelectrolyte membranes, processes for preparing polyelectrolyte membranes and polyelectrolyte membrane fuel cells.
  • FIGS. 1 and 2 of U.S. Patent Application Pub. No. 2005/0058864, and the accompanying text present a detailed illustration of the components of a fuel cell stack—this particular subject matter is expressly incorporated herein by reference.
  • PEM fuel cells have attracted considerable interest as sources of non-polluting, high-density power for automotive propulsion.
  • PEM fuel cells operate at temperatures up to 95° C. with external humidification being required to maintain proton conductivity that deteriorates rapidly as the membranes dry out.
  • Perfluorosulfonic acid membranes have been the preferred materials for PEM, but they suffer from poor mechanical integrity and they are expensive. Consequently, new alternative PEM materials are continuously being sought.
  • the present invention is directed to a process for preparing a polymer.
  • the process comprises sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer.
  • the sulfonating agent comprises oleum or SO 3 .
  • a process for preparing a proton exchange membrane comprises the steps of: (a) sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer and (b) forming the sulfonated perfluorocyclobutane polymer into a proton exchange membrane.
  • the sulfonating agent comprises oleum or SO 3 .
  • a fuel cell comprises a proton exchange membrane formed by sulfonating a perfluorocyclobutane polymer with oleum to form a sulfonated perfluorocyclobutane polymer and (b) forming the sulfonated perfluorocyclobutane polymer into a proton exchange membrane.
  • the sulfonating agent comprises oleum or SO 3 .
  • a process for assembling a device comprises the act of preparing a membrane electrode assembly.
  • the membrane electrode assembly comprises electrically conductive material on either side of a proton exchange membrane.
  • the proton exchange membrane is prepared according to a process comprising the act of sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer, wherein the sulfonating agent comprises oleum or SO 3 .
  • the device comprises an electrochemical conversion assembly comprising at least one electrochemical conversion cell configured to convert first and second reactants to electrical energy.
  • the electrochemical conversion cell comprises the membrane electrode assembly, an anode flowfield portion and a cathode flowfield portion defined on opposite sides of the membrane electrode assembly.
  • a first reactant supply configured to provide a first reactant to an anode side of the membrane electrode assembly via the anode flowfield portion
  • a second reactant supply configured to provide a second reactant to a cathode side of the membrane electrode assembly via said cathode flowfield portion.
  • FIG. 1 is a graph depicting that the amount of sulfonation is determined by the ratio of oleum to polymer used
  • FIG. 2 is a graph depicting the conductivity vs. % relative humidity of sulfonated perfluorocyclobutane-biphenyl vinyl ether (BPVE) polymers 4 with different Ion Exchange Capacities (I.E.C.s);
  • BPVE perfluorocyclobutane-biphenyl vinyl ether
  • FIG. 3 is a graph depicting conductivity vs. % relative humidity of sulfonated perfluorocyclobutane-hexafluoroisopropylidene biphenyl vinyl ether (BPVE 6F) copolymers, 6 with different I.E.C.s;
  • BPVE 6F perfluorocyclobutane-hexafluoroisopropylidene biphenyl vinyl ether
  • FIG. 4 is a graph depicting water uptakes for various sulfonated perfluorocyclobutane polymers
  • FIG. 5 is a graph depicting volume swell at 25 and 100° C. in water for PFCB Polymers, plotted as semi-log (A) and linear graph (B);
  • FIG. 6 is a graph of fuel cell data of sulfonated BPVE polymers depicting cell voltage (in volts) versus current density (in Amperes/cm 2 ), which has been IR-corrected for the experimentally measured High Frequency Resistance (HFR); and
  • FIG. 7 is a graph of fuel cell data of sulfonated BPVE 6F copolymers depicting cell voltage (in volts) versus current density (in Amperes/cm 2 ), which has been IR-corrected for the experimentally measured High Frequency Resistance (HFR).
  • HFR High Frequency Resistance
  • the inventors have discovered a new process for preparing new proton conducting membranes made with perfluorocyclobutanes polymers (PFCBs) having sulfonic acid groups (SPFCBs,), which may be used in PEM fuel cells that can operate over a broad range of relative humidity and at temperatures around 95° C.
  • PFCBs perfluorocyclobutanes polymers
  • SPFCBs sulfonic acid groups
  • the properties of the SPFCB films are dependent on the chemical structure and the ion exchange capacity of the film, which can be tailored by the reaction conditions used.
  • These SPFCB-films are reasonable alternatives to perfluorosulfonic acid membranes, presently being used in PEM fuel cells, because the sulfonated polymers have high intrinsic proton conductivity and inherent dimensional-, hydrolytic- and high-temperature stability.
  • PFCBs are commercially available from Tetramer Technologies, under license agreements from Dow Chemical. Examples of PFCBs are provided with the structures 1-3: The synthesis of PFCBs is described in U.S. Pat. Nos. 5,037,917 and 5,159,037—this particular subject matter is expressly incorporated herein by reference.
  • Prior art teaches a sulfonation procedure that uses chlorsulfonic acid, which has limited synthesis utility and scope and which produces inconsistent membrane materials.
  • the inventors have discovered a novel process for synthesizing SPFCBs.
  • the process comprises sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer.
  • the sulfonating agent comprises oleum, SO 3 or a combination thereof.
  • PFCBs are available for use in the present process, any of which may be employed herein.
  • the PFCB comprises the formula: wherein X is O or S; R is n is greater than about 20. In one embodiment, n is from about 20 to about 500. Specific examples of such PFCBs include, but are not limited to, structures 1-3, defined in detail above.
  • the oleum comprises 10% oleum. In another embodiment, the oleum comprises 20% oleum. In yet another embodiment, the oleum comprises 30% oleum.
  • various SPFCBs may be formed from reacting a PFCB with a sulfonating agent. In one embodiment, the sulfonated polymers have between 0-2 sulfonic acids per repeat unit.
  • SPFCBs examples include, but are not limited to, structures 4-6: Furthermore, one skilled in the art will appreciate the various experimental parameters in which the process for preparing the sulfonated polymer may be performed, any of which may be employed herein. In one embodiment, the process further comprises the step of dissolving the PFCB polymer in methylene chloride prior to sulfonating the PFCB. In another embodiment, the process is performed from about ⁇ 20° C. to about 200° C.
  • a process for preparing a proton exchange membrane comprises the steps of: (a) sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer and (b) forming the sulfonated perfluorocyclobutane polymer into a proton exchange membrane.
  • the sulfonating agent comprises oleum or SO 3 .
  • a fuel cell comprises a proton exchange membrane formed by sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer and (b) forming the sulfonated perfluorocyclobutane polymer into a proton exchange membrane.
  • the sulfonating agent comprises oleum or SO 3 .
  • SPFCB membranes prepared according to the present invention have markedly improved and consistent fuel cell performance compared with those of the prior art.
  • the SPFCB copolymer has an ion exchange capacity of from about 0.6 to about 2.5 meq/gram. In another embodiment, the SPFCB copolymer has an ion exchange capacity of from about 1.3 to about 2.0 meq/gram.
  • a process for assembling a device comprises the act of preparing a membrane electrode assembly.
  • the membrane electrode assembly comprises electrically conductive material on either side of a proton exchange membrane.
  • the proton exchange membrane is prepared according to a process comprising the act of sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer, wherein the sulfonating agent comprises oleum or SO 3 .
  • the device comprises an electrochemical conversion assembly comprising at least one electrochemical conversion cell configured to convert first and second reactants to electrical energy.
  • the electrochemical conversion cell comprises the membrane electrode assembly, an anode flowfield portion and a cathode flowfield portion defined on opposite sides of the membrane electrode assembly.
  • a first reactant supply configured to provide a first reactant to an anode side of the membrane electrode assembly via the anode flowfield portion
  • a second reactant supply configured to provide a second reactant to a cathode side of the membrane electrode assembly via said cathode flowfield portion.
  • the properties of the SPFCB films are dependent on the chemical structure and the ion exchange capacity of the films, and performance can be tailored by the reaction conditions used.
  • the amount of oleum specified in Table 1 is added to the respective polymer 1, 2 or 3, (ca 1 gram) dissolved in methylene chloride (5 mL) in a screw cap jar. The jar lid is secured and then the jar is shaken vigorously. A purple gel immediately forms, and then the jar is placed on a roll mill for between 0.5 and 1 hour. A clear liquid phase separates, which is decanted off and discarded, and the purple solid is added to vigorously stirred water (250 mL) using a Waring blender.
  • the polymer becomes swollen white crumbs, which are isolated by vacuum filtration, washed with water and then air-dried.
  • the sulfonated polymer (ca 1 g) readily dissolves in tetrahydrofuran (4 mL) and methanol (2 mL).
  • the solution is filtered through an 80—micron polypropylene filter cloth and is cast onto a glass plate (8-inch ⁇ 8 inch) using a six-inch coating applicator bar with an 18-mil coating gap.
  • the coated film is covered with a Pyrex glass dish, and then air-dried (to touch in about 10 minutes).
  • a free-standing film is produced after floating the film off the glass with water. After extensive washing with water and air-drying, a 25-micrometer thick film is obtained.
  • Pieces of the film (ca 0.02 g) are characterized by titration with standardized sodium hydroxide (0.010N) to determine its acid ion exchange capacity (see FIG. 1 ), by measuring proton conductivity versus percent relative humidity (see FIGS.
  • the ion exchange capacity of the sulfonated polymers 4-6 is dependent on the weight (or molar) ratio of the 30%-oleum used per gram of polymer (see FIG. 1 ).
  • the I.E.C. of the respective polymers can be specifically controlled by the amount of oleum added.
  • the sulfonation reaction is quite fast and non-selective towards the different biphenyl ether groups in the PFCB backbone, and reaction times are less than one hour.
  • the polymer 5 can be sulfonated with 30% oleum within 20 minutes under the conditions described, but poor films were obtained with both the starting polymer and the sulfonated polymer due to its low molecular weight. Thus, films of the sulfonated polymer 5 were too brittle to be evaluated.

Abstract

A process for preparing a polymer comprising sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer, wherein the sulfonating agent comprises oleum or SO3 is provided. A process for preparing proton exchange membranes and fuel cells comprising the proton exchange membrane are also provided.

Description

    BACKGROUND OF THE INVENTION
  • The present invention relates to electrochemical conversion cells, commonly referred to as fuel cells, which produce electrical energy by processing first and second reactants. For example, electrical energy can be generated in a fuel cell through the reduction (cathode reaction: O2+4H++4e−→2H2O) of an oxygen-containing gas and the oxidation (anode reaction: 2H2→4H++4e−) of a hydrogenous gas. By way of illustration and not limitation, a typical cell comprises a membrane electrode assembly positioned between a pair of flow fields accommodating respective ones of the reactants. More specifically, a cathode flowfield plate and an anode flowfield plate can be positioned on opposite sides of the membrane electrode assembly. The voltage provided by a single cell unit is typically too small for useful automotive power application so it is common to arrange a plurality of cells in a conductively coupled “stack” to increase the electrical output of the electrochemical conversion assembly.
  • By way of background, the conversion assembly generally comprises a membrane electrode assembly, an anode flowfield, and a cathode flowfield. The membrane electrode assembly in turn comprises a proton exchange membrane separating an anode and cathode. The membrane electrode assembly generally comprises, among other things, a catalyst supported by a high surface area support material and is characterized by enhanced proton conductivity under wet conditions. For the purpose of describing the context of the present invention, it is noted that the general configuration and operation of fuel cells and fuel cell stacks is beyond the scope of the present invention. Rather, the present invention is directed to particular polyelectrolyte membranes, processes for preparing polyelectrolyte membranes and polyelectrolyte membrane fuel cells. Regarding the general configuration and operation of fuel cells and fuel cell stacks, applicants refer to the vast collection of teachings covering the manner in which fuel cell “stacks” and the various components of the stack are configured. For example, a plurality of U.S. patents and published applications relate directly to fuel cell configurations and corresponding methods of operation. More specifically, FIGS. 1 and 2 of U.S. Patent Application Pub. No. 2005/0058864, and the accompanying text, present a detailed illustration of the components of a fuel cell stack—this particular subject matter is expressly incorporated herein by reference.
    • BRIEF SUMMARY OF THE INVENTION
  • Recently, proton exchange or polyelectrolyte membrane (PEM) fuel cells have attracted considerable interest as sources of non-polluting, high-density power for automotive propulsion. However, for widespread commercialization, low cost, high-performance PEMs with improved durability are still being sought. Presently, PEM fuel cells operate at temperatures up to 95° C. with external humidification being required to maintain proton conductivity that deteriorates rapidly as the membranes dry out. Perfluorosulfonic acid membranes have been the preferred materials for PEM, but they suffer from poor mechanical integrity and they are expensive. Consequently, new alternative PEM materials are continuously being sought.
  • The present invention is directed to a process for preparing a polymer. The process comprises sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer. The sulfonating agent comprises oleum or SO3.
  • In accordance with another embodiment of the present invention, a process for preparing a proton exchange membrane is provided. The process comprises the steps of: (a) sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer and (b) forming the sulfonated perfluorocyclobutane polymer into a proton exchange membrane. The sulfonating agent comprises oleum or SO3.
  • In accordance with yet another embodiment of the present invention, a fuel cell is provided. The fuel cell comprises a proton exchange membrane formed by sulfonating a perfluorocyclobutane polymer with oleum to form a sulfonated perfluorocyclobutane polymer and (b) forming the sulfonated perfluorocyclobutane polymer into a proton exchange membrane. The sulfonating agent comprises oleum or SO3.
  • In accordance with a further embodiment of the present invention, a process for assembling a device comprises the act of preparing a membrane electrode assembly. The membrane electrode assembly comprises electrically conductive material on either side of a proton exchange membrane. The proton exchange membrane is prepared according to a process comprising the act of sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer, wherein the sulfonating agent comprises oleum or SO3. The device comprises an electrochemical conversion assembly comprising at least one electrochemical conversion cell configured to convert first and second reactants to electrical energy. The electrochemical conversion cell comprises the membrane electrode assembly, an anode flowfield portion and a cathode flowfield portion defined on opposite sides of the membrane electrode assembly. A first reactant supply configured to provide a first reactant to an anode side of the membrane electrode assembly via the anode flowfield portion, and a second reactant supply configured to provide a second reactant to a cathode side of the membrane electrode assembly via said cathode flowfield portion.
    • BRIEF DESCRIPTION OF THE FIGURES
  • The following detailed description of specific embodiments of the present invention can be best understood when read in conjunction with the following figures.
  • FIG. 1 is a graph depicting that the amount of sulfonation is determined by the ratio of oleum to polymer used;
  • FIG. 2 is a graph depicting the conductivity vs. % relative humidity of sulfonated perfluorocyclobutane-biphenyl vinyl ether (BPVE) polymers 4 with different Ion Exchange Capacities (I.E.C.s);
  • FIG. 3 is a graph depicting conductivity vs. % relative humidity of sulfonated perfluorocyclobutane-hexafluoroisopropylidene biphenyl vinyl ether (BPVE 6F) copolymers, 6 with different I.E.C.s;
  • FIG. 4 is a graph depicting water uptakes for various sulfonated perfluorocyclobutane polymers;
  • FIG. 5 is a graph depicting volume swell at 25 and 100° C. in water for PFCB Polymers, plotted as semi-log (A) and linear graph (B);
  • FIG. 6 is a graph of fuel cell data of sulfonated BPVE polymers depicting cell voltage (in volts) versus current density (in Amperes/cm2), which has been IR-corrected for the experimentally measured High Frequency Resistance (HFR); and
  • FIG. 7 is a graph of fuel cell data of sulfonated BPVE 6F copolymers depicting cell voltage (in volts) versus current density (in Amperes/cm2), which has been IR-corrected for the experimentally measured High Frequency Resistance (HFR).
    • DETAILED DESCRIPTION
  • The inventors have discovered a new process for preparing new proton conducting membranes made with perfluorocyclobutanes polymers (PFCBs) having sulfonic acid groups (SPFCBs,), which may be used in PEM fuel cells that can operate over a broad range of relative humidity and at temperatures around 95° C. The properties of the SPFCB films are dependent on the chemical structure and the ion exchange capacity of the film, which can be tailored by the reaction conditions used. These SPFCB-films are reasonable alternatives to perfluorosulfonic acid membranes, presently being used in PEM fuel cells, because the sulfonated polymers have high intrinsic proton conductivity and inherent dimensional-, hydrolytic- and high-temperature stability.
  • PFCBs are commercially available from Tetramer Technologies, under license agreements from Dow Chemical. Examples of PFCBs are provided with the structures 1-3:
    Figure US20070099054A1-20070503-C00001
    The synthesis of PFCBs is described in U.S. Pat. Nos. 5,037,917 and 5,159,037—this particular subject matter is expressly incorporated herein by reference.
  • To form potentially useful PEMs, subsequent sulfonation of the PFCBs is required. Prior art teaches a sulfonation procedure that uses chlorsulfonic acid, which has limited synthesis utility and scope and which produces inconsistent membrane materials. The inventors have discovered a novel process for synthesizing SPFCBs. The process comprises sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer. The sulfonating agent comprises oleum, SO3 or a combination thereof. One skilled in the art will appreciate that various PFCBs are available for use in the present process, any of which may be employed herein. In one embodiment, the PFCB comprises the formula:
    Figure US20070099054A1-20070503-C00002
    wherein X is O or S;
    R is
    Figure US20070099054A1-20070503-C00003
    Figure US20070099054A1-20070503-C00004
    n is greater than about 20.
    In one embodiment, n is from about 20 to about 500. Specific examples of such PFCBs include, but are not limited to, structures 1-3, defined in detail above.
  • In addition, one skilled in the art will appreciate that various concentrations of the sulfonating agent may be employed to sulfonate a PFCB polymer, any of which may be employed herein. In one embodiment, the oleum comprises 10% oleum. In another embodiment, the oleum comprises 20% oleum. In yet another embodiment, the oleum comprises 30% oleum. Moreover, one skilled in the art will appreciate that various SPFCBs may be formed from reacting a PFCB with a sulfonating agent. In one embodiment, the sulfonated polymers have between 0-2 sulfonic acids per repeat unit. Examples of such SPFCBs include, but are not limited to, structures 4-6:
    Figure US20070099054A1-20070503-C00005
    Furthermore, one skilled in the art will appreciate the various experimental parameters in which the process for preparing the sulfonated polymer may be performed, any of which may be employed herein. In one embodiment, the process further comprises the step of dissolving the PFCB polymer in methylene chloride prior to sulfonating the PFCB. In another embodiment, the process is performed from about −20° C. to about 200° C.
  • In accordance with another embodiment of the present invention, a process for preparing a proton exchange membrane is provided. The process comprises the steps of: (a) sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer and (b) forming the sulfonated perfluorocyclobutane polymer into a proton exchange membrane. The sulfonating agent comprises oleum or SO3.
  • In accordance with yet another embodiment of the present invention, a fuel cell is provided. The fuel cell comprises a proton exchange membrane formed by sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer and (b) forming the sulfonated perfluorocyclobutane polymer into a proton exchange membrane. The sulfonating agent comprises oleum or SO3. As shown in the Example, SPFCB membranes prepared according to the present invention have markedly improved and consistent fuel cell performance compared with those of the prior art. In one embodiment, the SPFCB copolymer has an ion exchange capacity of from about 0.6 to about 2.5 meq/gram. In another embodiment, the SPFCB copolymer has an ion exchange capacity of from about 1.3 to about 2.0 meq/gram.
  • In accordance with a further embodiment of the present invention, a process for assembling a device comprises the act of preparing a membrane electrode assembly. The membrane electrode assembly comprises electrically conductive material on either side of a proton exchange membrane. The proton exchange membrane is prepared according to a process comprising the act of sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer, wherein the sulfonating agent comprises oleum or SO3. The device comprises an electrochemical conversion assembly comprising at least one electrochemical conversion cell configured to convert first and second reactants to electrical energy. The electrochemical conversion cell comprises the membrane electrode assembly, an anode flowfield portion and a cathode flowfield portion defined on opposite sides of the membrane electrode assembly. A first reactant supply configured to provide a first reactant to an anode side of the membrane electrode assembly via the anode flowfield portion, and a second reactant supply configured to provide a second reactant to a cathode side of the membrane electrode assembly via said cathode flowfield portion.
    • EXAMPLE
  • Treatment of Polymers with Structures 1, 2, and 3 with 30% Oleum.
  • The properties of the SPFCB films are dependent on the chemical structure and the ion exchange capacity of the films, and performance can be tailored by the reaction conditions used. The amount of oleum specified in Table 1 is added to the respective polymer 1, 2 or 3, (ca 1 gram) dissolved in methylene chloride (5 mL) in a screw cap jar. The jar lid is secured and then the jar is shaken vigorously. A purple gel immediately forms, and then the jar is placed on a roll mill for between 0.5 and 1 hour. A clear liquid phase separates, which is decanted off and discarded, and the purple solid is added to vigorously stirred water (250 mL) using a Waring blender. The polymer becomes swollen white crumbs, which are isolated by vacuum filtration, washed with water and then air-dried. The sulfonated polymer (ca 1 g) readily dissolves in tetrahydrofuran (4 mL) and methanol (2 mL).
  • The solution is filtered through an 80—micron polypropylene filter cloth and is cast onto a glass plate (8-inch×8 inch) using a six-inch coating applicator bar with an 18-mil coating gap. The coated film is covered with a Pyrex glass dish, and then air-dried (to touch in about 10 minutes). A free-standing film is produced after floating the film off the glass with water. After extensive washing with water and air-drying, a 25-micrometer thick film is obtained. Pieces of the film (ca 0.02 g) are characterized by titration with standardized sodium hydroxide (0.010N) to determine its acid ion exchange capacity (see FIG. 1), by measuring proton conductivity versus percent relative humidity (see FIGS. 2 and 3), and by determining water uptake after 1-hour immersion in water at 25 and 100° C. (boiling water), see FIG. 4. Percent volume swell is determined for the PFCB polymers as well, see FIG. 5. A piece of the film (4-inch×4-inch) is then tested in a fuel cell using electrodes made of catalyst coated diffusion media (CCDM) made with a coating of platinum on carbon (Tanaka) that is milled with A-K 900 SS PFSA ionomer solution and then coated on top of carbon-fiber diffusion media with a microporous layer.
    TABLE 1
    Reaction Conditions to Prepare Sulfonated Perfluorocyclobutane Polymers
    Made with 30% Oleum
    % H2O Up- oleum/
    IEC, meas IEC calcd take 100 C. polymer ratio FCD # Thickness μ
    Polymer 4
    BPVE 1.49 1.51 27.3 0.6171/1.0298 0.5992
    BPVE 1.66 1.65 28.7 0.7244/1.0096 0.7175
    BPVE 1.65 1.65 43.4 0.7289/1.0134 0.7193 1335 23
    BPVE 1.78 1.78 105 0.8168/1.0033 0.8141 1408 11
    BPVE 1.92 1.90 156 0.9655/1.0030 0.9626 1329 25
    Polymer 6
    BPVE 6F 1.52 1.51 95 0.6383/1.0030 0.6364 1410 22
    BPVE 6F 1.58 1.56 73.8 0.6776/1.0280 0.6591 1303
    BPVE 6F 1.73 1.73 164 0.7698/1.0412 0.7393 1313
    BPVE 6F 1.80 1.80 161 0.7927/1.0237 0.7743 1330 25
    BPVE 6F 1.93 1.93 474 0.932/1.116 0.8351 1320
  • The ion exchange capacity of the sulfonated polymers 4-6 is dependent on the weight (or molar) ratio of the 30%-oleum used per gram of polymer (see FIG. 1). Thus, the I.E.C. of the respective polymers can be specifically controlled by the amount of oleum added. The sulfonation reaction is quite fast and non-selective towards the different biphenyl ether groups in the PFCB backbone, and reaction times are less than one hour. The polymer 5 can be sulfonated with 30% oleum within 20 minutes under the conditions described, but poor films were obtained with both the starting polymer and the sulfonated polymer due to its low molecular weight. Thus, films of the sulfonated polymer 5 were too brittle to be evaluated.
  • Good fuel cell performances were obtained for films made of the SBPVE polymer 4 with ion exchange capacities between 1.4 and 1.9 meq. of sulfonic acid per gram (see FIG. 6). With the sulfonated copolymer 6, flooding of the fuel cell took place with the PEM that had an I.E.C. of 1.9 meq/g of sulfonic acid. The other materials with between 1.52 and 1.8 meq/g of sulfonic acid showed very good fuel cell performance under the high-relative humidity conditions used (see FIG. 7).
  • All of the fuel cell results are summarized in Table 2.
    TABLE 2
    Summary of Fuel Cell Tests on PFCB Polymers.
    Fuel Water Volume
    Cell Sulfonating Uptake Swell
    Polymer I.E.C. Test Agent Vuncorr LOW P, 50 kPa g Vuncorr High P, 170 kPa g Assessment 100 C. 100 C.
    BPVE- 1.4 FCD ClSO3H 0.361 v at 0.8 A/cm2 0.31 at 1.0 A/cm2 No Good x x
    6F (6) 1295
    BPVE- 1.5 FCD 30% oleum 0.556 v at 1.2 A/cm2 0.529 v at 1.2 A/cm2 Good 29 24
    6F (6) 1410
    BPVE- 1.58 FCD 30% oleum 0.604 v at 1.2 A/cm2 0.557 v at 1.2 A/cm2 Good 74 104
    6F (6) 1303
    BPVE 1.65 FCD 30% oleum 0.564 v at 1.2 A/cm2 0.529 v at 1.2 A/cm2 Good 43 36
    (4) 1335
    BPVE 1.68 FCD ClSO3H 0.268 v at 0.4 A/cm2  0.27 v at 0.6 A/cm2 No Good x x
    (4) 1309
    BPVE- 1.73 FCD 30% oleum 0.600 at 1.2 A/cm2 0.586 v at 1.2 A/cm2 Good 164 244
    6F (6) 1313
    BPVE- 1.75 FCD ClSO3H 0.434 v at 1.2 A/cm2  0.57 v at 1.2 A/cm2 Fair 36 x
    6F (6) 1394
    BPVE 1.78 FCD 30% oleum 0.629 v at 1.2 A/cm2 0.624 v at 1.2 A/cm2 Good 105 84
    (4) 1408
    BPVE- 1.8 FCD 30% oleum 0.625 v at 1.2 A/cm2  0.63 v at 1.2 A/cm2 Good 161 151
    6F (6) 1330
    BPVE 1.9 FCD 30% oleum 0.606 v at 1.2 A/cm2 0.637 v at 1.2 A/cm2 Good 156 238
    (4) 1329
    BPVE- 1.93 FCD 30% oleum 0.311 v at 1.2 A/cm2 0.493 v at 1.2 A/cm2 No Good 474 393
    6F (6) 1320
  • In general, there is considerable concern about the oxidative stability of hydrocarbon membranes in fuel cells, and one ex-situ test consists of an assessment of membrane stability on immersion in Fenton's reagent. The polymers 4 and 6 showed a 17 to 18 wt. % loss after 19 hours in a Fenton's test solution made with 4-ppm Fe2+ (ferrous chloride tetrahydrate) and 3% hydrogen peroxide in an oven set at 70° C. This compares with Nafion 112, which loses less than 0.5 wt. % under the same conditions.

Claims (13)

1. A process for preparing a polymer comprising sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer, wherein the sulfonating agent comprises oleum or SO3.
2. The process of claim 1, wherein the perfluorocyclobutane polymer comprises the formula:
Figure US20070099054A1-20070503-C00006
wherein:
X is O or S;
R is
Figure US20070099054A1-20070503-C00007
Figure US20070099054A1-20070503-C00008
n is greater than about 20.
3. The process of claim 2, wherein n is from about 20 to about 50.
4. The process of claim 2, wherein the perfluorocyclobutane polymer comprises the formula:
Figure US20070099054A1-20070503-C00009
wherein n is from about 20 to about 500.
5. The process of claim 1, wherein the sulfonated perfluorocyclobutane polymer comprises 0-2 sulfonic acid groups per repeating unit.
6. The process of claim 1, wherein oleum comprises 10% oleum, 20% oleum or 30% oleum.
7. The process of claim 1, further comprising the step of dissolving the perfluorocyclobutane polymer in methylene chloride prior to sulfonating the polymer.
8. The process of claim 1, wherein sulfonating a perfluorocyclobutane polymer yields a sulfonated perfluorocyclobutane polymer with an ion exchange capacity of from about 0.6 to about 2.5 meq/gram.
9. The process of claim 8, wherein sulfonating a perfluorocyclobutane polymer yields a sulfonated perfluorocyclobutane polymer with an ion exchange capacity of from about 1.3 to about 2.0 meq/gram.
10. The process of claim 1, wherein the process is performed from about −20° C. to about 200° C.
11. A process for preparing a proton exchange membrane comprising the steps of: (a) sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer and (b) forming the sulfonated perfluorocyclobutane polymer into a proton exchange membrane, wherein the sulfonating agent comprises oleum or SO3.
12. A fuel cell comprising the proton exchange membrane of claim 11.
13. A process for assembling a device, the process comprising the act of preparing a membrane electrode assembly, wherein: the membrane electrode assembly comprises electrically conductive material on either side of a proton exchange membrane; wherein the proton exchange membrane is prepared according to a process comprising the act of sulfonating a perfluorocyclobutane polymer with a sulfonating agent to form a sulfonated perfluorocyclobutane polymer, wherein the sulfonating agent comprises oleum or SO3; and wherein the device comprises an electrochemical conversion assembly comprising at least one electrochemical conversion cell configured to convert first and second reactants to electrical energy, the electrochemical conversion cell comprising the membrane electrode assembly, an anode flowfield portion and a cathode flowfield portion defined on opposite sides of the membrane electrode assembly, a first reactant supply configured to provide a first reactant to an anode side of the membrane electrode assembly via the anode flowfield portion, and a second reactant supply configured to provide a second reactant to a cathode side of the membrane electrode assembly via said cathode flowfield portion.
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Owner name: GM GLOBAL TECHNOLOGY OPERATIONS, INC., MICHIGAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:FULLER, TIMOTHY J.;SCHOENEWEISS, MICHAEL R.;REEL/FRAME:017220/0467

Effective date: 20060127

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION